102 00553 0619 Olin Sodium Hypochlorite Manual

SODIUM HYPOCHLORITE
PRODUCT STEWARDSHIP MANUAL

Table of Contents
Introduction 4
Safety 4
Responsible Care® 4
The Chlorine Institute and Continuous Improvement 4
Customer Notice 5
Olin Product Stewardship 6
Manufacturing 7
Locations 7
Product Grades 7

Properties 8
Certifications 8
Chemistry 8
Oxidation Power (Available Chlorine) 8
Importance of Density 9
Decomposition 9
Temperature Impact on Stability 10
Metals Impact on Stability 11
Dilution 11
Dilution and Excess Residual Alkalinity 12
Crystallization Points 12
Manufacturing Processes 13
Concentration Units 14
Shipping 15
Hazardous Material Transportation System 15
Sodium Hypochlorite Shipping Containers 16
Tank Trailers 16
Tank Cars 16
HAZMAT Training & Unloading Requirements 17
Written Procedures 17
Checklists 17
Training 17
General Unloading System Requirements 18
Tank Trailers 18
Tank Cars 18
Pad Gas System 19
Pad Gas Quality 19
Inspection 20
Transfer System 21
Transfer Hoses 21
Pumps 21
Valves 22
Piping 22
Piping Materials of Construction 22
Piping Installation 23
Piping Support 23
Pipe Glues 23
Pipeline Identification 23
Inspection and Replacement 23
SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 1

Storage Equipment 23
Materials of Construction 24
Titanium 24
Rubber Lined Steel 24
Fiberglass Reinforced Plastic and Dual Laminates 24
Poly Tanks 24
Fabricator Evaluation 24
Design Considerations 24
Sizing 24
Venting 25
Overflows 25
Receiving Pipeline 25
Filtration 25
Outlet Nozzles 25
Flexible Connections and Piping Support 25
Level Measurement 26
Tie Downs 26
Storage Tank Identification 26
Storage Tank Preventative Maintenance 26
Cleaning 26
Inspection 26
Storage Tank and Unloading Station Containment Systems 26
Incompatible Chemicals During Unloading 27
Personal Protection 28
Safety Data Sheets 28
Personal Protective Equipment 28
First Aid Procedures 29
General Guidelines 29
Safety Shower and Eyewashes 29
Responding to Emergencies 29
Spills and Leaks 30
General Guidelines 30
How to Respond to Spill Events 30
Special Considerations 31
Neutralization 31
Disposal 31
Analytical Guidelines 32
Importance of Accuracy 32
Sample Collection 32
Sample Handling 32
Analytical Method 32
Important Procedural Considerations 33
Discussion of Units 33
Best Practices 33
Residual Alkalinity Analytical Testing 33
Additional Information and Emergency Contacts 34
For Additional Information 34
Emergency Contacts 34
Trademarks 34
Graph Appendix 35

Introduction

Introduction
Introduction The Chlorine Institute and Continuous
Sodium hypochlorite, also known as hypochlorite, hypo, bleach or Improvement
NaOCl, is used in a wide range of industrial settings. Olin has long been
Olin has a long history of embracing and promoting chemical safety and
regarded as a dependable source of sodium hypochlorite, and our recent
is a founding member of The Chlorine Institute. The Chlorine Institute is
innovation in distribution has established Olin as the clear lead supplier
a technical trade association of companies involved in the safe production,
of industrial bleach in North America.
distribution, and use of chlorine, sodium and potassium hydroxides, sodium
Historically, sodium hypochlorite was transported by tank trailer to hypochlorite, and hydrogen chloride. Since its founding in 1924, Olin has
nearby markets. Beginning in 2007, Olin initiated tank car service supported The Chlorine Institute in promoting the continuous improvement
across North America for sodium hypochlorite, allowing for long- in safety, protection of human health and the environment, and security
distance transportation. No longer is sodium hypochlorite distribution associated with the production, transportation, handling, and use of sodium
considered a local activity. This innovative transportation mode, along hypochlorite and other chlor alkali chemicals. As a Chlorine Institute
with production and distribution facilities located strategically across the member, Olin is committed to adopting the Institute’s safety and stewardship
United States and eastern Canada, has transformed Olin into the largest initiatives to achieve measurable improvement over time. A number of
producer of sodium hypochlorite in North America. Chlorine Institute bulletins and pamphlets discussing the safe handling of
sodium hypochlorite are referenced in this handbook.
Olin’s reliable supply of sodium hypochlorite offers you the quality you
need in a wide variety of concentrations, and is backed by a customer Olin is also an active member of the American Chemistry Council (ACC),
support network that only Olin can provide. Check with your Olin America’s oldest trade association of its kind. The ACC represents
representative for particular solution strengths available in your market. companies engaged in the business of chemistry who are committed to
continuously improving the safety, health, environmental, and security
performance of the chemical industry. In addition, Olin is an active member
Safety of the Chemistry Industry Association of Canada (CIAC). The CIAC is
a trade association representing Canada’s leading chemistry companies
At Olin, safety and quality are integral to everything we do. Our goal
adhering to the principles of the ACC- initiated Responsible Care® program,
is zero when it comes to safety incidents, with a focus on preventing
which is now a global initiative with a focus on sustainable stewardship.
accidents, injuries, and chemical incidents not only within Olin, but
We incorporated the ACC’s Responsible Care® program and the CIAC’s
also in the communities we touch. Olin has internal processes to foster
standards into our business model at their introduction into the marketplace.
continuous improvement in the areas of product quality, environmental
Key aspects of the ACC’s and CIAC’s Responsible Care® initiatives include:
protection, safety, and product stewardship.
• Commitment made by the chemical industry to the safe, responsible,
and sustainable management of chemicals through their entire life
Responsible Care® cycle, and for their intended end use.
Olin has a long-standing policy to ensure that its operations do not • World-class performance initiative for the chemical industry.
have an adverse impact on the community or the environment. Olin is • Companies who are industry leaders, bound together by a commitment
committed to the guiding principles of Responsible Care®, a continuing to address challenges and continuously improve the performance of the
effort by the chemical industry to improve the responsible management chemical industry.
of chemicals. • Verifiable management systems to achieve Responsible Care®
goals via third-party auditors.
As a Responsible Care® Company, Olin follows the 12 Guiding Principles
and Codes of Management Practices that cover all aspects of research, Olin has a number of programs intended to foster continuous improvement
development, manufacture, distribution, transportation, use, and disposal with use of our chemicals. This handbook is intended to assist customers in
of products. These principles also extend to prompt reporting, customer understanding the chemistry, delivery, receipt, storage, and safe handling
counseling, community awareness, support of external research, and of sodium hypochlorite solutions – to help safeguard employee health,
promotion of Responsible Care® worldwide. encourage safe working practices, and protect the environment when
working with sodium hypochlorite. The handbook’s content primarily
Olin recognizes that no single entity can fully protect the quality of focuses on 12.5% by weight sodium hypochlorite, a predominant solution
our environment. However, by working together on a global basis, the strength in North America, along with some information concerning Olin’s
public, industry, and government can make the future brighter and safer. HyPure® Bleach.

Introduction
Customer Notice
Olin strongly encourages its customers to review both their handling
processes and their applications of Olin products from the standpoint of
human health and environmental quality. To help ensure that Olin products
are not used in ways for which they are not intended or tested, Olin
personnel are prepared to assist customers in dealing with ecological and
product safety considerations. Your Olin representative can arrange the
proper contacts. Also, Olin product literature, including Safety Data Sheets
(SDS), should be consulted prior to use of Olin products. For copies,
contact your Olin representative or the Olin location nearest you.
Olin believes the information and suggestions contained in this manual

to be accurate and reliable as of publication date. However, since use
conditions and disposal are not within its control, Olin assumes no
obligation or liability for such assistance and does not guarantee results
from use of such products or other information herein. No warranty,
express or implied, is given nor is freedom from any patent owned by
Olin or others to be inferred.
Information herein concerning laws and regulations is based on U.S.

federal laws and regulations, except when specific reference is made
to those of other jurisdictions. Since use conditions and governmental
regulations may differ from one location to another and may change
with time, it is the customer’s responsibility to determine whether Olin’s
products are appropriate for the customer’s use, and to assure that the
customer’s workplace and disposal practices are in compliance with laws,
regulations, ordinances, and other governmental enactments applicable in
the jurisdiction(s) having authority over the customer’s operations.

Olin Product Stewardship
Olin Product Stewardship

At Olin, our Product Stewardship program is guided by our core values of Integrity, Customer Success, Innovation, and People. We are committed to
the safe handling and use of our products – and enabling all of our collaborators throughout the value chain to do the same. As a Responsible Care®
company, we assess the safety, health, and environmental information on our products, and then take appropriate steps to protect employees, public
health, and the environment. Ultimately, the success of our product stewardship program rests with each and every individual involved with Olin
products – from the initial concept and research to the manufacture, sale, distribution, use, disposal, and recycling of each product.

Manufacturing
Locations Olin Bleach Production Locations

Olin has multiple sites throughout North America that manufacture sodium
sca n
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James
Saskatchewan
Bay
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hypochlorite solutions, commonly referred to as “bleach.” The capabilities

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of these sites are similar with slight differences in the grades of product
Bow
Peribonca
Winnipeg
available to meet specific market needs. Olin is uniquely positioned Red

BÉCANCOUR, QC
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Snake Missouri
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Columbia
to service your sodium hypochlorite needs as a true integrated North

Ottawa
Yellowstone
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American manufacturer with production facilities and terminals located Snak

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NIAGARA FALLS, NY
throughout the United States and eastern Canada. Production sites are
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Sacramento
LEMONT, IL
North
shown on the map included in this section. Through our network of

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Ohio
TRACY, CA
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as
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manufacturing facilities, shipping equipment, and terminals, we can ship

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Illinois
Color
Ohio
Missouri
Arkansas
HENDERSON, NV
just about anywhere within the United States and North America. For more
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Ohio
Color
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SANTA FE SPRINGS, CA CHARLESTON, TN

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information about your specific needs, contact an Olin representative.

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AUGUSTA, GA
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Red
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Gran
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MCINTOSH, AL
Miss
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Rio Grande
FREEPORT, TX
Lake
Okeechobee
Bleach Production Plants
Product Grades
Sodium hypochlorite solution grades are typically defined by differences in product assay and/or alkalinity content. From an industrial perspective, Olin
offers a variety of different product strengths depending on industries served and local market demands with 12.5 and 15.5 weight percent as
NaOCl solutions being the most prevalent. Olin production facilities incorporate additional blending systems that provide the ability to customize the
assay and alkalinity component concentrations to meet particular application requirements.
Olin also manufactures a high-strength, low-salt sodium hypochlorite solution known as HyPure® Sodium Hypochlorite or HyPure® Bleach (HPB), which
has an assay of up to 23 weight percent as NaOCl. HyPure® Bleach is not available in all North American markets (for example, western U.S. and west-
Canada provinces) and may not be suitable for your process. Contact your Olin representative for further discussions of HyPure® Bleach and its availability
in your market.

Properties
Certifications Equation 2:
Olin’s sodium hypochlorite solutions are well-suited for use in a variety NaOCl+2 KI+2 HAc→I2+ NaCl+2 KAc+H2O
of industrial and municipal applications. We offer product certification
upon request for various industry and regulatory standards including Equation 3 shows the oxidation of 2 moles of potassium iodide (KI) with 1
the American Water Works Association (AWWA B300), National mole of chlorine yields one mole of iodine (I2) and 2 moles of salt (KCl).
Sanitation Foundation (NSF Standard 60 requirements), as well as U.S.
Equation 3:
EPA pesticide registration and Canada Pest Management Regulatory
Agency (PMRA) registration. Contact your Olin sales representative to Cl2+2 KI→I2+2 KCl
discuss specifications, certifications, and product grades available in your
particular market. In other words, a mole of sodium hypochlorite will oxidize the same
amount of iodide as will a mole of chlorine. The molecular weight of
Chemistry NaOCl is 74.5 (23 + 16 + 35.5); the molecular weight of chlorine (Cl2) is
71 (2 × 35.5). The term “available chlorine” was coined to describe this
Sodium hypochlorite solutions are most often produced using an automated relationship in the sodium hypochlorite context. The ratio of molecular
continuous process. In early commercial production, hypochlorite was made weights (74.5/71), or 1.05, quantifies this relationship.
in a batch process, wherein Chlorine gas or liquid is injected into a dilute
caustic solution. To avoid over-chlorination and to maintain the excess To relate gallons of sodium hypochlorite solution to pounds of chlorine,
alkalinity required to produce a stable hypochlorite solution, chlorine the hypochlorite’s strength as expressed in units of available Cl2 must be
addition must be discontinued prior to complete depletion of the caustic converted to the equivalent pounds of chlorine to answer the question
present in the solution. Sodium hypochlorite manufacturing follows the above using the equation:
chemical reaction below which combines caustic soda and chlorine to
produce one mole of sodium chloride (NaCl) for each mole of sodium Equation 4:
hypochlorite (NaOCl). A mole is a measure of the number of molecules of a
compound. This one-to-one ratio of production products often garners the
Avail. Cl2 g/L (A) X 3.785 liters/U.S. Gal X 2.205
name of ‘equimolar sodium hypochlorite’ as a result.
lbs./1000 grams = lbs. Avail. Cl2/U.S. Gal solution
For example, 120 g/L available Cl2 X 3.785 X 2.205/1000 = 1 pound
Equation 1:
available Cl2/gallon of solution. Expressed differently, one gallon of
Cl2+2 NaOH→NaOCl+NaCl+H2O sodium hypochlorite solution having 120g/L available chlorine provides
the equivalent oxidizing power of one pound of chlorine, (120 g/L
available Cl2 = 1 lb. chlorine per gallon of solution). The unique one-
Oxidation Power (Available Chlorine) to-one ratio provides a convenient basis point when other hypochlorite
Disinfecting, bleaching and oxidizing are the major applications of this solution strengths (in grams per liter of available Cl2) are considered.
product. Before the development of sodium hypochlorite solutions,
chlorine was used directly for many of these applications. With the storage When evaluating other hypochlorite solutions for chlorine equivalency using
advantages of an aqueous solution, sodium hypochlorite solutions have available chlorine, always divide the grams per liter available chlorine by
replaced chlorine in many of these typical end uses. 120 g/L. For example, (150 g/L available Cl2 /120 g/L avail. Cl2) = 1.25.
In this example, one gallon of 150 g/L available Cl2 solution yields the
This leads to the obvious question: How much chlorine (Cl2) is available in equivalent of 1.25 pounds of chlorine gas. This ratio will then indicate how
a sodium hypochlorite (NaOCl) solution? much more (or less) equivalent chlorine is present in a given hypochlorite
solution compared to a fixed amount of chlorine gas. Similar calculations
Equation 2 shows the oxidation of 2 moles of potassium iodide (KI) with 1 can be performed using wt% NaOCl provided the solution density is known.
mole of sodium hypochlorite in a solution of acetic acid (HAc) yields one
mole of iodine (I2), 1 mole of salt (NaCl), 2 moles of Potassium Acetate
(KAc) and water.

Properties
Importance of Density –– Conversion between weight % and grams per liter (GPL) or trade %. The
‘Sodium Hypochlorite Solution Stability and Density at 70ºF’ graph illustrates
Density is a prevalent analytical tool used in petroleum how density affects this conversion.
and some chemical industries to quickly identify
contaminations and correlate product quality without Graph 1: Bleach Stability and Density at 70ºF
the use of expensive laboratory instrumentation or
performance of time-intensive “wet chemistry” tests.
Appropriate applications for use of density determination
in sodium hypochlorite should be well-understood and
judiciously chosen. When determining weight-based
calculations, performing an actual density analysis is
critical to predicting the most precise assay value for
a just-collected sample. However, the unique nuances
associated with chemical composition and production,
as well as the decomposition attribute of sodium
hypochlorite, can lead to erroneous conclusions when
density is incorrectly used to predict hypochlorite solution
assay. The specific gravity/density of a solution of chemical
compounds is a function of the compounds (what and how
much) that make up the solution. HyPure® Bleach solutions
have significantly lower concentrations of sodium chloride as
compared to the same strength of standard bleach solutions
and therefore have a lower specific gravity/density.
Sodium hypochlorite density is affected by a variety of Note: See Appendix for larger graph
factors. It is important to remember that the correlation
between sodium hypochlorite concentration and density
is not exact because all bleach solutions are a mixture Sodium hypochlorite strength is time dependent, with all solutions starting to lose assay
of a number of chemical compounds, such as sodium immediately after production. Unlike hypochlorite strength, density will remain unchanged
chloride, sodium hydroxide, etc. Therefore, a small over time. For immediately produced product, density will generally correlate with assay.
change in one of these compounds will alter the However, the correlation will continue to change as the solution ages and will yield
density without changing the sodium hypochlorite increasingly erroneous conclusions the older the hypochlorite solution is. Other factors such
concentration. For example: as metallic content of the hypochlorite, temperature exposure, and solution age become
• Density Effect on Flow Measurement increasingly critical with time because product assay is significantly affected by these
contributors. These attributes provide the rationale explaining why an aged hypochlorite
–– Flow measurement instruments such as mag
solution will have a significantly different assay than a freshly produced one, but density of
meters that are affected by changes will have
to be adjusted for this density difference. the solutions will remain unchanged. As a result, hypochlorite solution density (or specific
Devices that use volume displacement device gravity), should not be specified in chemical purchase specifications or acceptance
(rotameters, metering pumps, vortex meters, criteria because it is not a reliable predictor of sodium hypochlorite strength. When
etc.) will not be affected. precision is required for determining strength, assay titration is preferred.
• Level Measurement
For applications where density must be determined, there are several different test
–– Level instrumentation that relies on pressure methodologies available, including density meters, hydrometers, or use of a pipette-
(pressure gauges, differential pressure cells, and-weigh combination. When determining density via meter or hydrometer, the results will
etc.) will need to be recalibrated based on the need to be temperature-adjusted to yield the most accurate results. Facilities that have an
new density. analytical balance accurate to four decimal places often favor the pipette-and-weigh method. In
• Converting Between Volume and Weight Units this method, a 10mL sample is pipetted into a sample bottle and weighed. The corresponding
–– The density difference must be accounted weight is then divided by the sample volume (10mL) to obtain the solution density.
for when converting between weight and
U.S. gallons. Decomposition
–– Converting shipping container net weight
All sodium hypochlorite solutions continually decompose on standing after they are
to gallons.
produced. Decomposition cannot be avoided, but the rate of degradation can be slowed.
–– Filling bottles by volume and then weighing The effects of time, temperature, hypochlorite/ionic strength, and exposure to trace metals
the finished goods. are significant contributors.

Properties
Decomposition rates will be affected by impurities and handling Graph 2: Estimated Decomposition of 12.5 wt% Sodium
conditions. Equation 5 depicts the temperature-controlled decomposition Hypochlorite Solution
reaction. The thermal decomposition route primarily results in production
of chloride and chlorate ions.
Equation 5:
3 NaOCl + Temperature & Time →2 NaCl+NaClO3

The presence of trace metals catalyzes the sodium hypochlorite
decomposition according the following equation, which produces oxygen
and salt. Small bubbles of the gas will emanate from these particles and rise
to the surface provide telltale evidence of this problematic reaction. Many
times, these gas bubbles are barely visible to the naked eye or require use
of a microscope to see. Small amounts of nickel, cobalt, and copper
are particularly reactive even at parts per billion (ppb) levels. Oxygen
generation and the corresponding loss in assay (NaOCl) will continue until all Graph 3: Estimated Decomposition of 15.5 wt% Sodium
hypochlorite has been decomposed or until the trace metal has been removed Hypochlorite Solution
from the solution. Operational and safety concerns are associated with this
reaction (Eq.6). In some situations, oxygen content may be significant.
Temperature Impact on Stability

In most situations, the temperature and concentration at which the sodium
hypochlorite solutions are stored have the most impact on their stability
because decomposition is slowed as concentration and temperature
decrease, assuming all other conditions are similar and unchanged. As a
general rule, lower concentration solutions are more stable than higher
strength solutions, assuming that other conditions such as temperatures, pH
and metal ion concentrations are similar. Studies of sodium hypochlorite
solutions have shown that the decomposition rate increases by a factor of
approximately two to four times for every 10°C (18°F) temperature rise.
See the adjacent decomposition charts. In order to determine your best
option for minimizing product decomposition, each application should be Graph 4: Estimated Decomposition of Standard and HyPure® Bleach
reviewed based on hypochlorite strength, storage temperature, and storage
time. Closely related to temperature exposure is ultraviolet light-induced
decomposition. Shielding of storage systems and qualification samples from
sunlight exposure can eliminate this variable.
HyPure® Bleach (see adjacent Decomposition Graphs) exhibits

different decomposition characteristics as compared to standard sodium
hypochlorite solutions. Concentrated HyPure® Bleach will actually
degrade at a faster rate than other sodium hypochlorite solutions as a
result of the additional amount of active ingredient.
However, once diluted, HyPure® Bleach exhibits a slower decomposition

rate compared to a standard sodium hypochlorite solution of equal product
assay. We can look at this two different ways:
• At the same assay and temperature, HyPure® Bleach is about 40%
more stable than standard bleach.
• At the same temperature, a 20% stronger solution of HyPure®
Bleach will have the same stability as standard bleach. Note: See Appendix for larger graphs
The total amount of all chemical compounds dissolved in any bleach

solution is a major factor in determining how stable the bleach is.

Properties
The higher the purity of the bleach solution, the more stable it is. By metallic contents. Customer-controlled exposure opportunities encompass
removing salt in the manufacturing process, Olin manufactures a more all areas of product handling beginning at the unloading process and
pure product, which once diluted, offers greater stability of the solution. continuing through to product formulation and use. Because of the
potential significant impact to product quality, a rigorous management of
For example: all handling processes will be required to ensure all wetted surfaces are
• A 12.5% (wt% NaOCl) solution of sodium hypochlorite will metals-free (except for titanium and tantalum).
decompose to about 11.1% when stored for 20 days at 70°F.
The same concentration of diluted HyPure® Bleach will only Solution pH also can affect sodium hypochlorite stability. For most sites
decompose to about 11.9% in the same conditions. receiving inbound sodium hypochlorite, pH is not a significant stability
• A 15.5 wt% NaOCl solution of sodium hypochlorite will degrade factor as the importance of alkalinity (the ultimate source of pH) is well-
to approximately 12.5 wt% NaOCl over 20 days at 70°F. The same understood by most commercial producers. Because of this, adequate
concentration of diluted HyPure® Bleach will be at approximately alkalinity (and the resulting pH level) is added at the point of manufacture.
14.0 wt% NaOCl after 20 days at 70°F. However, alkalinity levels can become an important consideration for
customers who significantly change the solution composition, such as
Equation 6: in major product dilution, formulation, or during spill neutralization
activities. Stability can be adversely affected by either too little or too
2 NaOCl + Metals →2 NaCl+O2 much alkalinity. An alkalinity level of at least 0.1 weight % as NaOH is the
typical minimum alkalinity needed for stability. Your process may dictate
Metals Impact on Stability the need for a higher alkalinity.
Exposure to certain metals can also affect stability of both sodium
hypochlorite and HyPure® Bleach. Nickel, cobalt, copper, and iron have Dilution
the greatest impact, respectively.
Dilution of sodium hypochlorite is often chosen by customers to slow the
Graph 5: Metal-Induced Assay Loss (g/L) vs. Time (Hours) rate of product decomposition while in storage or to meet assay-specific
applications. Although many sources of water can be used for sodium
hypochlorite dilution, the most important aspects to consider when choosing
a dilution water source are generally hardness and metals content. Hard
water (high calcium and magnesium content) can cause precipitates and
scaling to occur in sodium hypochlorite solutions. Exposure of sodium
hypochlorite to dissolved metals in dilution water can accelerate product
decomposition similar to physical contact with metallic components and /or
may alter the color of the hypochlorite solution. In general, as water quality
improves, product scaling and precipitation are reduced and decomposition
rates decrease.
The dilution water should be analyzed to develop an impurity profile.

Note: See Appendix for larger graphs
Depending upon impurities, a treatment system may be required to upgrade
water quality to help minimize quality problems with the diluted product. A
reputable water treatment specialist can determine the best treatment method
The Metal-Induced Assay Loss graph depicts the significance of trace
and capacity to generate purified water for your particular application.
metallic exposure to hypochlorite stability. While cobalt is particularly
Table 1 summarizes typical water impurities of concern when diluting
reactive with sodium hypochlorite solutions, it is rarely found in day-to-
hypochlorite solutions. For bottling operations, additional water treatment
day operations and shipments, and therefore is typically not a significant
and product filtration may be required. Consult your Olin Technical
contributor in most applications. On the other hand, nickel is often encountered
Representative if additional information is needed.
since stainless metals are used in many chemical handling applications.
Simply transferring sodium hypochlorite through an unlined stainless steel
hose connector can initiate the decomposition reaction because of the presence
of the nickel component in stainless steel.
The major sources of metallic contamination are the quality of caustic

soda and dilution water used in the manufacturing process, and the
exposure to metals during delivery and handling. Many manufacturing
processes incorporate various types of filtration to control and/or remove
metallic contamination. However, for certain applications such as product
bottling, additional filtration steps may be required to further reduce

Properties
Table 1: Typical Dilution Water Impurities Frozen hypochlorite solutions can be thawed and used; however, care
Nickel must be exercised to avoid excessive heat application that will initiate
temperature decomposition of the solution. In some instances, the
Copper
crystallization process may result in precipitation of suspended materials
Cobalt
that will not easily dissolve upon thawing. Crystallization effects typically
Iron first appear on the solution surface or in small diameter piping/tubing
Component
Silica subjected to no or low-flow conditions.
Conductivity
Total Dissolved Solids Table 2: Crystallization Points (Chlorine Institute Data)
Total Hardness Weight % NaOCl Crystallization Point Crystallization Point
(ºF) (ºC)
20.0 28 -2.2
Dilution and Excess Residual Alkalinity 15.5 -21.5 -29.6

12 -3 -19.4
Another consideration for significant strength dilutions is the excess
6 18.5 -7.5
alkalinity in the diluted product. For minor dilutions, the excess actual
sodium hydroxide content in the product should be sufficient to maintain
the minimum level of about 0.1 wt% to ensure product stability. With more
significant dilutions, a small addition of caustic soda (sodium hydroxide) Care should be taken to prevent any bleach solution from freezing.
may be required to achieve the minimum level necessary for a stable At higher hypochlorite concentrations, the crystals that form when the
product. The quality of the caustic soda added can also negatively impact solution freezes are very corrosive to skin and eyes and should not be
sodium hypochlorite quality, especially in the areas of trace metals and salts. handled. These crystals can also cause plugging in piping and equipment.
To prevent the material from freezing, tank cars, tank trucks and piping
Unlike dilution of hypochlorite with water which is non-exothermic,
should be unloaded/drained promptly in cold weather. In extremely cold
addition of significant quantities of caustic soda will result in a temperature
climates, strong bleach solutions could be diluted to lower the freezing
gain of the solution. Solution cooling capabilities may be required for
point, which will also increase the stability of the material.
large volume alkali additions to minimize temperature-induced product
decomposition.
All sodium hypochlorite solutions require residual alkalinity, particularly

sodium hydroxide, to ensure product stability and to avoid generation
of chlorine gas. Sodium hydroxide and sodium carbonate are the typical
alkalinity sources. Sodium carbonate is not as effective in stabilizing
hypochlorite solutions, and is typically not intentionally added to achieve
higher alkalinity contents. Alkalinity determination becomes particularly
important in dilution activities or in chlorine-scrubbing applications
where dilute sodium hypochlorite is being produced. Review the Residual
Alkalinity Analytical Testing section for more information.
Crystallization Points
The freezing or crystallization temperature for bleach solutions is generally
a function of the hypochlorite concentration. Since sodium hypochlorite
solutions can contain varying amounts of several dissolved salts, the
ability to accurately predict the crystallization point of the solution can be
difficult. The amount of crystallization and the exact temperature at which
these attributes begin to appear are composition-specific and may vary
noticeably. For example, identical solution ”grades” of product supplied
from different manufacturers or production facilities will probably exhibit
differing crystallization properties when subjected to the same temperature
conditions. Solutions with higher concentrations of hypochlorite and/
or the other dissolved salts will generally begin to crystallize at higher
ambient temperatures than solutions containing lower concentrations of
hypochlorite and/or the other salts.

Manufacturing Processes
Processes
Chart 1: Sodium Hypochlorite Process Chart 2: HyPure® Bleach Process
Caustic Soda Chlorine Water

Chlorine (CI2)
Gas or Liquid
Chlorination Dilution
Diluted Sodium
Hydroxide (NaOH) Chlorinator Sodium Hypochlorite
Solution (NaOCI) Solution
HyPure® Sodium
Salt Separation Filtration Hypochlorite
Salt Trace Metals
Several of Olin’s manufacturing sites produce chlorine and sodium hydroxide Olin’s HyPure Bleach is manufactured using proprietary technology,
®
solutions that provide the raw materials for sodium hypochlorite production which produces a super concentrated, low-salt hypochlorite product. As
at all manufacturing sites. Sodium hypochlorite is easily produced in batch the name implies, HyPure® Sodium Hypochlorite is higher in purity due
and continuous processes by the introduction of chlorine into a diluted to the lower sodium chloride content. As a result, once it is diluted to a
sodium hydroxide solution. The ratio of chlorine addition to the amount of solution strength comparable to standard sodium hypochlorite, it is more
sodium hydroxide is controlled to allow for the excess caustic necessary stable. HyPure® Bleach is manufactured at concentrations up to 23 wt%
to stabilize the final product. Automated blending equipment allows for NaOCl and then undergoes further processing to remove additional trace
meeting various customer quality and strength requirements depending on metals and salt (NaCl). This increased purity means a slight difference
the final application. Once chlorination is completed, product is filtered to in the physical and chemical properties of the product when comparing
remove suspended impurities and then chilled before being sent to storage HyPure® Bleach to standard sodium hypochlorite.
or shipping container loading. By incorporating filtration and cooling
steps as integral components at our continuous manufacturing process, This special product has limited availability in North America. Contact
customers receiving Olin-produced sodium hypochlorite are provided your Olin Sales representative for details.
an inherent advantage, as these two practices play important roles in
minimizing product decomposition.

Concentration Units
Concentration
Strength or concentration of sodium hypochlorite may be expressed in a number of different ways in supplier certificates of quality, invoices, product
labels, dosage rates, or bid requirements. As a result, it is always critical to specify the units of concentration when referencing product strength.
The table below illustrates the importance of specifying assay units. A 12.5 weight percent NaOCl solution (a common industry strength standard) is
considerably different from a 12.5 trade percent solution. Additionally, a 12.5 weight percent solution is not the same as a 12.5 solution having units of
volume percent. ALWAYS specify units of concentration!
Table 3: Concentration of Sodium Hypochlorite
wt% NaOCl Wt% AvCl2 g/L AvCl2 Trade % Equivalent Cl2 Density (Theoretical)
(g NaOCl/100 g soln) (g AvCl2/100 g soln) (g/L soln) (g AvCl2/100 mL soln) (lb Cl2/ gal soln) g/ml lb/gal
Note 1 Note 1 Note 1

5.25 5.0 54 5.4 0.45 1.0793 8.99
6 5.7 62 6.2 0.52 1.0904 9.09
7 6.7 74 7.4 0.62 1.1053 9.21
8 7.6 85 8.5 0.71 1.1204 9.34
9 8.6 97 9.7 0.81 1.1356 9.46
10 9.5 110 11.0 0.92 1.1511 9.59
11 10.5 122 12.2 1.02 1.1667 9.72
12 11.4 135 13.5 1.13 1.1826 9.86
12.5 11.9 142 14.2 1.18 1.1906 9.92
13 12.4 148 14.8 1.24 1.1986 9.99
13.5 12.9 155 15.5 1.30 1.2067 10.06
14 13.3 162 16.2 1.35 1.2148 10.12
14.5 13.8 169 16.9 1.41 1.2230 10.19
15 14.3 176 17.6 1.47 1.2312 10.26
15.5 14.8 183 18.3 1.53 1.2394 10.33
16 15.2 190 19.0 1.59 1.2477 10.40
16.5 15.7 197 19.7 1.65 1.2561 10.47
Low Salt 17.5 16.7 200 20.0 1.67 1.2009 10.01
18 17.1 207 20.7 1.73 1.2072 10.06
18.5 17.6 214 21.4 1.78 1.2135 10.11
19 18.1 221 22.1 1.84 1.2199 10.17
19.5 18.6 228 22.8 1.90 1.2262 10.22
20 19.1 235 23.5 1.96 1.2326 10.27
20.5 19.5 242 24.2 2.02 1.2391 10.33
21 20.0 249 24.9 2.08 1.2455 10.38
21.5 20.5 256 25.6 2.14 1.2520 10.43
22 21.0 264 26.4 2.20 1.2585 10.49
22.5 21.4 271 27.1 2.26 1.2650 10.54
23 21.9 279 27.9 2.33 1.2716 10.60
Note 1: the conversion between wt% NaOCl, g/L AvCl2 and Trade % will change depending on the density used in the calculation.
AvCl2 = Available Chlorine Soln. = Solution g/L = gram per liter or gpl
One of the complicating factors in converting units involves the role of conversion between weight % and trade % can never be precise unless
the density in the calculation. Some units of measure, such as weight density of the particular solution in question is measured.
percent (wt%), compare the weight of NaOCl (gram) to the solution
weight (100 grams) while other units, such as grams per liter (g/L), Within a given context, such as a company department, a manufacturer’s
compare the weight of the NaOCl (grams) to the solution volume (liter). production and customer service group, or the order between a customer
and a specific supplier, the communication of concentration may be well
When converting between these units, the density of the solution must be understood. For clarity when dealing with others outside that context, units
used in the calculation. Because there is no direct relationship between should always be clearly defined and mentioned in the communication.
density and concentration for sodium hypochlorite solutions, the

Shipping
Hazardous Materials Transportation System The regulatory agencies are the governing bodies in the transportation arena
that oversee the safe movement of all hazardous materials whether by land,
The safe transport of hazardous materials such as sodium hypochlorite air, or water. They define and enforce the rules for the safe handling and
involves different organizations: transport of hazardous materials. Each regulatory agency has an enforcement
• Regulatory Agencies (Department of Transportation, Transport arm to assure compliance with record-keeping and equipment regulations.
Canada, Federal Railroad Administration, etc.) Penalties including fines and imprisonment can be imposed for
• Manufacturer (Olin) violations applicable of regulatory requirements.
• Carriers (Railroads &Trucking Companies) While the U.S. Department of Transportation (and Transport Canada for
• Receiving Customer Canadian shipments) regulates the movement of hazardous materials by
rail, road, and pipeline, enforcement of these regulations is carried out by
Each of the organizations plays an important role in the safe shipment of different agencies depending on the mode of shipment.
hazardous materials.
Olin’s responsibility in the hazardous materials transportation system
includes the safe operation of its loading facilities as well as maintaining
Table 4: Shipping Organizations
transportation equipment in good working order for shipment whether
Shipping Mode Enforcement Agency
owned, leased, or contracted by Olin. A number of inspection and
Federal Railroad Administration (FRA); maintenance activities are performed during the loading process to
Rail
Transport Canada
ensure safe and defect-free shipping containers. Olin’s goal is to ensure
Department of Transportation (DOT); the safety of our personnel and, to the extent possible, all those who
Roadway
Transport Canada
come in contact with a shipment of sodium hypochlorite, while effectively
Department of Transportation (DOT); State using our fleet and complying with all applicable laws.
Pipeline Regulatory Commission;
Transport Canada

Shipping
The carriers’ (rail and trucking companies) responsibility in the hazardous road weight limitations. The two major trailer constructions are rubber-
transportation system is to safely move the sodium hypochlorite shipping lined steel and fiberglass reinforced plastic (FRP) tanks with a compatible
containers from Olin to the customer. The carriers must comply with a resin corrosion barrier. Product unloading configurations include bottom
variety of regulations governing the movement of hazardous materials from discharge or a top-unloaded dip-leg arrangement.
agencies including the Department of Transportation, Transport Canada,
the Association of American Railroads, and individual state governmental Olin sodium hypochlorite trailers typically have a double-valve arrangement
agencies. Carriers (rail and truck) rely on the shipper (Olin and/or the on the outlet port. The internal valve is pneumatically or hydraulically
customer) to provide them with clean, safe, and secure sodium hypochlorite operated and can be closed remotely in case of an emergency. The
shipping equipment. unloading connections on each tank trailer are typically located at the
rear. A specification plate specifying tank fabrication, inspection, and
The customer’s responsibilities in the hazardous materials shipping process other regulatory information is typically located on the driver’s side of
are similar to Olin’s. Customers must follow the appropriate regulations the trailer frame near the front. Transport regulations require these trailers
in the handling and unloading of sodium hypochlorite containers, and in to be inspected on a scheduled frequency, including internal and external
the case of tank cars, prepare them for shipment back to Olin. A customer’s visual inspections as well as leak, thickness, and pressure testing. These
goal is to safely handle and unload sodium hypochlorite containers, comply inspection dates are stenciled on the front head or on the front driver side of
with all regulatory requirements, and where applicable, prepare the container the trailer. Tank trailers can be unloaded by the driver or by properly trained
for safe shipment back to Olin. It is important to note that in the case of tank employees (DOT/Transport Canada function-specific) at the customer’s
cars, the customers or end-users become the shipper of record when they or end user’s facility. Delivery tractors are equipped with an air compressor
offer the sodium hypochlorite container for shipment back to Olin. for pneumatic product transfer. Pumps are not provided with delivery
equipment for unloading.
Tank Cars
In 2007, Olin added tank cars (railcars) to its modes of shipment. This
proprietary fleet of specially lined and designed tank cars maintains
sodium hypochlorite quality throughout the shipment cycle. The tank cars
in Olin service for sodium hypochlorite meet DOT Spec 111A100W5.
This Olin innovation, along with process capabilities, has allowed the
creation of a bulk distribution paradigm to reach distant marketplaces
effectively. The typical shipping volume by tank car is approximately
17,500 gallons.
Numerous important regulatory, environmental, safety, and health

informational items are available on each tank car. Tags and stenciling
display required regulatory, car maintenance, and operating information
as well as safety, spill mitigation, and first-aid information along with
emergency response contacts.
Sodium Hypochlorite Shipping Containers Olin’s entire rail fleet is designed for top unloading only. The specific
unloading method and additional requirements are described in separate
Sodium hypochlorite solutions are shipped in a wide variety of container Technical Bulletins available for reference and future discussions.
sizes, bulk and non-bulk, to meet customers’ needs. Olin ships product
only in tank trailers and tank cars.
Tank Trailers
Olin contracts with trucking companies to deliver sodium hypochlorite
solutions by tank trailer, also known as cargo tanks. In some areas
of the United States, Olin operates its own trucking fleet for delivery
of the product. Tank trailers used in sodium hypochlorite service must
meet standards issued by the regulatory agencies (U.S. DOT, Transport
Canada) and include equipment that conforms to the Department of
Transportation (DOT) or Motor Carriers (MC) designations, which
as of the year 2017 were MC-307, DOT-407, MC-312, and DOT-412
designations. While tank trailer capacities can vary significantly, they
usually contain about 5,000 gallons of product based on over-the-

HAZMAT Training & Unloading Requirements
Written Procedures • Adequate tank inventory exists to safely receive the entire
shipping container contents
Establishment of robust unloading procedures should occur before product • Eyewash and safety shower units have been identified in the area
is received and then be reviewed on a periodic basis or revised when and verified that they are operational
operational practices dictate. Unloading procedures will be unique to • PPE has been inspected and put on prior to any connection activities
each facility, receiving area, and delivery mode. However, well-written
• Visual and mechanical inspections of the shipping container and
unloading procedures include a number of common attributes and
transfer hose(s) have been completed
components. Although the primary focus of the unloading procedure is to
ensure the correct product is safely delivered into the storage facility, it
also should be written to address personnel safety, unexpected events such Training
as spills, or other potential incidents. All procedures should be documented
with periodic training provided to ensure personnel understand the Since sodium hypochlorite is a hazardous material, all U.S. personnel,
procedure requirements. Verbal procedures for unloading should be who, in the course of their employment directly affect hazardous materials
avoided as they can foster inconsistency between staff members. transportation safety, must be properly trained or “qualified” in accordance
with 49 CFR 171-180 US DOT). An employee, whether full time, part
time, or temporary, who performs any portion of the hazardous materials
Checklists transportation, (loading or unloading of the hazardous material, providing
directives or guidance regarding the loading or unloading process), must
Use of pre- and post-unloading checklists offers the advantage of physically
comply with the Hazardous Materials Regulations. For Canada, this
carrying the key elements of the unloading procedure to the work area
would be classified under the Security and Transport Canada Transport
for review/completion. Checklists help ensure all key unloading items
of Dangerous Goods Act S.C 1992, c. 34 (Canada). 29 CFR 1910.120
are reviewed and inspected, fostering consistency between different staff
provides guidance for training of employees who are expected to handle
members. Typical components include:
hazardous material spills. Additionally, federal regulation (DOT-
• A review of paperwork (bill-of-lading and certificate of quality) 49CFR 177.834 (i) and Transport Canada (CSA B622) require shipping
to verify they match the shipping container placard, seal numbers, containers to be continuously monitored during the entire unloading
and receiving pipeline label
process by a qualified person located within 25 feet of the transfer.
• Delivery address and purchase order numbers are verified

General Unloading System Requirements
General Unloading System Requirements a block valve to prevent possible chemical drain-back when the
delivery hose is disconnected. Placement of a drain valve in the receiving
Unloading stations for receipt of tank trailer and tank car shipments pipeline can facilitate safe sample collection during the unloading process.
should be designed with safety and operational efficiency in mind. In Quick-connect fittings should be made of fluoropolymer-lined stainless
general terms, either delivery mode requires appropriately located safety steel or a compatible plastic such as PVC, high-density polyethylene, or
shower and eyewash stations, adequate lighting for possible night- glass-filled polypropylene. Installation of the receiving connector at a
time work, filtered pad gas, adequate secondary containment, chemically 45-degree downward angle is a preferred installation technique to reduce
compatible transfer hoses and connectors, and a source of rinse water to torque stresses induced during unloading. Angled receiving connectors
facilitate product residue removal. The ideal site design will minimize the are especially beneficial when plastic components are used. Since plastic
length of hose required for shipping container unloading as well as the pipe fittings lack the mechanical integrity of lined steel fittings and can easily
run for delivery of product to the storage tank. become worn or damaged, they should be inspected frequently and placed
on a replacement cycle that will prevent failure.
Connection points should be clearly identified to eliminate the possibility
of connecting the transfer hoses to the wrong unloading line or system. Tank Cars
For maximum effect, receiving pipelines should be clearly identified
near the delivery hose attachment point and include the words, “Sodium Tank car unloading stations
Hypochlorite” and “UN 1791.” This label terminology incorporates the should incorporate level track to
information found in bills-of-lading and other delivery paperwork, and maximize product transfers. An
therefore allows the delivery driver and site unloading staff to compare elevated platform and gangway
delivery documents against the receiving pipeline label and shipping system should be provided for
container placard. Consult The Chlorine Institute’s bulletin, “Avoiding safe egress and access from the
Accidental Mixing of Sodium Hypochlorite,” at www.chlorineinstitute.org top of the tank car. The platform
for additional details. should incorporate fall protection
devices such as protective cages,
Tank Trailers or equivalent fall arrest systems.
The pad gas filtration device and
Tank trailer unloading stations should be laid out to provide easy access to
hose connection, as well as the
the receiving pipeline connection. Where possible, drive-through unloading
receiving pipeline are typically
stations are preferred over backing of the trailer into the unloading station.
located within arm’s reach of the
In-plant street access should be designed to accommodate tractor-trailer
unloading platform, which limits
combinations and incorporate wide intersections. Reinforced concrete
hose length and associated clutter,
unloading pads sloped to a containment device such as a dedicated sump or Receiving Connections Example
while maximizing convenience for
French drain can provide a hard surface for trailer parking and an effective
component access.
means to collect and contain product drippings that might occur during the
unloading process. Where multiple chemicals are received in the same area Tank cars require a three-inch, four-bolt flanged connector to attach
as sodium hypochlorite, engineering and/or procedural provisions should be to the product outlet valve. Because of the elevated potential for
incorporated to avoid mixing of incompatibles. ”mechanical hammer” and other unloading stresses, the transfer hose
should have a robust support system in place to limit stresses on the tank
Receiving pipelines for tank trailers are typically installed at hip level
car connection. Because of these unloading stresses, a fluoropolymer-
(approximately 3 feet above grade). A two-inch male, quick-connect
lined, flanged metal connector is preferred for tank car unloading.
fitting is standard for customer receiving locations and should include

Pad Gas System
Pad Gas System • Piping made of compatible material of construction downstream of the
point-of-use filter (point in which chemical vapors may be present)
Experience has demonstrated that the gas padding systems can be a significant
• Pad gas connector hose made of product compatible material of
source of product contamination in the delivery container and that even a
construction
good system can fail. For this reason, an additional engineering control should
be installed at the end of the fixed pad gas piping (hose connection point) to • Effective pad gas system maintenance program
avoid introduction of rust and particulates into the shipping container. This
Because of the sensitivity of sodium hypochlorite to pad air contaminants,
engineering control requires the following components to be appropriately
all system components including the air compressor, air cooling and
designed and installed and that good operating practices be in place:
water drainers, pre- and after-filters, air drying and point-of-use filters/
• Point-of-use filter designed to remove moisture, particulates, and condensate drainers should be evaluated to determine appropriate
oil delivering pad gas quality meeting ISO Class 1 of the ISO equipment upgrades. System operation also should be evaluated because
STANDARD 8573 – 1 oil/water/particulate loading can vary under start/stop conditions. The
• Safety Features: Pressure regulator, pressure gauge, pressure relief minimum requirement for sodium hypochlorite shipping container pad air
valve, check valve, and purge/vent valve for safe line evacuation is ISO STANDARD 8573 – 1 (ISO Class 1) noted in the ‘International ISO
prior to disconnection Standards ISO 8573-1’ document. Note that the air does not have to be “dry”
• Dual isolation valves to a specific dew point, only “water droplet free.”
Corrosive Liquids Pad Gas Quality at Point of Use
NOTE: The diagram above represents components within a properly designed pad air system. Although those listed appear to be at the point of use, we
understand portions may be at the compressor, and others near point of use. It should be known that the objective of this diagram and information within is
intended to minimize any and all contaminates from entering the car during use. Therefore, any piping exposed to the vapors of solutions being offloaded
should be of chemical compatible materials of construction and a filter as close to the container shall be installed as a last means to prevent particles from
entering the shipping vessel.

Pad Gas System
Table 5: International ISO Standards ISO 8573-1International ISO Inspection
Standards ISO 8573-1
A timely and effective preventive maintenance program (see Inspection
Particulate Water Oil
Guidelines below) is critical for ensuring delivery of clean, water-droplet-
Max. Press. free and oil-free pad air to the shipping container over the long term.
Class Max. Size Max. Conc. Max. Conc.
Dew Point
Several general guidelines are applicable regardless of equipment or
µm ppm/mg/m3 °F/°C ppm/mg/m3
operating conditions. Maintenance guidelines issued from the compressor
1 0.1 0.08/0.1 -94/-70 0.008/0.01 manufacturer should be consulted and typically represent the minimum
2 1 0.80/1 -40/-40 0.08/0.1 frequency at which maintenance should be performed. In addition to
3 5 4.20/5 - 4/-20 0.83/1 performing scheduled component maintenance, a white-rag test should
4 15 6.70/8 37/+3 4.2/5 be performed at least once monthly to provide redundant verification of
proper system operation. When performed correctly, a clean white rag
5 40 8.30/10 45/+7 21/25
should be used to collect the compressed gas stream at regular, full-flow
6 - -/- 50/+10 -/-
rates for a duration of one to two minutes. Any discoloration will provide
indications of a malfunctioning filtration system.
High-pressure pad air can over-pressure the shipping container, resulting
in activation of the container’s safety relief device and chemical leakage. Table 6: Inspection Guidelines
The pad air should be regulated to a maximum of 25 psig for both tank car
and tank trailer unloading activities and be protected with a pressure relief
White rag test at point
device downstream of the regulator. The pressure relief device provides At least monthly
of use
important over-pressurization protection to the shipping container should
Trap and filter inspection/
the regulator fail. At least monthly
service
The primary isolation valve (see ‘Corrosive Liquids Pad Gas Quality at Inspection at each use
Pressure drop indicators
Service per manufacturer guidelines
Point of Use’ diagram above) marks the piping specification breakpoint
Filter replacement Daily inspection during use
between components designed for standard pad air service and components
designed for sodium hypochlorite vapor, and should be constructed of lined Per manufacturer guidelines, white-rag test
Hose and connector
or pressure drop
steel as discussed below. All components downstream of this valve must be
designed to accommodate possible exposure to sodium hypochlorite vapors. Daily visual inspection for evidence of
Regulator or check valves
fatigue
Downstream of the point-of-use filter, lined metallic piping or titanium Pressure relief device Annual preventive maintenance
must be used. Iron, galvanized steel, copper or other common pad air
piping materials will corrode and re-introduce contaminants downstream
of the filter. These materials should be avoided in their unlined versions
downstream of the point-of-use filter location. For a lined piping system, the
liner offers the chemical resistance needed while the metallic piping provides
the structural strength. Liners such as polyethylene, Teflon® polymer (PFA,
FEP, PTFE), PVDF (fluorinated polyvinylidene or Kynar® polymer) and
PVC/CPVC (polyvinylchloride/chlorinated polyvinylchloride), etc., are
compatible with sodium hypochlorite. A careful evaluation of material of
construction compatibility with sodium hypochlorite should be completed
during the liner selection process because product vapors can potentially
back feed into the pad air piping system under certain conditions.
Tank cars are equipped with a four-bolt flanged ‘air’ valve for
pressure padding and venting of the tank car. A two-inch flanged
connection rated for pressures of 150 psig should be permanently
affixed to the pad gas supply hose. A flanged adapter equipped with a
quick-connect fitting for attachment to the pad air hose is a variation
that may be a desired alternative. Fluoropolymer-lined stainless steel
fittings are preferred as they offer enhanced mechanical strength, are
chemically compatible, and can safely manage stored energy and stresses.
Tank trailers are typically connected to the pad air supply hose via a one-
inch “crow’s foot” connector (or Chicago coupling) appropriately pinned
to ensure a secure connection.

Transfer System
Lined Steel
Connector
for Strength
and Product
Quality
Transfer Hoses sodium hypochlorite and likely temperature ranges to be experienced

throughout a calendar year. The potential for external surface abrasion can
Bulk shipments of sodium hypochlorite will require a flexible hose to also influence the type of protective sheath, if any, chosen for the hose.
connect the shipping container to the storage tank’s receiving pipeline.
Although most tank trailer serviced customers rely on the carrier to As with all expendable components, hoses and hose connectors should
provide the transfer hose, use of customer-provided hoses remains an undergo a visual inspection prior to each use to identify and prevent potential
option. Tank car deliveries require customers to supply the transfer hose. failures. Use of an inspection checklist by a knowledgeable inspector
trained in defect identification helps maximize inspection effectiveness.
Hoses should be constructed of sodium hypochlorite-compatible materials The Association for Rubber Products Manufacturers’ bulletin, IP-11-7,
and be rated to withstand the working pressures expected during the transfer (www.arpminc.com) can provide added details regarding maintenance,
process. Hose construction must avoid any wetted metallic surfaces, such testing, and inspection of chemical hoses.
as pipe nipples or quick-connect fittings, because of the corrosive nature
of sodium hypochlorite and the sensitivity of this product to experience Pumps
metallic-induced decomposition. From a mechanical integrity standpoint,
metallic connector components that have a fluoropolymer or HDPE lining Pumps are typically selected based on service. Centrifugal, diaphragm,
on the wetted surface are the preferred construction. Polyethylene, including canned, and magnetically driven pumps are more common for high-
the Ultra-High Molecular Weight Polyethylene (UHMWPE or UHMW) volume transfers or for recirculation-type activities. Regardless of
subset and polypropylene are common lining materials of construction. The application, all internally wetted components must be constructed of
choice of material should be discussed with your hose vendor regarding sodium hypochlorite compatible materials, and the use of all metals except
expected service conditions including, but not limited to, strength of titanium must be avoided. Non-metallic materials such as Teflon®, Tefzel®,

Transfer System
Halar®, or Kynar® polymers, and polyvinylchloride are common internal and the mechanical capabilities of the organization’s maintenance
components for pumps. personnel should be evaluated before choosing pipeline materials.
Exposures to direct sunlight and wide temperature extremes, to identify
Design features are influenced by the type of pump selected. Positive just two common examples, are external stresses that can weaken non-
displacement pumps should incorporate a pressure relief device to protect metallic piping and lead to premature component failure. Threaded pipe
against ‘dead-heading’ situations whereas mechanically sealed centrifugal should be avoided as the pipe wall section containing the threads is
pumps should employ a seal-shaft shroud to help prevent potential seal thinner and more prone to failure or leakage. For flanged pipe installations
leakage from being slung onto nearby personnel or equipment. A low-amp in close proximity to personnel or equipment, installation of flange
cut-off switch should be considered for magnetically driven pumps to guarding should be considered. All piping systems should undergo
protect against “burn-out” resulting from operating under damaging low or scheduled integrity inspection, regardless of material of construction
no-flow conditions. utilized. Non-metallic piping typically requires even more frequent
inspection and replacement cycles.
Although piston, gear, and peristaltic positive displacement pumps are
most frequently used in metering situations, all pump styles have been Piping Materials of Construction
used successfully in these situations. The overriding factor in determining
There are a number of acceptable materials of construction for sodium
which type of pump to use may lie in past plant experience. The pump
hypochlorite piping systems. Each material of construction presents unique
type most familiar to maintenance personnel and for which spare parts
attributes, and in some instances requires special care in installation and
are readily available may be the best choice. A centrifugal pump coupled
inspection to help ensure successful long-term use. Structural strength,
with a measuring device (rotameter, mag meter, or mass flow meter, etc.)
chemical resistance, and operational conditions are important factors to
may prove easier to calibrate and more compatible with automated control
consider when selecting piping materials of construction.
systems than metering pumps. Without an independent flow-measurement
device, metering pumps require routine calibration to ensure accurate output. Because of their superior structural strength, metals are widely used in piping
service for many alkali chemicals. However, unlike many alkalis, sodium
“Vapor lock” caused by entrained gas can be a problem with centrifugal,
hypochlorite is highly reactive with most metals and metal alloys and is
diaphragm, and peristaltic pumps, especially in low-flow metering
compatible only with titanium or tantalum metal. Lined-steel piping using
applications. Typically, entrained gas is a result of trace-metal induced
thermoplastics such as polypropylene, polyvinylidene fluoride (PVDF or
product decomposition (oxygen gas formation), so efforts to eliminate the
Kynar® polymer) or polytetrafluoroethylene (PTFE or Teflon® polymer) as the
source of such contamination would be the preferred solution. However, this
problem can be minimized by sloping pump intake piping so that entrained liner is often used as an alternative pipe material for portions of the systems
gas bubbles move away from the pump suction or by employing other where mechanical stresses or impacts are expected. Lined metal is often
means of separating entrained gases before liquid reaches pump suction. chosen for the initial portion of the receiving pipeline, especially near the
hose connector where external stresses are expected to be more significant.
Valves PVC and CPVC are chemically compatible, non-metallic materials often
used in lower mechanical stress applications. Certain specialty grades of
Valve type selection will depend on the intended application. Materials
polyethylene also have been successfully used in sodium hypochlorite
of construction range from fluoropolymer-lined steel valves to plastic.
service. Pipe specifications should be at least schedule 80 or higher for most
Where cavity valves, such as ball or plug designs are used, a vented valve
applications. Mechanical impact from hazards such as liquid/gas mechanical
design should be used to prevent pressure buildup and potential valve or
hammer, temperature expansion/contraction cycles, pressure surges from
piping damage resulting from metallic-induced decomposition of sodium
pump start-up and operation, sunlight/ultraviolet light degradation, and
hypochlorite and associated buildup of decomposition gases. Vented valve
potential foot or vehicular contact should be carefully considered when
body designs will also be critical in pipe runs wherein sodium hypochlorite
selecting PVC/CPVC for sodium hypochlorite service. PVC/CPVC materials
liquid or residues may remain trapped between closed valves. Storage
are sensitive to these types of external stresses and if not properly installed,
tank outlets should be equipped with positive shut-off capability and avoid
supported, and inspected, can often fail unexpectedly during use.
the use of “butterfly” designs. Flanged or glued valves are preferred over
threaded valves as they eliminate the threaded connection, which is a For end-use applications such as dosing meters, small diameter PVC/
potential leakage point. CPVC piping is often used. As with larger diameter piping, proper support
is required. A protective enclosure such as a conduit or equivalent device
Piping should be used where foot or vehicular traffic is likely.
When making initial decisions about piping, it is critical to select the Most polyvinyl chloride monomers have recommended temperature
appropriate material of construction because sodium hypochlorite is ranges that should not be exceeded. In many instances, ambient conditions
incompatible with all metals except titanium and tantalum. Use of non- exceed these recommendations and elevate the risk of fracture. A related
metallic materials throughout is often embraced when only economic and factor is ultraviolet damage as a result of long-term sunlight exposure.
compatibility perspectives are considered. However, the role of external Repeated sunlight exposure will weaken monomer bonds, making the pipe
stresses in pipe life, effective means to mitigate their detrimental effects, more prone to fracture. Consult with your pipe vendor for added guidance.

Transfer System and Storage Equipment
Fiberglass reinforced plastic (FRP) has been used successfully in important because it can provide an additional layer of protection
hypochlorite service, but it requires extreme diligence in carefully managing against accidental delivery of the wrong chemical by providing a visual
all aspects of fabrication and installation. Successful service is typically reference of intended contents for delivery and unloading personnel.
dependent upon fabricator experience (those specializing in manufacturing The ASME/ ANSI A13.1 standard for pipe marking, requires an employer
pipe expressly intended for sodium hypochlorite), selecting the correct resin to use labels that state what a pipe
composition and the curing process (avoiding cobalt napthenate chemical contains and what possible hazards
cures), and using certified installers that employ stringent quality assurance are related to that substance. Always
methods, to name several critical aspects. review all federal, state, county, city/
municipality labeling requirements.
Piping Installation
Inspection and Replacement
Where possible, pipe runs should be installed to eliminate the presence
of low points because product left standing in pipelines can experience Pipe systems should undergo
decomposition (oxygen generation and chlorate formation) when not in use. scheduled inspections on a regular
Where low points cannot be avoided, installation of drain valves discharging basis. Although the entire pipeline
to a suitable containment system should be considered. Piping feeding system should be inspected, special
metering pumps creates a special situation wherein oxygen gas formation focus should be given to joints, sags,
can result in pump vapor lock. Installation of suction piping sloped up support systems, and connectors.
away from the pump can minimize gas collection and associated cavitation Pipe joints and flanges should be
concerns. For underground pipe installations, pipe should be placed in an inspected for evidence of product
impermeable trench with removable inspection covers. drippage indicating a softening of the
joint glue. Evidence of pipe sags, which can develop over time if inadequate
Piping Support support system spacing was chosen, should be reviewed. Pipe supports,
Adequate pipeline support is important regardless of material of hangers, and clamps should be closely inspected for loose pipe (pipe
construction. However, support becomes increasingly critical for non- movement) or evidence of wear at the contact point. The connecting
metallic systems as they generally have lower structural strength and surfaces of plastic, quick-connect hose fittings are prone to wear or cracking
require additional support consideration. Proper spacing of the support and should also be an inspection component. Inclusion of detailed training for
system (e.g., hangers, trays, or clamps) will be influenced by the pipe size, your inspector will be critical to maximizing inspection results.
operating temperature range, and the weight load of the filled pipe. Special
“Invisible” stresses inherent to the pipe system such as temperature extremes,
care is required with hangers, support devices, and clamps to ensure a
embrittlement, or external torque applications are not detected by typical visual
smooth contact surface, free of rough edges. They should not compress
inspection practices. By assigning a scheduled replacement cycle before
or distort the pipe but should allow axial movement resulting from changes
failure occurs, system reliability can be maximized.
in thermal expansion and contraction. Because of these factors, use of a
continuous support system should be strongly considered for non-metallic
pipe runs. If non-continuous support systems are chosen, consult your pipe Storage Tanks
vendor for recommended support spacing.
The tank selection process has a number of important components to
Pipe Glues consider. While many are obvious, others are not intuitive because of
the unique attributes of sodium hypochlorite. Tanks should be located to
Sodium hypochlorite will attack the fumed silica additive used as a minimize piping runs, accommodate shipping container movement for
thickening agent in some glues or cements intended to join PVC/CPVC inbound deliveries, and be installed in secure areas to avoid tampering/
(polyvinyl chloride and chlorinated polyvinyl chloride) components. vandalism concerns. Local, state, province, and federal environmental
Because of the likelihood of joint separation or leakage, only glues/cements regulations should be reviewed before tank installation. Local building codes
that are fumed silica-free should be used. Containers for these glues typically and fire regulations also may influence tank farm construction and location.
indicate their compatibility with oxidizers and alkalis. Proper preparation
of the surface and application techniques for the primer and cement are A part of the process of the purchase and installation of a new storage
important, but often overlooked, aspects of pipe installation. Proper tank should be planning for future inspection and replacement. Accurate
preparation of the glued joint is critical to long-term performance. Diligently records about the particulars of the tank design (drawings and notes) and
follow the glue manufacturer’s guidance for all assembly steps. materials of construction should be provided to those responsible for
ongoing maintenance and inspection of each tank. The tank vendor should
Pipeline Identification be asked to supply recommendations for initial inspection scheduling and
Labeling of pipelines provides critial information regarding the intended tank life expectancy. Proper replacement timing should always be intended
contents and associated product hazards. General pipeline labeling indicating to replace the vessel well before the end of its expected useful life.
the product and flow direction can be especially helpful when performing
line-tracing activities. The labeling of receiving pipelines is particularly

Storage Equipment
Materials of Construction Poly tanks have excellent chemical resistance and are often chosen
for smaller volume vessels. Lateral expansion and contraction of the
Titanium tank wall is a significant concern with poly tanks as the walls will tend
There are a limited number of materials that are chemically compatible to flex depending upon the product level inside the tank. The mechanical
with sodium hypochlorite. These materials can be categorized into metallic hammer associated with compressed air chemical deliveries, automated
and non-metallic systems. Titanium and tantalum are the only chemically valve cycling, and pump operations that introduce structural stress on
compatible metals and offer the longest lifetime. Their high cost generally poly tanks are other significant factors affecting tank service lifetimes.
limits use to critical applications such as reactor vessels and internal Additionally the use of bulkhead type fittings may significantly shorten
components of pumps, meters, valves, etc. the life of the tank because of the tendency to experience stress cracking
around the cutout for this type of fitting. As with FRP, poly vessels are
Rubber-Lined Steel sensitive to ultraviolet (UV) degradation and should incorporate the use of
Rubber-lined steel tanks are often selected for high-capacity vessels or a UV inhibitor for outdoor installations.
ones that are subjected to multiple fill/discharge cycles. The lining should
Long-term contact with hypochlorite causes embrittlement of the
be of a 100 percent chlorobutyl rubber composition. Rubber-lined storage
polymer so that a sudden mechanical shock can cause a catastrophic
tanks require a simple, but specialized mechanical integrity test (IP-4-13
failure of the tank. As with other non-metallic piping and tank materials,
“Procedure for Spark Testing Elastomeric Sheet Lining”) to evaluate lining
an inspection and replacement plan should be developed for poly tanks
integrity on a periodic basis. Exposure of lining to the product can result
so they are replaced before failure occurs.
in the exposed rubber surface dislodging or flaking over time. This flaking
phenomenon is often more pronounced for tank/liner combinations that HyPure® Bleach can be stored and handled in the same equipment as standard
have been exposed to different chemical service. For sensitive applications, a sodium hypochlorite solutions. Consult with your tank manufacturer to ensure
particulate filter on the tank discharge nozzle may be required. the tank is of adequate design to handle the increased corrosivity and oxidation
associated with this concentrated product. Insulation and cooling may be
Fiberglass Reinforced Plastic and Dual Laminates
needed if the material is held at high concentrations for long periods of time.
Fiberglass reinforced plastic (FRP) is frequently used in storage
applications and offers good mechanical strength and a failure mechanism Fabricator Evaluation
that is typically preceded by small leaks that warn of its weakened The fabrication and lining processes are critical to long-term success when
condition. However, fabricator experience, resin, curing mechanism, storing sodium hypochlorite. Industry experience has shown merely utilizing
and stored product strength are important variables influencing vessel chemically compatible material alone is not a guarantee for lengthy tank
performance. FRP vessels are sensitive to ultraviolet (UV) degradation and service lifetimes. The aggressiveness of sodium hypochlorite dictates
should incorporate the use of a UV inhibitor for tanks located outdoors. that special evaluations of the fabricator and the material of construction
should be performed, regardless of the type of construction chosen.
Hand-laid application of the reinforcement mat or chopped strand filament
Fabricators should be selected based on
winding is preferred over continuous filament wound construction. Should
the corrosion barrier fail, continuous wound filament reinforcement is at 1. Their experience in fabricating tanks intended for this product
a higher risk of chemical attack via product wicking, which increases the 2. The performance record of their tanks in sodium hypochlorite
risk of catastrophic failure. Avoid the use of cobalt napthenate as a curing service
agent because cobalt may catalyze hypochlorite decomposition upon 3. The fabrication process used.
failure of the corrosion barrier.
Once a fabricator is determined, it is important that the manufacturers’
FRP tanks also can be lined with a fluoropolymer such as PTFE, PVDF, recommendations on usage and preventative maintenance are strictly
etc. or PVC to produce a dual laminate vessel. Dual laminate construction followed. Capital, tank location, and desired service life will dictate the
offers the mechanical strength of FRP combined with a robust, chemically choice of the material of construction. However, if the storage tank is
compatible internal liner. properly specified and maintained, useful lifetime can be maximized.
Poly Tanks
High-density polyethylene (HDPE), cross-linked (XHDPE) and linear
Design Considerations
(HDLPE), have been successfully used in sodium hypochlorite service and
are typically known as poly or plastic tanks. However, fabricator experience, Sizing
resin, product strength, mechanical hammer, temperature, sunlight exposure, As part of the storage system strategy, the vessel should be large enough
and pipe connection methods are important variables influencing vessel to easily accommodate a full inbound bulk shipping container and
performance. If cross-linked HDPE is used, it is important to confirm that compensate for likely transit times and tank heels. A general rule of thumb
the resin chosen is suitable for sodium hypochlorite. Additionally, tanks is to size the tank at least 1.5 times as large as the full bulk shipping
should comply with ASTM D-1998, “Standard Specification for Upright container to maximize freight savings and have ample room to avoid
Polyethylene Storage Tanks.” tank overflows during filling. However, consumption rates also should

Storage Equipment
be considered because of the decomposition nature of the product. For overflow piping should discharge near ground level in an area and direction
low-volume requirements or where the tank is subjected to high ambient away from the typical area occupied by personnel. Consult your tank
temperature and sunlight exposure, a smaller tank volume might be fabricator for additional design guidance.
appropriate. Vertical tank designs, rather than horizontal, are preferred.
Receiving Pipeline
Venting
Two-inch piping is typical for tank trailer-serviced locations with short
Adequate venting is critical for ensuring a rapid release of air surge pipe runs, while three- or four-inch diameter pipelines are often used
when tanks are filled via pneumatic transfer. The tank will be subjected for tank car unloading to facilitate rapid product transfer. Pipe diameter
to a nearly immediate, large volume of compressed air at the end of the guidance will vary depending on site layout.
shipping container unloading process using pad air as the motive force.
Compressed air surges approaching 1200 SCFM, (Standard Cubic Feet per
Filtration
Minute) are typical from tank trailers, for example. Without an adequately
sized vent, the tank will temporarily act as a pressure vessel, which can Filtration of the product, whether it be from the shipping container to the
lead to tank wall flexing to accommodate the pressure load. Repeated flex storage tank or from the storage tank into your process should be considered.
cycles can weaken tank walls and could lead to catastrophic tank failure. There are several filtering technologies available for sodium hypochlorite
bulk unloading handling – from bag and cartridge, to vacuum, or pressure
As a general guide, tank vent diameters should be at least twice (2X) the filters. The sensitivity of your process will determine the level of need for a
size of the inlet piping diameter. Factors such as the length of the vent filtration system.
piping and number of turns can impede the release of compressed air and
will require further upsizing of the vent. It is important to consult the Outlet Nozzles
manufacturer on the type of venting system that should be designed to Selection of tanks with a low-point drain should be considered. Low-
support your bulk unloading system. point drains offer the benefits of complete product heel removal for
applications that are sensitive to product decomposition byproducts,
Overflows
such as chlorate. Low-point drains also facilitate periodic internal tank
If the tank becomes over-filled, overflow nozzles allow chemical that inspection and cleaning activities.
normally would spray out of the tank vent or man-way opening to be safely
channeled via directional piping into the containment system. Overflow Flexible Connections and Piping Support
nozzles and directional piping are generally sized at least 1.5 times (1.5X) Non-metallic tanks are also easily stressed from axial and lateral forces
larger than the inlet pipe to ensure adequate capacity. Overflow nozzles originating from factors such as the act of tank filling and the expansion/
should be installed below the roof line and on the sidewall of the tank. This contraction of attached discharge piping as ambient temperatures change.

Storage Equipment and Containment
Unsupported discharge piping connected to a heavy valve can exert significant Storage Tank Preventative Maintenance
torque on the tank’s outlet fitting area that can culminate in sidewall cracks/
damage. Rigid connections tend to concentrate these stresses in the nozzle
Cleaning
area of the tank. Installation of proper piping support and/or use of flexible
connectors may help eliminate many of these potential tank stressors. Tank Tank cleaning frequencies will be affected by factors such as the purity of
nozzles on non-metallic tanks should never be used for support of valves and the incoming product, consumption volumes, and internal tank inspection
piping. Consult your tank vendor for specific guidance. cycles. Tank rinsing may be desired for removal of sedimentation that
can occur over time, as well as removal of residual metallic contaminants
Level Measurement that may adhere to tank walls after the product has been consumed. Tanks
A level measurement system is important for maintaining process operation purchased with a ‘full drain’ nozzle will foster complete cleaning and
and for avoiding a possible overflow condition during inbound delivery. flush activities. Tanks equipped with ground-level man-ways can facilitate
Gauging systems range from simple visual readings to complex remote cleaning activities by providing convenient vessel access without the use
readouts. Under certain scenarios, the inventory may be read directly from of ladders and scaffolding.
the “shadow” of a translucent, clear-tinted poly tank equipped with markers
Inspection
molded into the side wall. External “sight glasses” can provide effective level
indications. However, similar to reading inventories from the “shadow” of a A periodic, scheduled inspection should be performed regardless of material
translucent tank, use of external “sight glasses” may also lead to erroneous of construction chosen. Personnel performing inspections should be given
readings under certain lighting conditions. External “sight glasses,” such specific guidance regarding areas to inspect and the types of failure/damage
as polyethylene or polypropylene tubing, also present an opportunity for to identify. Detailed criteria and photos can be useful inspection aids. Use
catastrophic loss of tank contents upon “sight glass” failure or damage. of a checklist has been found to be particularly helpful to ensure inspection
Differential pressure or electronic level indicators are frequently used for tank consistency between different personnel. For non-metallic tanks, the exterior
level measurement. Level indicators that are not immersed in the product of the tank should be inspected for evidence of drips or seepage, side-wall or
typically perform best, but all electronic level transmitters should be assigned roof bulges, and surface cracks or crazing, to name several key attributes and
a scheduled, periodic recalibration cycle to ensure accurate readings over the areas for inspection.
long term. Equipping the indicator to activate an alarm or automatic shutoff at
To enhance the efficacy of tank inspections, detailed records of previous
preset inventory levels can provide an important additional layer of protection
inspections that include photos and notes about the location of minor flaws
against accidental tank overflow conditions. The reliability of the high level
or routine wear will be extremely helpful. This information can be used
alarm or automatic shutoff can be enhanced by using an activation device
in determining the progress of wear and tear on the vessel and/or liner or
independent of the regular level transmitter (redundancy).
corrosion barrier. Over time these comparisons can improve the accuracy –
Posting the maximum allowable storage tank volume in a location clearly and the economy – of future inspection and replacement scheduling. Without
visible to unloading personnel will facilitate calculation of available an understanding of the performance characteristics of a particular material
volume for incoming chemical. This, coupled with a local level readout, of construction and tank design under your specific storage conditions,
will allow the unloading staff (and delivery driver for tank trailer it is difficult to make wise decisions about the timing of future tank
shipments) to monitor tank levels more effectively during unloading. inspections and replacement. Your tank vendor’s initial recommendations for
the frequency of these activities should be followed.
Tie Downs
Storage Tank and Unloading Station Containment Systems
Tanks should be adequately secured using tie downs installed from the
factory to prevent tank movement from high winds or seismic activity. A well-designed handling system should incorporate an effective secondary
containment system to contain potential drips or spills in product storage and
Storage Tank Identification unloading areas. Secondary containment regulations often vary by location,
Tanks should be clearly labeled to identify chemical contents. Labels or so it will be important to review local codes/city ordinances, as well as
stencils noting the entire, formal product name, e.g. “sodium hypochlorite,” province, state, and federal requirements when considering storage of sodium
are preferred and especially beneficial to contractors and others not hypochlorite, whether the tank is indoors or outdoors. As a general guide,
intimately familiar with the tank farm. Avoid use of “chlorine” or “liquid containment systems should be capable of holding at least 110 percent of the
chlorine” for identification as these terms are inaccurate and confusing. A largest tank capacity found in the contained area. Appropriate containment
misunderstanding may lead to unnecessary or inappropriate precautions being must be designed to address the most likely quantity of sodium hypochlorite
taken by emergency response personnel in an actual chemical incident. Such that would be discharged from the primary containment system (e.g.,
distractions and confusion can prevent prompt action to address the emergency container, equipment), such that the discharge will not escape secondary
condition to which they have responded. Labels should comply with OSHA’s containment before cleanup occurs. In determining the most likely quantity,
HAZCOM Standard, CFR 1910-1200 or with Canada’s WHMIS (Workplace the facility owner/operator should consider factors such as the typical
Hazardous Materials Information System) for Canadian sites. Certain local failure mode (e.g., overfill, fracture in container wall, etc.), resulting sodium
regulations, codes, or agencies may also dictate label content. hypochlorite flow rate, facility personnel response time, and the duration of
the discharge. In addition, the system designer should identify any bottlenecks

Containment and Incompatible Chemicals
and implement modifications that address them. Containment sizing should Incompatible Chemicals During Unloading
take into account “freeboard” space in the event of a heavy precipitation event
or other items that could be introduced into the secondary containment such as The oxidizing property of sodium hypochlorite requires
water or foam from a fire suppression system. that special care be taken to avoid incompatible chemical
Incompatible chemicals – especially those that release hazardous gases

contact, also known as accidental mixing. Accidental
mixing may result in personnel injury or environmental
ACIDS
when mixed – should be separated by walls within the overall containment damage as a result of introducing sodium hypochlorite
area and in the drain-system piping. residues to a wide variety of incompatible chemicals.
Although reactions vary depending on the chemical composition, sodium
There are a number of options for secondary containment systems including hypochlorite will generate chlorine gas when exposed to acids, acid residues,
concrete, double-walled tanks and open-top containment tanks. Concrete is or other chemicals that may lower the pH of the hypochlorite solution.
typically the preferred choice for bulk storage containment systems. A well- Production of oxygen gas and significant amounts of heat may accompany
designed system will have reinforced floors and walls. Application of an other reactions with sodium hypochlorite.
industrial coating can extend concrete containment lifetime and to limit the
potential of chemical migration through cracks or open expansion joints. The The opportunities for incompatible chemical contact at a storage facility
effectiveness of industrial coatings will be largely influenced by the overall are many and variable but typically can be grouped into three categories:
condition of the concrete, amount of surface preparation before application, 1. The shipping container unloading process
and the type of coating applied. Two-part epoxy coatings intended for strong
2. Secondary containment for unloading and storage
alkalis are preferred.
3. Small-containers, such as drip collection devices
Good maintenance and housekeeping practices that eliminate small
piping or pump leaks soon after they develop and that keep the area The Chlorine Institute (www.chlorineinstitute.org) bulletin, “Sodium
clean and dry will extend the life of the enclosure. Maintenance becomes Hypochlorite Incompatibility Chart,” provides a list of chemical families
critical as minor imperfections that allow chemical to contact the concrete that are incompatible with sodium hypochlorite. Design considerations to
structure may not be adequately rinsed away from rainfall or housekeeping help prevent accidental mixing are discussed in the ‘Unloading Station’
events. section of this manual and the SDS.
Double-walled tanks are often considered for vessels if there is limited

room for the tank and containment system. Use of a liquid-detection
monitor in the open space between the tanks can provide notification of
internal vessel failure. The double-walled feature does, however, impede
the ability to perform important visual inspections of the tank wall.
Shipping container unloading stations also should incorporate secondary

containment to collect leaks, spills, or wash-down water. Reinforced
concrete is generally the preferred material of choice for tank trailer
unloading station containment systems because most unloading areas
must be able to accommodate vehicular traffic weight loads. For tank car
unloading, the presence of railroad ties and the occasional need for track
maintenance make removable containment pans preferable to concrete
sumps or pits. Polyethylene or fiberglass reinforced plastic (FRP)
containment pans are offered from many containment system vendors
for liquids collection between track rails. They offer the benefit of being
removed for future track maintenance purposes. Routing of containment
system drains should avoid exposure to incompatible chemicals.

Personal Protection
Safety Data Sheets Personal Protective Equipment

Always review the SDS before handling sodium hypochlorite. Sodium hypochlorite is a corrosive material that can cause serious health
hazards if improperly handled. It is corrosive to the skin, eyes, mucous
Sodium hypochlorite is a corrosive and reactive compound. To prevent
membranes, and respiratory tract, and it may cause severe chemical burns
personnel injuries and environmental exposure, this manual and the most
to the eyes and skin. Bodily attack will vary with solution strength and
current Safety Data Sheet (SDS) should be reviewed and understood.
duration of exposure. Personal protective equipment (PPE) requirements
Personnel should be prepared to deal with both normal and abnormal
will vary by task and surrounding work environment. A formal PPE
situations. Never handle any sodium hypochlorite solution before you
hazard assessment should be performed to evaluate the appropriate PPE
have read the relevant SDS. Each SDS contains information for handling
gear necessary for a given task. Typically, such a risk analysis will result
particular solution strengths of sodium hypochlorite and has the most current
in different levels of PPE based on work duty. When work duties include
detailed information on health effects, handling precautions, and first aid,
as well as, additional sodium hypochlorite information this is not contained line-breaking activities such as transfer hose connection/disconnection or
maintenance work, use of full PPE, including chemically resistant jacket and
in this manual. The SDS must be readily accessible to all persons where the
pants, chemically resistant boots and gloves, goggles and a face shield are
product is being used. The most up-to-date SDS, provided by the supplier,
required. Consult the Chlorine Institute Pamphlet 65 for additional details.
should be available to and understood by all employees who work with
sodium hypochlorite. The most current SDS can be obtained from Olin at Clothing can be damaged upon contact with this material. Flame resistant
www.olinchloralkali.com. clothing (FRC) may have a higher rate of attack from sodium hypochlorite
than non-FRC cotton materials, especially at higher solution strengths.
Consult your PPE manufacturer for additional guidance.

First Aid Procedures
General Guidelines Responding to Emergencies

Prompt response to personal exposures is critical to minimize potential Each facility should maintain current procedures for handling emergencies
injurious consequences. Ensure that medical personnel are aware of the occurring both on-shift and after hours. If your facility meets the requirements
chemical(s) involved if exposure or injury occurs. Always review the of 29 CFR 1910.38 and external personnel will be expected to resolve the
most current Safety Data Sheet (SDS) on what to do should there be eye emergency, then you must have an Emergency Action Plan (EAP) which
contact, skin contact, ingestion, or inhalation of sodium hypochlorite and describes how employees will respond to different emergencies. Sites with
provide it to medical personnel administering care to injured persons. 10 or more employees must maintain a written EAP, although a written EAP
is always desirable. Periodic drills should be conducted to verify employees
Safety Shower and Eyewashes know the EAP and can carry out the duties identified in the EAP. In general, an
EAP should address:
A safety shower and eyewash station provide an important line of defense
• Means of reporting fires and other emergencies
against chemical injury should bodily contact with sodium hypochlorite
occur. Safety shower and eyewash units should fully comply with the • Evacuation procedures and emergency escape route identification
most current version of the American National Standards Institute (ANSI) • Procedures for operating critical controls prior to evacuation
Z358.1 standard, which addresses items such as equipment performance • Accounting of all employees
requirements, accessibility, and testing.
• Rescue and medical duty assignments
In general, safety shower and eyewash units should be located in areas that • Names with corresponding job titles to contact in emergencies
have the potential for chemical exposure, such as unloading, pumping,
or sampling locations. The safety device should be easily accessible An Emergency Preparedness Plan (EPP) is to be maintained for sites
and highly visible to expedite a user’s ability to locate and reach the that meet the requirements of 29 CFR 1920.38 (Emergency Action Plan)
device quickly. In some applications, multiple safety shower and eyewash and 29 CFR 1910.120 (Emergency Response Plan under the Process
stations may be required to provide unimpeded access to the safety device Safety Management Standard) wherein site employees will also act in
under “normal”, “abnormal”, and emergency conditions. Typical guidance a First Responder role. The EPP has additional detailed procedures that
includes locating a safety shower and eyewash unit within 10 seconds of specifically address First Responder roles such as training, emergency
unobstructed access to a potential source of exposure. Unobstructed access recognition and prevention, PPE and emergency equipment, decontami-
requires the safety appliance to be located on the same level as the hazard nation procedures, and establishing incident command, to name several
and be void of impediments such as containment walls, steps, doors, etc., components. The EPP should be periodically reviewed with your Local
which can interfere with the ability to reach the safety appliance quickly. Emergency Planning Committee (LEPC) to ensure compliance with
local, province, and state requirements. Like EAP’s, it is important to
Locating and operating the safety shower and eyewash unit at the onset conduct frequent plan drills. Including your LEPC or outside responder
of area work is encouraged as it provides the greatest assurance of device in facility drills can provide important insight into plan strengths and
operability. In addition to scheduled device activations to verify water flows, weaknesses, and can also strengthen relationships with the community.
safety shower and eyewash inspections should focus on changes that have
recently occurred affecting access and visibility, such as the “temporary”
storage of work equipment or materials near the device. Workers should
always be reminded that access to safety equipment must never be
compromised for convenience or improved efficiency.

Spills and Leaks
General Guidelines –– If external personnel will perform response duties, activate

the Emergency Action Plan.
In general, when encountering a leak or spill, the primary focus should –– If facility persons will perform response duties, activate the
be to always maintain your personal safety as well as those around Emergency Response Plan.
you. Consult your EAP or EPP regarding specific actions to take when
encountering a spill event. Ensure that you follow all state, province, Step 2 - Suit Up and Remediate
local, and municipal regulations pertaining to spills and spill response.
This would include the proper training required by personnel who are THESE STEPS SHOULD BE PERFORMED BY TRAINED,
expected to do the clean-up activities. KNOWLEDGEABLE PERSONNEL ONLY!
• Suit up with appropriate PPE per SDS and never respond alone.
How to Respond to Spill Events • Isolate and contain the spill with the use of inert materials (eg., sand,
dirt, etc.).
Step 1 - Evacuate and Activate
• Recover as much chemical as possible for re-use.
• Evacuate all personnel from the area and restrict access.
• For unusable material, transfer liquids and residues to an approved
• Maintain safe refuge away from and upwind of the spill area.
Hazardous Waste container for proper disposal.
• Active the site’s Emergency Plan.

Spills and Leaks
• Manifest and dispose of unusable materials, residues, and their There are a number of chemical options for neutralizing sodium hypochlorite,
containers consistent with all local, province, state and federal including sodium sulfite, sodium bisulfite, sodium thiosulfate, hydrogen
regulations. peroxide, and sulfur dioxide. Regardless of the method chosen, the sequence
• Neutralize affected area avoiding use of acids and low pH of neutralization steps is critical. To prevent generation of chlorine gas, always
neutralizing agents until all available chlorine has been neutralized. neutralize the hypochlorite active ingredient before lowering solution pH.
Consult Neutralization section and SDS for additional details.
Disposal
• Decontaminate all equipment, PPE, and materials.
Proper clean-up and disposal requires that liquids, residues, and
• Launder any clothing or jewelry prior to re-use.
neutralized materials are handled, stored, transported, and disposed in
Step 3 – Report accordance with local, province, state, and federal regulations.
• Immediately report spills in accordance with local, province, state,

and federal regulations.
Consult the SDS to determine the Reportable Quantity (RQ) threshold

for this material. Federal law requires that if the spill is greater than the RQ
it must be immediately reported to the National Response Center (NRC) at
800-424-8802. Consult local, province, state, and federal regulatory
agencies for specific requirements unique to your location. Additional
regulatory reporting requirements may vary by jurisdiction.
Special Considerations
Special care must be exercised when attempting to contain, neutralize,
and dispose of sodium hypochlorite spills. The strong reactive power
dictates that any absorbent material must be chemically inert to sodium
hypochlorite. Avoid use of items such as sawdust and rags, which can
react with sodium hypochlorite under certain conditions, and materials such
as “floor dry,” which typically contain organic components. Spill collection
equipment, such as shovels or recovery drums, should be verified clean and
void of incompatible residues.
Never introduce sodium hypochlorite to local sanitary treatment plants

or bodies of water without proper approvals. Sodium hypochlorite
can irreparably disrupt the biological processes of sewage treatment
operations and will result in harm to aquatic life. Chlorine gas also
might be released at the treatment plant if acidic waters are encountered
by the hypochlorite. Processing and containment area drains should be
periodically reviewed to ensure protective features such as engineering
and procedural controls are in place to prevent automatic release.
Neutralization
Neutralization is often favored for larger quantity spills, those which are
heavily contaminated and cannot be re-used, or in situations where the
resulting neutralized solution will be sent to a waste water treatment plant.
Neutralization methods for spill events described in this publication are not
intended to treat bodily exposures. Although the result of neutralization is
a less hazardous material, the process itself involves other chemicals, rapid
reactions, and in some instances the potential to generate other gases and
hazards. When neutralizing hypochlorite solutions, safety must be an integral
component throughout the process. Because of the potential for aggressive
reactions, only well-trained personnel should attempt neutralization.
Completing a hazard analysis before work begins will help identify the
critical engineering and procedural controls necessary for safe neutralization.

Analytical Guidelines
Importance of Accuracy capacity to avoid over-pressurization, leakage, or bottle bulging which may
be induced as the product warms in storage. The sample should be identified
The accurate determination of sodium hypochlorite assay is influenced and analyzed as soon as practical after collection—typically within two
by many factors including: sample point selection, sample technique, hours when stored at room temperature. Prior to analysis, the sample should
sample handling, analytical methodology, and analytical equipment and be kept away from heat sources and out of direct sunlight or other UV
technique. The assay of sodium hypochlorite will continually decline exposure as these factors will increase the decomposition rate of the product.
over time at a rate determined by a variety of factors including: sodium If there is going to be a significant delay in analysis, the sample should be
hypochlorite concentration, temperature, residual sodium hydroxide levels, cooled/refrigerated until analysis is possible.
and exposure to UV light and trace metals such as nickel, copper, and iron.
This manual describes a number of important guidelines to improve the Analytical Method
accuracy of assay determination of sodium hypochlorite in the shipping
container (tank truck or tank car). The steps and guidance presented should The most common analytical method used to determine assay of sodium
be thoroughly reviewed for applicability at a particular site with a hazard hypochlorite solutions is a titration with a standard sodium thiosulfate
review covering the site specific functions to identify the best procedures solution. The titration is based on the principle of ion substitution in a
and personal protective equipment (PPE) for the health and safety of site pH-buffered environment, where the substitution element (iodine) is
personnel and the environment. Refer to the Safety Data Sheet (SDS) for more easily titrated than the hypochlorite ion. In this method, a sample is
sodium hypochlorite for additional information on appropriate PPE. treated with excess potassium iodide, neutralized with glacial acetic acid,
and the liberated iodine is titrated with sodium thiosulfate. The titration
endpoint is determined using a starch indicator solution. The following
Sample Collection equations describe this method:
Whenever possible, the sample should be collected directly from the
shipping container using a clean and appropriately designed sample Equation 7:
collection device. Steps should be taken to avoid contaminating or
NaOCl+2 KI+2 HAc→I2+ NaCl+2 KAc+H2O
damaging the shipping container during sampling. If a shipping container
sample cannot be safely obtained, a properly designed sample point should
Equation 8:
be installed directly on the unloading piping where there is flow through
the sample point. Procedures should be in place to ensure the sample point Cl2+2 KI→I2+2 KCl
is purged sufficiently to provide a representative sample of the shipping
container. Consult the SDS for appropriate PPE to be worn during sample Equation 9:
collection activities.
I2+2 Na2S2O3→Na2 S4O6+2 NaI
Sample Handling The Chlorine Institute’s Pamphlet 96 “Sodium Hypochlorite Manual” is a
good reference document for the step-by-step procedure of this method. This
All wetted surfaces of sample collection equipment (thief, bottles, and bottle
document is available for download from the Chlorine Institute’s website
cap inserts) should be non-metallic. Sample bottles should be cleaned and
(www.chlorineinstitute.org) after registering with the site.
flushed with the sample media. Fill the bottle no more than two-thirds of its

Analytical Guidelines
Note for HyPure® Sodium Hypochlorite Users
When using the above reference procedure for the analysis of HyPure® Sodium Hypochlorite
gpl available chlorine = wt% NaOCl × 10 × SG/1.050
at concentrations greater than 17 wt% NaOCl, the volume of the aliquot of the sample should
be reduced by a factor of 2 in order to maintain an acceptable titration volume, due to the trade % available chlorine = wt% NaOCl × SG/1.050
much higher NaOCl concentration in this product. An adjustment to the calculation below
should be made by replacing 0.04 by 0.02. wt% available chlorine = wt% NaOCl ÷ 1.050
wt% = weight percent
Important Procedural Considerations
• The order of addition in sample preparation is important to follow gpl = grams per liter of solution
as instructed (sample aliquot, then distilled water, then potassium
iodide, followed by the acetic acid prior to titration). If the acid SG = specific gravity
is added prior to the potassium iodide, chlorine could be released
from the solution, creating an inaccurate analysis and possible NaOCl = Sodium Hypochlorite
safety hazard.
It is also important to communicate the full units when reporting sodium
• Glacial acetic acid solution must be used at the listed quantity to hypochlorite strength to ensure everyone is aware of the measurement
ensure complete neutralization of the sample. If too little or too being reported.
weak an acid is used, complete neutralization will not occur and
the analysis will result in a low assay.
• The normality of the sodium thiosulfate used in titration should be
Best Practices
standardized on a regular basis to ensure accuracy in calculation. • The use of an autotitrator can increase the accuracy and precision
A minimum of a monthly frequency should be considered. The of the analytical results when measuring Sodium Hypochlorite
thiosulfate solution will degrade over time and will not give an strength. Please contact Olin Technical Service personnel for
accurate analysis if an incorrect normality is used in calculations. additional assistance with autotitration systems.
• If a potassium iodide solution is being used in lieu of the crystals, • Starting the analysis using a weighed sample can improve the
the solution should be remade on a regular basis as well as it too, accuracy of the analysis by re-moving the error introduced by
will degrade over time. measuring the density of the solution.
• This procedure includes the use of a starch indicator to clarify
NOTE: The density will still need to be used to convert the result to other units.
the end point of titration. This indicator use is very important
in maintaining the accuracy of the analysis. The endpoint of • A study, such as a Gage R&R, should be used to determine the
the titration is very difficult to see without the use of the starch variation in results expected from the method and the analyst.
indicator and results will be inconsistent without its use. The study examines measurement system errors in terms of
• Distilled or deionized water should be used throughout the repeatability, or equipment variation, and reproducibility,
analysis. The use of lower quality water sources (such as tap or analyst to analyst variability. It is important to gain an
water) can lead to inaccurate results. understanding of the site’s capabilities in terms of accuracy and
precision as well as the factors that are influencing these results.
• Final points of consideration in this procedure are using the
appropriate quality equipment in the analysis (including Class A • Good laboratory practices and techniques should be included
pipettes and certified weigh scales with 4 decimal place accuracy) in the training for all personnel analyzing samples in order to
and properly training personnel in proper lab techniques, the improve consistency from person to person. Good laboratory
procedure, and the hazards involved. practices would include a robust training program, documented
procedures that utilize validated test methods, and the use of
statistical controls on equipment and reagents.
Discussion of Units
This calculation below determines the strength of the sodium hypochlorite
solution in weight percent NaOCl as shown below for the sample size
Residual Alkalinity Analytical Testing
described in the Pamphlet 96 analytical reference. Once the available chlorine has been neutralized with hydrogen
peroxide, a simple acid–base titration is performed to determine
wt% NaOCl = (ml Na2S2O3) × (Normality) × 3.723/ alkalinity. If the determination of amount of sodium hydroxide and
(0.040 × weight of original sample) sodium carbonate is needed, the titration is essentially the same but has
two endpoints. Use of pH testing to determine alkalinity levels is not
Hypochlorite strength can be expressed in other units. Because the density of recommended because of the inability of pH test methods (probes or
the solution changes with a variety of factors including caustic concentration, litmus papers) to yield accurate, reproducible test results. Alkalinity test
salt concentration, temperature, etc., it is critical to use a measured density (or methodology can be found in The Chlorine Institute’s Pamphlet 96. Like
specific gravity) in the following calculations for conversion. the assay analysis, this test can be performed by manual or auto titration.

Additional Information and Emergency Contacts
For Additional Information Emergency Contacts

In the event of an accident or chemical incident, refer to your site’s emergency
The Chlorine Institute
preparedness plan and the most current Safety Data Sheet (SDS). Should a
1300 Wilson Blvd.
chemical leak or spill occur, immediately contact the applicable regulatory
Suite 525 Arlington, VA 22209
agency and implement your site’s Emergency Action Plan or Emergency
(703)-894-4140
Preparedness Plan.
www.chlorineinstitute.org
• Pamphlet 96, “Sodium Hypochlorite Manual” In the U.S.: Call CHEMTREC (toll-free) (800) 567-7455
• “Avoiding Accidental Mixing of Sodium Hypochlorite” bulletin
In Canada: Call CANUTEC (collect) (613) 996-6666
• “Sodium Hypochlorite Incompatibility Chart”
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West Conshohocken, PA 19428 owners. All company, product and service names used in this website are
(877)-909-2786 for identification purposes only. Use of these names, logos, and brands
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Graph Appendix
Graph 1: Bleach Stability and Density at 70ºF
Graph 2: Estimated Decomposition of 12.5 wt% Sodium Hypochlorite Solution

Graph Appendix
Graph 3: Estimated Decomposition of 15.5 wt% Sodium Hypochlorite Solution
Graph 4: Estimated Decomposition of Standard and HyPure® Bleach

Graph Appendix
Graph 5: Metal-Induced Assay Loss (g/L) vs. Time (Hours)

North America Contact Information
USA: +1 844 238 3445 Info@olinbc.com
Canada: +1 877 304 4442 www.OlinChlorAlkali.com
Mexico: +55 1151884105
Notice: No freedom from any patent or other intellectual property rights owned by Olin or others is to be inferred. Olin assumes no obligation or liability for the information in this document. The
information provided herein is presented in good faith and is based on the best of Olin’s knowledge, information, and belief. Since use conditions at non-Olin facilities are beyond Olin’s control and
government requirements may differ from one location to another and may change with time, it is solely the Buyer’s responsibility to determine whether Olin’s products are appropriate for the Buyer’s
use, and to assure the Buyer’s workplace, use, and disposal practices are in compliance with applicable government requirements. Consequently, Olin assumes no obligation or liability for use of these
materials and makes no warranty, express or implied. The user of the information provided is solely responsible for compliance with any applicable government requirements. NO WARRANTIES
ARE GIVEN; ALL IMPLIED WARRANTIES OF MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE ARE EXPRESSLY EXCLUDED.
© Olin Corporation 2019

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SODIUM HYPOCHLORITE

PRODUCT STEWARDSHIP MANUAL

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 1

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 2

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 3

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 4

Olin believes the information and suggestions contained in this manual

Information herein concerning laws and regulations is based on U.S.

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 5

Olin Product Stewardship

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 6

Locations Olin Bleach Production Locations

hypochlorite solutions, commonly referred to as “bleach.” The capabilities

available to meet specific market needs. Olin is uniquely positioned Red

to service your sodium hypochlorite needs as a true integrated North

American manufacturer with production facilities and terminals located Snak

shown on the map included in this section. Through our network of

manufacturing facilities, shipping equipment, and terminals, we can ship

SANTA FE SPRINGS, CA CHARLESTON, TN

information about your specific needs, contact an Olin representative.

Bleach Production Plants

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 7

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 8

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 9

3 NaOCl + Temperature & Time →2 NaCl+NaClO3

Temperature Impact on Stability

HyPure® Bleach (see adjacent Decomposition Graphs) exhibits

However, once diluted, HyPure® Bleach exhibits a slower decomposition

The total amount of all chemical compounds dissolved in any bleach

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 10

The dilution water should be analyzed to develop an impurity profile.

The major sources of metallic contamination are the quality of caustic

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 11

Dilution and Excess Residual Alkalinity 15.5 -21.5 -29.6

All sodium hypochlorite solutions require residual alkalinity, particularly

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 12

Caustic Soda Chlorine Water

Salt Trace Metals

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 13

Note 1 Note 1 Note 1

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 14

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 15

Numerous important regulatory, environmental, safety, and health

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 16

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 17

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 18

Corrosive Liquids Pad Gas Quality at Point of Use

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 19

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 20

Transfer Hoses sodium hypochlorite and likely temperature ranges to be experienced

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 21

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 22

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 23

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 24

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 25

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 26

Incompatible chemicals – especially those that release hazardous gases

Double-walled tanks are often considered for vessels if there is limited

Shipping container unloading stations also should incorporate secondary

SODIUM HYPOCHLORITE PRODUCT STEWARDSHIP MANUAL 27