1 3rd Year Industrial Chemistry-I
1 3rd Year Industrial Chemistry-I
1 3rd Year Industrial Chemistry-I
Contents to be covered:-
Classify the chemical industry in terms of scale, raw materials, end use
and value addition
The discipline is also concerned with economics and the need to protect the
environment.
Classical and Industrial Chemistry
Difference between Classical and Industrial Chemistry
Definition
Industrial chemistry is defined as the branch of chemistry which applies
physical and chemical procedures towards the transformation of natural
raw materials and their derivatives to products that are of benefit to
humanity.
• Food production
• Shelter
• Protection
Classification of Industries
Classification of Industries
Industry is a general term that refers to all economic activities that deal with
production of goods and services. Goods and services are key words of industry.
Light industry require less capital investment to build than heavier industry.
Vehicles and
Basic chemicals
Classification of the Manufacturing Industry
Other measures used to classify industries include the weight or volume of
products handled and weight per cost of production.
For example the weight of steel produced per dollar is more than the weight
per dollar of a drug. In this case, steel industry is a heavy industry whereas
drug manufacture is a light industry.
Both inorganic and organic chemical industry can be either heavy or light
industry.
2) Specialty chemicals
3) Fine chemicals
The Structure of the Global Chemical Industry
1) Commodity chemicals (Industrial chemicals):
The global chemical industry is founded on Basic Inorganic Chemicals
(BIC) and Basic Organic Chemicals (BOC) and their intermediates.
Ethylene and propylene are usually among the top ten BOC. They are
used in the production of many organic chemicals including polymers.
The Structure of the Global Chemical Industry
2) Specialty chemicals:
These are high value-added products produced in low volumes, used in
extremely low quantities and sold on the basis of a specific function.
Therefore the global market share for each type is roughly as follows:
Fine chemicals: 2%
Raw materials for the Chemical Industry
Since there would be no chemical industry without raw materials, the subject
of raw materials is due for discussion at this stage.
All chemicals are derived from raw materials available in nature. The price
of chemicals depends on the availability of their raw materials.
These are the physical treatment steps, which are required to:
Put the raw materials in a form in which they can be reacted
chemically.
Put the product in a form which is suitable for the market.
Units that make up a chemical process
Examples of unit operations:
Agitation Dispersion Heat transfer
Atomization Distillation Humidification
Centrifuging Evaporation Mixing
Classification Filtration Pumping
Crushing Floatation Settling
Decanting Gas absorption Size reduction
The objective is to produce small particles from big ones for any of the following
reasons.
To reduce chunks of raw materials to workable sizes e.g. crushing of mineral ore.
To release valuable substances so that they can be separated from unwanted material.
To increase particles in number for the purpose of selling and to improve blending
efficiency of formulations, composites e.g. insecticides, dyes, paints.
Units that make up a chemical process
Jaw Crusher
When a solid is held between two planes
and pressure is applied on one plane, the
solid is fractured and breaks into
fragments when pressure is removed.
However, the importance of suitably preparing water for the chemical industry is
sometimes underemphasized.
Industrial waste waters present a complex and challenging problem to the chemical
engineer.
The solution is specific with each industry (indeed, almost with each plant or factory),
a few general principles may be observed: reuse of waste waters, recovery of by-
products to lessen the expense of treatment, and pooling of wastes to distribute
pollution or to effect a saving in neutralization costs.
Water in the Chemical Industry
The purity and the quantity of available water are very important in the
location of a chemical plant.
The ground water is more suitable usually for cooling purposes because of its
uniformly low summer and winter temperature.
But such water is generally harder, may cause scale, and hence may interfere
with heat transfer.
Hardness of Water and dissolved solids
Hardness is usually expressed in terms of the dissolved calcium and magnesium
salts calculated as calcium carbonate equivalent CaCO3.
Water hardness may be divided into two classes: carbonate and non-carbonate,
also frequently known as temporary and permanent hardness of water.
The total dissolved solids may range from a few parts per million in snow
water to several thousand parts per million in water from mineral springs.
These ions do not pose any health threat, but they can engage in reactions that
leave insoluble mineral deposits.
These deposits can make hard water unsuitable for many uses, and so a variety of
means have been developed to "soften" hard water; i.e., remove the calcium and
magnesium ions.
In small quantities, these deposits are not harmful, As these deposits build up,
however, they reduce the efficiency of heat transfer.
More serious is the situation in which industrial-sized water boilers become coated
with scale: the cost in heat-transfer efficiency can have a dramatic effect on power
bill.
The water is treated with a combination of slaked lime, Ca(OH)2 and soda ash,
Na2CO3.
Hence, it can dissociate in water to give one Ca2+ ion and two OH– ions for each unit
of Ca(OH)2 that dissolves.
The OH– ions react with Mg2+ ions in the water to form the insoluble precipitate. The
Ca2+ ions are unaffected by this reaction, and so we do not include them in the net
ionic reaction.
They are removed by the separate reaction with CO32– ions from the soda ash.
Mg2+ (aq) + 2OH– (aq) Mg(OH)2 (s)
Hardness of Water
Water treatment (softening) by Ion-exchange
Water softeners typically use a different process, known as ion exchange.
When water containing Ca2+ and Mg2+ ions is passed through the ion
exchanger, the Ca2+ and Mg2+ ions are more attracted to the anion groups than
the Na+ ions. Hence, they replace the Na+ ions on the beads, and so the Na+
ions (which do not form scale) go into the water in their place.
Hardness of Water
Water treatment (softening) by Ion-exchange
When hard water passes through the
ion exchanger (right), the calcium ions
in the hard water get exchanged by the
sodium ions in the ion exchanger.
In this facility, settleable solids and most suspended solids settle to the bottom
of the basin.
It is desirable to run pilot studies to determine the optimal chemicals and dosage
levels.
The use of a given chemical(s) and effluent quality must be carefully balanced
against the amount of additional sludge produced in the sedimentation step.
Filtration and membrane filtration
The newly emerging application of wastewater reuse is hyped to become the
most promising process for membranes in the water industry.
Membranes have been used in water and wastewater applications since the
1960's.
There are two classes of membrane process used in the water and wastewater
field:
The first category includes Reverse Osmosis (RO) and Nano Filtration (NF).
These membranes have a dense non porous separating layer cast onto a porous
support, and are used for the removal of dissolved substances.
Filtration and membrane filtration
The second category is membrane filtration. Membrane filtration process is a
physical separation method characterized by the ability to separate
molecules of different sizes and characteristics.
One of the longest established uses for membranes in water treatment is in the
use of reverse osmosis (RO) for desalinating seawater.
Ultrafiltration (UF)
Microfiltration (MF)
Manufacturing techniques have changed and improved in recent years and new
procedures are employed such as the burning of chlorine in hydrogen.
Hydrogen chloride can be generated in many ways, and thus several precursors
to hydrochloric acid exist.
Historical perspective
Hydrogen 'chloride was discovered in the' fifteenth century by Basilius
Valentinius.
Hydrochloric acid or Muriatic acid
Hydrochloric acid (HCl)
Commercial production of hydrochloric acid began in England when
legislation was passed prohibiting the indiscriminate discharge of hydrogen
chloride into the atmosphere.
This legislation forced manufacturers, using the LeBlanc process for soda ash,
to absorb the waste hydrogen chloride in water.
As more uses for hydrochloric acid were discovered, plants were built solely
for its production.
The largest users of hydrochloric acid are the petroleum, chemical, food and
metal industries.
Hydrochloric acid or Muriatic acid
Hydrochloric acid (HCl)
Industry experts estimate that activation of oil wells consumes about 30
percent of the acid sold.
The old salt-sulfuric acid method and the newer combustion method each supply
about 20 per cent. The Hargreaves process is used by only one company, although a
modified Hargreaves process is in operation at another plant.
Reactions and Energy Requirements
Reactions and Energy Requirements
The basic steps in the production of by-product acid include the removal of
any unchlorinated hydrocarbon followed by the absorption of the HCl in water.
A typical chlorination for illustration follows:
C6H6 + Cl2 → C6H5Cl + HCl
Since the chlorination of aliphatic and aromatic hydrocarbons evolves large
amounts of heat, special equipment is necessary for control of the temperature
of reaction.
The reactions of the salt-sulfuric acid process are endothermic.
NaCl + H2SO4 → HCl + NaHSO4
NaCl + NaHSO4 → HCl + Na2SO4
Summation:
2NaCl (s) + H2SO4 (l) → 2HCl (g) + Na2SO4 (s); ∆H = + 15.8KCal
Reactions and Energy Requirements
Reactions and Energy Requirements
The first reaction goes to completion at relatively low temperatures while the
second approaches completion only at elevated temperatures.
The reactions are forced to the right by the escape of the hydrogen chloride
from the reaction mass.
The reaction between hydrogen and chlorine is highly exothermic and goes
spontaneously to completion as soon as it is initiated
Salt Process for Hydrochloric acid Manufacturing
Salt process:
The salt process may be divided into the following unit operations (Op.) and
unit processes (Pr.):
Sulfuric acid and salt are roasted in a furnace to form hydrogen chloride
and sodium sulfate (salt cake) (Pr.).
The hot hydrogen chloride, contaminated with droplets of sulfuric acid and
particles of salt cake, is cooled by passing it through a series of S-shaped
Karbate coolers, cooled externally by water (Op.).
The cooled gas is then passed upward through a coke tower to remove
suspended foreign materials (Op.).
Salt Process for Hydrochloric acid Manufacturing
Salt process continued…
Purified hydrogen chloride from the top of the coke tower is absorbed in
water in a tantalum or Karbate absorber (Op.).
The rotary furnace is growing in usage. Here sulfuric acid and salt are
continuously mixed and heated.
Synthetic Process for Hydrochloric acid Manufacturing
Synthetic process:
The synthetic process generates hydrogen chloride by burning chlorine
in a few percent excess of hydrogen.
The purity of the ensuing acid is dependent upon the purity of the
hydrogen and chlorine.
Both of these gases (hydrogen and chlorine) are available in a very pure
state as by-products of the electrolytic process for caustic soda, this
synthetic method produces the purest hydrogen chloride of all the
processes.
The cooling and absorption are very similar to that employed in the salt
process.
Handling of Hydrochloric acid
Handling:
Hydrochloric acid is extremely corrosive to most of the common metals and
great care should be taken.
Higher concentrations up to just over 40% are chemically possible, but the
evaporation rate is then so high that storage and handling require extra
precautions, such as pressurization and cooling.
These include water treatment chemicals such as iron (III) chloride and
polyaluminium chloride (PAC).
Hydrochloric acid or Muriatic acid
4. pH control and neutralization
Hydrochloric acid can be used to regulate the acidity (pH) of solutions.
Fluorine was discovered by Scheele in 1771, but not isolated until 1886 by H.
Moissan after a period of more than 75 years of intensive effort by many
experimenters.
Aqueous hydrofluoric acid (HF) is used in the glass, metal and petroleum
industries, besides in the manufacture of many inorganic and acid fluorides.
Manufacturing of Hydrofluoric acid (HF)
Hydrofluoric acid (HF)
Both aqueous and anhydrous hydrofluoric acid are prepared in heated kilns by
the following reaction:
CaF2 (fluorspar) + H2SO4 → CaSO4 + 2HF
Aqueous acid is the older product and is formed by adsorbing the HF gases in
lead cooling and absorbing towers.
A large vent pipe conducts the hydrofluoric acid (HF) and other gaseous
products counter currently into sulfuric acid absorption towers for
dehydration.
Uses
Sulphuric acid is the most widely used chemical.
The largest single use of sulphuric acid is for making phosphate and
ammonium sulphate fertilizers.
Manufacturing of Sulphuric acid
Sulphuric acid (H2SO4)
Other uses include
Production of phosphoric acid.
Sulphuric acid is also used in large quantities in iron and steel making as a
pickling agent to remove oxidation, rust and scale from the metals.
Manufacturing process
Two processes, the lead-chamber and contact processes, are used for the
production of sulphuric acid.
In their initial steps, both processes require the use of sulphur dioxide.
Raw Materials and Manufacturing Process
Lead-chamber process
This process employs as reaction vessels large lead-sheathed brick towers.
In these towers, sulphur-dioxide gas, air, steam and oxides of nitrogen react to
yield sulphuric acid as fine droplets that fall to the bottom of the chamber.
Almost all the nitrogen oxides are recovered from the outflowing gas and are brought
back to the chamber to be used again. Sulphuric acid produced in this way is only
about 62 to 70 percent H2SO4, the rest is water.
The Lead chamber process has become obsolete and has been replaced by the contact
process due to the following reasons:
The first plants for contact process (before 1920) were built using platinum
catalysts.
Finely divided platinum, the most effective catalyst, has two disadvantages:
it is very expensive, and it is deactivated by certain impurities in ordinary
sulphur dioxide. They include compounds of arsenic, antimony and lead.
Manufacturing Process
Contact Process
In the middle of 1920s, vanadium catalysts started being used and have since
then replaced platinum.
By 1930, the contact process could compete with the chamber process and
because it produces high strength acid, it has almost replaced the chamber
process.
Flow Chart for Manufacturing of Sulphuric acid
Fig: The flow diagram for sulphuric acid manufacture by the contact process.
Main Steps Involved in Contact Process
Main steps in the plant of contact process are:
Production of sulphur dioxide gas
The combustion unit has a process gas cooler. The SO2 content of the
combustion gases is generally around 18% by volume and the O2 content is
low but higher than 3%.
The gases are generally diluted to 9-12% SO2 before entering the conversion
process.
S (s) + O2 (g) = SO2 (g), ∆H = -298.3 kJ at 25 ⁰C
Main Steps Involved in Contact Process
Conversion of SO2 into SO3
The design and operation of sulphuric acid plants are focused on the following gas phase
chemical reaction in the presence of a catalyst:
2SO2 (g) + O2 (g) = 2SO3 (g), ∆H = -98.3 kJ at 25 ⁰C
From thermodynamic and stoichiometric considerations, the following methods are available
to maximise the formation of SO3 for the O2/SO2/SO3 system:
Heat removal: the formation of SO3 is exothermic, so a decrease of temperature will be
favourable
Increased oxygen concentration
Removal of SO3
Raising the system pressure
Catalyst selection to reduce the working temperature
Longer reaction time
Main Steps Involved in Contact Process
Conditions employed for the conversion of SO2 into SO3
This reaction is a reversible reaction and the conditions used are a
compromise between equilibrium and rate considerations.
It is necessary to shift the position of the equilibrium as far as possible to the right in
order to produce the maximum possible amount of sulphur trioxide in the equilibrium
mixture.
Even though excess O2 would move the SO2 formation to the right, the 1:1 mixture
gives the best possible overall yield of sulphur trioxide (SO3).
In the absence of a catalyst the reaction is quite slow and is therefore carried
out in the presence of a vanadium oxide catalyst which has a long life because
it is not easily poisoned. Further more, vanadium catalyst has high conversion
efficiency.
Fig: Typical diagram of the converter and the multistage reactor for the conversion of SO2 into SO3.
Main Steps Involved in Contact Process
Absorption of SO3
Sulphuric acid (H2SO4) is obtained from the absorption of SO3 into sulphuric
acid with a concentration of at least 98%, followed by the adjustment of the
strength by the controlled addition of water.
SO3 (g) + H2O (l) = H2SO4 (l), ∆H = -130.4 kJ at 25 ⁰C
SO3 will react with water to form sulphuric acid (H2SO4). However,
converting the sulphur trioxide into sulphuric acid cannot be done by simply
adding water to the sulphur trioxide (SO3).
Direct mixing of SO3 with water by the above reaction is uncontrollable. The
exothermic nature of the reaction generates a fog or mist of sulphuric acid,
which is more difficult to work with than a liquid.
Main Steps Involved in Contact Process
Absorption of SO3
Instead, the sulphur trioxide is first dissolved in concentrated (98%) sulphuric acid to
form a product known as fuming sulphuric acid or oleum.
SO3 (g) + H2SO4 (l) = H2S2O7 (l)
The oleum can then be reacted safely with water to produce concentrated sulphuric
acid.
H2S2O7 (l) + H2O (l) = 2H2SO4 (l)
Environmental issues
Sulphuric acid is a constituent of acid rain, formed by atmospheric
oxidation of sulphur dioxide in the presence of water.
Sulphur dioxide is released when fuels containing sulphur such as oil and coal are
burned. The gas escapes into the atmosphere forming sulphuric acid. Sulphuric
acid is also formed naturally by oxidation of sulphide ores.
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