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Heat Exchanger Inspection PDF

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Heat Exchanger Inspection

The Heat Exchanger Inspection article provides you with information about
the inspection of the heat exchanger and heat exchanger testing during the
manufacturing phase, as well as in-service inspection in operating units.

Shell and Tube Heat Exchanger Inspection in Manufacturing Shop

The construction code for shell and tube heat exchangers is ASME Code
Section VIII, and it covers the minimum requirements for design, materials,
fabrication, inspection, testing, and preparation for initial delivery.

After the 2003 addenda of ASME Code Section VIII Div. 1, the design of the
shell and tube heat exchanger needs to be done based on Subsection C, in
UHX part. The design based on TEMA, or any similar code might be
accepted which meeting the requirements of UHX part.

The heat exchanger still is a pressure vessel and all requirements for ASME
pressure vessel does apply for heat exchanger as well. We are going to
avoid to repeat those requirements for the heat exchanger. There are several
inspection requirements that only apply to the heat exchanger and not
regular pressure vessel:

Tube Inspection - The tube outside diameter, inside diameter,


thickness, and ovarlity shall be checked before the building of the
tube bundle. You need to refer to ASME Section II to get the
acceptance tolerances.

For example, if your tube material is SA 179, you have to refer to


the SA 179 and that will refer you to the SA 450 (Specification for
General Requirements for Carbon, Ferritic Alloy, and Austenitic
Alloy Steel Tubes) for acceptance tolerance. You have to use your
caliper, machinist ruler, etc. to make these measurements and
make sure the values fall within acceptance range.

Tube Bundle Inspection - The bundle dimension shall be checked


based on the approved drawing. The baffle diameter and distance
between them shall be controlled and meet the acceptance
tolerances in the drawing.

The tightness of stay bolts and spacers must be controlled. The


shell cleanliness needs to be verified and make sure the inside
welds are complete and are ground as per drawing requirements.

Tube sheet Inspection - The Tube sheet shall be inspected before welding
to the shell. The whole diameter, grooves dimensions, drilling pattern, the
thickness of the tube sheet and surface finish shall be measured and
checked against acceptance tolerances in the approved drawing.

Tube Rolling Inspection - The tube rolling shall be checked based on


customer specification. The wall reduction (after rolling) and depth of roll
shall be measured and shall meet the customer specification. The wall
reduction should not be less than 5% and should not be more than 8% of the
tube wall thickness.

Leak Testing of Seal Weld (Tube to Tube sheet) - if seal welding


considered, then the leak test will be a mandatory requirement. The shell
side will be subjected to the air pressure, and water and soap solution will be
sprayed to the tube sheet to make sure all seal welds are defect free. The
bubble will be developed if there was any welding defect such as crack,
pinhole, etc.

Shell side Hydrostatic Testing - After manufacturing completion, the heat


exchange shell side will be subjected to the hydrostatic testing. The test
pressure amount shall be consistent with the value indicated in the approved
drawing. The holding time shall be based on the supplier approved test
procedure.

The pressure gages calibration and range shall be controlled. The pressure
gage range shall be within 1.5 thru 4 times of test pressure. The shell body
and welding seams shall be inspected. The tube sheet also shall be checked.
No leakage is allowed.
The test pump hose shall be disconnected, and no pressure drop is allowed.
The test result will be satisfactory if no leakage being observed and no
pressure being dropped while the shell side was under pressure.

Tubeside Hydrostatic Testing - After successful completion of shell side


hydrostatic testing, the bonnets are assembled, and tube side is subjected
to hydrostatic testing. Similarly, the amount of test pressure shall be as the
one indicated in the approved drawing. Other requirement is similar to the
shell test. No leakage and pressure drop shall be observed while the tube
side is under pressure.

Shell and Tube Heat Exchanger Application

Shell and Tube heat exchangers are the most popular type in the industry.
This type is made from 3 components as listed below:

 Two heads (one rear head, and the other one stationary head)
 Shell
 Tube

One fluid is in the tube side and the other one in the shell side. The heat
transfer is done through the tube wall.

So your heat exchanger with more tubes will have more heat transfer
surfaces, and at the same time will have a higher heat exchanger diameter.

There are different kinds of shell and tube heat exchangers with different
applications. The reason for the high amount of applications is that they are
easy to maintain.

Besides, the shell and tube heat exchanger is the only type that can be
designed and operated at a temperature greater than 360 degrees
centigrade, as well as in pressure higher than 30 bar.
In-Service Inspection of Shell and Tube Heat Exchanger

The In-Service Inspection code for shell and tube heat exchangers is API
STD 510. The other API recommended practices and codes also have to be
used in with this Code.

Some of these Recommended Practices are API RP 572, API RP 577, and
API RP 571, and also construction code sections might be used, such as
ASME Code Section VIII and ASME Code Section IX.

For repair, the requirement of API STD 510 or ASME-PCC-2 needs to be


met. The title of ASME-PCC-2, which was first published in 2006, is: “Repair
of Pressure Equipment and Piping.”

Please note: if your shell and tube heat exchanger is “U” stamped and you
need to do the repair, you have to use a Repair Organization holding an “R”
Stamp from the National Board Inspection Code.

The API 510 Pressure Vessel Inspectors are qualified persons to perform
shell and tube heat Exchanger inspection.

What are the Important Items in the Shell and Tube Heat Exchanger
Inspection in Overhaul?
Shell and Tube Heat Exchanger Inspections are categorized in the following way:

Shell and Structure in Heat Exchanger Inspection:


 Neutralization of Austenitic Stainless Steel shell, clads, liner or weld
overlay, which contains H2S service. The process needs to be done
based on approved procedures by a corrosion engineer.
 Neutralization is also required for shell material with admiralty brass
to reduce the risk of SCC.
 Neutralization of thermocouples, if necessary, and doing dye
penetration test
 Sampling from shell fouling and corrosion products and making lab
analysis and making interpretation by corrosion engineer (if
necessary)
 Cutting small area of insulation sheet and removing the insulation and
doing visual inspection for any sign of corrosion under insulation
 Thickness measurement of different parts of shell and shell nozzles
and making corrosion rate and remaining life calculation
 Inspection of shell cleaning and approval i.e. water jetting etc.
 Checking inside surface for any cladding, liner failure or separation
 Inspection of Shell flange gasket seating area for any erosion,
damage and cracking
 Inspection of longitudinal and circumferential weld joints, inlet and
outlet nozzles, reinforcement pads and small bore connections for
any crack, corrosion and mechanical damage and deformation
 Dye penetration test on weld joints that are susceptible to cracking,
austenitic flange face, weld overlay and cladding surface and
exchangers exposed to amine and caustic
 Hydrogen blistering inspection in hydrogen services (hand lamp
procedure)
 Heat exchanger support, steel structure, foundation, bolt and nut
inspection

Bonnet in Heat Exchanger Inspection

 Thickness measurement and making corrosion rate and remaining life calculation
 Girth flange inspection for corrosion and erosion
 Internal surface inspection for corrosion and fouling
 Painting inspection of external surface
 Dye penetration or magnetic particle examination of weld joints susceptible to
cracking

Tube Bundle in Heat Exchanger Inspection

 Taking care in the pulling out of tube bundle to avoid any mechanical
damage
 Sampling from tube side fouling and corrosion products and making
lab analysis and making interpretation by corrosion engineer (if
necessary)
 Controlling of water jetting or lancing cleaning process
 Controlling wire brushing process of inner tube edge and rolling area
(preparation for ID measurement)
 Inside diameter measurement in tubes and tubes rolling areas
 Rate off and accordingly plugging the tubes when their OD reaches to
the ID plus one thickness
 Retubing of tube bundle if more than 10% of tubes reach the above
rejection limit
 Inspection from tube bundle components such as tubesheet, tube, tie
rods and spacers, transfer baffles or support plate, impingement baffle,
floating head flange and floating head backing device
 Inspection from internal surface of tubes for corrosion and fouling
 Pulling out a sample tube for sectioning and corrosion anlaysis if
necessary
 Retubing when sectioning result proves the thickness is half of the
nominal value
 Visual inspection and dye penetration test from tube to tubesheet seal
or strength weld
 Eddy current testing if it is necessary
Channel in Heat Exchanger Inspection

 Thickness measurement and making corrosion rate and remaining life


calculation
 Inspection of gasket seating area, pass partition and nubbing for
corrosion and deformation
 Inspection of internal surface for fouling, corrosion and soundness of
linings (if any)
 Balance hole inspection for corrosion and erosion
 Welding joints inspection for any possible cracks
 Reinforcement pad inspection and doing soap test if necessary
 Cathodic protection anodes inspection and replacement if necessary
 Diaphragm and division box visual inspection and dye penetration test
of diaphragm for any possible cracks (for high pressure exchangers)

Channel Cover in Heat Exchanger Inspection

 Thickness measurement and making corrosion rate and remaining


life calculation
 Inspection of gasket seating area for corrosion and deformation
 Inspection for internal surface for fouling, liner, cladding and coating
soundness
 Soap test in channel cover with liner
 Lifting lug weld joint inspection for any possible crack

Floating Head Inspection:

 Thickness measurement and making corrosion rate and remaining life


calculation
 Inspection of gasket seating area, pass partition and nubbing for any
possible corrosion and deformation
 Girth flange weld joint inspection for any possible crack and corrosion
 Internal surface inspection for corrosion and fouling and soundness of
liner, coating and cladding (if any)

Expansion Joint Inspection


 The heat exchangers with expansion joints need to be inspected for:
 Flange inspections for corrosion and erosion
 Inspection from internal surface for corrosion and erosion
 Air test
 The tube and shell hydrostatic test need to be done after the above stated
inspection activities.

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