Heat Exchanger Inspection PDF
Heat Exchanger Inspection PDF
Heat Exchanger Inspection PDF
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.
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 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.
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.
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.
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:
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
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