Hydrocarbon Processing - November 2022 - 59

Heat Transfer
ed to repeat the analysis for higher shell
thickness (SCH 80S) to check whether
the increase in thickness coulc bring the
induced stresses within allowable limits.
For Load Case 1 for the SCH 80S
thick shell: The stress analysis was carried
out considering allowable stresses at
a design temperature of 690°C for both
the shell and inlet and outlet nozzles.
* The primary membrane stresses
for Sustained loads are tabulated in
TABLE 7, and the calculated stresses
are within the allowable limit.
* The primary membrane stresses
for Thermal loads are tabulated
in TABLE 8.
° The primary membrane stresses
at inlet the shell and inlet nozzle
are ~234% and ~239% of
allowable limits, respectievly.
° The primary membrane
stresses at the outlet shell
and outlet nozzle are within
allowable limits.
* The primary membrane stresses,
secondary membrane and bending
stresses, and fatigue stresses for
Occasional load are tabulated
in TABLE 9.
° The primary membrane stresses
at the inlet shell and inlet
nozzle are ~282% and ~286% of
allowable limits, respectively.
° The primary membrane
stresses at the outlet shell
and outlet nozzle are within
allowable limits.
° The secondary membrane and
bending stresses at the inlet and
outlet shells and nozzles are
within allowable limits.
° The fatigue stresses at the
inlet and outlet shells and inlet
and outlet nozzles are within
allowable limits.
The shell and nozzle failed with the
SCH 80S thickness, as well. Any further
increase in shell thickness to bring the
induced stress within allowable limits
could not be considred since the heater
supplier informed that any increase in
pipe schedule above 80S will result in
the shell's inside diameter becoming
smaller than the bundle diameter.
For Load Case 2 for the SCH 40S
thick shell: The stress analysis was carried
out considering the allowable stress
at an operating temperature of 130°C at
the inlet and 649°C at the outlet for both
shell and nozzles.
* The primary membrane stresses
for Sustained loads are tabulated
in TABLE 10. The calculated stresses
are within the allowable limits.
* The primary membrane stresses
for Thermal loads are tabulated in
TABLE 11. The calculated stresses at
the inlet and outlet shells, and the
inlet and outlet nozzles are within
the allowable limits.
FIG. 16. Load Case 2 (Occasional): Fatigue
stresses at the inlet and outlet for SCH 40S.
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MODERATOR: Lee Nichols
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Hydrocarbon Processing
Hydrocarbon Processing | NOVEMBER 2022 59
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Hydrocarbon Processing - November 2022

Table of Contents for the Digital Edition of Hydrocarbon Processing - November 2022

Industry Perspectives
Editorial Comment
Construction
Innovations
Digital Technologies
Optimization of ethylene in the processing of hydrocarbons
Shift focus to more open control technology
Integrated remote operations drive collaboration and autonomy
Reliability analysis of analyzers bridges the gap between assessing and addressing risk
Implement advanced level control techniques to improve crude distillation unit stabilizer performance
Leading capital projects in a VUCA environment
Trip your turbine troubles: Optimize the reliability of steam-driven turbines
Development of novel epoxy closed-cell foam for personnel and corrosion protection—Part 2
Obsolescence management in a manufacturing unit
Decarbonizing your fired heaters with hydrogen fuel
Mechanical design challenges in high-temperature electric heaters
Why sulfur plants fail: An in-depth study of sulfur recovery unit failures—Part 2
Advertiser Index
Hydrocarbon Processing - November 2022 - 1
Hydrocarbon Processing - November 2022 - 2
Hydrocarbon Processing - November 2022 - 3
Hydrocarbon Processing - November 2022 - Industry Perspectives
Hydrocarbon Processing - November 2022 - 5
Hydrocarbon Processing - November 2022 - 6
Hydrocarbon Processing - November 2022 - Editorial Comment
Hydrocarbon Processing - November 2022 - 8
Hydrocarbon Processing - November 2022 - 9
Hydrocarbon Processing - November 2022 - Construction
Hydrocarbon Processing - November 2022 - 11
Hydrocarbon Processing - November 2022 - Innovations
Hydrocarbon Processing - November 2022 - 11B
Hydrocarbon Processing - November 2022 - 12
Hydrocarbon Processing - November 2022 - Digital Technologies
Hydrocarbon Processing - November 2022 - 14
Hydrocarbon Processing - November 2022 - 15
Hydrocarbon Processing - November 2022 - 16
Hydrocarbon Processing - November 2022 - Optimization of ethylene in the processing of hydrocarbons
Hydrocarbon Processing - November 2022 - 18
Hydrocarbon Processing - November 2022 - 19
Hydrocarbon Processing - November 2022 - 20
Hydrocarbon Processing - November 2022 - Shift focus to more open control technology
Hydrocarbon Processing - November 2022 - 22
Hydrocarbon Processing - November 2022 - 23
Hydrocarbon Processing - November 2022 - 24
Hydrocarbon Processing - November 2022 - Integrated remote operations drive collaboration and autonomy
Hydrocarbon Processing - November 2022 - 26
Hydrocarbon Processing - November 2022 - 27
Hydrocarbon Processing - November 2022 - 28
Hydrocarbon Processing - November 2022 - 29
Hydrocarbon Processing - November 2022 - 30
Hydrocarbon Processing - November 2022 - Reliability analysis of analyzers bridges the gap between assessing and addressing risk
Hydrocarbon Processing - November 2022 - 32
Hydrocarbon Processing - November 2022 - 33
Hydrocarbon Processing - November 2022 - Implement advanced level control techniques to improve crude distillation unit stabilizer performance
Hydrocarbon Processing - November 2022 - 35
Hydrocarbon Processing - November 2022 - 36
Hydrocarbon Processing - November 2022 - Leading capital projects in a VUCA environment
Hydrocarbon Processing - November 2022 - 38
Hydrocarbon Processing - November 2022 - Trip your turbine troubles: Optimize the reliability of steam-driven turbines
Hydrocarbon Processing - November 2022 - 40
Hydrocarbon Processing - November 2022 - 41
Hydrocarbon Processing - November 2022 - 42
Hydrocarbon Processing - November 2022 - 43
Hydrocarbon Processing - November 2022 - 44
Hydrocarbon Processing - November 2022 - 45
Hydrocarbon Processing - November 2022 - 46
Hydrocarbon Processing - November 2022 - Development of novel epoxy closed-cell foam for personnel and corrosion protection—Part 2
Hydrocarbon Processing - November 2022 - 48
Hydrocarbon Processing - November 2022 - 49
Hydrocarbon Processing - November 2022 - 50
Hydrocarbon Processing - November 2022 - Obsolescence management in a manufacturing unit
Hydrocarbon Processing - November 2022 - 50B
Hydrocarbon Processing - November 2022 - Decarbonizing your fired heaters with hydrogen fuel
Hydrocarbon Processing - November 2022 - 52
Hydrocarbon Processing - November 2022 - 53
Hydrocarbon Processing - November 2022 - 54
Hydrocarbon Processing - November 2022 - Mechanical design challenges in high-temperature electric heaters
Hydrocarbon Processing - November 2022 - 56
Hydrocarbon Processing - November 2022 - 57
Hydrocarbon Processing - November 2022 - 58
Hydrocarbon Processing - November 2022 - 59
Hydrocarbon Processing - November 2022 - 60
Hydrocarbon Processing - November 2022 - Why sulfur plants fail: An in-depth study of sulfur recovery unit failures—Part 2
Hydrocarbon Processing - November 2022 - 62
Hydrocarbon Processing - November 2022 - 63
Hydrocarbon Processing - November 2022 - 64
Hydrocarbon Processing - November 2022 - 65
Hydrocarbon Processing - November 2022 - Advertiser Index
Hydrocarbon Processing - November 2022 - 67
Hydrocarbon Processing - November 2022 - 68
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