Inflection Point Engineering Heat Exchanger Engineering Curriculum

S and T

Module from the Heat Exchanger Engineering Curriculum curriculum.

Module 2 - TEMA Shell and Tube Types · Learning Objectives · 1. Decode TEMA 3-letter designation (front head / shell / rear head) · 2. Select TEMA Class R (refinery), C (commercial), B (chemical) · 3. Choose shell type (E, F, J, G, H, K, X) by service · 4. Choose head type by thermal growth and cleaning requirements · 5. Apply fixed, U-tube, floating head, pull-through, or packed head · TEMA Shell Types

Type Name Passes Typical Use Pressure Drop Note
E One-pass shell 1 shell / 1 or 2 tube Most common Moderate Standard
F Two-pass shell longitudinal baffle 2 shell / 2 or 4 tube Large LMTD correction Moderate Leakage concerns
J Divided flow 1 shell / 2 tube Low dP, vacuum Low Used for vacuum towers overhead
G Split flow 1 shell Horizontal thermosyphon Low Horizontal reboiler
H Double split flow 1 shell Large horizontal thermosyphon Very low Large unit
K Kettle reboiler 1 shell Reboiler with vapor space Very low Bubbling service
X Cross flow 1 shell Low dP cooling Very low Inlet/outlet distributors
TEMA Head Types
Type Function Accessible Thermal Growth Cost Use
A Bonnet (integral flange) No (remove bolted cover) Fixed Low Cleanable front
B Bonnet one-piece No Fixed Low Non-fouling front
C Channel integral tubesheet No Fixed Medium Removable bundle
N Channel integral with shell No Fixed Low Not removable
L Fixed tubesheet No None - must PWHT Low Dirty shell
M Fixed tubesheet bonnet No None Low Cheap fixed
P Outside packed floating head Limited High High Large thermal
S Floating head with backing device Yes High High Most common
T Pull-through floating head Yes High Medium Easy pull
U U-tube bundle Front only High Low Cleaning shell-side only

Source: Heat_Exchanger_Engineering_Curriculum_v1.xlsx · Sheet: S and T