Navigation by alphabet
A B C D E F G H I J K L M N O P Q R S T U V W X Y Z
Absorbing media, interaction phenomena in,
Absorption of thermal radiation:
Absorption coefficient,
Absorption spectra in gases,
Absorptivity:
Acentric factor:
Acetaldehyde:
Acetic acid:
Acetic anhydride:
Acetone:
Acetonitrile:
Acetophenone:
Acetylene:
Acetylenes
Ackerman correction factor in condensation,
Acoustic methods, for fouling mitigation,
Acoustic vibration of heat exchangers,
Acrolein:
Acrylic acid:
Active systems for augmentation of heat transfer:
Additives:
Adiabatic flows, compressible, in duct,
Admiralty brass,
Advanced models for furnaces,
Agitated beds, heat transfer to,
Agitated vessels,
Ahmad scaling method for critical heat flux in flow boiling of nonaqueous fluids,
Air:
Air-activated gravity conveyor,
Air-cooled heat exchangers:
Air preheaters, fouling in,
Albedo for single scatter in radiation,
Alcohols:
Aldehydes:
Aldred, D L,
Allyl alcohol:
Allyl chloride (-chloropropane)
Alternating direction (ADR) method, for solution of implicit finite difference equations,
Aluminum, spectral characteristics of anodized surfaces,
Aluminum alloys, thermal and mechanical properties,
Aluminium brass,
Ambrose-Walton corresponding states method, for vapour pressure,
Amides:
Amines:
Ammonia:
tert-Amyl alcohol:
Analogy between heat and mass and momentum transfer
Analytical solution of groups, for calculation of thermodynamic
Anelasticity,
Angled tubes, use in increasing flooding rate in reflux condensation,
Aniline:
Anisotropy of elastic properties,
Annular distributor in shell-and-tube heat exchangers,
Annular ducts:
Annular (radial) fins, efficiency
Annular flow (gas-liquid):
Annular flow (liquid-liquid),
Annular flow (liquid-liquid-gas),
Anti-foulants,
Antoine equation, for vapour pressure,
Aqueous solutions, as heat transfer media,
Arc welding of tubes into tube sheets:
Archimedes number,
Area of tube outside surface in shell-and-tube heat exchangers:
Argon:
Arithmetic mean temperature difference, definition,
Armstrong, Robert C
Aromatics:
ASME VIII code, for mechanical design of shell-and-tube heat exchangers:
Assisted convection:
Attachment, of fouling layers,
Augmentation of heat transfer
Augmentation of Heat Transfer
Condensation Enhancement
Augmentation of Boiling and Evaporation
active systems for:
entropy generation in,
in boiling,
in condensation,
in kettle reboilers,
in microfluidic systems,
nanoparticles for,
passive systems for:
phase change materials for,
in shell-and-tube heat exchangers using low finned tubes,
system impact of,
Austenitic stainless steels,
Average phase velocity in multiphase flows,
Axial flow reboilers,
Axial wire attachments, for augmentation of condensation,
Azeotropes, condensation of
Index
HEDH
A
Absorbing media, interaction phenomena in,
Absorption of thermal radiation:
Absorption coefficient,
Absorption spectra in gases,
Absorptivity:
Acentric factor:
Acetaldehyde:
Acetic acid:
Acetic anhydride:
Acetone:
Acetonitrile:
Acetophenone:
Acetylene:
Acetylenes
Ackerman correction factor in condensation,
Acoustic methods, for fouling mitigation,
Acoustic vibration of heat exchangers,
Acrolein:
Acrylic acid:
Active systems for augmentation of heat transfer:
Additives:
Adiabatic flows, compressible, in duct,
Admiralty brass,
Advanced models for furnaces,
Agitated beds, heat transfer to,
Agitated vessels,
Ahmad scaling method for critical heat flux in flow boiling of nonaqueous fluids,
Air:
Air-activated gravity conveyor,
Air-cooled heat exchangers:
Air preheaters, fouling in,
Albedo for single scatter in radiation,
Alcohols:
Aldehydes:
Aldred, D L,
Allyl alcohol:
Allyl chloride (-chloropropane)
Alternating direction (ADR) method, for solution of implicit finite difference equations,
Aluminum, spectral characteristics of anodized surfaces,
Aluminum alloys, thermal and mechanical properties,
Aluminium brass,
Ambrose-Walton corresponding states method, for vapour pressure,
Amides:
Amines:
Ammonia:
tert-Amyl alcohol:
Analogy between heat and mass and momentum transfer
Analytical solution of groups, for calculation of thermodynamic
Anelasticity,
Angled tubes, use in increasing flooding rate in reflux condensation,
Aniline:
Anisotropy of elastic properties,
Annular distributor in shell-and-tube heat exchangers,
Annular ducts:
Annular (radial) fins, efficiency
Annular flow (gas-liquid):
Annular flow (liquid-liquid),
Annular flow (liquid-liquid-gas),
Anti-foulants,
Antoine equation, for vapour pressure,
Aqueous solutions, as heat transfer media,
Arc welding of tubes into tube sheets:
Archimedes number,
Area of tube outside surface in shell-and-tube heat exchangers:
Argon:
Arithmetic mean temperature difference, definition,
Armstrong, Robert C
Aromatics:
ASME VIII code, for mechanical design of shell-and-tube heat exchangers:
Assisted convection:
Attachment, of fouling layers,
Augmentation of heat transfer
B
C
D
E
F
G
H
I
J
K
L
M
N
O
P
Q
R
S
T
U
V
W
X
Y
Z
Augmentation of Heat Transfer
Condensation Enhancement
Augmentation of Boiling and Evaporation
active systems for:
entropy generation in,
in boiling,
in condensation,
in kettle reboilers,
in microfluidic systems,
nanoparticles for,
passive systems for:
phase change materials for,
in shell-and-tube heat exchangers using low finned tubes,
system impact of,
Austenitic stainless steels,
Average phase velocity in multiphase flows,
Axial flow reboilers,
Axial wire attachments, for augmentation of condensation,
Azeotropes, condensation of
Download the citation in the EndNote formatOpen in a new tab.
Download the citation in the RefWorks formatOpen in a new tab.
Download the citation in the BibTex formatOpen in a new tab.
Extension of the Method to Other Shell, Baffle and Tube Bundle Geometries
DOI 10.1615/hedhme.a.000257
3.3.11 Extension of the method to other shell, baffle, and tube bundle geometries
Jerry Taborek
The Delaware method, as originally developed and on which the method presented here is based, is more or less explicitly confined to the design of fully-tubed E-shell configurations using plain tubes. However, there are many process reasons-better balance required between the shell-side and the tube-side heat transfer coefficients, vibration problems, more effective use of available shell-side pressure drop in low-pressure-drop cases, etc. — that lead to the importance of applying the method to variant configurations.
The most important alternative geometries and how the method can be adapted to them are dealt with in this section. However, only a few can be described explicitly at this time. Others are explained only qualitatively, as additional correlational work is necessary. It is foreseen that these will be included in a forthcoming supplement.
For detailed description of the various shell and bundle geometries, refer to Section 4.2.
A. Divided flow, TEMA J shell
A diagramatic sketch of this arrangement is shown in Figure 1 with a single inlet nozzle and two outlet nozzles.
... You need a subscriptionOpen in a new tab. to view the full text of the article. If you already have the subscription, please login here
© 2024 by Begell House, Inc.