Request a Trial or Demo
Access & Subscription Policy
Privacy Policy
Begell Digital Portal
Open in a new tab.
Heat Exchanger
Design Handbook
Subscription:
Guest
Home
About HEDH Multimedia
Editorial Board
Index
Content Map
HEDH Widgets
My HEDH
Content Map
HEDH
A
B
C
D
E
E-type shells in shell-and-tube heat exchangers:
Ebert and Panchal equation, for crude oil fouling,
Eckert number,
Eddy viscosity:
Eddy diffusivity, of heat,
Edge, D,
Edwards, D K
EEC code for thermal design of heat exchangers,
Effective diffusivity,
Effective thermal conductivity of fixed beds,
Effective tube length in shell-and-tube heat exchangers,
Effectiveness of a heat exchanger:
Efficiency of fins,
Eicosane:
Eicosene:
Ejectors, in flash distillation plant,
EJMA (Expansion Joint Manufacturers Association), standards for expansion bellows
Elastic properties of solids:
El-Dessouky, H,
Electrical enhancement processes, in heat transfer augmentation,
Electric fields, effect on properties of rheologically complex materials,
Electric fields, in augmentation of condensation,
Electrical process heater, specification of,
Electrokinetics, for heat transfer augmentation in microfluidic systems,
Electromagnetic theory of radiation,
Electrostatic fields in augmentation of heat transfer,
Elements:
Elhadidy relation between heat and momentum transfer,
Embedding methods for radiative heat transfer in nonisothermal gases,
Embittlement, of stainless steels,
Emission of thermal radiation, in solids,
Emissivity:
Emitting media, interaction phenomena with,
Emulsions, viscosity of,
EN13445 (European Pressure Vessel Codes), design of heat exchangers to,
Shell-and-Tube Heat Exchanger Design to EN13445
It's an article
basis for design with,
bellows, shell,
brittle fracture,
cones under internal pressure,
cylinders and spheres under internal pressure,
design by formula,
dished heads under internal pressure,
external pressure,
fatigue,
flat ends,
floating head components,
girth flanges,
Shell-and-Tube Heat Exchanger Design to EN13445
It's an article
alternative rules for,
comparison of EN13445 method with original Taylor Forge method,
lap jointed,
with full face gaskets,
gross plastic deformation,
inspection,
limpet coils,
materials of construction in,
nozzles,
pipe loads (on nozzles and attachments),
pressure testing,
progressive plastic deformation,
saddle supports,
safety factors in,
specification of duty in,
tolerances,
tubesheets and tubes,
vessels of rectangular cross section,
welds,
Enclosures:
Energy equation:
Energy recovery, maximum, in heat exchanger network design,
Enhanced surfaces, fouling in,
Enhancement devices:
Enlargements in pipes:
Enthalpy:
Entrainment in annular gas-liquid flow
Entrance effects in heat and mass transfer:
Entrance lengths, hydrodynamic in pipe flow,
Entrance losses for tube inlet in shell-and-tube heat exchanger,
Entry losses in plate heat exchangers,
Entropy generation and minimisation
Environmental impact, of fouling,
Eotvos number:
Epstein, N,
Epstein matrix, for fouling,
Equalizing rings, for expansion bellows,
Equilibrium interphase:
Equilibrium vapor nucleus,
Equivalent sand roughness,
Ergun equation, for pressure drop in fixed beds
ESDU correlations:
Esters:
Ethane:
Ethanol:
Ethers:
Ethyl acetate:
Ethylacetylene:
Ethylacrylate:
Ethylamine:
Ethylbenzene:
Ethyl benzoate:
Ethyl butanoate:
Ethylcyclohexane:
Ethylcyclopentane:
Ethyl formate:
Ethylene:
Ethylene diamine:
Ethylene glycol:
Ethylene oxide:
Ethylmercaptan:
1-Ethylnaphthalene:
2-Ethylnaphthalene:
Ethyl proprionate:
Ethyl propylether:
Ettouney, H,
Euler number:
Eutectic mixtures, condensation of forming immiscible liquids,
Evaporation:
Evaporative crystallisers,
Evaporators:
Exergy, definition of,
Exergy analysis,
Exit losses for tubes in shell-and-tube exchanger,
Expansion bellows, for shell-and-tube heat exchangers:
EJMA (Expansion Joint Manufacturers Association), standards for
Expansion joints, mechanical design of:
Expansion of tubes into tube sheets:
Expansion turbine, lost work in,
Explosively clad plate,
Explosive welding of tubes into tube sheets
Explosive expansion joints,
Extended surfaces (see also Fins)
Externally induced convection, in kettle reboilers,
Extinction coefficient,
Extinction efficiency,
Eyring fluid (non-Newtonian),
F
G
H
I
J
K
L
M
N
O
P
Q
R
S
T
U
V
W
X
Y
Z
Z
Y
X
W
V
U
T
S
R
Q
P
O
N
M
L
K
J
I
H
G
F
Eyring fluid
(non-Newtonian),
Extinction efficiency,
Extinction coefficient,
Externally induced
convection, in kettle
reboilers,
Extended surfaces
(see also Fins)
Explosive expansion
joints,
Explosive welding of
tubes into tube sheets
Explosively clad plate,
Expansion turbine,
lost work in,
Expansion of tubes
into tube sheets:
Expansion joints,
mechanical design of:
EJMA (Expansion Joint
Manufacturers
Association),
standards for
Expansion bellows, for
shell-and-tube heat
exchangers:
Exit losses for tubes in
shell-and-tube
exchanger,
Exergy analysis,
Exergy, definition of,
Evaporators:
Evaporative
crystallisers,
Evaporation:
Eutectic mixtures,
condensation of
forming immiscible
liquids,
Euler number:
Ettouney, H,
Ethyl propylether:
Ethyl proprionate:
2-Ethylnaphthalene:
1-Ethylnaphthalene:
Ethylmercaptan:
Ethylene oxide:
Ethylene glycol:
Ethylene diamine:
Ethylene:
Ethyl formate:
Ethylcyclopentane:
Ethylcyclohexane:
Ethyl butanoate:
Ethyl benzoate:
Ethylbenzene:
Ethylamine:
Ethylacrylate:
Ethylacetylene:
Ethyl acetate:
Ethers:
Ethanol:
Ethane:
Esters:
ESDU correlations:
Ergun equation, for
pressure drop in fixed
beds
Equivalent sand
roughness,
Equilibrium vapor
nucleus,
Equilibrium
interphase:
Equalizing rings, for
expansion bellows,
Epstein matrix, for
fouling,
Epstein, N,
Eotvos number:
Environmental
impact, of fouling,
Entropy generation
and minimisation
Entry losses in plate
heat exchangers,
Entrance losses for
tube inlet in
shell-and-tube heat
exchanger,
Entrance lengths,
hydrodynamic in pipe
flow,
Entrance effects in
heat and mass
transfer:
Entrainment in
annular gas-liquid flow
Enthalpy:
Enlargements in
pipes:
Enhancement
devices:
Enhanced surfaces,
fouling in,
Energy recovery,
maximum, in heat
exchanger network
design,
Energy equation:
Enclosures:
welds,
vessels of rectangular
cross section,
tubesheets and tubes,
tolerances,
specification of duty
in,
safety factors in,
saddle supports,
progressive plastic
deformation,
pressure testing,
pipe loads (on nozzles
and attachments),
nozzles,
materials of
construction in,
limpet coils,
inspection,
gross plastic
deformation,
with full face gaskets,
lap jointed,
comparison of
EN13445 method with
original Taylor Forge
method,
alternative rules for,
Shell-and-Tube Heat
Exchanger Design to
EN13445
girth flanges,
floating head
components,
flat ends,
fatigue,
external pressure,
dished heads under
internal pressure,
design by formula,
cylinders and spheres
under internal
pressure,
cones under internal
pressure,
brittle fracture,
bellows, shell,
basis for design with,
Shell-and-Tube Heat
Exchanger Design to
EN13445
EN13445 (European
Pressure Vessel
Codes), design of heat
exchangers to,
Emulsions, viscosity
of,
Emitting media,
interaction
phenomena with,
Emissivity:
Emission of thermal
radiation, in solids,
Embittlement, of
stainless steels,
Embedding methods
for radiative heat
transfer in
nonisothermal gases,
Elhadidy relation
between heat and
momentum transfer,
Elements:
Electrostatic fields in
augmentation of heat
transfer,
Electromagnetic
theory of radiation,
Electrokinetics, for
heat transfer
augmentation in
microfluidic systems,
Electrical process
heater, specification
of,
Electric fields, in
augmentation of
condensation,
Electric fields, effect
on properties of
rheologically complex
materials,
Electrical
enhancement
processes, in heat
transfer
augmentation,
El-Dessouky, H,
Elastic properties of
solids:
EJMA (Expansion Joint
Manufacturers
Association),
standards for
expansion bellows
Ejectors, in flash
distillation plant,
Eicosene:
Eicosane:
Efficiency of fins,
Effectiveness of a
heat exchanger:
Effective tube length
in shell-and-tube heat
exchangers,
Effective thermal
conductivity of fixed
beds,
Effective diffusivity,
EEC code for thermal
design of heat
exchangers,
Edwards, D K
Edge, D,
Eddy diffusivity, of
heat,
Eddy viscosity:
Eckert number,
Ebert and Panchal
equation, for crude oil
fouling,
E-type shells in
shell-and-tube heat
exchangers:
E
D
C
B
A
HEDH
Popular Articles
Shell-and-Tube Heat Exchanger Design to EN13445
Subscriber Login
Login via your home institution
Login
Add to Citation Manager
Download the citation in the EndNote format
Download the citation in the RefWorks format
Download the citation in the BibTex format