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Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
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Industry
CPC
F25J1/00
This industry / category may be too specific. Please go to a parent level for more data
Parent Industries
F
MECHANICAL ENGINEERING LIGHTING HEATING WEAPONS BLASTING ENGINES OR PUMPS
F25
Refrigeration
F25J
LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
Current Industry
F25J1/00
Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
Sub Industries
F25J1/0002
characterised by the fluid to be liquefied
F25J1/0005
Light or noble gases
F25J1/0007
Helium
F25J1/001
Hydrogen
F25J1/0012
Primary atmospheric gases
F25J1/0015
Nitrogen
F25J1/0017
Oxygen
F25J1/002
Argon
F25J1/0022
Hydrocarbons
F25J1/0025
Boil-off gases "BOG" from storages
F25J1/0027
Oxides of carbon
F25J1/003
characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
F25J1/0032
using the feed stream itself or separated fractions from it
F25J1/0035
by gas expansion with extraction of work
F25J1/0037
of a return stream
F25J1/004
by flash gas recovery
F25J1/0042
by liquid expansion with extraction of work
F25J1/0045
by vaporising a liquid return stream
F25J1/0047
using an "external" refrigerant stream in a closed vapor compression cycle
F25J1/005
by expansion of a gaseous refrigerant stream with extraction of work
F25J1/0052
by vaporising a liquid refrigerant stream
F25J1/0055
originating from an incorporated cascade
F25J1/0057
after expansion of the liquid refrigerant stream with extraction of work
F25J1/006
characterised by the refrigerant fluid used
F25J1/0062
Light or noble gases, mixtures thereof
F25J1/0065
Helium
F25J1/0067
Hydrogen
F25J1/007
Primary atmospheric gases, mixtures thereof
F25J1/0072
Nitrogen
F25J1/0075
Oxygen
F25J1/0077
Argon
F25J1/008
Hydrocarbons
F25J1/0082
Methane
F25J1/0085
Ethane; Ethylene
F25J1/0087
Propane; Propylene
F25J1/009
Hydrocarbons with four or more carbon atoms
F25J1/0092
Mixtures of hydrocarbons comprising possibly also minor amounts of nitrogen
F25J1/0095
Oxides of carbon
F25J1/0097
Others
F25J1/02
requiring the use of refrigeration
F25J1/0201
using only internal refrigeration means
F25J1/0202
in a quasi-closed internal refrigeration loop
F25J1/0203
using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle (not used)
F25J1/0204
as a single flow SCR cycle
F25J1/0205
as a dual level SCR refrigeration cascade
F25J1/0207
as at least a three level SCR refrigeration cascade
F25J1/0208
in combination with an internal quasi-closed refrigeration loop
F25J1/0209
as at least a three level refrigeration cascade
F25J1/021
using a deep flash recycle loop
F25J1/0211
using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle
F25J1/0212
as a single flow MCR cycle
F25J1/0214
as a dual level refrigeration cascade with at least one MCR cycle
F25J1/0215
with one SCR cycle
F25J1/0216
using a C3 pre-cooling cycle
F25J1/0217
as at least a three level refrigeration cascade with at least one MCR cycle
F25J1/0218
with one or more SCR cycles
F25J1/0219
in combination with an internal quasi-closed refrigeration loop
F25J1/0221
using the cold stored in an external cryogenic component in an open refrigeration loop
F25J1/0222
in combination with an intermediate heat exchange fluid between the cryogenic component and the fluid to be liquefied
F25J1/0223
in combination with the subsequent re-vaporisation of the originally liquefied gas at a second location to produce the external cryogenic component
F25J1/0224
in combination with an internal quasi-closed refrigeration loop
F25J1/0225
using other external refrigeration means not provided before
F25J1/0227
within a refrigeration cascade
F25J1/0228
Coupling of the liquefaction unit to other units or processes, so-called integrated processes
F25J1/0229
Integration with a unit for using hydrocarbons
F25J1/023
for the combustion as fuels
F25J1/0231
for the working-up of the hydrocarbon feed
F25J1/0232
integration within a pressure letdown station of a high pressure pipeline system
F25J1/0234
Integration with a cryogenic air separation unit
F25J1/0235
Heat exchange integration
F25J1/0236
providing refrigeration for different processes treating not the same feed stream
F25J1/0237
integrating refrigeration provided for liquefaction and purification/treatment of the gas to be liquefied
F25J1/0238
Purification or treatment step is integrated within one refrigeration cycle only
F25J1/0239
Purification or treatment step being integrated between two refrigeration cycles of a refrigeration cascade
F25J1/0241
wherein the overhead cooling comprises providing reflux for a fractionation step
F25J1/0242
Waste heat recovery
F25J1/0243
Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
F25J1/0244
Operation; Control and regulation; Instrumentation
F25J1/0245
Different modes
F25J1/0247
start-up of the process
F25J1/0248
Stopping of the process
F25J1/0249
Controlling refrigerant inventory
F25J1/025
Details related to the refrigerant production or treatment
F25J1/0251
Intermittent or alternating process, so-called batch process
F25J1/0252
Control strategy
F25J1/0254
controlling particular process parameter
F25J1/0255
controlling the composition of the feed or liquefied gas
F25J1/0256
Safety aspects of operation
F25J1/0257
Construction and layout of liquefaction equipments
F25J1/0258
vertical layout of the equipments within in the cold box
F25J1/0259
Modularity and arrangement of parts of the liquefaction unit and in particular of the cold box
F25J1/0261
Details of cold box insulation, housing and internal structure
F25J1/0262
Details of the cold heat exchange system
F25J1/0263
using different types of heat exchangers
F25J1/0264
Arrangement of heat exchanger cores in parallel with different functions
F25J1/0265
comprising cores associated exclusively with the cooling of a refrigerant stream
F25J1/0267
using flash gas as heat sink
F25J1/0268
using a dedicated refrigeration means
F25J1/0269
Arrangement of liquefaction units or equipments fulfilling the same process step
F25J1/027
Inter-connecting multiple hot equipments upstream of the cold box
F25J1/0271
Inter-connecting multiple cold equipments within or downstream of the cold box
F25J1/0272
Multiple identical heat exchangers in parallel
F25J1/0274
Retrofitting or revamping of an existing liquefaction unit
F25J1/0275
adapted for special use of the liquefaction unit
F25J1/0276
Laboratory or other miniature devices
F25J1/0277
Offshore use
F25J1/0278
Unit being stationary
F25J1/0279
Compression of refrigerant or internal recycle fluid
F25J1/0281
characterised by the type of prime driver
F25J1/0282
Steam turbine as the prime mechanical driver
F25J1/0283
Gas turbine as the prime mechanical driver
F25J1/0284
Electrical motor as the prime mechanical driver
F25J1/0285
Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings
F25J1/0287
including an electrical motor
F25J1/0288
using work extraction by mechanical coupling of compression and expansion of the refrigerant, so-called companders
F25J1/0289
Use of different types of prime drivers of at least two refrigerant compressors in a cascade refrigeration system
F25J1/029
Mechanically coupling of different refrigerant compressors in a cascade refrigeration system to a common driver
F25J1/0291
Refrigerant compression by combined gas compression and liquid pumping
F25J1/0292
Refrigerant compression by cold or cryogenic suction of the refrigerant gas
F25J1/0294
Multiple compressor casings/strings in parallel
F25J1/0295
Shifting of the compression load between different cooling stages within a refrigerant cycle or within a cascade refrigeration system
F25J1/0296
Removal of the heat of compression
F25J1/0297
using an externally chilled fluid
F25J1/0298
Safety aspects and control of the refrigerant compression system
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