WO2012057505A2 - Natural gas liquefaction process - Google Patents
Natural gas liquefaction process Download PDFInfo
- Publication number
- WO2012057505A2 WO2012057505A2 PCT/KR2011/007994 KR2011007994W WO2012057505A2 WO 2012057505 A2 WO2012057505 A2 WO 2012057505A2 KR 2011007994 W KR2011007994 W KR 2011007994W WO 2012057505 A2 WO2012057505 A2 WO 2012057505A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- refrigerant
- natural gas
- cooling
- heat exchange
- cycle
- Prior art date
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 142
- 238000000034 method Methods 0.000 title claims abstract description 113
- 239000003345 natural gas Substances 0.000 title claims abstract description 70
- 239000003507 refrigerant Substances 0.000 claims abstract description 159
- 238000001816 cooling Methods 0.000 claims abstract description 64
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 19
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 17
- 239000001273 butane Substances 0.000 claims description 12
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 11
- 238000005057 refrigeration Methods 0.000 claims description 11
- 238000009835 boiling Methods 0.000 claims description 9
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 27
- 239000001294 propane Substances 0.000 description 12
- 230000000694 effects Effects 0.000 description 7
- 239000007789 gas Substances 0.000 description 5
- 239000003949 liquefied natural gas Substances 0.000 description 4
- 238000007906 compression Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000004781 supercooling Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000002427 irreversible effect Effects 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0022—Hydrocarbons, e.g. natural gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
- F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
- F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
- F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
- F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
- F25J1/0055—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream originating from an incorporated cascade
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
- F25J1/008—Hydrocarbons
- F25J1/0085—Ethane; Ethylene
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
- F25J1/008—Hydrocarbons
- F25J1/009—Hydrocarbons with four or more carbon atoms
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0211—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle
- F25J1/0217—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as at least a three level refrigeration cascade with at least one MCR cycle
- F25J1/0218—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as at least a three level refrigeration cascade with at least one MCR cycle with one or more SCR cycles, e.g. with a C3 pre-cooling cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
- F25J1/0292—Refrigerant compression by cold or cryogenic suction of the refrigerant gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/62—Separating low boiling components, e.g. He, H2, N2, Air
Definitions
- the present invention relates to a natural gas liquefaction process, and more particularly, to configure the pre-cooling cycle to take advantage of both the pure refrigerant cycle and the mixed refrigerant cycle, the efficiency of the liquefaction process, while the equipment of the liquefaction system is small and the structure is simple
- the present invention relates to a natural gas liquefaction process that is easy to operate.
- C3 / MR Process One of the most popular liquefaction processes in operation is the 'Propane Pre-cooled Mixed Refrigerant Process' (or C3 / MR Process).
- the basic structure of the C3 / MR process is as shown in FIG.
- 'C3' represents a propane refrigerant cycle
- 'MR' represents a mixed refrigerant cycle.
- 'C' represents a compressor
- 'AC' represents an after-cooler
- 'V' represents a valve
- 'HX' represents a heat exchanger.
- the feed gas is pre-cooled to approximately 240 K by a multi-stage propane (C3) refrigerant cycle.
- the precooled feed gas is condensed and sub-cooled to approximately 113 K by a mixed refrigerant cycle, ie through heat exchange with the mixed refrigerant (MR) in a heat exchanger.
- MR mixed refrigerant
- the general characteristics of the pure refrigerant cycle and the mixed refrigerant cycle are maintained. That is, pure refrigerant cycles are simple in structure and easy to operate, but require a large number of refrigeration stages.
- Mixed refrigerant cycles are complex and difficult to operate, but can achieve high efficiency with only a few components. Each cycle features the same characteristics in the C3 / MR process.
- the mixed refrigerant cycle of the C3 / MR process for liquefying (and subcooling) the pre-cooled feed gas is usually a mixture consisting of nitrogen, methane, ethane, and propane.
- Use refrigerant By appropriately selecting the composition of these components, and depending on the difference in boiling points of the components, the mixed refrigerant is suitably separated from the gaseous refrigerant portion and the liquid refrigerant portion, and then liquefied natural gas through each refrigerant portion.
- the mixed refrigerant cycle of the / MR process only a small number of facilities can show high efficiency.
- the pure refrigerant cycle of the C3 / MR process for precooling the feed gas uses a pure refrigerant called propane refrigerant, which is simple in structure and easy to operate, but usually requires three or four pressure stages. Is required.
- propane refrigerant a pure refrigerant
- the focus is on simplicity in the precooling cycle (large number of installations, but the structure itself is simple), and efficiency in liquefaction cycles (the number of installations, but the structure itself is complex and efficient). It can be seen that.
- the liquefaction (supercooling) cycle of the DMR process is basically the same as the liquefaction (supercooling) cycle of the C3 / MR process, that is, the mixed refrigerant cycle.
- the liquefaction cycle of the DMR process unlike the C3 / MR process, another mixed refrigerant cycle is used to precool the feed gas.
- the precooling cycle in the DMR process unlike the liquefaction cycle in the DMR process, usually does not have a gas-liquid separator.
- the DMR process focuses on efficiency in both precooling and liquefaction cycles. However, it is known that the efficiency of the actual DMR process is substantially lower than that of the C3 / MR process.
- the mixed refrigerant cycle is known to be more efficient than the pure refrigerant cycle.
- the structure itself is that the mixed refrigerant cycle is more complicated than the pure refrigerant cycle.
- many proposals have been made to improve the efficiency of the entire liquefaction process by applying mixed refrigerant cycles to refrigeration cycles for liquefying (supercooling) the pre-cooled natural gas. Therefore, there is a great need for research on pre-cooling cycles having a simple structure and excellent efficiency.
- the present invention has been made to solve the above problems, the object of the present invention is to configure the pre-cooling cycle to take advantage of both the pure refrigerant cycle and the mixed refrigerant cycle, the efficiency of the liquefaction process, while the equipment of the liquefaction system It provides a natural gas liquefaction process that is low in cost, simple in structure, and easy to operate.
- a closed loop pre-cooling cycle to pre-cool the natural gas and a closed loop liquefying cycle
- the first and second precooling cycles for precooling the natural gas supplied together in the same first heat exchange region through respective pure refrigerants are performed.
- the closed circuit liquefaction cycle includes at least one liquefaction cycle for liquefying natural gas precooled through the mixed refrigerant, and the first and second precooling cycles are closed circuit refrigeration cycles.
- the pure refrigerant of the first precooling cycle may be ethane (C2) refrigerant
- the pure refrigerant of the second precooling cycle may be butane (C4) refrigerant.
- the first and second precooling cycles may include compressing the pure refrigerant, cooling the compressed refrigerant, additionally cooling the cooled refrigerant in the first heat exchange area, and expanding the additionally cooled refrigerant. It may include a step.
- the closed circuit liquefaction cycle may include: compressing the mixed refrigerant, cooling the compressed refrigerant, additionally cooling the cooled refrigerant in the first heat exchange area to partially condense, and boiling the partially condensed refrigerant. Separating the liquid refrigerant portion and the gaseous refrigerant portion according to the difference of, cooling the natural gas pre-cooled in the second heat exchange region by using the liquid refrigerant portion, and using the gaseous refrigerant portion by a third And secondarily cooling the naturally cooled natural gas in the heat exchange zone.
- the primary cooling may include: a first step of cooling the liquid refrigerant part through heat exchange in the second heat exchange region, a second step of expanding the cooled refrigerant part through the first step, and the And a third step of cooling the natural gas by exchanging the refrigerant portion expanded through the second step with the natural gas in the second heat exchange region.
- the secondary cooling may include a cooling step of cooling the gaseous refrigerant part through heat exchange in the second heat exchange area, and a heat exchange of the refrigerant part cooled through the cooling step in the third heat exchange area.
- Natural gas liquefaction process according to the present invention has the effect that the pre-cooling cycle can be configured with a relatively small number of facilities because the pre-cooling cycle pre-cools the natural gas in only one pressure step.
- the natural gas liquefaction process according to the present invention has the effect that the structure itself is simple and easy operation of the liquefaction system because each pre-cooling cycle uses a pure refrigerant.
- the natural gas liquefaction process according to the present invention has the effect that the efficiency of the liquefaction process is very excellent because two pre-cooling cycles are arranged in parallel to pre-cool the natural gas in the same heat exchange zone.
- FIG. 1 is a flowchart illustrating a natural gas liquefaction process according to an embodiment of the present invention.
- FIG. 2 is a graph showing the temperature profile in the precooling region of a conventional C3-MR process.
- FIG. 4 is a graph illustrating a temperature profile in a precooling region of a liquefaction process according to an embodiment of the present invention.
- FIG. 5 is a temperature-entropy diagram of ethane and propane cycles in a liquefaction process in accordance with one embodiment of the present invention.
- 6 to 8 are graphs showing exergy use and irreversibility of the conventional CR / MR process, the conventional DMR process, and the precooling step of the liquefaction process according to an embodiment of the present invention, respectively.
- FIG. 9 is a flow chart illustrating a conventional C3 / MR process.
- FIG. 10 is a flowchart conceptually illustrating a conventional DMR process.
- FIG. 1 is a flowchart illustrating a natural gas liquefaction process according to an embodiment of the present invention.
- the natural gas is precooled using a closed loop pre-cooling cycle, and a closed loop liquefying cycle is used. It can be applied to the natural gas liquefaction process to liquefy the pre-cooled natural gas.
- the liquefaction process according to the present embodiment may further include a refrigeration cycle for cooling the mixed refrigerant or further cooling the natural gas.
- the liquefaction process according to this embodiment includes a closed loop refrigeration cycle for precooling the supplied natural gas and a closed loop refrigeration cycle for liquefying (or liquefying and subcooling) the precooled natural gas. Since the refrigeration cycles according to the present embodiment are all closed loop cycles, each cycle undergoes one closed cycle while independently undergoing the steps of compression-condensation-expansion-evaporation.
- the closed circuit refrigeration cycle that is, the closed circuit precooling cycle for precooling the supplied natural gas, includes two different precooling cycles. These two precooling cycles are of course also closed circuit refrigeration cycles.
- the natural gas supplied as shown in FIG. 1 is precooled by the first precooling cycle and the second precooling cycle in the first heat exchange region 110 (described later).
- the first precooling cycle is a ethane (C2) refrigerant cycle
- the second precooling cycle is a butane (C4) refrigerant cycle). That is, the supplied natural gas is precooled by the pure refrigerant of the first precooling cycle and the pure refrigerant of the second precooling cycle in the same heat exchange region of the first heat exchange region 110.
- the first precooling cycle and the second precooling cycle are each compressed, condensed, expanded, and evaporated.
- the pure refrigerant first flows into the compressors 151 and 161 through the conduits 201 and 401 and is compressed. Pure refrigerant then enters and cools the coolers 152 and 162 through conduits 202 and 402.
- This compression and cooling process can be made in multiple stages as shown in FIG. That is, a plurality of compressors and coolers can be connected in series. In this case, the cooled pure refrigerant flows back into the compressors 153 and 163 through the conduits 203 and 403, and the compressed pure refrigerant is again cooled through the conduits 204 and 404. It may be introduced into and cooled. As such, when the compressor is configured in multiple stages and the pure refrigerant is compressed in multiple stages, the required power of the compressor can be reduced.
- the pure refrigerant compressed and cooled as described above may be further cooled through heat exchange with the refrigerant flowing into the conduits 205 and 405 and the first heat exchange region 110, and through this process, the pure refrigerant may be condensed. have. However, as described below, depending on the boiling point of the pure refrigerant, the pure refrigerant may be condensed by cooling by the cooler described above. In this case, in the condensed state, the pure refrigerant may flow into the first heat exchange region 110 to be further cooled. Cooling of the refrigerant in the first heat exchange region 110 may be performed by the refrigerant flowing back into the first heat exchange region 110 through the conduits 207 and 407.
- the pure refrigerant cooled through the heat exchange in the first heat exchange region 110 as described above is introduced into the expansion valves 155 and 165 through the conduits 206 and 406, expanded and cooled, and then the conduits 207 and 407. Into the first heat exchange region 110 again through) can cool the natural gas and the refrigerant.
- the first precooling cycle and the second precooling cycle are arranged in parallel to form a closed circuit cycle to precool the natural gas complementarily supplied in the first heat exchange region 110.
- the most important feature in the liquefaction process according to the present embodiment is that two closed loop refrigeration cycles employing pure refrigerant are arranged in parallel to precool the natural gas supplied in the same heat exchange zone.
- ethane (C2) refrigerant and butane (C4) refrigerant are used as the pure refrigerant of the first and second precooling cycles.
- C3 / MR process a pure refrigerant composed of propane (C3) is used for precooling of natural gas, and in the aforementioned DMR process, 45.5 mole% of ethane (C2) and propane (C3) 4.9 for precooling of natural gas.
- a mixed refrigerant consisting of mole% and butane (C4) 49.6 mole% is used.
- the liquefaction process according to the present embodiment is arranged in parallel as described above to take advantage of the advantages of the two basic structures as described above, that is, the use of pure refrigerant and the use of mixed refrigerant for precooling. Two pure refrigerant cycles are used. In addition, the efficiency of the overall liquefaction process can be optimized by constituting two pure refrigerant cycles with an ethane cycle and a butane cycle.
- the mixed refrigerant in the pre-cooling step of the above-described DMR process is composed of ethane, propane and butane components, but contains very little propane components. In the liquefaction process according to the present embodiment, the precooling effect due to the above propane components is used. It can be said that it is replacing by the effect of the cycle.
- Natural gas precooled through the two pure refrigerant cycles as described above is liquefied (or liquefied and supercooled) through the mixed refrigerant cycle.
- the mixed refrigerant partially condensed through the heat exchange in the first heat exchange region 110 is introduced into the gas-liquid separator 171 through the conduit 301, and according to the difference in boiling point, The second coolant part is separated into a lower boiling point than the coolant part. That is, the partially condensed mixed refrigerant may be divided into a first refrigerant portion separated into the liquid refrigerant portion due to the high boiling point through the gas-liquid separator 171 and a second refrigerant portion separated into the gaseous refrigerant portion due to the low boiling point. have.
- the first refrigerant portion thus separated is introduced into the second heat exchange region 120 through the conduit 302 and cooled. Cooling of this refrigerant portion may be through heat exchange with the refrigerant entering the second heat exchange region 120 through the conduit 304.
- the cooled refrigerant portion enters and expands into expansion valve 172 through conduit 303.
- the expanded refrigerant portion may be mixed with the second refrigerant portion, which will be described later, and then introduced back into the second heat exchange region 120 through conduit 304 to cool other refrigerants and liquefy natural gas. Then, the mixed refrigerant may be cooled through a ethane cycle and a butane cycle together with the natural gas supplied to the first heat exchange region 110 after being subjected to a series of compression and cooling processes.
- the separated second refrigerant portion then enters the second heat exchange zone 120 through the conduit 306 and is cooled. Cooling of this refrigerant portion may be through heat exchange with the refrigerant entering the second heat exchange region 120 through the conduit 304. The cooled refrigerant portion enters and condenses the third heat exchange region 130 through conduit 307. Condensation of this refrigerant portion may be accomplished through heat exchange with the refrigerant entering the third heat exchange region 130 through the conduit 309. The condensed refrigerant portion enters and expands into expansion valve 173 through conduit 308.
- the expanded refrigerant portion enters the third heat exchange region 130 again through the conduit 309 to condense the refrigerant introduced into the third heat exchange region 130 through heat exchange and liquefy or supercool the natural gas.
- the liquefied natural gas may be expanded by the expansion valve 181 and then introduced into the storage tank.
- the refrigerant part which has completed the heat exchange in the third heat exchange area 130 may be mixed with the aforementioned first refrigerant part and flowed back into the second heat exchange area 120.
- the three heat exchange regions 110, 120, and 130 described above may be provided together in one heat exchange means as shown in FIG. 1, or may be provided in three heat exchange means, respectively.
- the heat exchange means may also be a conventional heat exchanger.
- 2 and 3 show the temperature distribution in the precooling region of the above-described C3-MR process and DMR process, respectively.
- Propane (C3) in the C3-MR process is a pure refrigerant and passes through several stages of pressure steps, so that the temperature distribution appears in a stepped manner as shown in FIG.
- the temperature distribution in the precooling zone of the DMR process changes gradually, with a minimum difference (3K) in the middle of the heat exchange zone.
- 4 and 5 show the temperature distribution in the precooling region of the liquefaction process according to the present embodiment and the temperature-entropy diagrams of the ethane and butane cycles in the liquefaction process according to the present embodiment, respectively.
- the cold stream temperature is ethane refrigerant and butane.
- the butane refrigerant after pre-cooling the natural gas is condensed during the multi-stage compression and cooling process through the compressor and the cooler, and then flows back into the heat exchange area into the liquid phase (see reference numeral 5 of FIGS. 4 and 5).
- the temperature of the hot stream has only one horizontal region (see 6-7 in FIG. 4) in response to the condensation of the ethane refrigerant.
- Exergy efficiency defined as the ratio of increase of exergy to power input, is 34.3%, 30.5%, and 31.5% in each liquefaction process, as shown in FIGS. appear.
- C3 / MR process a plurality of pressure stages are required and a large number of equipments are required.
- each pre-cooling cycle pre-cools the natural gas with only one pressure step
- the pre-cooling cycle can be configured with a relatively small number of facilities, and each pre-cooling cycle uses pure refrigerant. Since the structure itself is simple and the operation of the liquefaction system is easy, the liquefaction process is very excellent because the ethane refrigerant cycle and the butane refrigerant cycle are arranged in parallel to precool the natural gas in the same heat exchange area.
- the liquefaction process according to the present embodiment has both the advantages of the structure of pre-cooling natural gas by using pure refrigerant and the structure of pre-cooling natural gas by employing mixed refrigerant, and have very high efficiency (liquefaction known to date).
- the efficiency of the liquefaction process according to this embodiment is very good considering that the C3 / MR process is one of the very high efficiency processes.
- the irreversibility in the precooling step of each liquefaction process is represented by dividing into four groups of valve (V), aftercooler (AC), compressor (C), heat exchanger (HX), as shown in Figs. Can be.
- V valve
- AC aftercooler
- C compressor
- HX heat exchanger
- the C3 / MR process is relatively irreversible by the valve compared to the liquefaction process according to this embodiment.
- the DMR process is relatively irreversible by the cooler compared to the liquefaction process according to the present embodiment.
- the liquefaction process according to the present embodiment has a lower irreversibility by the valve and the cooler than the two liquefaction processes described above, while the irreversibility by the heat exchanger is high.
- the pre-cooling cycle pre-cools the natural gas in only one pressure step
- the pre-cooling cycle can be constituted by a relatively small number of facilities, and the structure of each pre-cooling cycle uses pure refrigerant. It is a natural gas liquefaction process that has a very high efficiency of the liquefaction process because it is simple and easy to operate the liquefaction system, and two precooling cycles are arranged in parallel to precool the natural gas in the same heat exchange area. There is a possibility.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
Description
Claims (6)
- 밀폐회로 예냉 사이클(closed loop pre-cooling cycle)을 이용하여 천연가스를 예냉시키고 밀폐회로 액화 사이클(closed loop liquefying cycle)을 이용하여 예냉된 천연가스를 액화시키는 천연가스 액화공정에 있어서,In a natural gas liquefaction process of pre-cooling natural gas using a closed loop pre-cooling cycle and liquefying the pre-cooled natural gas using a closed loop liquefying cycle,상기 폐 루프 예냉 사이클은 각각의 순수 냉매를 통해 동일한 제1 열교환 영역 내에서 공급된 천연가스를 함께 예냉시키는 제1 및 제2 예냉 사이클을 포함하고, 상기 밀폐회로 액화 사이클은 혼합 냉매를 통해 예냉된 천연가스를 액화시키는 적어도 하나의 액화 사이클을 포함하며, 상기 제1 및 제2 예냉 사이클은 밀폐회로 냉동 사이클인 것을 특징으로 하는 천연가스 액화공정.The closed loop precooling cycle includes first and second precooling cycles for precooling together natural gas supplied in the same first heat exchange region through respective pure refrigerants, and the closed circuit liquefaction cycle is precooled through the mixed refrigerant. And at least one liquefaction cycle for liquefying natural gas, wherein the first and second precooling cycles are closed circuit refrigeration cycles.
- 청구항 1에 있어서,The method according to claim 1,상기 제1 예냉 사이클의 순수 냉매는 에탄(C2) 냉매이고, 상기 제2 예냉 사이클의 순수 냉매는 부탄(C4) 냉매인 것을 특징으로 하는 천연가스 액화공정.The pure refrigerant of the first precooling cycle is an ethane (C2) refrigerant, the pure refrigerant of the second precooling cycle is a butane (C4) refrigerant.
- 청구항 1에 있어서,The method according to claim 1,상기 제1 및 제2 예냉 사이클은, 순수 냉매를 압축하는 단계, 압축된 냉매를 냉각하는 단계, 냉각된 냉매를 상기 제1 열교환 영역 내에서 추가적으로 냉각하는 단계, 및 추가적으로 냉각된 냉매를 팽창하는 단계를 포함하는 것을 특징으로 하는 천연가스 액화공정.The first and second precooling cycles may include: compressing the pure refrigerant, cooling the compressed refrigerant, further cooling the cooled refrigerant in the first heat exchange zone, and expanding the additionally cooled refrigerant. Natural gas liquefaction process comprising a.
- 청구항 1에 있어서,The method according to claim 1,상기 폐 루프 액화 사이클은, 혼합 냉매를 압축하는 단계, 압축된 냉매를 냉각하는 단계, 냉각된 냉매를 상기 제1 열교환 영역 내에서 추가적으로 냉각하여 부분적으로 응축하는 단계, 부분적으로 응축된 냉매를 비등점의 차이에 따라 액상 냉매 부분과 기상 냉매 부분으로 분리하는 단계, 상기 액상 냉매 부분을 이용하여 제2 열교환 영역 내에서 예냉된 천연가스를 일차적으로 냉각하는 단계, 및 상기 기상 냉매 부분을 이용하여 제3 열교환 영역 내에서 일차적으로 냉각된 천연가스를 이차적으로 냉각하는 단계를 포함하는 것을 특징으로 하는 천연가스 액화공정.The closed loop liquefaction cycle includes: compressing a mixed refrigerant, cooling the compressed refrigerant, additionally cooling the cooled refrigerant in the first heat exchange zone to partially condense, and partially boiling the partially condensed refrigerant to a boiling point. Separating the liquid refrigerant portion and the gaseous refrigerant portion according to the difference, first cooling the natural gas pre-cooled in the second heat exchange region using the liquid refrigerant portion, and using the gaseous refrigerant portion to perform a third heat exchange. Natural gas liquefaction process comprising the step of secondarily cooling the naturally cooled natural gas in the region.
- 청구항 4에 있어서,The method according to claim 4,상기 일차적으로 냉각하는 단계는, 상기 액상 냉매 부분을 상기 제2 열교환 영역 내에서의 열교환을 통해 냉각하는 제1 단계, 상기 제1 단계를 통해 냉각된 냉매 부분을 팽창하는 제2 단계, 및 상기 제2 단계를 통해 팽창된 냉매 부분과 상기 천연가스를 상기 제2 열교환 영역 내에서 열교환시켜 상기 천연가스를 냉각하는 제3 단계를 포함하는 것을 특징으로 하는 천연가스 액화공정.The primary cooling may include a first step of cooling the liquid refrigerant part through heat exchange in the second heat exchange region, a second step of expanding the cooled refrigerant part through the first step, and the first step. And a third step of cooling the natural gas by exchanging the refrigerant portion expanded through the two steps with the natural gas in the second heat exchange region.
- 청구항 4에 있어서,The method according to claim 4,상기 이차적으로 냉각하는 단계는, 상기 기상 냉매 부분을 상기 제2 열교환 영역 내에서의 열교환을 통해 냉각하는 냉각 단계, 상기 냉각 단계를 통해 냉각된 냉매 부분을 상기 제3 열교환 영역 내에서의 열교환을 통해 응축하는 응축 단계, 상기 응축 단계를 통해 응축된 냉매 부분을 팽창하는 팽창 단계, 및 상기 팽창 단계를 통해 팽창된 냉매 부분과 상기 천연가스를 상기 제3 열교환 영역 내에서 열교환시켜 상기 천연가스를 냉각하는 단계를 포함하는 것을 특징으로 하는 천연가스 액화공정.The secondary cooling may include a cooling step of cooling the gaseous refrigerant part through heat exchange in the second heat exchange region, and a refrigerant part cooled through the cooling step through heat exchange in the third heat exchange region. A condensation step of condensing, an expansion step of expanding the refrigerant part condensed through the condensation step, and cooling the natural gas by heat-exchanging the expanded refrigerant part and the natural gas in the third heat exchange area through the expansion step. Natural gas liquefaction process comprising the step.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2011321145A AU2011321145B2 (en) | 2010-10-26 | 2011-10-25 | Natural gas liquefaction process |
US13/881,588 US20130263623A1 (en) | 2010-10-26 | 2011-10-25 | Natural gas liquefaction process |
CA2816047A CA2816047C (en) | 2010-10-26 | 2011-10-25 | Natural gas liquefaction process |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020100104618A KR101037226B1 (en) | 2010-10-26 | 2010-10-26 | Natural gas liquefaction process |
KR10-2010-0104618 | 2010-10-26 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2012057505A2 true WO2012057505A2 (en) | 2012-05-03 |
WO2012057505A3 WO2012057505A3 (en) | 2012-08-30 |
Family
ID=44366646
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/KR2011/007994 WO2012057505A2 (en) | 2010-10-26 | 2011-10-25 | Natural gas liquefaction process |
Country Status (5)
Country | Link |
---|---|
US (1) | US20130263623A1 (en) |
KR (1) | KR101037226B1 (en) |
AU (1) | AU2011321145B2 (en) |
CA (1) | CA2816047C (en) |
WO (1) | WO2012057505A2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101396921B1 (en) * | 2013-04-24 | 2014-05-19 | 상 욱 김 | Constant temperatur maintaining control type cooling apparatus for cryogenic environment |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20160109177A1 (en) | 2014-10-16 | 2016-04-21 | General Electric Company | System and method for natural gas liquefaction |
EP3230669A4 (en) | 2014-12-12 | 2018-08-01 | Dresser Rand Company | System and method for liquefaction of natural gas |
CN106440656B (en) * | 2016-11-02 | 2022-02-15 | 中国寰球工程有限公司 | Carbon dioxide precooling two-stage nitrogen expansion natural gas liquefaction system |
US11585608B2 (en) * | 2018-02-05 | 2023-02-21 | Emerson Climate Technologies, Inc. | Climate-control system having thermal storage tank |
US11149971B2 (en) | 2018-02-23 | 2021-10-19 | Emerson Climate Technologies, Inc. | Climate-control system with thermal storage device |
US11346583B2 (en) | 2018-06-27 | 2022-05-31 | Emerson Climate Technologies, Inc. | Climate-control system having vapor-injection compressors |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20050110026A (en) * | 2003-03-18 | 2005-11-22 | 에어 프로덕츠 앤드 케미칼스, 인코오포레이티드 | Integrated multiple-loop refrigeration process for gas liquefaction |
US7127914B2 (en) * | 2003-09-17 | 2006-10-31 | Air Products And Chemicals, Inc. | Hybrid gas liquefaction cycle with multiple expanders |
US20080141711A1 (en) * | 2006-12-18 | 2008-06-19 | Mark Julian Roberts | Hybrid cycle liquefaction of natural gas with propane pre-cooling |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5791160A (en) * | 1997-07-24 | 1998-08-11 | Air Products And Chemicals, Inc. | Method and apparatus for regulatory control of production and temperature in a mixed refrigerant liquefied natural gas facility |
US6412302B1 (en) * | 2001-03-06 | 2002-07-02 | Abb Lummus Global, Inc. - Randall Division | LNG production using dual independent expander refrigeration cycles |
EP1613909B1 (en) * | 2003-03-18 | 2013-03-06 | Air Products And Chemicals, Inc. | Integrated multiple-loop refrigeration process for gas liquefaction |
EP1929227B1 (en) * | 2005-08-09 | 2019-07-03 | Exxonmobil Upstream Research Company | Natural gas liquefaction process for lng |
US20100147024A1 (en) * | 2008-12-12 | 2010-06-17 | Air Products And Chemicals, Inc. | Alternative pre-cooling arrangement |
-
2010
- 2010-10-26 KR KR1020100104618A patent/KR101037226B1/en active IP Right Grant
-
2011
- 2011-10-25 US US13/881,588 patent/US20130263623A1/en not_active Abandoned
- 2011-10-25 WO PCT/KR2011/007994 patent/WO2012057505A2/en active Application Filing
- 2011-10-25 CA CA2816047A patent/CA2816047C/en active Active
- 2011-10-25 AU AU2011321145A patent/AU2011321145B2/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20050110026A (en) * | 2003-03-18 | 2005-11-22 | 에어 프로덕츠 앤드 케미칼스, 인코오포레이티드 | Integrated multiple-loop refrigeration process for gas liquefaction |
US7086251B2 (en) * | 2003-03-18 | 2006-08-08 | Air Products And Chemicals, Inc. | Integrated multiple-loop refrigeration process for gas liquefaction |
US7127914B2 (en) * | 2003-09-17 | 2006-10-31 | Air Products And Chemicals, Inc. | Hybrid gas liquefaction cycle with multiple expanders |
US20080141711A1 (en) * | 2006-12-18 | 2008-06-19 | Mark Julian Roberts | Hybrid cycle liquefaction of natural gas with propane pre-cooling |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101396921B1 (en) * | 2013-04-24 | 2014-05-19 | 상 욱 김 | Constant temperatur maintaining control type cooling apparatus for cryogenic environment |
Also Published As
Publication number | Publication date |
---|---|
KR101037226B1 (en) | 2011-05-25 |
AU2011321145A1 (en) | 2013-05-30 |
AU2011321145B2 (en) | 2015-03-05 |
US20130263623A1 (en) | 2013-10-10 |
WO2012057505A3 (en) | 2012-08-30 |
CA2816047A1 (en) | 2012-05-03 |
CA2816047C (en) | 2016-01-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2012057505A2 (en) | Natural gas liquefaction process | |
WO2011136544A2 (en) | Natural gas liquefaction process with refrigerant separation | |
WO2011136543A2 (en) | Natural gas liquefaction process | |
KR101281914B1 (en) | Natural gas liquefaction process | |
GB1590891A (en) | Refrigeration method and apparatus | |
WO2012023752A2 (en) | Natural gas liquefaction process | |
AU2017203215B2 (en) | Liquefaction method and system | |
KR20180034251A (en) | Mixed refrigerant cooling process and system | |
KR101037249B1 (en) | Natural gas liquefaction process | |
KR100991859B1 (en) | A fluid cooling system and a method for cooling a fluid using the same | |
KR20140003260A (en) | Natural gas liquefaction system and method using the same | |
AU2017202953A1 (en) | Natural gas liquefaction process | |
KR101107437B1 (en) | Natural gas liquefaction process | |
RU2556731C2 (en) | Method to liquefy natural gas by cooling mixtures, containing at least one non-saturated hydrocarbon | |
KR101037277B1 (en) | Natural gas liquefaction process | |
KR20120016568A (en) | Natural gas liquefaction process and system using the same | |
KR101123977B1 (en) | Natural gas liquefaction process and system using the same | |
KR101616626B1 (en) | Natural gas liquefaction process | |
KR101464433B1 (en) | Natural gas liquefaction process | |
KR101153100B1 (en) | Natural gas liquefaction process | |
KR101620182B1 (en) | Natural gas liquefaction process | |
US20240200868A1 (en) | Device and method for pre-cooling a stream of a target fluid to a temperature less than or equal to 90 k | |
KR101615444B1 (en) | Natural gas liquefaction process | |
KR20110081497A (en) | Natural gas liquefaction process and system using the same | |
KR101620183B1 (en) | Natural gas liquefaction process |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 11836597 Country of ref document: EP Kind code of ref document: A2 |
|
ENP | Entry into the national phase |
Ref document number: 2816047 Country of ref document: CA |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
ENP | Entry into the national phase |
Ref document number: 2011321145 Country of ref document: AU Date of ref document: 20111025 Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 13881588 Country of ref document: US |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 11836597 Country of ref document: EP Kind code of ref document: A2 |