CN204678750U - A kind of natural gas liquefaction device realizing mix refrigerant recovery, re-injection - Google Patents
A kind of natural gas liquefaction device realizing mix refrigerant recovery, re-injection Download PDFInfo
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- CN204678750U CN204678750U CN201520315219.0U CN201520315219U CN204678750U CN 204678750 U CN204678750 U CN 204678750U CN 201520315219 U CN201520315219 U CN 201520315219U CN 204678750 U CN204678750 U CN 204678750U
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- heat exchanger
- coolant compressor
- cold
- plate
- refrigerant
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 238000011084 recovery Methods 0.000 title claims abstract description 19
- 239000003345 natural gas Substances 0.000 title claims abstract description 16
- 238000002347 injection Methods 0.000 title claims abstract description 13
- 239000007924 injection Substances 0.000 title claims abstract description 13
- 239000003507 refrigerant Substances 0.000 title abstract description 46
- 239000000203 mixture Substances 0.000 title abstract description 31
- 239000002826 coolant Substances 0.000 claims description 57
- 239000004215 Carbon black (E152) Substances 0.000 claims description 18
- 229930195733 hydrocarbon Natural products 0.000 claims description 18
- 150000002430 hydrocarbons Chemical class 0.000 claims description 18
- 239000007789 gas Substances 0.000 claims description 16
- 239000007791 liquid phase Substances 0.000 claims description 16
- 239000012071 phase Substances 0.000 claims description 9
- 239000007792 gaseous phase Substances 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 15
- 239000007788 liquid Substances 0.000 abstract description 8
- 230000003044 adaptive effect Effects 0.000 abstract description 4
- 239000012808 vapor phase Substances 0.000 description 9
- 238000010992 reflux Methods 0.000 description 8
- 239000003949 liquefied natural gas Substances 0.000 description 6
- 238000000926 separation method Methods 0.000 description 5
- 238000000605 extraction Methods 0.000 description 4
- 241000543741 Hexamermis Species 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
Classifications
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- 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
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- 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
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- 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
- F25J1/0212—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 a single flow MCR 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
- F25J1/0244—Operation; Control and regulation; Instrumentation
- F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
- F25J1/0247—Different modes, i.e. 'runs', of operation; Process control start-up of the process
-
- 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
- F25J1/0244—Operation; Control and regulation; Instrumentation
- F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
- F25J1/0249—Controlling refrigerant inventory, i.e. composition or quantity
-
- 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
- F25J2220/64—Separating heavy hydrocarbons, e.g. NGL, LPG, C4+ hydrocarbons or heavy condensates in general
-
- 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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/60—Expansion by ejector or injector, e.g. "Gasstrahlpumpe", "venturi mixing", "jet pumps"
Abstract
The utility model relates to the natural gas liquefaction device that can realize refrigerant-recovery, re-injection, designated lane is increased in plate-fin heat exchanger, for reclaiming the mix refrigerant in refrigerant-cycle systems, and arrange private processes by its again re-injection enter in refrigerant system, be applicable to recovery and the re-injection of cold-producing medium when refrigerant liquid gasifying device stops and again drives, and the recovery of cold-producing medium and re-injection during adjustment cold-producing medium proportioning, solve the problem of refrigerant-recovery difficulty, liquefying plant variable working condition adaptive capacity difference.
Description
Technical field
The utility model relates to and a kind ofly realizes the recovery of mix refrigerant, the natural gas liquefaction device of re-injection, is applicable to the recovery of the mix refrigerant adopted in hybrid refrigeration liquefying plant, re-injection.
Background technology
The natural gas liquefaction flow process that natural gas liquefaction device adopts has several different pattern, divides, can have following three kinds of modes: Cascade, mix refrigerant liquefaction flow path with refrigeration modes, the liquefaction flow path of band decompressor.Cascade energy consumption is minimum, but dynamic equipment is many, operation more complicated; There is the shortcomings such as energy consumption is large, operation relative complex in the liquefaction flow path with decompressor; Mix refrigerant liquefaction flow path advantage is that energy consumption is little, and dynamic equipment is few, applies all comparatively general in Basicloadtype liquefying plant and peak regulation type liquefying plant.
But there is the problem such as refrigerant-recovery difficulty, device variable working condition adaptive capacity difference in mix refrigerant liquefaction flow path.When usual device stops, the cold-producing medium light component that especially wherein price is higher gets only emptying feeding torch because being difficult to recovery, cause significant wastage, the utility model proposes a kind of mix refrigerant recovery process and device, to solve the problem of refrigerant-recovery difficulty, liquefying plant variable working condition adaptive capacity difference.
Utility model content
The utility model provides and a kind ofly realizes the recovery of mix refrigerant, the natural gas liquefaction device of re-injection, is applicable to by refrigerant-cycle systems when mix refrigerant liquefying plant stops, and the mix refrigerant namely in ice chest and coolant compressor reclaims; Natural gas completes liquefaction at ice chest, and the heat exchanger components in ice chest is plate-fin heat exchanger.
This device comprises coolant compressor, the coolant compressor cooler be connected successively with coolant compressor and coolant compressor divide flow container, ice chest, its heat exchanger components is plate-fin heat exchanger, heavy hydrocarbon separator, cold-producing medium pans, first, second, third, fourth choke valve, and injector;
First heat exchanger channels of plate-fin heat exchanger connects heavy hydrocarbon separator, the arrival end of the second heat exchanger channels of the top gas phase end connecting plate fin heat exchanger of heavy hydrocarbon separator, and the port of export of the second heat exchanger channels connects LNG product storage tank;
Coolant compressor divides flow container liquid phase end after the 3rd heat exchanger channels of plate-fin heat exchanger, be connected to one end of second throttle, is connected to coolant compressor entrance after the 5th heat exchanger channels of the other end connecting plate fin heat exchanger of second throttle;
Coolant compressor divides flow container gas phase end to be divided into two-way, and the first via is connected to the ejection gas arrival end of injector after connecting the 4th choke valve; Second tunnel is divided into again two branch roads after the 4th heat exchanger channels of plate-fin heat exchanger, wherein the first branch road is connected to one end of first throttle valve after going out the 4th heat exchanger channels of plate-fin heat exchanger, coolant compressor entrance is connected to after 5th heat exchanger channels of the other end connecting plate fin heat exchanger of first throttle valve, second branch road continues to enter the 6th heat exchanger channels after going out the 4th heat exchanger channels of plate-fin heat exchanger, is then connected to cold-producing medium pans through the 3rd choke valve; The ejection gas port of export of injector is connected to the pipeline between first throttle valve and the 5th heat exchanger channels (arrival end), cold-producing medium pans gaseous phase outlet pipe is also connected to the pipeline between first throttle valve and the 5th heat exchanger channels (arrival end), and cold-producing medium pans liquid-phase outlet pipe is connected to the driven fluid arrival end of injector.
When liquefying plant normally runs, its technical process comprises natural gas liquefaction and mixed-refrigerant cycle:
Natural gas liquefaction: first raw natural gas enters in the heat exchanger channels of plate-fin heat exchanger and carry out precooling, enter heavy hydrocarbon separator after being cooled to-30 DEG C ~-60 DEG C (such as-40 DEG C ~-50 DEG C) and carry out gas-liquid separation, be heavy hydrocarbon by isolated liquid bottom heavy hydrocarbon separator V-1, the heat exchanger channels entering plate-fin heat exchanger is continued by the isolated vapor phase stream stock in heavy hydrocarbon separator top, and be cooled to wherein-130 DEG C ~-166 DEG C (such as-140 DEG C ~-150 DEG C), obtain liquefied natural gas and LNG.
Mixed-refrigerant cycle: mix refrigerant enters coolant compressor, be pressurized to 1.2 ~ 5.4MPa (such as 1.5 ~ 5.0MPa, absolute pressure), after cooling, gas-liquid separation, vapor phase refrigerant enters the heat exchanger channels of plate-fin heat exchanger by the road, the reflux passage entering plate-fin heat exchanger after the end extraction of this heat exchanger channels enters first throttle valve throttling to 0.2 ~ 0.8MPa (such as 0.4 ~ 0.6MPa) provides cold for it, then returns coolant compressor entrance; Liquid phase refrigerant enters the heat exchanger channels of plate-fin heat exchanger, the reflux passage entering plate-fin heat exchanger after the end extraction of this heat exchanger channels enters second throttle throttling to 0.2 ~ 0.8MPa (such as 0.4 ~ 0.6MPa) provides cold for it, then returns coolant compressor entrance.
When liquefying plant stops, the technical process that mix refrigerant reclaims is as follows:
The heat exchanger channels being specifically designed to and reclaiming mix refrigerant is increased in plate-fin heat exchanger, when liquefying plant stops or when adjusting cold-producing medium proportioning, the vapor phase refrigerant going out coolant compressor flow through plate-fin heat exchanger be specifically designed to the heat exchanger channels reclaiming mix refrigerant after be liquefied, go out the cold-producing medium of this passage through choke valve reducing pressure by regulating flow to 0.2 ~ 0.8MPa (such as 0.4 ~ 0.6MPa), liquid phase after throttling enters in cold-producing medium pans and stores, gas phase enters the reflux passage of plate-fin heat exchanger from the gaseous phase outlet of cold-producing medium pans and returns the entrance of coolant compressor, after coolant compressor supercharging, reenter the heat exchanger channels being specifically designed to recovery mix refrigerant repeat said process (namely, liquefaction, throttling), the liquid phase going out coolant compressor can be stored in coolant compressor outlet tank or enter in a normal temperature refrigerant-recovery tank arranged separately from the liquid-phase outlet of coolant compressor outlet tank and store,
Cold-producing medium in cold-producing medium pans by the branch line arranged at coolant compressor outlet tank gaseous phase outlet, refills in refrigerant-cycle systems at the end of again driving or adjusting cold-producing medium proportioning by liquefying plant; Now coolant compressor starts, vapor phase refrigerant through coolant compressor supercharging enters injector after throttling, as power gas, the liquid phase injection in cold-producing medium pans is entered in injector, through entering coolant compressor entrance by the reflux passage of plate-fin heat exchanger after the two mixing, the cold-producing medium thus in cold-producing medium pans is refilled in refrigerant-cycle systems.
Advantage of the present utility model:
1, by the cold in parking period ice chest, the liquefaction of the vapor phase refrigerant of compressor outlet is also reclaimed, the loss of cold-producing medium can be reduced to greatest extent;
2, by time reclaiming or supplementary cold-producing medium, the ratio of adjustment mix refrigerant and flow, can improve the variable working condition adaptive capacity of liquefying plant.
Accompanying drawing explanation
Fig. 1 is process chart of the present utility model.
Wherein, C-1, coolant compressor E-1, coolant compressor cooler E-2, plate-fin heat exchanger V-1, heavy hydrocarbon separator V-2, coolant compressor divide flow container V-3, cold-producing medium pans X-1, first throttle valve X-2, second throttle X-3, the 3rd choke valve X-4, the 4th choke valve J-1, injector.
Detailed description of the invention
The utility model provides a kind of recovery process and device of mix refrigerant, and be applicable to by refrigerant-cycle systems when mix refrigerant liquefying plant stops, the mix refrigerant namely in ice chest and coolant compressor reclaims; Natural gas completes liquefaction in ice chest, and the heat exchanger components in ice chest is plate-fin heat exchanger E-2.
A retracting device for mix refrigerant, this device comprises a coolant compressor C-1, and the coolant compressor cooler E-1 be connected successively with coolant compressor C-1 and coolant compressor divide flow container V-2; An ice chest, its heat exchanger components is plate-fin heat exchanger E-2; A heavy hydrocarbon separator V-1; A cold-producing medium pans V-3; First, second, third, fourth choke valve X-1, X-2, X-3, X-4; An injector J-1;
First heat exchanger channels 1 of plate-fin heat exchanger E-2 connects heavy hydrocarbon separator V-1, the arrival end of second heat exchanger channels of the top gas phase end connecting plate fin heat exchanger E-2 of heavy hydrocarbon separator V-1, and the port of export of the second heat exchanger channels connects LNG product storage tank;
Coolant compressor divides flow container V-2 liquid phase end after the 3rd heat exchanger channels 3 of plate-fin heat exchanger E-2, be connected to one end of second throttle X-2, is connected to coolant compressor C-1 entrance after the 5th heat exchanger channels 5 of the other end connecting plate fin heat exchanger E-2 of second throttle X-2;
Coolant compressor divides flow container V-2 gas phase end to be divided into two-way, and the first via is connected to the ejection gas arrival end of injector J-1 after connecting the 4th choke valve X-4; Second tunnel is divided into again two branch roads after the 4th heat exchanger channels 4 of plate-fin heat exchanger E-2, wherein the first branch road is connected to one end of first throttle valve X-1 after going out the 4th heat exchanger channels 4 of plate-fin heat exchanger E-2, coolant compressor C-1 entrance is connected to after 5th heat exchanger channels 5 of the other end connecting plate fin heat exchanger E-2 of first throttle valve X-1, second branch road continues to enter the 6th heat exchanger channels 6 after going out the 4th heat exchanger channels 4 of plate-fin heat exchanger E-2, is then connected to cold-producing medium pans through the 3rd choke valve X-3; The port of export of injector J-1 is connected to the pipeline between first throttle valve X-1 and the 5th heat exchanger channels 5 (arrival end), cold-producing medium pans V-3 gaseous phase outlet pipe is connected to the pipeline between first throttle valve X-1 and the 5th heat exchanger channels 5 (arrival end), and cold-producing medium pans V-3 liquid-phase outlet pipe is connected to the driven fluid arrival end of injector J-1.
The technical process of said apparatus is further illustrated below in conjunction with accompanying drawing.
When liquefying plant normally runs, its technical process comprises natural gas liquefaction and mixed-refrigerant cycle:
Natural gas liquefaction: first raw natural gas enters in the first passage 1 of plate-fin heat exchanger E-2 and carry out precooling, enter heavy hydrocarbon separator V-1 after being cooled to-30 DEG C ~-60 DEG C and carry out gas-liquid separation, be heavy hydrocarbon by isolated liquid bottom heavy hydrocarbon separator V-1, the second channel 2 entering plate-fin heat exchanger is continued by the isolated vapor phase stream stock in heavy hydrocarbon separator V-1 top, and be cooled to-130 DEG C ~-166 DEG C wherein, obtain liquefied natural gas and LNG.
Mixed-refrigerant cycle: mix refrigerant enters coolant compressor, be pressurized to 1.2 ~ 5.4MPa, after cooling, gas-liquid separation, vapor phase refrigerant by the road S-2 enters the four-way 4 of plate-fin heat exchanger, the reflux passage (Five-channel) 5 entering plate-fin heat exchanger after the end extraction of four-way 4 enters first throttle valve X-1 throttling to 0.2 ~ 0.8MPa provides cold for it, then returns coolant compressor entrance; Liquid phase refrigerant enters the third channel 3 of plate-fin heat exchanger, the reflux passage 5 entering plate-fin heat exchanger after the end extraction of third channel 3 enters second throttle X-2 throttling to 0.2 ~ 0.8MPa provides cold for it, then returns coolant compressor entrance.
When liquefying plant stops, the technical process that mix refrigerant reclaims is as follows:
The Hexamermis spp 6 being specifically designed to and reclaiming mix refrigerant is increased in plate-fin heat exchanger, the vapor phase refrigerant going out coolant compressor flows through pipeline S-2 successively, be liquefied after the four-way 4 of plate-fin heat exchanger and Hexamermis spp 6, go out the cold-producing medium of Hexamermis spp 6 through choke valve X-3 reducing pressure by regulating flow to 0.2 ~ 0.8MPa, liquid phase after throttling enters in cold-producing medium pans V-3 and stores, gas phase enters in pipeline S-4 from the gas phase of cold-producing medium pans V-3, then the entrance of coolant compressor is returned through the reflux passage 5 of plate-fin heat exchanger, coolant compressor cooler is entered after coolant compressor supercharging, then divide after flow container gas-liquid separation through coolant compressor and enter plate-fin heat exchanger heat exchanger channels repetition said process (namely, liquefaction, throttling process), the liquid phase going out coolant compressor can be stored in coolant compressor outlet tank V-2 or enter in a normal temperature refrigerant-recovery tank arranged separately from the liquid-phase outlet of coolant compressor outlet tank V-2 and store.
When liquefying plant is driven again, adopt following technical process that mix refrigerant is refilled refrigerant-cycle systems:
Branch line S-1 is set at coolant compressor outlet tank V-2 gaseous phase outlet, when again driving for liquefying plant or adjust mix refrigerant proportioning, the cold-producing medium in cold-producing medium pans V-3 is refilled in refrigerant-cycle systems; Now coolant compressor starts, vapor phase refrigerant through coolant compressor supercharging enters injector J-1 by pipeline S-1 after the 4th choke valve X-4, as power gas, the liquid phase injection in cold-producing medium pans V-3 is entered in injector J-1, after the two mixing, the reflux passage 5 of S-4, plate-fin heat exchanger enters coolant compressor entrance by the road successively, and the cold-producing medium thus in cold-producing medium pans V-3 is refilled in refrigerant-cycle systems.
Also recovery and the re-injection flow process of above-mentioned cold-producing medium can be adopted during hybrid refrigeration liquefying plant adjustment cold-producing medium proportioning.Wherein, when adjusting mix refrigerant proportioning, implementing the technical process that mix refrigerant reclaims, at the end of adjustment mix refrigerant, implementing the technical process that above-mentioned mix refrigerant refills refrigerant-cycle systems.
Claims (1)
1. one kind can realize the natural gas liquefaction device of refrigerant-recovery, re-injection, it is characterized in that, this device comprises coolant compressor, the coolant compressor cooler be connected successively with coolant compressor and coolant compressor divide flow container, ice chest, and its heat exchanger components is plate-fin heat exchanger, heavy hydrocarbon separator, cold-producing medium pans, first, second, third, fourth choke valve, and injector;
First heat exchanger channels of plate-fin heat exchanger connects heavy hydrocarbon separator, the arrival end of the second heat exchanger channels of the top gas phase end connecting plate fin heat exchanger of heavy hydrocarbon separator, and the port of export of the second heat exchanger channels connects LNG product storage tank;
Coolant compressor divides flow container liquid phase end after the 3rd heat exchanger channels of plate-fin heat exchanger, be connected to one end of second throttle, is connected to coolant compressor entrance after the 5th heat exchanger channels of the other end connecting plate fin heat exchanger of second throttle;
Coolant compressor divides flow container gas phase end to be divided into two-way, and the first via is connected to the ejection gas arrival end of injector after connecting the 4th choke valve; Second tunnel is divided into again two branch roads after the 4th heat exchanger channels of plate-fin heat exchanger, wherein the first branch road is connected to one end of first throttle valve after going out the 4th heat exchanger channels of plate-fin heat exchanger, coolant compressor entrance is connected to after 5th heat exchanger channels of the other end connecting plate fin heat exchanger of first throttle valve, second branch road continues to enter the 6th heat exchanger channels after going out the 4th heat exchanger channels of plate-fin heat exchanger, is then connected to cold-producing medium pans through the 3rd choke valve; The ejection gas port of export of injector is connected to the pipeline between first throttle valve and the 5th heat exchanger channels, cold-producing medium pans gaseous phase outlet pipe is also connected to the pipeline between first throttle valve and the 5th heat exchanger channels, and cold-producing medium pans liquid-phase outlet pipe is connected to the driven fluid arrival end of injector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520315219.0U CN204678750U (en) | 2015-05-15 | 2015-05-15 | A kind of natural gas liquefaction device realizing mix refrigerant recovery, re-injection |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520315219.0U CN204678750U (en) | 2015-05-15 | 2015-05-15 | A kind of natural gas liquefaction device realizing mix refrigerant recovery, re-injection |
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| CN204678750U true CN204678750U (en) | 2015-09-30 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3351881A1 (en) * | 2017-01-24 | 2018-07-25 | GE Oil & Gas, LLC | Continuous mixed refrigerant optimization for the production of liquefied natural gas (lng) |
| CN111397082A (en) * | 2020-04-01 | 2020-07-10 | 宁波奥克斯电气股份有限公司 | Refrigerant recovery system and control method |
| CN114484951A (en) * | 2022-02-08 | 2022-05-13 | 珠海格力电器股份有限公司 | Mixed refrigerant recovery and purification device and control method thereof |
| US11460244B2 (en) | 2016-06-30 | 2022-10-04 | Baker Hughes Oilfield Operations Llc | System and method for producing liquefied natural gas |
| CN115164461A (en) * | 2022-06-16 | 2022-10-11 | 四川七化建化工工程有限公司 | Mixed refrigerant recovery system and method for liquefied natural gas device |
-
2015
- 2015-05-15 CN CN201520315219.0U patent/CN204678750U/en not_active Withdrawn - After Issue
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11460244B2 (en) | 2016-06-30 | 2022-10-04 | Baker Hughes Oilfield Operations Llc | System and method for producing liquefied natural gas |
| EP3351881A1 (en) * | 2017-01-24 | 2018-07-25 | GE Oil & Gas, LLC | Continuous mixed refrigerant optimization for the production of liquefied natural gas (lng) |
| CN108344251A (en) * | 2017-01-24 | 2018-07-31 | 通用电气石油和天然气有限责任公司 | The continuous mix refrigerant of production for liquefied natural gas (LNG) optimizes |
| CN108344251B (en) * | 2017-01-24 | 2022-08-23 | 通用电气石油和天然气有限责任公司 | Continuous mixed refrigerant optimization for production of Liquefied Natural Gas (LNG) |
| CN111397082A (en) * | 2020-04-01 | 2020-07-10 | 宁波奥克斯电气股份有限公司 | Refrigerant recovery system and control method |
| CN114484951A (en) * | 2022-02-08 | 2022-05-13 | 珠海格力电器股份有限公司 | Mixed refrigerant recovery and purification device and control method thereof |
| CN114484951B (en) * | 2022-02-08 | 2022-12-02 | 珠海格力电器股份有限公司 | Mixed refrigerant recovery and purification device and control method thereof |
| CN115164461A (en) * | 2022-06-16 | 2022-10-11 | 四川七化建化工工程有限公司 | Mixed refrigerant recovery system and method for liquefied natural gas device |
| CN115164461B (en) * | 2022-06-16 | 2024-01-19 | 四川七化建化工工程有限公司 | Mixed refrigerant recovery system and method of liquefied natural gas device |
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