CN107906362A - A kind of LNG gasification system - Google Patents
A kind of LNG gasification system Download PDFInfo
- Publication number
- CN107906362A CN107906362A CN201710338821.XA CN201710338821A CN107906362A CN 107906362 A CN107906362 A CN 107906362A CN 201710338821 A CN201710338821 A CN 201710338821A CN 107906362 A CN107906362 A CN 107906362A
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- lng
- valve
- heaters
- storage tank
- shut
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- 238000002309 gasification Methods 0.000 title claims abstract description 48
- 238000003795 desorption Methods 0.000 claims abstract description 26
- 230000001105 regulatory effect Effects 0.000 claims abstract description 15
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 4
- 239000007791 liquid phase Substances 0.000 claims description 16
- 239000012071 phase Substances 0.000 claims description 15
- 230000008859 change Effects 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 27
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 210000004209 hair Anatomy 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
- F17C7/02—Discharging liquefied gases
- F17C7/04—Discharging liquefied gases with change of state, e.g. vaporisation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
- F17C13/025—Special adaptations of indicating, measuring, or monitoring equipment having the pressure as the parameter
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
- F17C13/026—Special adaptations of indicating, measuring, or monitoring equipment having the temperature as the parameter
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/04—Arrangement or mounting of valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
- F17C2205/0332—Safety valves or pressure relief valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0338—Pressure regulators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0302—Heat exchange with the fluid by heating
- F17C2227/0309—Heat exchange with the fluid by heating using another fluid
- F17C2227/0316—Water heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/04—Methods for emptying or filling
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/0626—Pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/0631—Temperature
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The present invention provides a kind of LNG gasification system, including：LNG storage tank, air temperature type LNG gasification device is connected with the LNG storage tank, water-bath type LNG heaters, BOG heaters, storage tank boosting gasifier, EAR heaters, the LNG storage tank is connected to LNG tank cars by booster of unloading, the water-bath type LNG heaters, BOG heaters are connected to pressure regulating metering device by room temperature gas phase pipe, pressure regulating metering device is connected to the municipal gas supply pipe of middle pressure, device for adding odor is equipped between medium pressure municipal administration gas supply pipe and pressure regulating metering device, ball valve is equipped between device for adding odor and the municipal gas supply pipe of middle pressure, spark arrester is installed on the desorption tube of diffusing tower upstream.Present invention design is reasonable, and work efficiency is high, and the low temperature LNG after supercharging, into main air-heating type gasifier, with being converted into gaseous state NG after air heat-exchange and raising temperature, outlet temperature is 10 DEG C lower than environment temperature, most afterwards through pressure regulation, metering, after be sent into gas ductwork.
Description
Technical field
The present invention relates to fuel gas transmission field, is specially a kind of LNG gasification system.
Background technology
LNG has become the main source of the gas or transition view that can not use pipeline gas supply city at present, and many
Use the supplement source of the gas or peak regulation source of the gas in pipeline gas supply city.LNG gasification station is one and receives, stores and distribute LNG
Satellite station, and cities and towns or gas enterprise from manufacturer transfer LNG to the intermediate regulations place of user.LNG gasification station relies on
Its construction period it is short and can the satisfaction gas market demand rapidly advantage, gradually in the numerous economic hairs of China's southeastern coast
Reach, the small and medium-sized cities of energy scarcity are built up, become the transition supply facility before permanent supply facility or pipeline gas reach.
LNG is transported to gasification station by tank car, increases groove interior pressure using LNG boosters of unloading, by LNG in tank car send to
Storage in LNG low-temperature storage tanks.When being arranged outside LNG storage tank, first pass through storage tank from pressure charging system, raise pressure of storage tank, so
Storage tank liquid-phase outlet valve is opened afterwards, is sent the LNG in storage tank to gasifier by pressure differential, through pressure regulation, metering, adds the work such as smelly
Sequence is sent into municipal gas ductwork.When outdoor environment temperature is relatively low, and the natural gas temperature of air-heating type gasifier outlet is less than 5 DEG C,
Series connection water-bath type heater need to be exported in air-heating type gasifier, the natural gas after gasification is heated.But current gasification
System design is unreasonable, inconvenient to use, and there are security risk.
The content of the invention
Technical problem solved by the invention is to provide a kind of LNG gasification system, to solve to carry in above-mentioned background technology
The problem of going out.
Technical problem solved by the invention is realized using following technical scheme：A kind of LNG gasification system, including：LNG
Storage tank, air temperature type LNG gasification device, water-bath type LNG heaters, BOG heaters, storage tank boosting gas are connected with the LNG storage tank
Change device, EAR heaters, the LNG storage tank is connected to LNG tank cars, the water-bath type LNG heaters, BOG by booster of unloading
Heater is connected to pressure regulating metering device by room temperature gas phase pipe, and pressure regulating metering device is connected to the municipal gas supply pipe of middle pressure,
Device for adding odor is equipped between medium pressure municipal administration gas supply pipe and pressure regulating metering device, device for adding odor is supplied with the municipal combustion gas of middle pressure
Ball valve, the LNG storage tank, air temperature type LNG gasification device, water-bath type LNG heaters, BOG heaters, storage tank liter are equipped between tracheae
Pressure gasifier, EAR heaters are connected to diffusing tower by desorption tube, and spark arrester is provided with the desorption tube of diffusing tower upstream.
One LNG liquid-phase tube of the LNG storage tank is connected to LNG fillers, and side is connected to desorption tube on LNG liquid-phase tubes, puts
Separate tube is equipped with shut-off valve, and in parallel on shut-off valve to be equipped with safety valve, another LNG liquid-phase tube of the LNG storage tank is connected to storage
Tank boosts gasifier, and storage tank boosting gasifier desorption tube is connected to diffusing tower, and desorption tube is equipped with shut-off valve, parallel connection on shut-off valve
Equipped with safety valve.
The LNG liquid-phase tubes of the LNG storage tank are connected to air temperature type LNG gasification device, air temperature type LNG gasification device and LNG storage tank
Between LNG liquid-phase tubes be equipped with pneumatic operated valve, shut-off valve, safety valve is installed in LNG storage tank.
The room temperature gas phase pipe of the air temperature type LNG gasification device is connected to water-bath type LNG heaters, water-bath type LNG heaters
Room temperature gas phase pipe between air temperature type LNG gasification device is equipped with shut-off valve, and the desorption tube of air temperature type LNG gasification device, which is equipped with, to be cut
Only valve, it is in parallel on shut-off valve to be equipped with safety valve.
Be equipped with shut-off valve between desorption tube between the water-bath type LNG heaters and spark arrester, on shut-off valve parallel connection set
There is safety valve.
The room temperature gas phase pipe of the BOG heaters is connected to water-bath type LNG heaters, water-bath type LNG heaters and air temperature
Room temperature gas phase pipe between formula LNG gasification device is equipped with shut-off valve, and the desorption tube of air temperature type LNG gasification device is equipped with shut-off valve,
It is in parallel on shut-off valve to be equipped with safety valve.
The pressure regulating metering device includes two sets of pressure regulation metering pipelines in parallel, and the pressure regulation metering pipeline is equipped with four
Ball valve, is equipped with turbine flowmeter, is equipped between the 3rd ball valve and the 4th ball valve between first ball valve and second ball valve
Two pressure regulators.
Compared with prior art, the beneficial effects of the invention are as follows：Present invention design is reasonable, and work efficiency is high, after supercharging
Low temperature LNG, into main air-heating type gasifier, with being converted into gaseous state NG after air heat-exchange and raising temperature, outlet temperature compares environment
Temperature is 10 DEG C low, most afterwards through pressure regulation, metering, after be sent into gas ductwork.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention.
The LNG storage tank pipeline that Fig. 2 is the present invention connects enlarged drawing.
The air temperature type LNG gasification device pipeline that Fig. 3 is the present invention connects enlarged drawing.
The water-bath type LNG heater lines that Fig. 4 is the present invention connect enlarged drawing.
The pressure regulating metering device pipeline that Fig. 5 is the present invention connects enlarged drawing.
Embodiment
In order to make the implement technical means of the present invention, creation characteristic, reached purpose and effect easy to understand, tie below
Conjunction is specifically illustrating, and the present invention is further explained.
As shown in Fig. 1~5, a kind of LNG gasification system, including：LNG storage tank 1, is connected with air temperature type in the LNG storage tank 1
LNG gasification device 2, water-bath type LNG heaters 3, BOG heaters 4, storage tank boosting gasifier 5, EAR heaters 6, the LNG storage tank
1 is connected to LNG tank cars by booster of unloading, and the water-bath type LNG heaters 3, BOG heaters 4 pass through room temperature gas phase Guan Lian
Pressure regulating metering device 7 is connected to, pressure regulating metering device 7 is connected to the municipal gas supply pipe of middle pressure, medium pressure municipal administration gas supply
Device for adding odor 8 is equipped between pipe and pressure regulating metering device 7, ball valve is equipped between device for adding odor 8 and the municipal gas supply pipe of middle pressure,
The LNG storage tank 1, air temperature type LNG gasification device 2, water-bath type LNG heaters 3, BOG heaters 4, storage tank boosting gasifier 5, EAR
Heater 6 is connected to diffusing tower by desorption tube, and spark arrester is provided with the desorption tube of diffusing tower upstream.
One LNG liquid-phase tube of the LNG storage tank 1 is connected to LNG fillers, and side is connected to desorption tube on LNG liquid-phase tubes, puts
Separate tube is equipped with shut-off valve, and in parallel on shut-off valve to be equipped with safety valve, another LNG liquid-phase tube of the LNG storage tank 1 is connected to storage
Tank boosts gasifier 5, and storage tank boosting 5 desorption tube of gasifier is connected to diffusing tower, and desorption tube is equipped with shut-off valve, on shut-off valve simultaneously
Connection is equipped with safety valve.
The LNG liquid-phase tubes of the LNG storage tank 1 are connected to air temperature type LNG gasification device 2, and air temperature type LNG gasification device 2 and LNG is stored up
LNG liquid-phase tubes between tank 1 are equipped with pneumatic operated valve, shut-off valve, and safety valve is provided with LNG storage tank 1.
The room temperature gas phase pipe of the air temperature type LNG gasification device 2 is connected to water-bath type LNG heaters 3, water-bath type LNG heating
Room temperature gas phase pipe between device 3 and air temperature type LNG gasification device 2 is equipped with shut-off valve, on the desorption tube of air temperature type LNG gasification device 2
It is in parallel on shut-off valve to be equipped with safety valve equipped with shut-off valve.
Be equipped with shut-off valve between desorption tube between the water-bath type LNG heaters 3 and spark arrester, on shut-off valve parallel connection set
There is safety valve.
The room temperature gas phase pipe of the BOG heaters 4 is connected to water-bath type LNG heaters 3, water-bath type LNG heaters 3 and sky
Room temperature gas phase pipe between warm formula LNG gasification device 2 is equipped with shut-off valve, and the desorption tube of air temperature type LNG gasification device 2 is equipped with cut-off
Valve, it is in parallel on shut-off valve to be equipped with safety valve.
The pressure regulating metering device 7 includes two sets of pressure regulation metering pipelines in parallel, and the pressure regulation metering pipeline is equipped with four
A ball valve, is equipped with turbine flowmeter, is set between the 3rd ball valve and the 4th ball valve between first ball valve and second ball valve
There are two pressure regulators.
LNG of the present invention is stored using tank container, is transported to LNG gasification station by highway, is passed through unloading deck in unloading deck
The horizontal special booster of unloading set is pressurized container storage tank, is sent LNG to 60m3 low temperature LNG tank using pressure difference and stored.
Under the conditions of inoperative, the temperature of LNG storage is -162 DEG C in storage tank, and pressure is normal pressure；Under operating condition, booster is by storage tank
LNG supercharging.Low temperature LNG after supercharging, into main air-heating type gasifier, with being converted into gaseous state NG after air heat-exchange and raising temperature
Degree, outlet temperature is 10 DEG C lower than environment temperature, most afterwards through pressure regulation, metering, after be sent into gas ductwork.
The basic principles, main features and the advantages of the invention have been shown and described above.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and modifications of the present invention are possible, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the present invention by appended claims and
Its equivalent thereof.
Claims (7)
1. a kind of LNG gasification system, including：LNG storage tank, it is characterised in that：Air temperature type LNG gas is connected with the LNG storage tank
Change device, water-bath type LNG heaters, BOG heaters, storage tank boosting gasifier, EAR heaters, the LNG storage tank increases by unloading
Depressor is connected to LNG tank cars, and the water-bath type LNG heaters, BOG heaters are connected to pressure regulation metering by room temperature gas phase pipe and fill
Put, pressure regulating metering device is connected to the municipal gas supply pipe of middle pressure, medium pressure municipal administration gas supply pipe and pressure regulating metering device
Between be equipped with device for adding odor, be equipped with ball valve, the LNG storage tank, air temperature type between device for adding odor and the municipal gas supply pipe of middle pressure
LNG gasification device, water-bath type LNG heaters, BOG heaters, storage tank boosting gasifier, EAR heaters are connected to by desorption tube
Diffusing tower, is provided with spark arrester on the desorption tube of diffusing tower upstream.
A kind of 2. LNG gasification system according to claim 1, it is characterised in that：One LNG liquid phase of the LNG storage tank
Pipe is connected to LNG fillers, and other on LNG liquid-phase tubes to be connected to desorption tube, desorption tube is equipped with shut-off valve, on shut-off valve parallel connection be equipped with
Safety valve, another LNG liquid-phase tube of the LNG storage tank are connected to storage tank boosting gasifier, storage tank boosting gasifier desorption tube
It is connected to diffusing tower, desorption tube is equipped with shut-off valve, in parallel on shut-off valve to be equipped with safety valve.
A kind of 3. LNG gasification system according to claim 1, it is characterised in that：The LNG liquid-phase tubes of the LNG storage tank connect
Air temperature type LNG gasification device is connected to, the LNG liquid-phase tubes between air temperature type LNG gasification device and LNG storage tank are equipped with pneumatic operated valve, cut-off
Valve, is provided with safety valve in LNG storage tank.
A kind of 4. LNG gasification system according to claim 1, it is characterised in that：The room temperature of the air temperature type LNG gasification device
Gas phase pipe is connected to water-bath type LNG heaters, the room temperature gas phase pipe between water-bath type LNG heaters and air temperature type LNG gasification device
It is equipped with shut-off valve, the desorption tube of air temperature type LNG gasification device is equipped with shut-off valve, in parallel on shut-off valve to be equipped with safety valve.
A kind of 5. LNG gasification system according to claim 1, it is characterised in that：The water-bath type LNG heaters and back-fire relief
It is equipped with shut-off valve between desorption tube between device, it is in parallel on shut-off valve to be equipped with safety valve.
A kind of 6. LNG gasification system according to claim 1, it is characterised in that：The room temperature gas phase pipe of the BOG heaters
Water-bath type LNG heaters are connected to, the room temperature gas phase pipe between water-bath type LNG heaters and air temperature type LNG gasification device is equipped with
Shut-off valve, the desorption tube of air temperature type LNG gasification device are equipped with shut-off valve, in parallel on shut-off valve to be equipped with safety valve.
A kind of 7. LNG gasification system according to claim 1, it is characterised in that：The pressure regulating metering device includes two sets
Pressure regulation metering pipeline in parallel, the pressure regulation metering pipeline is equipped with four ball valves, between first ball valve and second ball valve
Equipped with turbine flowmeter, two pressure regulators are equipped between the 3rd ball valve and the 4th ball valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710338821.XA CN107906362A (en) | 2017-05-15 | 2017-05-15 | A kind of LNG gasification system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710338821.XA CN107906362A (en) | 2017-05-15 | 2017-05-15 | A kind of LNG gasification system |
Publications (1)
| Publication Number | Publication Date |
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| CN107906362A true CN107906362A (en) | 2018-04-13 |
Family
ID=61840045
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201710338821.XA Pending CN107906362A (en) | 2017-05-15 | 2017-05-15 | A kind of LNG gasification system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108506722A (en) * | 2018-04-25 | 2018-09-07 | 天津良华新能源科技有限公司 | A kind of LNG gasification station |
| CN108716615A (en) * | 2018-06-14 | 2018-10-30 | 蚌埠艾普压缩机制造有限公司 | A kind of gasification installation for LNG |
| CN108799829A (en) * | 2018-06-14 | 2018-11-13 | 蚌埠艾普压缩机制造有限公司 | A kind of LNG gasification device |
| CN114087537A (en) * | 2020-08-24 | 2022-02-25 | 安瑞科(廊坊)能源装备集成有限公司 | Temperature control device for LNG (liquefied Natural gas) filling and LNG filling method |
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| CN202065680U (en) * | 2011-04-14 | 2011-12-07 | 北京中燃伟业燃气有限公司 | Liquefied natural gas (LNG) gasification pressure regulating gas supply device |
| CN202158352U (en) * | 2011-04-14 | 2012-03-07 | 北京中燃伟业燃气有限公司 | L-CNG (liquefied-compressed natural gas) dual-gas resource gas supply device |
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| CN108716615A (en) * | 2018-06-14 | 2018-10-30 | 蚌埠艾普压缩机制造有限公司 | A kind of gasification installation for LNG |
| CN108799829A (en) * | 2018-06-14 | 2018-11-13 | 蚌埠艾普压缩机制造有限公司 | A kind of LNG gasification device |
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| CN108716615B (en) * | 2018-06-14 | 2020-05-22 | 蚌埠艾普压缩机制造有限公司 | A gasification equipment for LNG |
| CN114087537A (en) * | 2020-08-24 | 2022-02-25 | 安瑞科(廊坊)能源装备集成有限公司 | Temperature control device for LNG (liquefied Natural gas) filling and LNG filling method |
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