CN103697327B - A kind of zero-emission liquid feeding system and method thereof - Google Patents

A kind of zero-emission liquid feeding system and method thereof Download PDF

Info

Publication number
CN103697327B
CN103697327B CN201310675721.8A CN201310675721A CN103697327B CN 103697327 B CN103697327 B CN 103697327B CN 201310675721 A CN201310675721 A CN 201310675721A CN 103697327 B CN103697327 B CN 103697327B
Authority
CN
China
Prior art keywords
valve
pump
storage tank
liquid
reservoir
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201310675721.8A
Other languages
Chinese (zh)
Other versions
CN103697327A (en
Inventor
程章展
鲁雪生
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU CRYOTE CRYOGENIC TECHNOLOGY CO., LTD.
Original Assignee
JIANGSU CRYOTE CRYOGENIC TECHNOLOGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JIANGSU CRYOTE CRYOGENIC TECHNOLOGY Co Ltd filed Critical JIANGSU CRYOTE CRYOGENIC TECHNOLOGY Co Ltd
Priority to CN201310675721.8A priority Critical patent/CN103697327B/en
Publication of CN103697327A publication Critical patent/CN103697327A/en
Application granted granted Critical
Publication of CN103697327B publication Critical patent/CN103697327B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

The invention discloses a kind of zero-emission liquid feeding system and method thereof, it comprises storage tank, heat exchanger, low-temperature receiver, reservoir, pump, liquid outlet, the first valve, the second valve, the 3rd valve; Wherein storage tank gas vent, the first valve, heat exchanger, reservoir, the 3rd valve, pump, liquid outlet are connected in turn, storage tank liquid outlet is connected with pump intake through the second valve, heat exchanger is connected with low-temperature receiver, liquid feeding system of the present invention can also comprise pump pond, makes pump be connected with pump pond or pump is placed in pump pond. The present invention is used for again condensation storage tank and flows into the boil-off gas in storage tank because leaking the hot boil-off gas generating and use procedure from external system, has avoided boil-off gas directly to discharge the environmental problem and the wasting of resources that cause.

Description

A kind of zero-emission liquid feeding system and method thereof
Technical field
The present invention relates to fluid storage and transportation art, relate in particular to a kind of zero-emission liquid feeding system and method thereof.
Background technology
In chemical industry, liquid is generally stored in large-scale storage tank. Some liquid, because boiling point is lower, easily absorb the generation of the leakage thermal conductance induced evaporation gas of storage tank. In use, because circulation needs, boil-off gas also can flow in storage tank from external system. The accumulation of boil-off gas will cause tank internal pressure to rise, to the withstand voltage formation test of storage tank. If storage tank by too high compression failure, will cause inner material to be directly discharged in environment, to environment, also cause direct economic loss simultaneously. Solve the original processing mode of boil-off gas problem for often initiatively discharge is a part of by boil-off gas at regular intervals, although this scheme has ensured the safety of storage tank, but make material in storage tank have certain loss, and the discharge of boil-off gas also pollutes the environment, and produce noise in discharge process.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, a kind of zero-emission liquid feeding system and method thereof are provided.
A kind of zero-emission liquid feeding system comprises storage tank, heat exchanger, low-temperature receiver, reservoir, pump, liquid outlet, the first valve, the second valve, the 3rd valve; Wherein storage tank gas vent, the first valve, heat exchanger, reservoir, the 3rd valve, pump, liquid outlet are connected in turn, and storage tank liquid outlet is connected with pump intake through the second valve, and heat exchanger is connected with low-temperature receiver.
A kind of zero-emission liquid feeding system comprises storage tank, heat exchanger, low-temperature receiver, reservoir, pump, liquid outlet, the first valve, the second valve, the 3rd valve, pump pond; Wherein storage tank gas vent, the first valve, heat exchanger, reservoir, the 3rd valve, pump pond the first entrance, pump, liquid outlet are connected in turn, and storage tank liquid outlet is connected with pump pond the second entrance through the second valve, and heat exchanger is connected with low-temperature receiver.
A kind of zero-emission liquid feeding system comprises storage tank, heat exchanger, low-temperature receiver, reservoir, pump, liquid outlet, the first valve, the second valve, the 3rd valve, pump pond; Wherein storage tank gas vent, the first valve, heat exchanger, reservoir, the 3rd valve, pump pond, the second valve, storage tank liquid outlet are connected in turn, and pump is placed in pump pond, and pump is connected with liquid outlet, and heat exchanger is connected with low-temperature receiver.
Described a kind of zero-emission liquid feeding system, the low-temperature receiver described in it is refrigeration plant or cold fluid.
Described a kind of zero-emission liquid feeding system, described in it, the pressure of the connector of storage tank and the second valve is greater than the pressure of pump pond and the second valve connector.
Described a kind of zero-emission liquid feeding system, described in it, the liquid level of storage tank is higher than the entrance of pump.
A kind of step of zero-emission liquid feeding method is as follows:
1) the first valve, the 3rd valve is initially closed condition, and the second valve is initially opening; Open the first valve, the gas in storage tank enters heat exchanger, after gas and low-temperature receiver heat exchange, is condensed into liquid, flows into reservoir; In reservoir, have after liquid, close the second valve, open the 3rd valve, the liquid in reservoir flows out from the 3rd valve, then is delivered to liquid outlet by pump, realizes boil-off gas liquefaction;
2) the 3rd valve is initially closed condition, and the second valve is initially opening; Liquid in storage tank flows out from the second valve, then is delivered to liquid outlet by pump.
A kind of step of zero-emission liquid feeding method is as follows:
1) the first valve, the 3rd valve is initially closed condition, and the second valve is initially opening; Open the first valve, the gas in storage tank enters heat exchanger, after gas and low-temperature receiver heat exchange, is condensed into liquid, flows into reservoir; In reservoir, have after liquid, close the second valve, open the 3rd valve, the liquid in reservoir is through the 3rd valve inflow pump pond, then is delivered to liquid outlet by pump, realizes boil-off gas liquefaction;
2) the 3rd valve is initially closed condition, and the second valve is initially opening; Liquid in storage tank is through the second valve inflow pump pond, then is delivered to liquid outlet by pump.
The present invention is used for again condensation storage tank and flows into the boil-off gas in storage tank because leaking the hot boil-off gas generating and use procedure from external system, has avoided boil-off gas directly to discharge the environmental problem and the wasting of resources that cause.
Brief description of the drawings
Fig. 1 is zero-emission liquid feeding system schematic;
Fig. 2 is zero-emission liquid feeding system (pump pond is connected with pump) schematic diagram;
Fig. 3 is zero-emission liquid feeding system (pump is in pump pond) schematic diagram;
In figure, storage tank 1, heat exchanger 2, low-temperature receiver 3, reservoir 4, pump 5, liquid outlet 6, the first valve 7.1, the second valve 7.2, the 3rd valve 7.3, pump pond 8.
Detailed description of the invention
As shown in Figure 1, zero-emission liquid feeding system comprises storage tank, heat exchanger, low-temperature receiver, reservoir, pump, liquid outlet, the first valve, the second valve, the 3rd valve; Wherein storage tank gas vent, the first valve, heat exchanger, reservoir, the 3rd valve, pump, liquid outlet are connected in turn, and storage tank liquid outlet is connected with pump intake through the second valve, and heat exchanger is connected with low-temperature receiver.
As shown in Figure 2, zero-emission liquid feeding system comprises storage tank, heat exchanger, low-temperature receiver, reservoir, pump, liquid outlet, the first valve, the second valve, the 3rd valve, pump pond; Wherein storage tank gas vent, the first valve, heat exchanger, reservoir, the 3rd valve, pump pond the first entrance, pump, liquid outlet are connected in turn, and storage tank liquid outlet is connected with pump pond the second entrance through the second valve, and heat exchanger is connected with low-temperature receiver.
As shown in Figure 3, zero-emission liquid feeding system comprises storage tank, heat exchanger, low-temperature receiver, reservoir, pump, liquid outlet, the first valve, the second valve, the 3rd valve, pump pond; Wherein storage tank gas vent, the first valve, heat exchanger, reservoir, the 3rd valve, pump pond, the second valve, storage tank liquid outlet are connected in turn, and pump is placed in pump pond, and pump is connected with liquid outlet, and heat exchanger is connected with low-temperature receiver.
Described low-temperature receiver is refrigeration plant or cold fluid. The pressure of the connector of described storage tank and the second valve is greater than the pressure of pump pond and the second valve connector. The liquid level of described storage tank is higher than the entrance of pump.
A kind of step of zero-emission liquid feeding method is as follows:
1) the first valve 7.1, the three valves 7.3 are initially closed condition, and the second valve 7.2 is initially opening; Open the first valve 7.1, the gas in storage tank 1 enters heat exchanger 2, after gas and low-temperature receiver 3 heat exchange, is condensed into liquid, flows into reservoir 4; In reservoir 4, have after liquid, close the second valve 7.2, open the 3rd valve 7.3, the liquid in reservoir 4 flows out from the 3rd valve 7.3, then is delivered to liquid outlet 6 by pump 5, realizes boil-off gas liquefaction;
2) the 3rd valve 7.3 is initially closed condition, and the second valve 7.2 is initially opening; Liquid in storage tank 1 flows out from the second valve 7.2, then is delivered to liquid outlet 6 by pump 5.
A kind of step of zero-emission liquid feeding method is as follows:
1) the first valve 7.1, the three valves 7.3 are initially closed condition, and the second valve 7.2 is initially opening; Open the first valve 7.1, the gas in storage tank 1 enters heat exchanger 2, after gas and low-temperature receiver 3 heat exchange, is condensed into liquid, flows into reservoir 4; In reservoir 4, have after liquid, close the second valve 7.2, open the 3rd valve 7.3, the liquid in reservoir 4 is through the 3rd valve 7.3 inflow pump ponds 8, then is delivered to liquid outlet 6 by pump 5, realizes boil-off gas liquefaction;
2) the 3rd valve 7.3 is initially closed condition, and the second valve 7.2 is initially opening; Liquid in storage tank 1 is through the second valve 7.2 inflow pump ponds 8, then is delivered to liquid outlet 6 by pump 5.
The course of work of the present invention is as follows:
Boil-off gas in storage tank arrives heat exchanger by the first valve, with low-temperature receiver heat exchange, is condensed into liquid after transferring heat to low-temperature receiver. Liquid flows into reservoir and stores. Reservoir reaches after the liquid level of setting, flows out, and be delivered to liquid outlet by pump from the 3rd valve. Liquid in storage tank also can and be delivered to liquid outlet by pump by the second valve. Liquid, before entering pump, can be introduced into according to actual needs pump pond and store.
The present invention is used for again condensation storage tank and flows into the boil-off gas in storage tank because leaking the hot boil-off gas generating and use procedure from external system, has avoided boil-off gas directly to discharge the environmental problem and the wasting of resources that cause.

Claims (5)

1. a zero-emission liquid feeding method, is characterized in that, its step is as follows:
1) the first valve (7.1), the 3rd valve (7.3) is initially closed condition, and the second valve (7.2) is initially opening; Open the first valve (7.1), the gas in storage tank (1) enters heat exchanger (2), after gas and low-temperature receiver (3) heat exchange, is condensed into liquid, flows into reservoir (4); Reservoir has after liquid in (4), close the second valve (7.2), open the 3rd valve (7.3), the liquid in reservoir (4) flows out from the 3rd valve (7.3), be delivered to liquid outlet (6) by pump (5) again, realize boil-off gas liquefaction;
2) the 3rd valve (7.3) is initially closed condition, and the second valve (7.2) is initially opening; Liquid in storage tank (1) flows out from the second valve (7.2), then is delivered to liquid outlet (6) by pump (5).
2. a zero-emission liquid feeding method, is characterized in that, its step is as follows:
1) the first valve (7.1), the 3rd valve (7.3) is initially closed condition, and the second valve (7.2) is initially opening; Open the first valve (7.1), the gas in storage tank (1) enters heat exchanger (2), after gas and low-temperature receiver (3) heat exchange, is condensed into liquid, flows into reservoir (4); Reservoir has after liquid in (4), close the second valve (7.2), open the 3rd valve (7.3), the liquid in reservoir (4) is through the 3rd valve (7.3) inflow pump pond (8), be delivered to liquid outlet (6) by pump (5) again, realize boil-off gas liquefaction;
2) the 3rd valve (7.3) is initially closed condition, and the second valve (7.2) is initially opening; Liquid in storage tank (1) is through the second valve (7.2) inflow pump pond (8), then is delivered to liquid outlet (6) by pump (5).
3. use a zero-emission liquid feeding system for method as claimed in claim 1, it is characterized in that comprising storage tank (1), heat exchanger (2), low-temperature receiver (3), reservoir (4), pump (5), liquid outlet (6), the first valve (7.1), the second valve (7.2), the 3rd valve (7.3); Wherein storage tank (1) gas vent, the first valve (7.1), heat exchanger (2), reservoir (4), the 3rd valve (7.3), pump (5), liquid outlet (6) are connected in turn, storage tank (1) liquid outlet is connected with pump (5) entrance through the second valve (7.2), and heat exchanger (2) is connected with low-temperature receiver (3); Described low-temperature receiver (3) is refrigeration plant or cold fluid; The pressure of the connector of described storage tank (1) and the second valve (7.2) is greater than the pressure of pump pond (8) and the second valve (7.2) connector; The liquid level of described storage tank (1) is higher than the entrance of pump (5).
4. use a zero-emission liquid feeding system for method as claimed in claim 2, it is characterized in that comprising storage tank (1), heat exchanger (2), low-temperature receiver (3), reservoir (4), pump (5), liquid outlet (6), the first valve (7.1), the second valve (7.2), the 3rd valve (7.3), pump pond (8); Wherein storage tank (1) gas vent, the first valve (7.1), heat exchanger (2), reservoir (4), the 3rd valve (7.3), pump pond (8) first entrances, pump (5), liquid outlet (6) are connected in turn, storage tank (1) liquid outlet is connected with pump pond (8) second entrances through the second valve (7.2), and heat exchanger (2) is connected with low-temperature receiver (3); Described low-temperature receiver (3) is refrigeration plant or cold fluid; The pressure of the connector of described storage tank (1) and the second valve (7.2) is greater than the pressure of pump pond (8) and the second valve (7.2) connector; The liquid level of described storage tank (1) is higher than the entrance of pump (5).
5. use a zero-emission liquid feeding system for method as claimed in claim 2, it is characterized in that comprising storage tank (1), heat exchanger (2), low-temperature receiver (3), reservoir (4), pump (5), liquid outlet (6), the first valve (7.1), the second valve (7.2), the 3rd valve (7.3), pump pond (8); Wherein storage tank (1) gas vent, the first valve (7.1), heat exchanger (2), reservoir (4), the 3rd valve (7.3), pump pond (8), the second valve (7.2), storage tank (1) liquid outlet are connected in turn, pump (5) is placed in pump pond (8), pump (5) is connected with liquid outlet (6), and heat exchanger (2) is connected with low-temperature receiver (3); Described low-temperature receiver (3) is refrigeration plant or cold fluid; The pressure of the connector of described storage tank (1) and the second valve (7.2) is greater than the pressure of pump pond (8) and the second valve (7.2) connector; The liquid level of described storage tank (1) is higher than the entrance of pump (5).
CN201310675721.8A 2013-12-13 2013-12-13 A kind of zero-emission liquid feeding system and method thereof Expired - Fee Related CN103697327B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310675721.8A CN103697327B (en) 2013-12-13 2013-12-13 A kind of zero-emission liquid feeding system and method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310675721.8A CN103697327B (en) 2013-12-13 2013-12-13 A kind of zero-emission liquid feeding system and method thereof

Publications (2)

Publication Number Publication Date
CN103697327A CN103697327A (en) 2014-04-02
CN103697327B true CN103697327B (en) 2016-05-18

Family

ID=50358951

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310675721.8A Expired - Fee Related CN103697327B (en) 2013-12-13 2013-12-13 A kind of zero-emission liquid feeding system and method thereof

Country Status (1)

Country Link
CN (1) CN103697327B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104110574B (en) * 2014-07-29 2016-08-31 江苏克劳特低温技术有限公司 A kind of cryogenic gas condensate recovery system and method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101421554A (en) * 2006-04-13 2009-04-29 氟石科技公司 Lng vapor handling configurations and methods
CN101975335A (en) * 2010-09-26 2011-02-16 上海交通大学 Reliquefaction device for boil-off gas from liquefied natural gas vehicle gas filling station
CN102182919A (en) * 2011-03-26 2011-09-14 宁波鲍斯能源装备股份有限公司 Device and method for recovery and reliquefaction of boil-off gas of liquefied natural gas
CN102269327A (en) * 2011-07-28 2011-12-07 中国寰球工程公司 Recovery system and recovery method for vapor in storage tank
CN103443435A (en) * 2011-03-11 2013-12-11 大宇造船海洋株式会社 Method for driving system for supplying fuel to marine structure having re-iquefying device and high-<wbr/>pressure natural gas injection engine
CN203604986U (en) * 2013-12-13 2014-05-21 杭州克劳特低温设备有限公司 Zero-emission liquid charging system

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58180898A (en) * 1982-04-14 1983-10-22 Ishikawajima Harima Heavy Ind Co Ltd Method and apparatus for cooling low-temperature piping
JPH02240499A (en) * 1989-03-14 1990-09-25 Chiyoda Corp Evaporated gas processing for liquefied natural gas storage facility
JP3250233B2 (en) * 1991-05-13 2002-01-28 石川島播磨重工業株式会社 Heavyweight LNG tank prevention device
JP3664862B2 (en) * 1997-10-03 2005-06-29 三菱重工業株式会社 LNG cold heat storage method and apparatus, and BOG reliquefaction method using cold storage heat and apparatus thereof
JP4996987B2 (en) * 2007-06-12 2012-08-08 東京瓦斯株式会社 Reliquefaction device and reliquefaction method for BOG generated in LNG storage tank
JP2008309190A (en) * 2007-06-12 2008-12-25 Tokyo Gas Co Ltd Device and method for re-liquefying bog generated in lng storage tank

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101421554A (en) * 2006-04-13 2009-04-29 氟石科技公司 Lng vapor handling configurations and methods
CN101975335A (en) * 2010-09-26 2011-02-16 上海交通大学 Reliquefaction device for boil-off gas from liquefied natural gas vehicle gas filling station
CN103443435A (en) * 2011-03-11 2013-12-11 大宇造船海洋株式会社 Method for driving system for supplying fuel to marine structure having re-iquefying device and high-<wbr/>pressure natural gas injection engine
CN102182919A (en) * 2011-03-26 2011-09-14 宁波鲍斯能源装备股份有限公司 Device and method for recovery and reliquefaction of boil-off gas of liquefied natural gas
CN102269327A (en) * 2011-07-28 2011-12-07 中国寰球工程公司 Recovery system and recovery method for vapor in storage tank
CN203604986U (en) * 2013-12-13 2014-05-21 杭州克劳特低温设备有限公司 Zero-emission liquid charging system

Also Published As

Publication number Publication date
CN103697327A (en) 2014-04-02

Similar Documents

Publication Publication Date Title
CN104141881A (en) Heat transfer system utilizing normal temperature compressor to compress cryogenic medium
CN204372900U (en) Boiler blow-off waste-heat recovery device
CN103697327B (en) A kind of zero-emission liquid feeding system and method thereof
CN204421694U (en) Can the titanium tube heat exchanger of effective improving heat exchanging efficiency
CN106066681A (en) Cabinet-level computer server cooling system
CN203604986U (en) Zero-emission liquid charging system
CN203262159U (en) Dairy product ultra high temperature sterilization system
CN203968568U (en) A kind of airborne liquid cooling system
CN204187824U (en) There is the Teat pump boiler of air injection enthalpy-increasing
CN204569398U (en) A kind of novel practical refrigerant fluid filling structure
CN202802797U (en) Negative pressure steam heating equipment
CN205156674U (en) Closed -system cooling tower system of preventing frostbite
CN204051648U (en) The hot water temperature keeping device of reactor
CN105363320B (en) A kind of new and effective dealcoholysis formaldehyde absorbing tower
CN203911671U (en) Hydropower station unit energy conservation and environment protection phase change cooling device
CN203132219U (en) Water-consumption-free air-sac respiration condenser
CN206056383U (en) A kind of heat exchanger circulation
CN204247158U (en) Thinning vessel condenser pipe
CN205284885U (en) Pasteurization machine cooling hot water recovery utilizes device
CN204717840U (en) A kind of villa type solar energy and various energy resources complementary hot-water system
CN103727663A (en) Crude oil heating system of directly-heated type air source heat pump
CN104019543A (en) Waste water heat energy recycling device
CN203671908U (en) Directly-heated type air source heat pump crude oil heating system
CN205783221U (en) Eliminate the device of pump chamber gas collection in heating system
CN203323104U (en) Exhaust waste heat recycling device of deaerator

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
ASS Succession or assignment of patent right

Owner name: JIANGSU CROUT CRYOGENIC TECHNOLOGY CO., LTD.

Free format text: FORMER OWNER: HANGZHOU KELAOTE LOW TEMPERATURE EQUIPMENT CO., LTD.

Effective date: 20141211

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 310007 HANGZHOU, ZHEJIANG PROVINCE TO: 213022 CHANGZHOU, JIANGSU PROVINCE

TA01 Transfer of patent application right

Effective date of registration: 20141211

Address after: 213022 Jiangsu city of Changzhou province Hehai West New District No. 538 state electromechanical Park Building No. 17

Applicant after: JIANGSU CRYOTE CRYOGENIC TECHNOLOGY CO., LTD.

Address before: Room 161, C building, No. 525 Xixi Road, Xihu District, Zhejiang, Hangzhou 310007, China

Applicant before: HANGZHOU KELAOTE LOW TEMPERATURE EQUIPMENT CO., LTD.

C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160518

Termination date: 20191213