CN206478441U - Liquefied natural gas BOG recovery systems - Google Patents

Liquefied natural gas BOG recovery systems Download PDF

Info

Publication number
CN206478441U
CN206478441U CN201621489929.6U CN201621489929U CN206478441U CN 206478441 U CN206478441 U CN 206478441U CN 201621489929 U CN201621489929 U CN 201621489929U CN 206478441 U CN206478441 U CN 206478441U
Authority
CN
China
Prior art keywords
bog
natural gas
liquefied natural
gas
engine
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.)
Active
Application number
CN201621489929.6U
Other languages
Chinese (zh)
Inventor
张冲
梁鹏飞
梅亮
郝世超
刘成荣
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.)
China Shipbuilding Heavy Industries (shanghai) New Energy Co Ltd
Original Assignee
China Shipbuilding Heavy Industries (shanghai) New Energy 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 China Shipbuilding Heavy Industries (shanghai) New Energy Co Ltd filed Critical China Shipbuilding Heavy Industries (shanghai) New Energy Co Ltd
Priority to CN201621489929.6U priority Critical patent/CN206478441U/en
Application granted granted Critical
Publication of CN206478441U publication Critical patent/CN206478441U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/30Use of alternative fuels, e.g. biofuels

Abstract

The utility model discloses liquefied natural gas BOG recovery systems, it includes engine, speed changer, refrigeration machine, heat exchanger, the BOG gases in liquefied natural gas tube top portion, and a part introduces engine, and a part introduces refrigeration machine;The both sides of speed changer are connected with engine, refrigeration machine respectively by the first connecting shaft, the second connecting shaft, heat exchanger is arranged on blast pipe and positioned at the downstream of catalysis bag, the water inlet of hot-water line is connected with the delivery port of heat exchanger, and the delivery port of hot-water line is connected with boiler.In the utility model, a part of gaseous state BOG can make driven by engine refrigeration machine that another part gaseous state BOG is converted into liquefied natural gas, and the exhaust heat of engine can be reclaimed using heat exchanger.The utility model is applied to the optimization design of liquefied natural gas BOG retracting devices.

Description

Liquefied natural gas BOG recovery systems
Technical field
The utility model is related to a kind of liquefied natural gas BOG recovery technologies, is characterized in a kind of liquefaction with engine day Right gas BOG recovery systems.
Background technology
Liquefied natural gas, main component is methane, and it is fossil energy most clean on the earth to be recognized.Colourless, tasteless, nothing Poison and non-corrosiveness, its volume is about the 1/625 of same amount gaseous natural gas volume, and the quality of liquefied natural gas is only consubstantiality ponding 45% or so.Its manufacturing process is the natural gas purification processing for first producing gas field, after being liquefied through a succession of ultralow temperature, is utilized LNG carrier is transported.It is very small to air pollution after liquefied natural gas burning, and liberated heat is big, so liquefaction day Right gas is a kind of more advanced energy.Liquefied natural gas is that natural gas is compressed, is cooled to its boiling point (- 161.5 DEG C) temperature After become liquid, usual LNG storage is in -161.5 degrees Celsius, 0.1MPa or so low-temperature storage tank.Its it is main into It is divided into methane, is transported, gasified again when using with special purpose ship or tank car.
Liquefied natural gas (LNG) is a kind of energy of clean and effective, compared with gasoline, diesel oil and compressed natural gas (CNG), With the obvious advantage such as safe, economy is strong, negative environment effects are small, energy storage density is high.Therefore, LNG fires as automobile Material, is widely used in city bus, heavy truck and intercity bus, and matched LNG gas stations are also synchronously obtained quickly Development.Because LNG is cryogen, although LNG filling gas station equipments have good insulation, in the mistake for storing and operating Cheng Zhong, due to natural heat transfer and system cooling needs, inevitably results from a number of LNG steams, i.e., BOG.With the increase of BOG quantity, raise the temperature and pressure of LNG systems, when reaching to a certain degree, it has to which release BOG To reduce the pressure of system.Inherently a kind of very clean fuel of BOG, is discharged into and a kind of meaningless wave is not only in air Take, and fuel gas is discharged into air, with potential danger.Counted according to certain LNG gas station, the BOG numbers discharged every year Measure close to the station year for the 5% of LNG total amounts, economic loss exceedes 40 × 104 yuan.In addition, main component is methane in BOG, and first Alkane is a kind of greenhouse effects very strong gas, and the greenhouse effects coefficient (GWP) of methane is 21 times of carbon dioxide.Therefore, we BOG must be paid attention to diffuses problem.This not only conforms with the principles and policies of energy-saving and emission-reduction, is also the economy and safety for improving device The important measures of property.But in existing technology, in the main air in the past of BOG based on discharge.
The content of the invention
The utility model for above-mentioned the deficiencies in the prior art there is provided a kind of liquefied natural gas BOG recovery systems, can be with BOG gases are made effectively to be reclaimed.
The utility model realizes that the utility model includes liquefied natural gas storage tanks, started by following technology Machine, blast pipe, catalysis bag, the first BOG gas fairlead, the first control valve, preheater, the first connecting shaft, speed changer, the second connection Axle, refrigeration machine, the 2nd BOG gas fairlead, the second control valve, liquefied natural gas delivery pipe, cryogenic pump, the 3rd control valve, cold water Pipe, heat exchanger, hot-water line, boiler, the air inlet of blast pipe are connected with the exhaust duct of engine, and catalysis bag is arranged in exhaust Guan Shang, the air inlet of the first BOG gas fairleads with being connected at the top of liquefied natural gas storage tanks, the first BOG gas fairleads Gas outlet is connected with engine, and the first control valve, preheater are sequentially arranged on the first BOG gas fairleads, and the two of speed changer Side is connected with engine, refrigeration machine respectively by the first connecting shaft, the second connecting shaft, the air inlet of the 2nd BOG gas fairleads with It is connected at the top of liquefied natural gas storage tanks, the gas outlet of the 2nd BOG gas fairleads is connected with the air inlet of refrigeration machine, the Two control valves are arranged on the 2nd BOG gas fairleads, and the import of liquefied natural gas delivery pipe is connected with the liquid outlet of refrigeration machine, The outlet of liquefied natural gas delivery pipe is connected with the bottom of liquefied natural gas storage tanks, cryogenic pump, the 3rd control valve cloth successively Put in liquefied natural gas delivery pipe, heat exchanger is arranged on blast pipe and positioned at the downstream of catalysis bag, the delivery port of cold water pipe Be connected with the water inlet of heat exchanger, the water inlet of hot-water line is connected with the delivery port of heat exchanger, the delivery port of hot-water line with Boiler is connected.
Further, in the utility model, engine is natural gas engine, the first control valve, the second control valve, Three control valves are magnetic valve.
The beneficial effects of the utility model are:The utility model is reasonable in design, simple in construction, it is possible to use BOG gas sheets The energy of body rotates driven by engine refrigeration machine, and liquefy another part BOG gases, realizes BOG zero-emissions.Additionally can be real The recovery of existing engine exhaust heat.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment;
Label in accompanying drawing is respectively:1st, liquefied natural gas storage tanks, 2, engine, 3, blast pipe, 4, generator, 5, One BOG gas fairleads, the 6, first control valve, 7, preheater, the 8, first connecting shaft, 9, speed changer, the 10, second connecting shaft, 11, system Cold, the 12, the 2nd BOG gas fairleads, the 13, second control valve, 14, liquefied natural gas delivery pipe, 15, cryogenic pump, the 16, the 3rd control Valve processed, 17, cold water pipe, 18, heat exchanger, 19, hot-water line, 20, boiler.
Embodiment
Embodiment of the present utility model is elaborated below in conjunction with the accompanying drawings, the present embodiment is with the utility model technical side Premised on case, detailed embodiment and specific operating process are given, but protection domain of the present utility model is not limited to down The embodiment stated.
Embodiment
Embodiment of the present utility model as shown in figure 1, the utility model include liquefied natural gas storage tanks 1, engine 2, Blast pipe 3, the 4, the first BOG gas fairlead 5 of catalysis bag, the first control valve 6, preheater 7, the first connecting shaft 8, speed changer 9, second Connecting shaft 10, refrigeration machine 11, the 2nd BOG gas fairlead 12, the second control valve 13, liquefied natural gas delivery pipe 14, cryogenic pump 15, 3rd control valve 16, cold water pipe 17, heat exchanger 18, hot-water line 19, boiler 20, the air inlet of blast pipe 3 and the row of engine 2 Air flue is connected, and catalysis bag 4 is arranged on blast pipe 3, air inlet and the liquefied natural gas storage tanks 1 of the first BOG gas fairlead 5 Top be connected, the gas outlet of the first BOG gas fairlead 5 is connected with engine 2, and the first control valve 6, preheater 7 are successively It is arranged on the first BOG gas fairlead 5, the both sides of speed changer 9 are by the first connecting shaft 8, the second connecting shaft 10 respectively with starting Machine 2, refrigeration machine 11 are connected, and the air inlet of the 2nd BOG gas fairlead 12 is connected with the top of liquefied natural gas storage tanks 1, the The gas outlet of two BOG gas fairleads 12 is connected with the air inlet of refrigeration machine 11, and the second control valve 13 is arranged in the 2nd BOG gas and drawn In outlet pipe 12, the import of liquefied natural gas delivery pipe 14 is connected with the liquid outlet of refrigeration machine 11, liquefied natural gas delivery pipe 14 Outlet be connected with the bottom of liquefied natural gas storage tanks 1, it is natural that cryogenic pump 15, the 3rd control valve 16 are sequentially arranged in liquefaction On letter shoot 14, heat exchanger 18 is arranged on blast pipe 3 and positioned at the downstream of catalysis bag 4, and the delivery port of cold water pipe 17 is with changing The water inlet of hot device 18 is connected, and the water inlet of hot-water line 19 is connected with the delivery port of heat exchanger 18, the water outlet of hot-water line 19 Mouth is connected with boiler 20, and the first control valve 6, the second control valve 13, the 3rd control valve 16 are magnetic valve.
In implementation process of the present utility model, the band of engine 2 can be made into a part of BOG gases in engine 2 Dynamic refrigeration machine 11 is worked, and another part BOG gases in liquefied natural gas storage tanks 1 are converted into liquefied natural gas.Meanwhile, start The waste heat that machine 2 discharges gas can be reclaimed by heat exchanger 18, make cold water be changed into being stored in after hot water in boiler 20.

Claims (2)

1. a kind of liquefied natural gas BOG recovery systems, including liquefied natural gas storage tanks (1), engine (2), blast pipe (3), Catalysis bag (4), the air inlet of blast pipe (3) is connected with the exhaust duct of engine (2), and catalysis bag (4) is arranged in blast pipe (3) On, it is characterised in that also including the first BOG gas fairlead (5), the first control valve (6), preheater (7), the first connecting shaft (8), Speed changer (9), the second connecting shaft (10), refrigeration machine (11), the 2nd BOG gas fairlead (12), the second control valve (13), liquefaction day Right letter shoot (14), cryogenic pump (15), the 3rd control valve (16), cold water pipe (17), heat exchanger (18), hot-water line (19), heat Water tank (20), the air inlet of the first BOG gas fairlead (5) at the top of liquefied natural gas storage tanks (1) with being connected, the first BOG The gas outlet of gas fairlead (5) is connected with engine (2), and the first control valve (6), preheater (7) are sequentially arranged in the first BOG On gas fairlead (5), the both sides of speed changer (9) by the first connecting shaft (8), the second connecting shaft (10) respectively with engine (2), Refrigeration machine (11) is connected, the air inlet of the 2nd BOG gas fairlead (12) with being connected at the top of liquefied natural gas storage tanks (1), The gas outlet of 2nd BOG gas fairlead (12) is connected with the air inlet of refrigeration machine (11), and the second control valve (13) is arranged in On two BOG gas fairleads (12), the import of liquefied natural gas delivery pipe (14) is connected with the liquid outlet of refrigeration machine (11), liquefaction The outlet of gas delivering pipe (14) is connected with the bottom of liquefied natural gas storage tanks (1), cryogenic pump (15), the 3rd control valve (16) it is sequentially arranged in liquefied natural gas delivery pipe (14), heat exchanger (18) is arranged on blast pipe (3) and positioned at catalysis bag (4) downstream, the delivery port of cold water pipe (17) is connected with the water inlet of heat exchanger (18), and the water inlet of hot-water line (19) is with changing The delivery port of hot device (18) is connected, and the delivery port of hot-water line (19) is connected with boiler (20).
2. liquefied natural gas BOG recovery systems according to claim 1, it is characterised in that the engine (2) is natural Gas engine, first control valve (6), the second control valve (13), the 3rd control valve (16) are magnetic valve.
CN201621489929.6U 2016-12-31 2016-12-31 Liquefied natural gas BOG recovery systems Active CN206478441U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621489929.6U CN206478441U (en) 2016-12-31 2016-12-31 Liquefied natural gas BOG recovery systems

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621489929.6U CN206478441U (en) 2016-12-31 2016-12-31 Liquefied natural gas BOG recovery systems

Publications (1)

Publication Number Publication Date
CN206478441U true CN206478441U (en) 2017-09-08

Family

ID=59750265

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621489929.6U Active CN206478441U (en) 2016-12-31 2016-12-31 Liquefied natural gas BOG recovery systems

Country Status (1)

Country Link
CN (1) CN206478441U (en)

Similar Documents

Publication Publication Date Title
CN104265512B (en) High-pressure/low-pressure gas supply system of ship power plant
CN203162531U (en) High-pressure gas supply system of marine power plant
WO2021008619A1 (en) Oil-tanker gas supply system using two fuels, and oil tanker
WO2017031986A1 (en) Lng fueling station employing bog energy storage and pressure differential
WO2021008620A1 (en) Gas supply system employing two fuels for use in ultra-large container ship, and ultra-large container ship
CN104791602B (en) The LNG gaseous fuels air supply method and device that BOG is preferentially utilized
CN105179933B (en) Universal aircraft power system with liquefied natural gas (LNG) as fuel and fuel supply method of universal aircraft power system
CN102913752B (en) Unloading and liquid adding device for skid-type liquid adding station and unloading and liquid adding method
CN204060975U (en) A kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment
CN204345267U (en) A kind of small-sized LNG gas station storage tank BOG recovering device
CN202252834U (en) Wharf boat LNG (liquefied natural gas) filling station
CN104278975A (en) Method and system for collecting seabed combustible ice
CN204227033U (en) A kind of separated type ice chest being applicable to small liquid rock gas powered ship
CN104197635B (en) A kind of LNG fuels and energies ship harbour stops re-liquefied system and liquifying method
CN206478441U (en) Liquefied natural gas BOG recovery systems
CN205781982U (en) LNG filling station is unloaded without pump, is filled and charging system
CN103321616B (en) The collection way of sea bed methane hydrate and system
CN106678538A (en) Multi-energy complementary liquefied natural gas BOG recycling method and implementation device thereof
CN116950809A (en) LNG power ship fuel gas recovery system, control method thereof and ship
CN206346845U (en) BOG is used as dual fuel engine peculiar to vessel and supplements fuel air supply system
CN206346844U (en) LNG composite air supplies system peculiar to vessel
CN203082531U (en) ANG (absorption natural gas) and LNG (liquefied natural gas) dual-fuel gas supply system
CN204554355U (en) A kind of recovering device for LNG storage and transportation apparatus overpressure relief
CN106640427A (en) Liquefied natural gas BOG recovery and power generation method and implementing device thereof
CN103291253B (en) The collecting device of sea bed gas hydrates

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant