CN205014035U - LNG gasification heating and central heating system combination system in winter - Google Patents

LNG gasification heating and central heating system combination system in winter Download PDF

Info

Publication number
CN205014035U
CN205014035U CN201520611421.8U CN201520611421U CN205014035U CN 205014035 U CN205014035 U CN 205014035U CN 201520611421 U CN201520611421 U CN 201520611421U CN 205014035 U CN205014035 U CN 205014035U
Authority
CN
China
Prior art keywords
lng
central heating
gasification
water
heating
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
CN201520611421.8U
Other languages
Chinese (zh)
Inventor
杜玉吉
冯海晨
蒋丹丹
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.)
Changzhou Energy Saving Research Institute Co Ltd
Original Assignee
Changzhou Energy Saving Research Institute 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 Changzhou Energy Saving Research Institute Co Ltd filed Critical Changzhou Energy Saving Research Institute Co Ltd
Priority to CN201520611421.8U priority Critical patent/CN205014035U/en
Application granted granted Critical
Publication of CN205014035U publication Critical patent/CN205014035U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

The utility model discloses a LNG gasification heating and central heating system combination system in winter, a serial communication port, including LNG vaporizing station system and central heating system, the water -bath heating ware of LNG vaporizing station system passes through the central heating station that pipeline connects central heating system, and some carries the water -bath heating ware through pipeline the hot water at central heating station, and another part is passed through the pipe -line transportation and is given the central heating system 0 heat supply. The utility model discloses let two sets of independent systems of LNG vaporizing station system and central heating system combine together, realize the complementary utilization of the energy, LNG complete gasification and reach suitable gasification temperature when the outside air temperature was relatively low winter has been realized, optimize the complete set gasification equipment among the LNG vaporizing station, still can reduce air gasification equipment's volume when reducing the investment to a certain extent, save the heat source of water -bath heating ware, including electric power or fuel, reduced the running cost.

Description

A kind of LNG gasification heating and central heating system association system in winter
Technical field
The utility model relates to a kind of energy recovery utilizing system.
Background technique
LNG has become the valuable source of energy strategy structural adjustment and deposit, and LNG industry also becomes one of current global evolution industry the swiftest and the most violent.LNG must could grid-connected air feed after heating and gasifying when practical application, and therefore these gasification installations are visual plants indispensable in LNG transmission & distribution application system.The LNG heating and gasifying device that current China commonly uses mainly contains water hot type gasification installation, submersible burning hot type gasification installation, air heating type gasification installation, vapor heating type gasification installation and middle heat-carrying agent hot type gasification installation etc., these devices respectively have advantage, deficiency and applicable situation, but all have in energy-conservation, consumptive material and use etc. and be worth improving the place of improving.The selection of thermal source has very large impact to the gasification of LNG and performance driving economy.If Fig. 1 is LNG vaporizing station process flow diagram, the storage temperature under LNG Liquefied natural gas (LNG) normal pressure is-162 DEG C, is transported to vaporizing station by low-temperature tanker, and the pressurized machine utilizing tank car to carry at unloading deck pressurizes to tank car, utilizes pressure reduction LNG to be delivered to storage tank and stores.During gasification by storage tank pressurized machine by after LNG supercharging, adopt the mode of air temperature type gasification+heating water bath gasify and heat gas phase rock gas, finally by pressure regulation, measure, add smelly rear feeding transmission and distribution network.In the process, the boil-off gas (BOG) of LNG tank car, storage tank inputs pipe network after adopting BOG air temperature type heater to heat, and the safe dispersing gas of superpressure (EAG) of storage tank, vaporizer adopts EAG air temperature type heater to heat, emptying through exhaust stack.As Fig. 2, for LNG gasifying process figure, although use wider air heating type gasification installation structure simple in current LNG vaporizing station, do not consume the energy, operating cost is low, but its shortcoming is large by environmental influence in running, when the temperature of the surroundings is low, the easy frosting of its fin and affect the gasification of LNG, sometimes because ambient temperature is too low, cause gasification efficiency greatly to reduce, at this moment needing, water-bath type heater is set again it is heated further.Water-bath type heater is different according to thermal source, mainly contains hot water heating formula, combustion heating formula, electric heating etc., and when the NG outlet temperature after the gasification of sky temperature vaporizer is generally lower than 0 DEG C, just automatically starting water-bath heater need heat further to it.Water-bath type heater is generally volumetric heat exchanger, its structure is for put into hot water tank by heat conduction coil pipe, utilize the hot water in shell side, to the low temperature be immersed in inner heat conduction coil pipe, other carries out heating and gasifying, makes its Outlet Gas Temperature meet the requirement (general temperature is higher than 5 DEG C) of pipeline transport gas.When outside air temperature is low especially, need in LNG gasifying process to consume a large amount of thermals source to meet the outlet temperature of other rock gas.Energy consumption is comparatively large, and operating cost is higher.
Model utility content
The purpose of this utility model is to provide a kind of LNG gasification heating and central heating system association system in winter, and the delivery produced by central heating system as the thermal source of water-bath heater, replaces traditional heater to LNG vaporizing station, reduces and invests.
The technological scheme that the utility model provides is:
A kind of LNG gasification heating and central heating system association system in winter, it is characterized in that, comprise LNG vaporizing station system and central heating system, the water-bath heater of LNG vaporizing station system connects the central heating stations of central heating system by conveyance conduit, central heating stations hot water a part is transported to water-bath heater by conveyance conduit, another part by Cemented filling to terminal temperature difference heat supply.
The hot water that the utility model produces by utilizing central heat supply energy source station, while provide heat supply to serve for terminal temperature difference, a part of hot water is delivered in LNG vaporizing station, as the thermal source of water-bath heater through delivery pipe.The LNG(liquified natural gas of-145 DEG C) first become temperature lower than the gaseous natural gas (NG) of 0 DEG C through the gasification of empty temperature vaporizer under cryogenic, and then through the gaseous natural gas being warming up to more than 5 DEG C further of water-bath heater, then through the follow-up pressure regulation of vaporizing station, measure, add smelly after deliver in natural gas transmission and distribution pipe network.The utility model has following beneficial effect:
1, allow LNG vaporizing station system and central heating system two independently system of overlapping combine, realize energy complementation and utilize;
2, achieve LNG be gasified totally when outside air temperature is relatively low in the winter time and reach suitable gasification temperature;
3, optimize the complete gasification installation in LNG vaporizing station, while reducing investment, also can reduce the volume of air gasification device to a certain extent;
4, eliminate the thermal source of water-bath heater, comprise electric power or fuel, reduce operating cost.
Accompanying drawing explanation
Fig. 1 is traditional LNG vaporizing station process flow diagram.
Fig. 2 is traditional LNG gasifying process flow chart in winter.
Fig. 3 is principle schematic of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 3, a kind of LNG gasification heating and central heating system association system in winter, comprise LNG vaporizing station system and central heating system, the water-bath heater of LNG vaporizing station system connects the central heating stations of central heating system by conveyance conduit, central heating stations hot water a part is transported to water-bath heater by conveyance conduit, another part by Cemented filling to terminal temperature difference heat supply.
The utility model is LNG vaporizing station and central heating system use in conjunction in winter.Winter, when working, transports by LNG Liquefied natural gas (LNG) tank car the LNG Liquefied natural gas of coming, sends the liquid in car to LNG storage tank store for future use by mouth of unloading.Tank car boosts to about 0.6MPa by from pressurization system, unloads liquid by pressure reduction.During use, open storage tank from pressurization system, boost to about 0.6MPa, then opening storage tank liquid valve is transported in air temperature type vaporizer by LNG, the liquified natural gas (LNG) of-145 DEG C fully contacts with air, absorb the heat of air to gasify the gaseous natural gas (NG) become lower than 0 DEG C, due to temperature when natural gas temperature now still can not reach NG transmission pipeline network, therefore the NG after gasification needs to continue to heat up, enter in water-bath heater, water-bath heater is volumetric heat exchanger, be NG in tube side, shell side is the hot water of 50 DEG C carried by conveyance conduit from the central heating stations of central heating system, both are in heat exchanger after abundant heat exchange, the temperature of NG rises to more than 5 DEG C, pass through natural gas pressure regulating again, measuring apparatus and device for adding odor, final transmission & distribution use to downstream gas equipment.And air conditioning hot heat-exchange temperature be down to 43 DEG C converge with the air-conditioning backwater of user side after, return to in energy source station, complete circulation.

Claims (1)

1. a LNG gasification heating and central heating system association system in winter, it is characterized in that, comprise LNG vaporizing station system and central heating system, the water-bath heater of LNG vaporizing station system connects the central heating stations of central heating system by conveyance conduit, central heating stations hot water a part is transported to water-bath heater by conveyance conduit, another part by Cemented filling to terminal temperature difference heat supply.
CN201520611421.8U 2015-08-13 2015-08-13 LNG gasification heating and central heating system combination system in winter Active CN205014035U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520611421.8U CN205014035U (en) 2015-08-13 2015-08-13 LNG gasification heating and central heating system combination system in winter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520611421.8U CN205014035U (en) 2015-08-13 2015-08-13 LNG gasification heating and central heating system combination system in winter

Publications (1)

Publication Number Publication Date
CN205014035U true CN205014035U (en) 2016-02-03

Family

ID=55212637

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520611421.8U Active CN205014035U (en) 2015-08-13 2015-08-13 LNG gasification heating and central heating system combination system in winter

Country Status (1)

Country Link
CN (1) CN205014035U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108240718A (en) * 2016-12-26 2018-07-03 蓝焰高科(天津)燃气技术有限公司 A kind of energy automatically supplies the driving compression type heat pump assembly of multifunction burning mechanism of qi

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108240718A (en) * 2016-12-26 2018-07-03 蓝焰高科(天津)燃气技术有限公司 A kind of energy automatically supplies the driving compression type heat pump assembly of multifunction burning mechanism of qi

Similar Documents

Publication Publication Date Title
CN104265512B (en) High-pressure/low-pressure gas supply system of ship power plant
CN109114418A (en) A kind of gasification station with plunger pump
CN107076358B (en) It is unloaded with BOG accumulation of energy pressure difference LNG gas station, liquid feeding, re-liquefied and accumulation of energy method
CN202158352U (en) L-CNG (liquefied-compressed natural gas) dual-gas resource gas supply device
CN103672394B (en) A kind of without pump LNG refueling system and LNG Liquefied natural gas processing method
CN204678044U (en) Liquefied natural gas filling station is utilized to discard the system of natural gas power
CN104006295A (en) Method and apparatus for displacement type pressure conveying of low-temperature liquefied gas
CN105840983B (en) A kind of LNG skid-mounted gas feeder
CN203641887U (en) Urban emergency peak-regulating LNG gas storage
CN104791602A (en) LNG (liquefied natural gas) fuel supply method and device utilizing BOG (boil-off gas) preferentially
CN111765369A (en) LNG filling online saturation adjusting mechanism and control method
CN107906362A (en) A kind of LNG gasification system
CN205014035U (en) LNG gasification heating and central heating system combination system in winter
CN107388033B (en) A kind of liquefied natural gas supplying system and its application method
CN202791322U (en) LNG (liquefied natural gas) gasification station
CN206694826U (en) A kind of LNG gasification system
CN210267858U (en) LNG cold energy and exhaust-heat boiler waste heat refrigerated simultaneous cooling system
CN205118654U (en) System for BOG who retrieves production of LNG storage tank is as hydrogen manufacturing fuel gas
CN204592854U (en) The LNG gaseous fuel air feeder that BOG preferentially utilizes
CN205014038U (en) LNG gasification cold energy is retrieved and traditional cooling cooling tower combination system
CN103615660B (en) A kind of water bath type vaporizer utilizing engine waste heat energy
CN203322724U (en) LNG (Liquefied Natural Gas) skid-mounted gas filling device
CN206310233U (en) Liquefied natural gas storage tank BOG gas cold energy recycle systems
CN207945482U (en) A kind of system integrating natural gas, electric power, heat and cold transmission & distribution
CN105485515A (en) Fueling system and fueling method for LNG receiving station

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant