CN112923769A - Zero-cold-source natural gas excess pressure recycling system - Google Patents

Zero-cold-source natural gas excess pressure recycling system Download PDF

Info

Publication number
CN112923769A
CN112923769A CN202110304316.XA CN202110304316A CN112923769A CN 112923769 A CN112923769 A CN 112923769A CN 202110304316 A CN202110304316 A CN 202110304316A CN 112923769 A CN112923769 A CN 112923769A
Authority
CN
China
Prior art keywords
heat exchanger
natural gas
pipeline
expander
gearbox
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.)
Pending
Application number
CN202110304316.XA
Other languages
Chinese (zh)
Inventor
王强
张雪辉
朱阳历
王星
李辉
陈海生
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.)
National Energy Large Scale Physical Energy Storage Technology R & D Center Of Bijie High Tech Industrial Development Zone
Institute of Engineering Thermophysics of CAS
Original Assignee
National Energy Large Scale Physical Energy Storage Technology R & D Center Of Bijie High Tech Industrial Development Zone
Institute of Engineering Thermophysics of CAS
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 National Energy Large Scale Physical Energy Storage Technology R & D Center Of Bijie High Tech Industrial Development Zone, Institute of Engineering Thermophysics of CAS filed Critical National Energy Large Scale Physical Energy Storage Technology R & D Center Of Bijie High Tech Industrial Development Zone
Priority to CN202110304316.XA priority Critical patent/CN112923769A/en
Publication of CN112923769A publication Critical patent/CN112923769A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0014Recuperative heat exchangers the heat being recuperated from waste air or from vapors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The invention discloses a cold source natural gas excess pressure recycling system, wherein an output shaft of an expander (1) is connected with a gearbox (2), a transmission shaft of the gearbox (2) is connected with rotary mechanical equipment (3), the expander (1) is connected with a heat exchanger A (4), the heat exchanger A (4) is connected with a cold storage tank (5), the cold storage tank (5) is connected with a variable frequency pump (6), the variable frequency pump 6 is connected with a heat exchanger B (9), the heat exchanger B (9) is connected with the heat exchanger A (4), the heat exchanger B (9) is connected with a system lubricating oil station (11), the heat exchanger B (9) is sequentially connected with the rotary mechanical equipment (3), the gearbox (2) and the expander (1), the gearbox (2) and the rotary mechanical equipment (3) are sequentially connected and then connected with the system lubricating oil station (11). The invention can convert the pressure energy of the natural gas into mechanical energy, can realize the recycling of the cold energy of the natural gas and simultaneously avoids the limitation of geographical positions.

Description

Zero-cold-source natural gas excess pressure recycling system
Technical Field
The invention belongs to the technical field of mechanical equipment, and particularly relates to a zero-cold-source natural gas residual pressure recycling system.
Background
The natural gas is a relatively clean energy, and is conveyed through a pipeline in a high-pressure mode after being mined, and is subjected to pressure regulation step by step through pressure regulation stations at different stages, and finally supplied to users for use. In the pressure regulating process of the pressure regulating station, the pressure energy of the natural gas is directly lost and wasted through the pressure regulating station. The pressure regulating station is replaced by the expansion machine, so that the pressure energy of the natural gas can drive mechanical equipment to rotate and be converted into mechanical energy, and the mechanical energy can be further converted into energy in other forms, such as electric energy, heat energy and the like. When the expander is used for replacing a pressure regulating station for pressure reduction, a lubricating oil station needs to be configured for the expander, a gear box, a mechanical rotating device and the like, a corresponding lubricating oil cooling system needs to be configured for long-time work, the lubricating oil temperature is prevented from being too high, the cooling system is separately configured, a cold source needs to be configured for the cooling system, the manufacturing cost of the system is increased, and the limitation of the geographic environment is also caused.
Disclosure of Invention
The invention aims to overcome the defects and provide a zero-cold-source natural gas residual pressure recycling system which can convert the pressure energy of natural gas into mechanical energy, can recycle the cold energy and avoids the limitation of geographical positions.
The purpose of the invention and the main technical problem of solving the invention are realized by adopting the following technical scheme:
the invention discloses a cold source natural gas residual pressure recycling and efficient utilizing system, which comprises an expander, a gearbox, rotary mechanical equipment, a heat exchanger A, a cold storage tank and a heat exchanger B, wherein: the inlet of the expander is connected with the side of a natural gas high-pressure pipe network, the output shaft of the expander is connected with a gearbox, a transmission shaft of the gearbox is connected with rotary mechanical equipment, the outlet of the expander is connected with the inlet of a heat exchanger A through a pipeline, the outlet of the heat exchanger A is connected with the side of a natural gas low-pressure pipe network through a pipeline, the other outlet of the heat exchanger A is connected with the inlet of a cold storage tank through a pipeline, the outlet of the cold storage tank is connected with the inlet of a variable-frequency pump through a pipeline, the outlet of the variable-frequency pump is connected with the inlet of a heat exchanger B through a pipeline which is sequentially provided with a check valve and a regulating valve, the outlet of the heat exchanger B is connected with the other inlet of the heat exchanger A through a pipeline which is provided with a thermodetector A, a variable-frequency pump B is, The gearbox and the rotary mechanical equipment are connected in sequence and then connected with an inlet of a system lubricating oil station through a pipeline.
Compared with the prior art, the invention has obvious beneficial effects, and the technical scheme can show that: the outlet of the expansion machine is connected with the inlet of the heat exchanger, the heat exchanger absorbs the cold energy generated by the expansion machine, and the cold energy is absorbed and then stored in the cold storage tank: the expander is connected with the rotating equipment through a gear box; the cold storage tank is connected with the heat exchanger of the expansion engine oil station through a pipeline; when the expander works, the expander drives the gear box to rotate, and the gear box drives the rotating equipment to rotate. The temperature of the low temperature natural gas after the expander can reach about 30 degrees below zero, utilize the heat exchanger to absorb this part cold energy, store in the cold storage tank, the cold storage tank passes through the heat exchanger of governing valve and system lubrication oil station and is connected, utilize the cold energy that high pressure natural gas produced behind the expander, the lubricating oil at cooling system lubrication oil station, the cold source of lubrication oil station heat exchanger is supplied with has been avoided, the direct loss of cold energy after having avoided utilizing the expander to replace the pressure regulating station has been avoided, the cold source that system lubrication oil station lubricating oil cooling needs has also been avoided, the use economy of system device has been improved, the restriction of geographical position has been avoided simultaneously.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
The labels in the figure are:
1. an expander; 2. a gearbox; 3. rotating mechanical equipment; 4. a heat exchanger A; 5. a cold storage tank; 6. a variable frequency pump A; 7. a check valve; 8. adjusting a valve; 9. a heat exchanger B; 10. a thermodetector A; 11. a system lube station; 12. a variable frequency pump B; 13. a temperature measuring instrument B; 14. a pressure sensor.
Detailed Description
The following detailed description will be made on specific embodiments, structures, features and effects of the system for recycling residual pressure of natural gas as a cooling source according to the present invention with reference to the accompanying drawings and preferred embodiments.
Referring to fig. 1, the zero-cold-source natural gas residual pressure recycling system of the present invention includes an expander 1, a transmission 2, a rotating mechanical device 3, a heat exchanger a4, a cold storage tank 5, and a heat exchanger B9, wherein: the inlet of an expander 1 is connected with the side of a natural gas high-pressure pipe network, the output shaft of the expander 1 is connected with a gearbox 2, the transmission shaft of the gearbox 2 is connected with a rotary mechanical device 3, the outlet of the expander 1 is connected with the inlet of a heat exchanger A4 through a pipeline, the outlet of a heat exchanger A4 is connected with the side of a natural gas low-pressure pipe network through a pipeline, the other outlet of the heat exchanger A4 is connected with the inlet of a cold storage tank 5, the outlet of the cold storage tank 5 is connected with the inlet of a variable-frequency pump 6 through a pipeline, the outlet of the variable-frequency pump 6 is connected with the inlet of a heat exchanger B9 through a pipeline which is sequentially provided with a check valve 7 and a regulating valve 8, the outlet of the heat exchanger B9 is connected with the other inlet of a heat exchanger A4 through a pipeline which is provided with a thermodetector A10, a variable-frequency pump B12 is arranged on, The gearbox 2, the expansion machine 1, the gearbox 2 and the rotary mechanical equipment 3 are connected in sequence and then connected with an inlet of a system lubricating oil station 11 through a pipeline.
The working principle is as follows: when the expander 1 is connected to a pipe network, the expander 1 starts to work under the action of pressure difference between the high-pressure pipe network side and the low-pressure pipe network side, the heat exchanger A4 absorbs cold energy of a natural gas medium passing through the expander 1 and stores the cold energy in the cold storage tank 5, the working pressure of the variable frequency pump 6 and the opening of the regulating valve 8 are adjusted according to the measured temperature of the thermodetector B13, the speed and the time of the cooling working medium flowing through the heat exchanger B9 are controlled, so that the temperature of high-temperature circulating lubricating oil of the system lubricating oil station 11 reaches the set temperature, meanwhile, the variable frequency pump 12, connected with the heat exchanger B9, of the system lubricating oil station 11 provides lubricating oil pressure required by normal work of the system, and therefore the purposes of converting the pressure energy of the natural gas pipe network into rotary mechanical energy by the expander 1 and recycling the cold energy at the outlet of the expander 1 by. The invention avoids the problem of cooling lubricating oil by using a water cooling mode in the prior art, and can effectively avoid the problem that the natural gas excess pressure utilization site is limited by the geographical position.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention in any way, and any simple modification, equivalent change and modification made to the above embodiment according to the technical spirit of the present invention are within the scope of the present invention without departing from the technical spirit of the present invention.

Claims (6)

1. The utility model provides a cold source natural gas excess pressure retrieves high-efficient system of utilizing, includes expander (1), gearbox (2), rotating machinery equipment (3), heat exchanger A (4), cold storage tank (5), heat exchanger B (9), its characterized in that: the output shaft of expander (1) is connected with gearbox (2), gearbox (2) transmission shaft is connected with rotating mechanical equipment (3), the export of expander (1) is imported through pipe connection heat exchanger A (4), another export of heat exchanger A (4) is through pipeline and cold storage tank (5) access connection, the export of cold storage tank (5) is imported through pipe connection inverter pump (6), the pipeline connection heat exchanger B (9) import of inverter pump 6 export through installing check valve (7) and governing valve (8) in proper order, heat exchanger B (9) export is through pipeline and another access connection of heat exchanger A (4), another import and system's lubricating oil station (11) exit linkage of heat exchanger B (9), another export of heat exchanger B (9) is through pipeline and connects gradually rotating mechanical equipment (3), gearbox (2), expander (1), gearbox (2), The rotary mechanical equipment (3) is connected with an inlet of a system lubricating oil station (11) through a pipeline after being sequentially connected.
2. The system for recovering and efficiently utilizing the residual pressure of the natural gas of the cold source as claimed in claim 1, wherein: the other outlet of the heat exchanger B (9) is connected with a pipeline of the rotating mechanical equipment (3) and is sequentially provided with a temperature measuring instrument B (13) and a pressure sensor (14).
3. The system for recovering and efficiently utilizing the residual pressure of the natural gas of the cold source as claimed in claim 1, wherein: the outlet of the heat exchanger B (9) is connected with the other inlet of the heat exchanger A (4) through a pipeline provided with a thermodetector A (10).
4. The system for recovering and efficiently utilizing the residual pressure of the natural gas of the cold source as claimed in claim 1, wherein: a variable frequency pump B (12) is arranged on a pipeline connected between the other inlet of the heat exchanger B (9) and the outlet of the system lubricating oil station (11).
5. The system for recovering and efficiently utilizing the residual pressure of the natural gas of the cold source as claimed in claim 1, wherein: the inlet of the expander (1) is connected with the side of the natural gas high-pressure pipe network.
6. The system for recovering and efficiently utilizing the residual pressure of the natural gas of the cold source as claimed in claim 1, wherein: the outlet of the heat exchanger A (4) is connected with the natural gas low-pressure pipeline network side through a pipeline.
CN202110304316.XA 2021-03-22 2021-03-22 Zero-cold-source natural gas excess pressure recycling system Pending CN112923769A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110304316.XA CN112923769A (en) 2021-03-22 2021-03-22 Zero-cold-source natural gas excess pressure recycling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110304316.XA CN112923769A (en) 2021-03-22 2021-03-22 Zero-cold-source natural gas excess pressure recycling system

Publications (1)

Publication Number Publication Date
CN112923769A true CN112923769A (en) 2021-06-08

Family

ID=76175409

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110304316.XA Pending CN112923769A (en) 2021-03-22 2021-03-22 Zero-cold-source natural gas excess pressure recycling system

Country Status (1)

Country Link
CN (1) CN112923769A (en)

Similar Documents

Publication Publication Date Title
Garvey et al. Analysis of a wind turbine power transmission system with intrinsic energy storage capability
CN106523303A (en) Interaction heat dissipation device and method used for wind power generation reduction gear box
CN205779037U (en) A kind of turbine shaft seal gas leakage entrance bearing housing that solves causes the system of oil deterioration
Wang et al. Experimental study on the performance of oil-free twin-screw expanders for recovering energy in fuel cell systems
CN103711535A (en) Environment thermal energy conversion method and device used for providing power through environment thermal energy
CN102392694A (en) Heating cogeneration generator unit
WO2014017943A1 (en) Hermetically sealed turbo expander system for use in organic rankine cycles and organic rankine cycle plant
CN215373657U (en) Zero-cold-source natural gas excess pressure recycling system
CN106286790B (en) A kind of heat dissipating method of combined radiating device for wind-power electricity generation reduction gear box
CN101769179A (en) Environment-friendly energy conservation and emission reduction system
CN204024736U (en) ORC (organic Rankine cycle) low-temperature generating and the steam turbine generation electricity generating device that intercouples
CN112923769A (en) Zero-cold-source natural gas excess pressure recycling system
CN202370596U (en) Heating heat supply combined heat and power generation power generator set
CN108915783A (en) A kind of lubricating system of positive-displacement expansion engine
CN206256940U (en) A kind of deep cooling liquid air energy storage systems of waste heat boosting type
CN115013220B (en) Compact geothermal energy compressed air energy storage system and method based on medium-deep dry-hot rock
CN102808661A (en) Axial-flow type generator set utilizing organic rankine cycle (ORC)
CN202768083U (en) Axial-flow type generator set utilizing organic working medium Rankine cycle
CN103388676A (en) Efficient coupling variable-frequency speed regulating system and speed regulating method
CN201874629U (en) Throttled heat energy recycling system
CN102748254A (en) Natural gas differential pressure generating transforming machine set based on solar heating and implementation method thereof
CN202381273U (en) Mobile energy supply device based on compressed natural gas
CN206531353U (en) Heat energy feed system and cold energy feed system
CN206754782U (en) Generating set lubricating oil exchange system
CN201606121U (en) Environmental-protection energy-saving emission-reduction waste-heat smoke-gas recycling system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination