CN203640686U - Compression expansion separation heating system with vortex tube throttle valve for high-hydrogen-sulfide-content natural gas - Google Patents
Compression expansion separation heating system with vortex tube throttle valve for high-hydrogen-sulfide-content natural gas Download PDFInfo
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- CN203640686U CN203640686U CN201320593998.1U CN201320593998U CN203640686U CN 203640686 U CN203640686 U CN 203640686U CN 201320593998 U CN201320593998 U CN 201320593998U CN 203640686 U CN203640686 U CN 203640686U
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Abstract
The utility model discloses a compression expansion separation heating system with a vortex tube throttle valve for high-hydrogen-sulfide-content natural gas. The system comprises the vortex tube throttle valve, a heat exchange separator, a pressure meter, a temperature meter, a flow meter and a heating furnace, wherein a top outlet of the vortex tube throttle valve is connected with an inlet of a heat exchange coil pipe of the heat exchange separator; an outlet of the heat exchange coil pipe is connected with an inlet of the heating furnace; an outlet of the heating furnace is connected with a natural gas output pipeline; a lower outlet of the vortex tube throttle valve is connected with an inlet of the heat exchange separator; an outlet of the heat exchange separator is connected with the natural gas output pipeline; a bottom condensed liquid outlet of the heat exchange separator is connected with a recovery pipeline. According to the system, the vortex tube throttle valve is combined with the heat exchange separator; high pressure energy of the mouth of a well in a gas field is fully utilized; through the vortex tube throttle valve, the pressure reducing and throttling effects are achieved, pressure energy is converted into kinetic energy of the natural gas, high-temperature wet gas is separated from low-temperature dry gas, and cold energy required for condensing the natural gas is saved in the heat exchange process of the high-temperature wet gas and the low-temperature dry gas.
Description
Technical field
The utility model is a kind of hydrogen sulfide bearing gas vortex tube choke valve compression-expansion separated heating system, is mainly used in high sulfur-containing natural gas heating transport field in high Oil & gas field in sulfur development process.
Background technology
China's sulfur-containing gas resource is very abundant, and to the end of the year 2007, accumulative total is verified high sulfur-containing natural gas reserves and exceeded 7000 × 10
8m
3, account for and verify 1/6 of natural gas gross reserves, be mainly distributed in Sichuan the Northeast and Bohai gulf basin, along with the increasing of marine facies resource exploration dynamics, China is high containing H
2s and CO
2natural gas proved reserves will enter the rapid growth phase.
Domestic and international high sulfur Gas Fields has obtained rich experience on gathering and transportation technology, has formed the technology of a set of maturation.Similar with conventional gas field, the gas collection technique of high sulfur-containing natural gas mainly contains two kinds of individual well gas collection and gas gathering station many wells gas collections.Gas transmission mode is mainly divided into dry method gas transmission and wet method gas transmission, and the former refers to the conveying after gas dehydration, and the latter refers to the natural gas moisture conveying after water jacket furnace heating.Short distance gas gathering line generally adopts heating moisture to carry, and after long distance line adopts gas gathering station dehydration, dry gas is carried.
The firing equipment of conventional gas is through technical development and improvement for many years, and its technology is ripe, at present domestic equal can the production by designed, designed of the firing equipment of conventional gas.But along with the exploitation in the high sulfur-containing natural gas fields such as general phosgene field, need to be applicable to the firing equipment of high sulfur-containing natural gas, this kind of equipment domestic cannot production at present, complete equipment all need to be from external import, and not only equipment manufacturing cost is high, and delivery cycle is also very long.
Summary of the invention
The purpose of this utility model is to provide a kind of hydrogen sulfide bearing gas vortex tube choke valve compression-expansion separated heating system, solves the problem that above-mentioned prior art exists.
The utility model comprises vortex tube choke valve, heat exchange segregator, pressure gauge, thermometer, flow meter and heating furnace, vortex tube choke valve top exit is connected with the import of the heat exchange coil of heat exchange segregator, the outlet of heat exchange coil is connected with heating furnace import, and furnace outlet is connected with natural gas multi-purpose station pipeline; Vortex tube choke valve lower part outlet is connected with the import of heat exchange segregator, and the outlet of heat exchange segregator is connected with natural gas multi-purpose station pipeline, and the condensate liquid outlet at bottom of heat exchange segregator is connected with reclaim line.
Pressure gauge, thermometer and flow meter are located at respectively on the tube connector of the heat exchange coil of heat exchange segregator and the outlet at bottom of heating furnace inlet connecting branch and heat exchange segregator and natural gas multi-purpose station pipeline by order.
Vortex tube choke valve is vertically installed, low temperature dry gas outlet upper, high temperature moisture outlet under.
Operating principle of the present utility model is:
High sulfur-containing natural gas high pressure moisture enters vortex tube choke valve from the import of vortex tube choke valve, expand and separate by compression eddy flow, high sulfur-containing natural gas high pressure moisture is separated into low temperature dry gas and high temperature moisture, the high temperature moisture heat exchange that enters heat exchange segregator the heat exchange coil that low temperature dry gas enters heat exchange segregator from vortex tube choke valve upper top low temperature dry gas outlet and vortex tube choke valve lower part outlet separating out, condenses sedimentation in high temperature moisture, out enter reclaim line from heat exchange segregator outlet at bottom, low temperature dry gas after heat exchange enters heating furnace heating, it is defeated the high temperature dry gas becoming with the high temperature moisture that exports out from heat exchange segregator bottom high temperature dry gas after heating mixes.
The utility model has the advantages that:
The utility model combines vortex tube choke valve with heat exchange segregator, make full use of the high pressure energy of gas field well head, not only realized the effect of step-down throttling by vortex tube choke valve, and pressure energy is converted into the kinetic energy of natural gas, realize separating of high temperature moisture and low temperature dry gas, high temperature moisture and low temperature dry gas heat transfer process have been saved the needed cold energy of natural gas condensation.Moisture less low temperature dry gas is passed into heating furnace heating and can effectively weaken the corrosion of high sulfur-containing natural gas to Tube in Furnace, this positive role of having chosen to high sulfur-containing natural gas firing equipment material.While native system directly enters heating furnace heating with natural gas to be compared, and the temperature of low temperature dry gas is relatively low, and it is large that heat transfer temperature difference becomes, under identical heat transfer power and thermal transmittance condition, heat exchange area reduces, and this is conducive to reduce heating furnace structure size, realize miniaturization, reduce the equipment investment of heating furnace.
Accompanying drawing explanation
Accompanying drawing 1 is utility model structural representation.
In figure: 1-natural gas inlet tube, the import of 2-vortex tube choke valve, 3-vortex tube choke valve, the outlet of 4-low temperature dry gas, the outlet of 5-high temperature moisture, 6-heat exchange segregator, 7-pressure gauge, 8-thermometer, 9-flow meter, 10-heating furnace, 11-natural gas multi-purpose station pipeline, 12-reclaim line.
The specific embodiment
For further disclosing the technical solution of the utility model, elaborate by embodiment below in conjunction with Figure of description: the utility model comprises vortex tube choke valve 3, heat exchange segregator 6, pressure gauge 7, thermometer 8, flow meter 9 and heating furnace 10, vortex tube choke valve top exit is connected with the import of the heat exchange coil of heat exchange segregator, the outlet of heat exchange coil is connected with heating furnace import, and furnace outlet is connected with natural gas multi-purpose station pipeline; Vortex tube choke valve lower part outlet is connected with the import of heat exchange segregator, and the outlet of heat exchange segregator is connected with natural gas multi-purpose station pipeline, and the condensate liquid outlet at bottom of heat exchange segregator is connected with reclaim line.High sulfur-containing natural gas high pressure moisture enters vortex tube choke valve by natural gas inlet tube 1 from vortex tube choke valve import 2, expand and separate by compression eddy flow, high sulfur-containing natural gas high pressure moisture is separated into low temperature dry gas and high temperature moisture, the high temperature moisture heat exchange that enters heat exchange segregator the heat exchange coil that low temperature dry gas enters heat exchange segregator from vortex tube choke valve upper top low temperature dry gas outlet 4 and vortex tube choke valve lower part outlet separating out, condenses sedimentation in high temperature moisture, out enter reclaim line 12 from the condensate liquid outlet at bottom of heat exchange segregator.Low temperature dry gas after heat exchange enters heating furnace heating, and the high temperature becoming with the high temperature moisture that exports out from heat exchange segregator bottom high temperature dry gas after heating is defeated natural gas multi-purpose station pipeline 11 mixes in gas.If pressure is that 15Mpa, temperature are that 50 ℃ of high sulfur-containing natural gas moistures enter vortex tube choke valve 3, the pressure decreased of the pressure of low temperature dry gas outlet 4 and high temperature moisture outlet 5 is 7MPa, low temperature dry gas outlet temperature can be reduced to 20 ℃, it is 65 ℃ that the temperature of high temperature moisture outlet 5 can raise, after heat exchange segregator heat exchange, in high temperature moisture, moisture and heavy hydrocarbon partial condensation remove.It is defeated natural gas multi-purpose station pipeline 11 mixes that low temperature dry gas enters the high temperature dry gas becoming with the high temperature moisture that exports out from heat exchange segregator bottom high temperature dry gas after heating furnace 11 heating.High sulfur-containing natural gas moisture is after native system is processed, and wet gas is moisture to be removed more than 30%, and dewpoint temperature can reduce more than 30%.
Above-mentioned wet gas component is as follows:
Component title | mol/% |
CH 4 | 88.68 |
C 2H 6 | 0.04 |
C3+ | 0 |
CO 2 | 5.37 |
H 2S | 5.02 |
N 2 | 0.75 |
He | 0.06 |
H 2 | 0.14 |
Claims (3)
1. a hydrogen sulfide bearing gas vortex tube choke valve compression-expansion separated heating system, comprise vortex tube choke valve, heat exchange segregator, pressure gauge, thermometer, flow meter profit heating furnace, it is characterized in that: vortex tube choke valve top exit is connected with the import of the heat exchange coil of heat exchange segregator, the outlet of heat exchange coil is connected with heating furnace import, and furnace outlet is connected with natural gas multi-purpose station pipeline; Vortex tube choke valve lower part outlet is connected with the import of heat exchange segregator, and the outlet of heat exchange segregator is connected with natural gas multi-purpose station pipeline, and the condensate liquid outlet at bottom of heat exchange segregator is connected with reclaim line.
2. hydrogen sulfide bearing gas vortex tube choke valve compression-expansion separated heating system according to claim 1, is characterized in that pressure gauge, thermometer and flow meter are located at respectively in the heat exchange coil outlet and heating furnace inlet connecting branch and the outlet at bottom of heat exchange segregator and the tube connector of natural gas multi-purpose station pipeline of heat exchange segregator by order.
3. hydrogen sulfide bearing gas vortex tube choke valve compression-expansion separated heating system according to claim 1, is characterized in that flowing pipe choke valve and vertically installs, and top exit is made as the outlet of low temperature dry gas, and outlet at bottom is made as the outlet of high temperature moisture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201320593998.1U CN203640686U (en) | 2013-09-10 | 2013-09-10 | Compression expansion separation heating system with vortex tube throttle valve for high-hydrogen-sulfide-content natural gas |
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CN201320593998.1U CN203640686U (en) | 2013-09-10 | 2013-09-10 | Compression expansion separation heating system with vortex tube throttle valve for high-hydrogen-sulfide-content natural gas |
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CN203640686U true CN203640686U (en) | 2014-06-11 |
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CN201320593998.1U Expired - Fee Related CN203640686U (en) | 2013-09-10 | 2013-09-10 | Compression expansion separation heating system with vortex tube throttle valve for high-hydrogen-sulfide-content natural gas |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106153317A (en) * | 2016-06-21 | 2016-11-23 | 江苏大学 | One automatically controls vortex tube energy separation testing stand and control method thereof |
CN108691519A (en) * | 2017-04-07 | 2018-10-23 | 中国石油化工股份有限公司 | The heating system of natural gas wellhead |
CN109681151A (en) * | 2019-01-29 | 2019-04-26 | 重庆欣雨压力容器制造有限责任公司 | A kind of shale gas well head gas high-pressure treatment apparatus |
-
2013
- 2013-09-10 CN CN201320593998.1U patent/CN203640686U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106153317A (en) * | 2016-06-21 | 2016-11-23 | 江苏大学 | One automatically controls vortex tube energy separation testing stand and control method thereof |
CN106153317B (en) * | 2016-06-21 | 2018-12-14 | 江苏大学 | A kind of automatic control vortex tube energy separation testing stand and its control method |
CN108691519A (en) * | 2017-04-07 | 2018-10-23 | 中国石油化工股份有限公司 | The heating system of natural gas wellhead |
CN108691519B (en) * | 2017-04-07 | 2020-09-08 | 中国石油化工股份有限公司 | Heating system of natural gas well head |
CN109681151A (en) * | 2019-01-29 | 2019-04-26 | 重庆欣雨压力容器制造有限责任公司 | A kind of shale gas well head gas high-pressure treatment apparatus |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140611 Termination date: 20170910 |
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CF01 | Termination of patent right due to non-payment of annual fee |