CN107387155A - A kind of coal bed gas automatic blending control system and regulation and control method - Google Patents
A kind of coal bed gas automatic blending control system and regulation and control method Download PDFInfo
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- CN107387155A CN107387155A CN201710812353.5A CN201710812353A CN107387155A CN 107387155 A CN107387155 A CN 107387155A CN 201710812353 A CN201710812353 A CN 201710812353A CN 107387155 A CN107387155 A CN 107387155A
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- valve
- link
- regulating valves
- concentration
- pid regulating
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- 238000002156 mixing Methods 0.000 title claims abstract description 29
- 239000003245 coal Substances 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims abstract description 20
- 230000001105 regulatory effect Effects 0.000 claims abstract description 48
- 238000000605 extraction Methods 0.000 claims abstract description 39
- 238000001514 detection method Methods 0.000 claims description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 230000000740 bleeding effect Effects 0.000 claims description 3
- 239000000203 mixture Substances 0.000 abstract description 16
- 238000005516 engineering process Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000012237 artificial material Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012790 confirmation Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21F—SAFETY DEVICES, TRANSPORT, FILLING-UP, RESCUE, VENTILATION, OR DRAINING IN OR OF MINES OR TUNNELS
- E21F7/00—Methods or devices for drawing- off gases with or without subsequent use of the gas for any purpose
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21F—SAFETY DEVICES, TRANSPORT, FILLING-UP, RESCUE, VENTILATION, OR DRAINING IN OR OF MINES OR TUNNELS
- E21F17/00—Methods or devices for use in mines or tunnels, not covered elsewhere
- E21F17/18—Special adaptations of signalling or alarm devices
Landscapes
- Engineering & Computer Science (AREA)
- Mining & Mineral Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Accessories For Mixers (AREA)
Abstract
The present invention relates to a kind of coal bed gas automatic blending control system and regulation and control method, belong to technology for coal mine gas field.The system includes mash gas extraction link, wind resource assessment link, blending mechanism and output link；Two inputs of the mash gas extraction link and the wind resource assessment link respectively with the blending mechanism are connected, and the output link is connected with the output end of the blending mechanism.Technical scheme provided by the invention, the coal bed gas in pipeline can be automatically regulated, to ensure the stability of the coal bed gas after mixture and accuracy.
Description
Technical field
The invention belongs to technology for coal mine gas field, is related to a kind of coal bed gas automatic blending control system and regulation and control method.
Background technology
Coal bed gas is a kind of cleaning, efficient high-grade energy, at the same be also influence Safety of Coal Mine Production one it is big it is fatal because
Element.The generation of gas accident how is reduced during Safety of Coal Mine Production, makes full use of this high-quality cleaning resource of coal bed gas,
The concern of country and society is enjoyed always.
The application of coal bed gas is very extensive, may be used as industrial fuel, fuel used to generate electricity, motor vehicle fuel and important change
Work raw material, if extraction coal seam gas concentration it is too low can not utilize if need to empty safely.Either by watt with explosion hazard
This gas is changed into the energy and utilized, or by burn means carry out safety dumping, be required in advance by mash gas extraction gas with it is weary
Wind or higher concentration gas mixture are continuous, the stable source of the gas of finite concentration scope.Coal bed gas mixture is mainly using artificial at present
Regulation, it is impossible to realize continuous, automatic, safety regulation well, it is difficult to ensure that after mixture source of the gas stability and accuracy, and
The security and economy problems that regulating time is long, air inlet wave zone can not be overcome, it is difficult to meet application demand.Therefore, grind
The coal bed gas automatic blending control system and regulation and control method that to send out a kind of fast and reliable seem particularly necessary.
The content of the invention
In view of this, it is an object of the invention to provide a kind of coal bed gas automatic blending control system and regulation and control method, energy
The coal bed gas in pipeline is enough automatically regulated, to ensure the stability of the coal bed gas after mixture and accuracy.
To reach above-mentioned purpose, the present invention provides following technical scheme：
A kind of coal bed gas automatic blending control system, the system include mash gas extraction link, wind resource assessment link, blending
Mechanism and output link；The mash gas extraction link and the wind resource assessment link are defeated with two of the blending mechanism respectively
Entering end to be connected, the output link is connected with the output end of the blending mechanism, wherein：The mash gas extraction link includes extraction
Gas tube, mash gas extraction infomation detection mechanism, the first PID regulating valves and have been sequentially distributed on the mash gas extraction pipeline
One fast valve, wherein, outwards it is vented by exhaust-valve between the first PID regulating valves and first fast valve；The wind
Gas-removing link includes wind resource assessment pipeline, and the wind resource assessment pipeline is connected with least one wind for being used to inject wind resource assessment
Well idle air pipeline；The output link includes output channel, be sequentially distributed on the output channel You Hunqi infomation detections mechanism,
Second fast valve and the 2nd PID regulating valves.
Further, distribution is included in the mash gas extraction infomation detection mechanism and the Hun Qi infomation detections mechanism
Laser methane sensor, ultrasonic flowmeter, pressure gauge and thermometer.
Further, the degree of regulation of the first PID regulating valves and the 2nd PID regulating valves is faster than described first
The degree of regulation for closing valve and second fast valve is high.
Further, the water seal fire arrestor being connected with the 2nd PID regulating valves is additionally provided with the output channel.
A kind of regulation and control method, methods described include：
The mixed gas by the output of blending mechanism is predefined in the air inflow needed for synchronization, and according to the air inlet
Amount, determines the first PID regulating valves and the valve opening value of the first fast valve in mash gas extraction link；
The first PID regulating valves and the first fast valve are set according to the valve opening value, and adjusted in output link
The second fast valve and the 2nd PID regulating valves, to cause the concentration of mixed gas to be in the range of the first default safe concentration；
The first PID regulating valves and the 2nd PID regulating valves are progressively adjusted, to cause the concentration of the mixed gas to be in
In the range of second default safe concentration；Wherein, the described second default safe concentration scope is less than the described first default safe concentration
Scope；
The concentration of the mixed gas of fluctuation is prejudged whether beyond the described second default safe concentration scope, if so, regulation described the
One fast valve and second fast valve, to cause the concentration of the mixed gas after regulation to be in the described first default safe concentration scope
It is interior；
The concentration of the mixed gas of fluctuation is prejudged whether beyond the described first default safe concentration scope, if so, being taken out described in opening
Air bleeding valve in mash gas link, to empty mash gas extraction, and close the 2nd PID regulating valves and second quick valve.
Further, the second fast valve and the 2nd PID regulating valves in output link are adjusted, to cause the concentration of mixed gas
Include in the range of default safe concentration：
The minimum and peak of the default safe concentration scope are determined, and according to the minimum and the highest
Value, obtain the adjustable range of second fast valve and the 2nd PID regulating valves；
Second fast valve and the 2nd PID are progressively adjusted in the adjustable range according to default stepping opening value to adjust
Save valve.
The beneficial effects of the present invention are：
Automating, being intelligent for mixture process, reduces the labor intensity and uncertainty of artificial material mixing's process, and carry
Mixture speed and mixture precision are risen.Anticipation method therein efficiently solve air inlet methane concentration produce larger fluctuation when caused by
The security and economy problems that rear end mixture gas utilizes.
Brief description of the drawings
In order that the purpose of the present invention, technical scheme and beneficial effect are clearer, the present invention provides drawings described below and carried out
Explanation：
Fig. 1 is the structural representation of coal bed gas automatic blending control system in the application；
Regulate and control the flow chart of method in Fig. 2 the application.
Embodiment
Below in conjunction with accompanying drawing, the preferred embodiments of the present invention are described in detail.
Referring to Fig. 1, the application provides a kind of coal bed gas automatic blending control system, the system includes mash gas extraction chain
Road, wind resource assessment link, blending mechanism and output link；The mash gas extraction link and the wind resource assessment link respectively with
Two inputs of the blending mechanism are connected, and the output link is connected with the output end of the blending mechanism, wherein：
The mash gas extraction link includes mash gas extraction pipeline 1, and extraction watt has been sequentially distributed on the mash gas extraction pipeline 1
This infomation detection mechanism, the first PID regulating valves 2 and the first fast valve 3, wherein, the first PID regulating valves 2 and described the
Outwards it is vented by exhaust-valve 4 between one fast valve 3；
The wind resource assessment link includes wind resource assessment pipeline 5, and the wind resource assessment pipeline 5 is connected with least one and is used for
Inject the ventilating shaft idle air pipeline 6 of wind resource assessment；
The output link includes output channel 7, be sequentially distributed on the output channel 7 You Hunqi infomation detections mechanism,
Second fast valve 8 and the 2nd PID regulating valves 9.
In the present embodiment, include in the mash gas extraction infomation detection mechanism and the Hun Qi infomation detections mechanism
Distributed laser methane sensor 10, ultrasonic flowmeter 11, pressure gauge 12 and thermometer 13.
In the present embodiment, the degree of regulation of the first PID regulating valves 2 and the 2nd PID regulating valves 9 is than institute
The degree of regulation for stating the first fast valve 3 and second fast valve 8 is high.
In the present embodiment, the water seal being connected with the 2nd PID regulating valves 9 is additionally provided with the output channel 7
Spark arrester.
Specifically, the mash gas extraction pipeline can input mash gas extraction, and the ventilating shaft idle air pipeline can be arranged aweather watt
Wind resource assessment is inputted in this pipeline, the wind resource assessment and the mash gas extraction can mix in mechanism is blended.In addition, pass through
Mash gas extraction infomation detection mechanism can measure concentration, flow velocity, pressure and the temperature of mash gas extraction.Similarly, by mixing gas
Infomation detection mechanism can measure concentration, flow velocity, pressure and the temperature of mixed gas.
In the present embodiment, can be realized to air in pipeline by the first PID regulating valves and the 2nd PID regulating valves
Accurate adjustment, the coarse adjustment to the gas in pipeline can be realized by the first fast valve and the second fast valve.The exhaust-valve can be
When necessary, the mash gas extraction of injection is discharged to outside pipeline and gone.The water seal fire arrestor can ensure that rear end uses mixed gas
Safety, avoid on fire.
Referring to Fig. 2, the application also provides a kind of regulation and control being applied in above-mentioned coal bed gas automatic blending control system
Method, methods described include：
S1：Predefine by blending mechanism output mixed gas in the air inflow needed for synchronization, and according to it is described enter
Tolerance, determine the first PID regulating valves and the valve opening value of the first fast valve in mash gas extraction link；
S2：The first PID regulating valves and the first fast valve are set according to the valve opening value, and adjust output link
In the second fast valve and the 2nd PID regulating valves, to cause the concentration of mixed gas to be in the range of the first default safe concentration；
S3：The first PID regulating valves and the 2nd PID regulating valves are progressively adjusted, to cause the concentration of the mixed gas
In the range of the second default safe concentration；Wherein, the described second default safe concentration scope is less than the described first default safety
Concentration range；
S4：The concentration of the mixed gas of fluctuation is prejudged whether beyond the described second default safe concentration scope, if so, described in regulation
First fast valve and second fast valve, to cause the concentration of the mixed gas after regulation to be in the described first default safe concentration model
In enclosing；
S5：The concentration of the mixed gas of fluctuation is prejudged whether beyond the described first default safe concentration scope, if so, described in opening
Air bleeding valve in mash gas extraction link, to empty mash gas extraction, and close the 2nd PID regulating valves and described second quick
Valve.
In the present embodiment, the second fast valve and the 2nd PID regulating valves in output link are adjusted, to cause mixed gas
Concentration be in the range of default safe concentration and include：
The minimum and peak of the default safe concentration scope are determined, and according to the minimum and the highest
Value, obtain the adjustable range of second fast valve and the 2nd PID regulating valves；
Second fast valve and the 2nd PID are progressively adjusted in the adjustable range according to default stepping opening value to adjust
Save valve.
In actual application, the following steps can be distributed：
1) system boot, regulation-control model is coupled by parameters such as concentration, flows, according to mixed gas aimed concn, passes through regulation and control
Model calculates the air inflow that mixed gas needs in synchronization, can obtain valve opening value by tabling look-up and sets valve opening,
Mixed gas concentration after mixture is transferred in the scope of default safe concentration by the second fast valve Fast Coarse, the scope can represent
For x%-e1-e2 to x%+e1+e2.Wherein, x can represent targeted security concentration value, and e1 and e2 represent fluctuation of concentration value.
2) valve aperture is automatically adjusted, by presetting the minimum of safe concentration scope, peak, obtains valve stroke
Scope, the scope of PID governor valve controls is set, avoids the hyperharmonic of system from shaking.
3) after manual confirmation anticipation accuracy, the regulation of PID regulating valves automatic fine is begun through, progressively arrives fluctuation regulation
In the range of x%-e1 to x%+e1, now major control precision.
4) when the unexpected fluctuation of anticipation inlet gas concentration has exceeded fine adjustment range, the valve opening of fast valve, control are directly adjusted
Charge flow rate, ensureing the stability and security of gas after mixture, now mainly value speed, required precision is relatively low, from
And reduce control time.
5) when the unexpected fluctuation of anticipation inlet gas concentration has exceeded coarse adjustment safe concentration scope, air inlet is emptied by exhaust-valve,
Rear end is prevented to utilize.
The beneficial effects of the present invention are：
Automating, being intelligent for mixture process, reduces the labor intensity and uncertainty of artificial material mixing's process, and carry
Mixture speed and mixture precision are risen.Anticipation method therein efficiently solve air inlet methane concentration produce larger fluctuation when caused by
The security and economy problems that rear end mixture gas utilizes.
Finally illustrate, preferred embodiment above is merely illustrative of the technical solution of the present invention and unrestricted, although logical
Cross above preferred embodiment the present invention is described in detail, it is to be understood by those skilled in the art that can be
Various changes are made to it in form and in details, without departing from claims of the present invention limited range.
Claims (6)
1. a kind of coal bed gas automatic blending control system, it is characterised in that the system includes mash gas extraction link, wind resource assessment
Link, blending mechanism and output link；The mash gas extraction link and the wind resource assessment link respectively with the blender
Two inputs of structure are connected, and the output link is connected with the output end of the blending mechanism, wherein：
The mash gas extraction link includes mash gas extraction pipeline, and mash gas extraction information has been sequentially distributed on the mash gas extraction pipeline
Testing agency, the first PID regulating valves and the first fast valve, wherein, the first PID regulating valves and first fast valve it
Between be outwards vented by exhaust-valve；
The wind resource assessment link includes wind resource assessment pipeline, and the wind resource assessment pipeline is connected with least one and is used to inject wind
The ventilating shaft idle air pipeline of gas-removing；
The output link includes output channel, and You Hunqi infomation detections mechanism, second fast is sequentially distributed on the output channel
Close valve and the 2nd PID regulating valves.
2. system according to claim 1, it is characterised in that the mash gas extraction infomation detection mechanism and the mixed gas letter
Include distributed laser methane sensor, ultrasonic flowmeter, pressure gauge and thermometer in breath testing agency.
3. system according to claim 1, it is characterised in that the first PID regulating valves and the 2nd PID regulating valves
Degree of regulation of the degree of regulation than first fast valve and second fast valve it is high.
4. system according to claim 1, it is characterised in that be additionally provided with the output channel and the 2nd PID
The connected water seal fire arrestor of regulating valve.
5. a kind of regulation and control method being applied in the coal bed gas automatic blending control system as described in any in Claims 1-4,
Characterized in that, methods described includes：
The mixed gas by the output of blending mechanism is predefined in the air inflow needed for synchronization, and according to the air inflow, really
Determine the first PID regulating valves and the valve opening value of the first fast valve in mash gas extraction link；
The first PID regulating valves and the first fast valve are set according to the valve opening value, and adjust the in output link
Two fast valves and the 2nd PID regulating valves, to cause the concentration of mixed gas to be in the range of the first default safe concentration；
The first PID regulating valves and the 2nd PID regulating valves are progressively adjusted, to cause the concentration of the mixed gas to be in second
In the range of default safe concentration；Wherein, the described second default safe concentration scope is less than the described first default safe concentration scope；
The concentration of the mixed gas of fluctuation is prejudged whether beyond the described second default safe concentration scope, if so, regulation described first is fast
Valve and second fast valve are closed, to cause the concentration of the mixed gas after regulation to be in the range of the described first default safe concentration；
The concentration of the mixed gas of fluctuation is prejudged whether beyond the described first default safe concentration scope, if so, opening the extraction watt
Air bleeding valve in this link, to empty mash gas extraction, and close the 2nd PID regulating valves and second quick valve.
6. according to the method for claim 5, it is characterised in that the second fast valve and second in regulation output link
PID regulating valves, to cause the concentration of mixed gas is in the range of default safe concentration to include：
The minimum and peak of the default safe concentration scope are determined, and according to the minimum and the peak, is obtained
Take the adjustable range of second fast valve and the 2nd PID regulating valves；
Second fast valve and the 2nd PID are progressively adjusted in the adjustable range according to default stepping opening value to adjust
Valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710812353.5A CN107387155A (en) | 2017-09-11 | 2017-09-11 | A kind of coal bed gas automatic blending control system and regulation and control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710812353.5A CN107387155A (en) | 2017-09-11 | 2017-09-11 | A kind of coal bed gas automatic blending control system and regulation and control method |
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| Publication Number | Publication Date |
|---|---|
| CN107387155A true CN107387155A (en) | 2017-11-24 |
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| CN201710812353.5A Pending CN107387155A (en) | 2017-09-11 | 2017-09-11 | A kind of coal bed gas automatic blending control system and regulation and control method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111119984A (en) * | 2019-12-30 | 2020-05-08 | 煤炭科学技术研究院有限公司 | System and method for intensive utilization of regional gas network and mutual feedback control of mine gas extraction |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| UA16122U (en) * | 2006-02-27 | 2006-07-17 | Lease Entpr O F Zasiadko Mine | Method for utilization of mine methane-air mix |
| CN102562131A (en) * | 2010-12-24 | 2012-07-11 | 上海攀极投资有限公司 | Coal mine gas comprehensive application system and application method thereof |
| CN202690117U (en) * | 2012-04-01 | 2013-01-23 | 浙江亿扬能源科技有限公司 | Ventilation air collecting and mixing system |
| CN202909645U (en) * | 2012-11-15 | 2013-05-01 | 苏州新思气体***有限公司 | Automatic nitrogen-hydrogen proportioning and mixing device |
| CN104033174A (en) * | 2014-06-10 | 2014-09-10 | 中国矿业大学 | Safe and automatic methane concentration regulation system and method |
| CN204460275U (en) * | 2014-12-31 | 2015-07-08 | 重庆川然节能技术有限公司 | A kind of combustion energy saving safety control system |
| CN105498563A (en) * | 2015-12-29 | 2016-04-20 | 中煤科工集团重庆研究院有限公司 | Coal-mine gas mixing system and mixing method |
| WO2017097733A1 (en) * | 2015-12-07 | 2017-06-15 | Dürr Systems Ag | A mixing and processing system of ventilation air methane and coal mine methane |
-
2017
- 2017-09-11 CN CN201710812353.5A patent/CN107387155A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| UA16122U (en) * | 2006-02-27 | 2006-07-17 | Lease Entpr O F Zasiadko Mine | Method for utilization of mine methane-air mix |
| CN102562131A (en) * | 2010-12-24 | 2012-07-11 | 上海攀极投资有限公司 | Coal mine gas comprehensive application system and application method thereof |
| CN202690117U (en) * | 2012-04-01 | 2013-01-23 | 浙江亿扬能源科技有限公司 | Ventilation air collecting and mixing system |
| CN202909645U (en) * | 2012-11-15 | 2013-05-01 | 苏州新思气体***有限公司 | Automatic nitrogen-hydrogen proportioning and mixing device |
| CN104033174A (en) * | 2014-06-10 | 2014-09-10 | 中国矿业大学 | Safe and automatic methane concentration regulation system and method |
| CN204460275U (en) * | 2014-12-31 | 2015-07-08 | 重庆川然节能技术有限公司 | A kind of combustion energy saving safety control system |
| WO2017097733A1 (en) * | 2015-12-07 | 2017-06-15 | Dürr Systems Ag | A mixing and processing system of ventilation air methane and coal mine methane |
| CN105498563A (en) * | 2015-12-29 | 2016-04-20 | 中煤科工集团重庆研究院有限公司 | Coal-mine gas mixing system and mixing method |
Non-Patent Citations (2)
| Title |
|---|
| 王树强;倪洪启;于江华;: "基于PID的煤层气掺混控制***的设计", no. 07 * |
| 秦黄辉 等: "制冷与空调自动化", vol. 1, 哈尔滨工程大学出版社, pages: 17 - 18 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111119984A (en) * | 2019-12-30 | 2020-05-08 | 煤炭科学技术研究院有限公司 | System and method for intensive utilization of regional gas network and mutual feedback control of mine gas extraction |
| CN111119984B (en) * | 2019-12-30 | 2021-05-07 | 煤炭科学技术研究院有限公司 | System and method for intensive utilization of regional gas network and mutual feedback control of mine gas extraction |
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Application publication date: 20171124 |