CN204718348U - High-temperature hot-air and coal slime drying control system are produced in coal mine light concentration mash gas oxidation - Google Patents
High-temperature hot-air and coal slime drying control system are produced in coal mine light concentration mash gas oxidation Download PDFInfo
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- CN204718348U CN204718348U CN201520320184.XU CN201520320184U CN204718348U CN 204718348 U CN204718348 U CN 204718348U CN 201520320184 U CN201520320184 U CN 201520320184U CN 204718348 U CN204718348 U CN 204718348U
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Abstract
The utility model relates to the oxidation of a kind of coal mine light concentration mash gas and produces high-temperature hot-air and coal slime drying control system, comprise the low concentration gas air distribution subsystem, the gas heat counter flow oxidation that connect successively and produce high-temperature hot-air subsystem and safety interlocking RACS, described low concentration gas air distribution subsystem comprises mash gas extraction pipeline and is arranged on the combined type spark arrester on mash gas extraction pipeline, gas-distributing fan, a sensing methane concentration device successively; Described gas heat counter flow oxidation is produced high-temperature hot-air subsystem and is comprised blending controller, oxidation unit pressure fan, hot counter flow oxidation device; Described safety interlocking RACS comprises the Material Sensor be arranged on coal slime feeder, is arranged on the temperature sensor of drying drum entrance, the pressure sensor be arranged on low temperature outlet pipe, the high temperature adjustable valve being arranged on the outlet of hot counter flow oxidation device high-temperature hot-air and controller.Compared with prior art, the utility model has security advantages of higher.
Description
Technical field
The utility model relates to coal mine light concentration mash gas remote conveying feed technique, especially relates to the oxidation of a kind of coal mine light concentration mash gas and produces high-temperature hot-air and coal slime drying control system.
Background technology
The concentration produced in process of coal mining lower than 7% low concentration gas because of can not be civilian, internal combustion engine generating can not be used for, therefore be in emptying state for a long time.The greenhouse effects of methane are etc. 21 times of quality carbon dioxide greenhouse effect, and direct discharge not only exacerbates global greenhouse effect, pollutes environment, also causes the significant wastage of resource.
Meanwhile, the raw coal of coal mining passes through a large amount of coal slime of the selected rear generation of coal preparation plant, and due to many unfavorable conditions such as high-moisture, high viscosity, low heat value of coal slime, coal slime is difficult to realize the direct application in industrial circle.Coal preparation plant takes to land process to coal slime, and such processing mode exists many drawbacks: one is contaminated environment, easily causes the secondary pollution problem of environment of mining area; Two is can not make full use of coal slime to be worth, and causes economic loss; Three is stack area greatly, increases corresponding management cost.Along with the enforcement of National Sustainable Development Strategies, the reasonable development of the mineral resources such as coal has become important topic with comprehensive utilization, fully develops very urgent as the discarded object coal slime of stacking of leaving unused.Make good use of valuable coal slime resource, make it to turn waste into wealth, considerable economic benefit can not only be produced, also solve coal slime and stack the series of problems such as land occupation impact production and contaminated environment.
The appearance of coal slime drying system alleviates this difficult problem, and coal slime drier can the product of coal such as rapid draing coal slime, and promote coal slime added value, economize energy, increases economic efficiency.After drying dehydration, coal slime can be directly used in boiler combustion and generating, and traditional coal slime dry technology is adopt the technique of combustion furnace fire coal generation heat smoke to produce high-temperature hot-air to dry for wet coal slime, is that waste is coal-fired on the one hand, also causes environmental pollution simultaneously.From energy-saving and emission-reduction, the angle of making rational use of resources, adopt low concentration gas to produce high-temperature hot-air by hot counter flow oxidation and dry technology is carried out to wet coal slime, take full advantage of heat energy, reduce exhaust emissions, reduce the pollution to environment, this technology has higher economic benefit and environmental benefit.
Utility model content
The purpose of this utility model be exactly provide that a kind of security is high to overcome defect that above-mentioned prior art exists, the oxidation of the coal mine light concentration mash gas of economize energy produces high-temperature hot-air and coal slime drying control system.
The purpose of this utility model can be achieved through the following technical solutions:
High-temperature hot-air and coal slime drying control system are produced in a kind of coal mine light concentration mash gas oxidation, it is characterized in that, comprise the low concentration gas air distribution subsystem, the gas heat counter flow oxidation that connect successively and produce high-temperature hot-air subsystem and safety interlocking RACS, described low concentration gas air distribution subsystem comprises mash gas extraction pipeline and is arranged on the combined type spark arrester on mash gas extraction pipeline, gas-distributing fan, a sensing methane concentration device successively; Described gas heat counter flow oxidation is produced high-temperature hot-air subsystem and is comprised the blending controller be arranged on successively on mash gas extraction pipeline, oxidation unit pressure fan, hot counter flow oxidation device; Described safety interlocking RACS comprises the Material Sensor be arranged on coal slime feeder, is arranged on the temperature sensor of drying drum entrance, the pressure sensor be arranged on low temperature outlet pipe, the high temperature adjustable valve being arranged on the outlet of hot counter flow oxidation device high-temperature hot-air and controller.
Described controller is connected with Material Sensor, temperature sensor, pressure sensor, high temperature adjustable valve, gas-distributing fan, an oxidation unit pressure fan respectively.
Described hot counter flow oxidation device is connected with high temperature adjustable valve by high-temperature hot-air pipeline.
Controlled temperature cabinet is provided with between described high temperature adjustable valve and drying drum.
Described controlled temperature cabinet is provided with low-temperature heat source or air duct.
Described safety interlocking RACS also comprises the power module be connected with controller, gas-distributing fan, oxidation unit pressure fan and a high temperature adjustable valve respectively.
Compared with prior art, the utility model has the following advantages:
1) by blowing system the concentration of mash gas extraction to be reduced to after below 3% at gas conveying head end and to carry out long-distance sand transport again, original unavailable low concentration gas is utilized, and improve the security of gas conveying, decrease conveying equipment investment
2) adopt hot counter flow oxidation device oxidation low concentration gas to produce high-temperature hot-air and replace traditional coal furnace, namely achieve the utilization of coal mine gas, economize energy, decrease toxic emission simultaneously, reduce the pollution to environment.
3) fault sensor and temperature sensor are set over the whole system, for the hot counter flow oxidation equipment of chain control and coal slime drying system, ensure the security of operation of coal slime drying system.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is that safety interlocking of the present utility model controls schematic diagram.
Wherein 1 is mash gas extraction pipeline, and 2 is combined type spark arrester, and 3 is a gas-distributing fan, 4 is sensing methane concentration device, and 5 is blending controller, and 6 is oxidation unit pressure fan, 7 is hot counter flow oxidation device, and 8 is high-temperature hot-air pipeline, and 9 is high temperature adjustable valve, 10 is controlled temperature cabinet, and 11 is other low-temperature heat source or air duct, and 12 is Material Sensor, 13 is temperature sensor, and 14 is coal slime feeder, and 15 is drying drum, 16 is drying system air-introduced machine, and 17 is pressure sensor, and 18 is low temperature outlet pipe.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in detail.
Embodiment
As shown in Figure 1 and Figure 2, high-temperature hot-air and coal slime drying control system are produced in the oxidation of a kind of coal mine light concentration mash gas, comprise low concentration gas blowing system, gas heat counter flow oxidation produces high-temperature hot-air system, safety interlocking control system.Low concentration gas blowing system comprises mash gas extraction pipeline 1 and 2, the gas-distributing fan 3 of combined type spark arrester above thereof.Described gas heat counter flow oxidation is produced high-temperature hot-air system and is comprised blending controller 5, oxidation unit pressure fan 6, hot counter flow oxidation device 7 and high-temperature hot-air pipeline 8.Described safety interlocking control system comprises the sensing methane concentration device 4 be arranged on mash gas extraction pipeline 1, the Material Sensor 12 be arranged on coal slime feeder, the temperature sensor 13 being arranged on drum inlet, the pressure sensor 17 be arranged on low temperature outlet pipe, the high temperature adjustable valve 9 being arranged on the outlet of hot counter flow oxidation device high-temperature hot-air and controller 19 and power supply 20 etc.
During system cloud gray model, mash gas extraction sends into combined type spark arrester 2 through mash gas extraction pipeline 1, when sensing methane concentration device 4 records the setting value of mash gas extraction concentration higher than controller 19, controller 19 sends instruction and controls a gas-distributing fan 3 and open, and by a gas-distributing fan 3, air is sent into gas tube.When sensing methane concentration device 4 records the setting value of mash gas extraction concentration lower than controller 19, controller 19 sends instruction and controls a gas-distributing fan 3 and shut down.Methane gas is after blending controller 5 regulates, send into hot counter flow oxidation device 7 through oxidation unit pressure fan 6 to be oxidized, the high-temperature hot-air produced after oxidation is delivered to high temperature adjustable valve 9 through high-temperature hot-air pipeline 8, mix with the hot blast sent here through other low-temperature heat source or air duct 11 or air after high-temperature hot-air after regulating is delivered to controlled temperature cabinet 10, mixed hot blast is delivered in drying drum 15 and is dried for wet coal slime.Gas after drying for wet coal slime is drawn by drying system air-introduced machine 16 and is discharged through low temperature outlet pipe 18.Material Sensor 12 signal on coal slime feeder 14 is sent into controller 19, via controller 19 analytic operation, when the material of coal slime feeder 14 is lower than whole coal slime drying system technological requirement, controller 19 sends instruction control high temperature adjustable valve 9 and reduces until cut out completely gradually.Temperature sensor 13 before drying drum 15 is sent into controller 19, and when the temperature value that the temperature of temperature sensor 13 requires higher than drying drum 15, controller 19 sends instruction and controls high temperature adjustable valve 9 and reduce until cut out completely gradually.When pressure sensor 17 blackout on low temperature outlet pipe 18 being detected when controller 19, controller 19 sends instruction control high temperature adjustable valve 9 and directly cuts out.
Claims (6)
1. high-temperature hot-air and coal slime drying control system are produced in a coal mine light concentration mash gas oxidation, it is characterized in that, comprise the low concentration gas air distribution subsystem, the gas heat counter flow oxidation that connect successively and produce high-temperature hot-air subsystem and safety interlocking RACS, described low concentration gas air distribution subsystem comprises mash gas extraction pipeline and is arranged on the combined type spark arrester on mash gas extraction pipeline, gas-distributing fan, a sensing methane concentration device successively; Described gas heat counter flow oxidation is produced high-temperature hot-air subsystem and is comprised the blending controller be arranged on successively on mash gas extraction pipeline, oxidation unit pressure fan, hot counter flow oxidation device; Described safety interlocking RACS comprises the Material Sensor be arranged on coal slime feeder, is arranged on the temperature sensor of drying drum entrance, the pressure sensor be arranged on low temperature outlet pipe, the high temperature adjustable valve being arranged on the outlet of hot counter flow oxidation device high-temperature hot-air and controller.
2. high-temperature hot-air and coal slime drying control system are produced in a kind of coal mine light concentration mash gas oxidation according to claim 1, it is characterized in that, described controller is connected with Material Sensor, temperature sensor, pressure sensor, high temperature adjustable valve, gas-distributing fan, an oxidation unit pressure fan respectively.
3. high-temperature hot-air and coal slime drying control system are produced in a kind of coal mine light concentration mash gas oxidation according to claim 1, and it is characterized in that, described hot counter flow oxidation device is connected with high temperature adjustable valve by high-temperature hot-air pipeline.
4. high-temperature hot-air and coal slime drying control system are produced in a kind of coal mine light concentration mash gas oxidation according to claim 1, it is characterized in that, are provided with controlled temperature cabinet between described high temperature adjustable valve and drying drum.
5. high-temperature hot-air and coal slime drying control system are produced in a kind of coal mine light concentration mash gas oxidation according to claim 4, and it is characterized in that, described controlled temperature cabinet is provided with low-temperature heat source or air duct.
6. high-temperature hot-air and coal slime drying control system are produced in a kind of coal mine light concentration mash gas oxidation according to claim 1, it is characterized in that, described safety interlocking RACS also comprises the power module be connected with controller, gas-distributing fan, oxidation unit pressure fan and a high temperature adjustable valve respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520320184.XU CN204718348U (en) | 2015-05-18 | 2015-05-18 | High-temperature hot-air and coal slime drying control system are produced in coal mine light concentration mash gas oxidation |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520320184.XU CN204718348U (en) | 2015-05-18 | 2015-05-18 | High-temperature hot-air and coal slime drying control system are produced in coal mine light concentration mash gas oxidation |
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| Publication Number | Publication Date |
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| CN204718348U true CN204718348U (en) | 2015-10-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520320184.XU Expired - Fee Related CN204718348U (en) | 2015-05-18 | 2015-05-18 | High-temperature hot-air and coal slime drying control system are produced in coal mine light concentration mash gas oxidation |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109187925A (en) * | 2018-09-18 | 2019-01-11 | 太原理工大学 | A kind of abandoned mine goaf gas-liquid counter current three-dimensional analog simulation pilot system |
| CN110174021A (en) * | 2019-05-28 | 2019-08-27 | 浙江亿扬能源科技有限公司 | A kind of waste heat comprehensive utilization system and operation method for realizing the drying of coal mine wet stock using low concentration gas |
| CN111141138A (en) * | 2020-02-11 | 2020-05-12 | 山东理工大学 | Device and method for reducing oxygen content of hot air for drying coal slime in gas oxidation furnace |
-
2015
- 2015-05-18 CN CN201520320184.XU patent/CN204718348U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109187925A (en) * | 2018-09-18 | 2019-01-11 | 太原理工大学 | A kind of abandoned mine goaf gas-liquid counter current three-dimensional analog simulation pilot system |
| CN110174021A (en) * | 2019-05-28 | 2019-08-27 | 浙江亿扬能源科技有限公司 | A kind of waste heat comprehensive utilization system and operation method for realizing the drying of coal mine wet stock using low concentration gas |
| CN111141138A (en) * | 2020-02-11 | 2020-05-12 | 山东理工大学 | Device and method for reducing oxygen content of hot air for drying coal slime in gas oxidation furnace |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right | ||
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Effective date of registration: 20191016 Granted publication date: 20151021 |
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| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20220621 Granted publication date: 20151021 |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151021 Termination date: 20200518 |