CN203613148U - Microwave coal dry distillation equipment - Google Patents
Microwave coal dry distillation equipment Download PDFInfo
- Publication number
- CN203613148U CN203613148U CN201320689908.9U CN201320689908U CN203613148U CN 203613148 U CN203613148 U CN 203613148U CN 201320689908 U CN201320689908 U CN 201320689908U CN 203613148 U CN203613148 U CN 203613148U
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- microwave
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- feeding
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Abstract
The utility model provides microwave coal dry distillation equipment and effectively solves the problems of unstable feeding and blanking and the like of existing microwave coal dry distillation equipment. The scheme is as follows: the equipment comprises a transverse feeding screw conveyor, a buffer section is connected onto a discharging port below the feeding screw conveyor, a lower port of the buffer section is communicated with a microwave action chamber, the microwave action chamber is connected with a microwave source system through a microwave transmission system, the upper part of the microwave action chamber is communicated with a gas collection pipeline, a lower port of the microwave action chamber is communicated with a cooling section, a lower port of the cooling section is communicated with a transverse discharging screw conveyor, and a temperature measuring device is mounted in the microwave action chamber; and the feeding screw conveyor, the microwave source system, the temperature measuring device and the discharging screw conveyor are connected onto a controller respectively. The equipment is novel and unique in structure, stable feeding and blanking of raw coal can be realized, the microwave heating temperature and the material heating time can be well controlled, and the dry distillation effect on the raw coal is improved.
Description
Technical field
The utility model relates to microwave equipment, particularly a kind of equipment of microwave destructive distillation coal.
Background technology
Microwave reaction kettle is mainly used in chemical industry, medical science, oil, dyestuff, biochemistry waits chemical reaction and the heating in Industrial processes cooling, liquid extraction, the change procedures such as gas absorption, and microwave produces from inside with having heat for the heat effect of inhaling ripple material, do not need thermal conduction, heating is fast, the heating properties that uniform temperature fields etc. are unique, research is also found, microwave has non-thermal effect to some chemical reaction, this microwave chemical reaction has significant promoter action with respect to thermal chemical reaction, not only can improve speed of response, Reaction time shorten, also can improve reaction conversion ratio, to these chemical reactions, have fast, efficiently, the feature such as energy-conservation, the equipment of traditional microwave destructive distillation coal is mostly direct loading and unloading, its loading and unloading process is not steady, can not can not effectively control the amount of the loading and unloading of material.
Utility model content
For above-mentioned situation, for overcoming the defect of prior art, the object of the utility model is just to provide a kind of equipment of microwave destructive distillation coal, has effectively solved the problems such as existing microwave destructive distillation coal equipment loading and unloading shakiness.
The scheme of its solution is, comprise horizontal feeding spiral conveyer, on the discharge port of feeding spiral conveyer below, be connected with buffering disconnected, the disconnected lower port of buffering is communicated with microwave action chamber, on microwave action chamber, be connected with microwave source system through microwave transmission system, top, microwave action chamber is communicated with getter pipeline, microwave action chamber lower port is communicated with cooling section, cooling section lower port is communicated with horizontal discharging spiral conveyor, microwave action is equipped with temperature measuring equipment in chamber, described feeding spiral conveyer, microwave source system, temperature measuring equipment and discharging spiral conveyor are connected on controller.
The utility model novel structure uniqueness, not only can realize raw coal loading and unloading steady, and can be good at Heating temperature to microwave and to controlling the heat-up time of material, increased the effect to the former dry distillation of coal.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described in further detail.
Provided by Fig. 1, the utility model comprises horizontal feeding spiral conveyer, on the discharge port of feeding spiral conveyer below, be connected with buffering disconnected 2, disconnected 2 lower port of buffering are communicated with microwave action chamber 3, on microwave action chamber 3, be connected with microwave source system 5 through microwave transmission system 4, 3 tops, microwave action chamber are communicated with getter pipeline 6, microwave action chamber 3 lower port are communicated with cooling section 7, cooling section 7 lower port are communicated with horizontal discharging spiral conveyor, temperature measuring equipment 9 is housed in microwave action chamber 3, described feeding spiral conveyer, microwave source system 5, temperature measuring equipment 9 and discharging spiral conveyor are connected on controller.
Said temperature measuring equipment 9 is temperature sensor.
On said microwave action chamber 3, viewing window 10 is housed.
Hopper 11 is housed on the opening for feed of said feeding spiral conveyer.
The discharge port place of said discharging spiral conveyor is connected with receiving hopper 12.
Said feeding spiral conveyer or discharging spiral conveyor comprise the sleeve 1 of horizontal closed at both ends and are placed in the motor 8 of sleeve 1 end, the output shaft of motor 8 connects through shaft coupling the rotating shaft being placed in sleeve 1, rotating shaft is provided with helical feed blade face, there is opening for feed sleeve 1 upper end, and there is discharge port sleeve 1 lower end.
When the utility model uses, raw coal under the effect of feeding spiral conveyer in breeze way 2 enters microwave action chamber 3, because cooling section 7 belows are connected to horizontal discharging spiral discharging machine, control the discharging speed of discharging spiral conveyor, make material on cooling section 7 to the certain height of the interior accumulation in microwave action chamber 3, and then regulate discharging spiral conveyor to make the material of upper end at the interior stop in microwave action chamber 3 30-60 minute, regulate microwave heating to 550-700 ℃, fully after reaction, raw coal is broken down into gas mixture, coal tar and coke, gas mixture is after getter pipeline 6 is collected, be separated into coal tar, coke(oven)gas, virgin ammonia liquor and clumsy etc., coke is expelled in receiving hopper 12 through discharging spiral conveyor, in reaction process, microwave power and mass transport speed are all adjustable, and under the control of temperature automatic regulating power and carry defeated degree (comprising loading and unloading).
The utility model novel structure uniqueness, not only can realize raw coal loading and unloading steady, and can be good at Heating temperature to microwave and to controlling the heat-up time of material, increased the effect to the former dry distillation of coal.
Claims (6)
1. the equipment of a microwave destructive distillation coal, comprise horizontal feeding spiral conveyer, it is characterized in that, on the discharge port of feeding spiral conveyer below, be connected with buffering disconnected (2), disconnected (2) lower port of buffering is communicated with microwave action chamber (3), microwave action chamber (3) is upper is connected with microwave source system (5) through microwave transmission system (4), top, microwave action chamber (3) is communicated with getter pipeline (6), microwave action chamber (3) lower port is communicated with cooling section (7), cooling section (7) lower port is communicated with horizontal discharging spiral conveyor, temperature measuring equipment (9) is housed in microwave action chamber (3), described feeding spiral conveyer, microwave source system (5), temperature measuring equipment (9) and discharging spiral conveyor are connected on controller.
2. according to the equipment of a kind of microwave destructive distillation coal described in right 1, it is characterized in that, said temperature measuring equipment (9) is temperature sensor.
3. according to the equipment of a kind of microwave destructive distillation coal described in right 1, it is characterized in that, viewing window (10) is housed on said microwave action chamber (3).
4. according to the equipment of a kind of microwave destructive distillation coal described in right 1, it is characterized in that, hopper (11) is housed on the opening for feed of said feeding spiral conveyer.
5. according to the equipment of a kind of microwave destructive distillation coal described in right 1, it is characterized in that, the discharge port place of said discharging spiral conveyor is connected with receiving hopper (12).
6. according to the equipment of a kind of microwave destructive distillation coal described in right 1, it is characterized in that, said feeding spiral conveyer or discharging spiral conveyor comprise the sleeve (1) of horizontal closed at both ends and are placed in the motor (8) of sleeve (1) end, the output shaft of motor (8) connects through shaft coupling the rotating shaft being placed in sleeve (1), rotating shaft is provided with helical feed blade face, there is opening for feed sleeve (1) upper end, and there is discharge port sleeve (1) lower end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320689908.9U CN203613148U (en) | 2013-11-05 | 2013-11-05 | Microwave coal dry distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320689908.9U CN203613148U (en) | 2013-11-05 | 2013-11-05 | Microwave coal dry distillation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203613148U true CN203613148U (en) | 2014-05-28 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320689908.9U Expired - Fee Related CN203613148U (en) | 2013-11-05 | 2013-11-05 | Microwave coal dry distillation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203613148U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104962300A (en) * | 2015-06-24 | 2015-10-07 | 南京三乐微波技术发展有限公司 | Coal microwave dry distillation equipment and coal microwave dry distillation treatment method thereof |
-
2013
- 2013-11-05 CN CN201320689908.9U patent/CN203613148U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104962300A (en) * | 2015-06-24 | 2015-10-07 | 南京三乐微波技术发展有限公司 | Coal microwave dry distillation equipment and coal microwave dry distillation treatment method thereof |
| CN104962300B (en) * | 2015-06-24 | 2018-03-13 | 南京三乐微波技术发展有限公司 | Coal microwave destructive distillation equipment and its coal microwave destructive distillation processing method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20140528 Termination date: 20161105 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |