CN205501192U - Novel coal pyrolysis reactor - Google Patents
Novel coal pyrolysis reactor Download PDFInfo
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- CN205501192U CN205501192U CN201620106505.0U CN201620106505U CN205501192U CN 205501192 U CN205501192 U CN 205501192U CN 201620106505 U CN201620106505 U CN 201620106505U CN 205501192 U CN205501192 U CN 205501192U
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Abstract
The utility model discloses a novel coal pyrolysis reactor. It includes the combustion chamber, the pyrolysis chamber, the coal bunker, the valve, the cooling and purification device, the basin, the regenerator, outer coal supply trachea, arrange cinder notch and switching -over valve, the combustion chamber top is provided with two pyrolysis chambers, pyrolysis chamber upper portion is provided with the coal bunker through the valve, the combustion chamber bottom is provided with the basin, the basin links to each other with the regenerator, the regenerator links to each other with another regenerator through the switching -over valve, another regenerator links to each other with the combustion chamber, the pyrolysis chamber still links to each other with the cooling and purification device through the pipeline, the cooling and purification device respectively with outer coal supply trachea, it links to each other to arrange the cinder notch. The utility model discloses simple structure, reaction effect is good, the brown coal of can effectively changeing, economic environmental protection, the practicality is strong.
Description
Technical field
This utility model relates to pyrolytic reaction technical field, is specifically related to a kind of Novel coal pyrolysis reactor.
Background technology
Brown coal upgrading Land use systems mainly has: drying and dehydrating, gasification and low temperature pyrogenation Poly-generation.Wherein, brown
Coal drying and dehydrating technology development comparative maturity, but which is the highest to brown coal trans-utilization rate, following by main
During being applied to pretreatment of raw material；Brown coal main flow gasification technology at home there is certain suitability,
There is project construction case；Brown coal low temperature pyrogenation Poly-generation is many due to side-product, and systematicness integrated technique need to enter one
Step development is perfect, and needs to consider production marketing problem.But current brown coal low-temperature pyrolysis reactor is also deposited
In some defects, need to carry out some structure improvement, to meet Production requirement.
Utility model content
For solving the problems referred to above, this utility model provides a kind of Novel coal pyrolysis reactor, simple in construction,
Reaction effect is good, it is possible to effectively convert brown coal, economic and environment-friendly, practical.
For achieving the above object, the technical scheme that this utility model is taked is: a kind of Novel coal pyrolysis reactor,
Including combustor, pyrolysis chamber, coal bunker, valve, cooling purifying device, tank, regenerator, give gas outward
Pipe, slag-drip opening and reversal valve, combustor is provided above Liang Ge pyrolysis chamber, and top, pyrolysis chamber is set by valve
Being equipped with coal bunker, bottom of combustion chamber is provided with tank, and tank is connected with regenerator, regenerator by reversal valve with
Another regenerator is connected, and another regenerator is connected with combustor, and pyrolysis chamber fills with cooling and purifying also by pipeline
Putting connected, cooling purifying device is connected with outer coal supply trachea, slag-drip opening respectively.
As preferably, described reversal valve is connected with air intlet and exhanst gas outlet the most respectively.
As preferably, the described air themperature in air intlet is 20 DEG C, in described exhanst gas outlet
Flue-gas temperature is less than 200 DEG C.
This utility model has the advantages that simple in construction, and reaction effect is good, it is possible to effectively convert brown
Coal, economic and environment-friendly, practical.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
In order to make the purpose of this utility model and advantage clearer, below in conjunction with embodiment to this practicality
Novel it is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain
This utility model, is not used to limit this utility model.
As it is shown in figure 1, this utility model embodiment provides a kind of Novel coal pyrolysis reactor, including burning
Room 1, pyrolysis chamber 2, coal bunker 3, valve 4, cooling purifying device 5, tank 6, regenerator 7, outer confession
Gas pipe 8, slag-drip opening 9 and reversal valve 10, combustor 1 is provided above Liang Ge pyrolysis chamber 2, pyrolysis chamber
2 tops are provided with coal bunker 3 by valve 4, are provided with tank 6, tank 6 and accumulation of heat bottom combustor 1
Room 7 is connected, and regenerator 7 is connected with another regenerator by reversal valve 10, another regenerator and combustor
1 be connected, pyrolysis chamber 2 is connected with cooling purifying device 5 also by pipeline, cooling purifying device 5 respectively with
Outer coal supply trachea 8, slag-drip opening 9 are connected.
It should be noted that described reversal valve 10 the most respectively with air intlet 11 and exhanst gas outlet 12 phase
Even.
Additionally, the air themperature in described air intlet 11 is 20 DEG C, in described exhanst gas outlet 12
Flue-gas temperature be less than 200 DEG C.
Brown coal are entered pyrolysis chamber from charge door by this detailed description of the invention.Pyrolysis chamber's temperature controls
Between 900-1000 DEG C, brown coal at high temperature disinfection, start simultaneously at decomposition.Pyrolysis gas is through supercooling
Purifying, a part is sent into combustor and is provided heat, and another part is as giving gas outward.Combustor uses accumulation of heat
Formula combustion technology, utilizes the high-temperature flue gas preheated air that burning produces.Tar and sewage can use extraction point
From, tar can make raw oil or as industrial chemicals.The residue that pyrolysis produces after terminating, can be by push rod
Pushing tank cooling, then sorting is used.
The above is only preferred implementation of the present utility model, it is noted that for the art
For those of ordinary skill, on the premise of without departing from this utility model principle, it is also possible to make some improvement
And retouching, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (3)
- null1. a Novel coal pyrolysis reactor，It is characterized in that，Including combustor (1)、Pyrolysis chamber (2)、Coal bunker (3)、Valve (4)、Cooling purifying device (5)、Tank (6)、Regenerator (7)、Outer coal supply trachea (8)、Slag-drip opening (9) and reversal valve (10)，Combustor (1) is provided above Liang Ge pyrolysis chamber (2)，Pyrolysis chamber (2) top is provided with coal bunker (3) by valve (4)，Combustor (1) bottom is provided with tank (6)，Tank (6) is connected with regenerator (7)，Regenerator (7) is connected with another regenerator by reversal valve (10)，Another regenerator is connected with combustor (1)，Pyrolysis chamber (2) is connected with cooling purifying device (5) also by pipeline，Cooling purifying device (5) respectively with outer coal supply trachea (8)、Slag-drip opening (9) is connected.
- A kind of Novel coal pyrolysis reactor the most according to claim 1, it is characterised in that described reversal valve (10) is connected with air intlet (11) and exhanst gas outlet (12) the most respectively.
- A kind of Novel coal pyrolysis reactor the most according to claim 2, it is characterised in that the described air themperature in air intlet (11) is 20 DEG C, and the described flue-gas temperature in exhanst gas outlet (12) is less than 200 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620106505.0U CN205501192U (en) | 2016-01-28 | 2016-01-28 | Novel coal pyrolysis reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620106505.0U CN205501192U (en) | 2016-01-28 | 2016-01-28 | Novel coal pyrolysis reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205501192U true CN205501192U (en) | 2016-08-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201620106505.0U Active CN205501192U (en) | 2016-01-28 | 2016-01-28 | Novel coal pyrolysis reactor |
Country Status (1)
| Country | Link |
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| CN (1) | CN205501192U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109097075A (en) * | 2018-08-24 | 2018-12-28 | 内蒙古大学 | A kind of pyrolysis of coal method of Utilization of Coal thermal decomposition product, heat |
| CN112797411A (en) * | 2020-12-16 | 2021-05-14 | 华润环保发展有限公司 | Energy-saving solid waste pyrolysis device and solid waste pyrolysis process method |
-
2016
- 2016-01-28 CN CN201620106505.0U patent/CN205501192U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109097075A (en) * | 2018-08-24 | 2018-12-28 | 内蒙古大学 | A kind of pyrolysis of coal method of Utilization of Coal thermal decomposition product, heat |
| CN112797411A (en) * | 2020-12-16 | 2021-05-14 | 华润环保发展有限公司 | Energy-saving solid waste pyrolysis device and solid waste pyrolysis process method |
| CN112797411B (en) * | 2020-12-16 | 2023-10-20 | 华润环保发展有限公司 | Energy-saving solid waste pyrolysis device and solid waste pyrolysis process method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |