CN205188207U - Continuous system charcoal device - Google Patents
Continuous system charcoal device Download PDFInfo
- Publication number
- CN205188207U CN205188207U CN201520843878.1U CN201520843878U CN205188207U CN 205188207 U CN205188207 U CN 205188207U CN 201520843878 U CN201520843878 U CN 201520843878U CN 205188207 U CN205188207 U CN 205188207U
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- CN
- China
- Prior art keywords
- furnace
- pipeline
- burner
- carbide furnace
- rotary carbide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Abstract
The utility model discloses a continuous system charcoal device, including rotatory retort (1), gasifier (2), draught fan (6), pipeline (7) and combustor (9), rotatory retort (1) is connected with combustor (9) through pipeline (7), gasifier (2) are connected with combustor (9) through pipeline (7), draught fan (6) set up in the pipeline, can take out and carry to burner and provide the heat for the retort rotating combustible gas that retort and gasifier produced, be close to rotatory retort (1) in the pipeline and locate still to be equipped with valve (8), close when initial, open behind the production combustible gas in rotatory retort (1) for the combustible gas is taken out and is carried to combustor (9) and light the continue to heat furnace body in the stove. The utility model discloses system charcoal device can go out the charcoal in succession, can the accurate control time, the temperature, and product quality and output can both be protected, and the product charcoal volume of unit interval is that more than 20 times of charcoal are made to the tradition.
Description
Technical field
The utility model relates to charcoal processing art, particularly relates to a kind of carbonizing device continuously.
Background technology
Organism (as timber, bamboo wood) is mainly made up of Mierocrystalline cellulose, hemicellulose and xylogen, there is many premium propertiess such as intensity is high, good toughness, hard, the fine and closely woven porous of the carbonization product quality being raw material production with it, specific surface area is large, adsorptive power is strong, not only can be used for the side such as fuel, purifying air deodorizing, environmental protection water purification, soil improvement, environment damping and, and can be used for radioprotective and the high-technology field such as electromagnetic shielding material, flame-proof composite material, fruit thin Perserving materials, health care material and industrial semiconductor material.
Tradition charcoal processing technique is nearly all adopt native formula kiln, and different operations is responsible for by each kiln, and raw material is shifted by the mode of a dead lift by centre, and charring furnace mostly is fixed, raw material is heated uneven, and carbonization degree is low, and its seed output and quality is all difficult to be protected.Traditional charcoal processing technique all adopts special fuel to provide thermal source in addition, and energy-output ratio is large, and the dust content of eliminating is large, does not meet the requirements of the times of current energy-conserving and environment-protective.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, and proposing one can charcoal processing continuously, and the carbonizing device of energy-conserving and environment-protective and carbonizing method.
For solving above technical problem, the technical scheme that the utility model adopts is: a kind of carbonizing device continuously, comprises rotary carbide furnace, vapourizing furnace, induced draft fan, pipeline and burner;
Described rotary carbide furnace is connected with burner by pipeline;
Described vapourizing furnace is connected with burner by pipeline, for providing combustible gas to burner preheating body of heater during device initialization;
Described induced draft fan is arranged in the duct, and the combustible gas that rotary carbide furnace and vapourizing furnace produce can be extracted out and be delivered to burner combustion for charring furnace provides heat;
Also be provided with valve near rotary carbide furnace place in described pipeline, close time initial, open after producing combustible gas in rotary carbide furnace, combustible gas in stove is extracted out and is delivered to burner to light continuation heating furnace body.
Further, described rotary carbide furnace comprises opening for feed and body of heater, and described opening for feed is arranged at body of heater one end, is rotated progressively pushed ahead by material by body of heater; Described body of heater is rotationally connected by rolling ring and pedestal, and described body of heater is provided with gear ring, by driven by motor ring gear against rotation.
Further, described rotary carbide furnace also comprises discharge port refrigerating unit.
Further, described induced draft fan is adjustable speed blower fan.
Further, also include spray column, for removing the dust of vapourizing furnace and rotary carbide furnace generation.
Further, cooling tower and oily-water seperating equipment is also provided with after described spray column.
In addition, the utility model additionally provides a kind of carbonizing method continuously, comprises the following steps:
Step one, lights the gas making point match in vapourizing furnace, produces combustible fumes;
Step 2, opens induced draft fan, and the combustible fumes produced in vapourizing furnace is caused burner;
Step 3, opens rotary carbide furnace, and small part raw material is put into rotary carbide furnace;
Step 4, when rotary carbide furnace temperature reaches 500 DEG C, starts a large amount of charging feedstock;
Step 5, opens the valve near rotary carbide furnace place, after the combustible fumes produced is caused burner stable burning, closes vapourizing furnace in rotary carbide furnace;
Step 6, when rotary carbide furnace temperature raises further and reaches design temperature, by regulating induced draft fan rotating speed size to control the gas quantity entered in burner, makes to keep this temperature in stove;
Step 7, the discharge port refrigerating unit opening rotary carbide furnace cools powdered carbon and collects.
Further, the water content of described vapourizing furnace gas making point match is lower than 10%, and the raw material adding rotary carbide furnace is fragmental, and its water content is lower than 20%.
Further, also comprise in described step 2 and step 5 and combustible fumes is sprayed, remove dust.
Further, also comprise the combustible fumes after to spray and carry out condensation and oily water separation.
The beneficial effect that the technical scheme that the utility model adopts has is:
(1) the utility model carbonizing device automatically can go out charcoal continuously, can accurately period, temperature, and quality product and output can be protected, and the carbon yield of unit time is more than 20 times of traditional charcoal processing.
(2) the utility model adopts rotary carbide furnace, and raw material is contained in High Temperature Furnaces Heating Apparatus, interlayer external high temperature dry vacuum distillation, and carbon yield is high, is heated evenly, carbonization degree 100%.
(3) the utility model gas fuel burning of utilizing raw material self to produce is to provide thermal source, air input size is directly controlled by induced draft fan, thus carbonization temperature can be controlled arbitrarily, guarantee powdered carbon stay in grade, and flue gas is through spray and cooling separation afterfire, discharges environmental protection more.
(4) the utility model charcoal processing raw material is the bamboo wood chip that particle after fragmentation or purchase come, and the specific surface area that such starting material are heated increases greatly, thus greatly shortens carbonization time, improves output, and charing evenly, and carbonization degree improves greatly.
(5) the utility model charring furnace discharge port is provided with refrigerating unit, and powdered carbon can directly pack.
Accompanying drawing explanation
Fig. 1 is the composition structural representation of a kind of continuous carbonizing device of the utility model;
Fig. 2 is the schematic flow sheet of the utility model carbonizing method.
In figure: 1-rotary carbide furnace; 2-vapourizing furnace; 3-spray column; 4-cooling tower; 5-oily-water seperating equipment; 6-induced draft fan; 7-pipeline; 8-valve; 9-burner; 11-body of heater; 12-opening for feed; 13-gear ring; 14-rolling ring; 15-motor; 16-pedestal; 17-discharge port refrigerating unit.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is further described.
As shown in Figure 1, a kind of carbonizing device continuously, comprises rotary carbide furnace 1, vapourizing furnace 2, induced draft fan 6, pipeline 7, burner 9, spray column 3, cooling tower 4 and oily-water seperating equipment 5.
Described rotary carbide furnace 1 is connected with burner 9 by pipeline 7;
Described vapourizing furnace 2 is connected with burner 9 by pipeline 7, for providing combustible gas to burner 9 preheating body of heater 11 during device initialization;
Described induced draft fan 6 is adjustable speed blower fan, arranges in the duct, the combustible gas that rotary carbide furnace 1 and vapourizing furnace 2 produce can be extracted out and be delivered to burner 9 and burn for charring furnace provides heat;
Also be provided with valve 8 near rotary carbide furnace 1 place in described pipeline, close time initial, open after producing combustible gas in rotary carbide furnace 1, combustible gas in stove is extracted out and is delivered to burner 9 to light continuation heating furnace body 11.
Described rotary carbide furnace 1 comprises opening for feed 12 and body of heater 11, and described opening for feed is arranged at body of heater 11 one end, is rotated progressively pushed ahead by material by body of heater 11; Described body of heater 11 is rotationally connected by rolling ring 14 and pedestal 16, and described body of heater 11 is provided with gear ring 13, drives ring gear against rotation by motor 15.
Described rotary carbide furnace 1 also comprises discharge port refrigerating unit 17.
Before the combustible fumes produced by vapourizing furnace 2 and rotary carbide furnace 1 enters burner 9, respectively through spray column 3, cooling tower 4 and oily-water seperating equipment 5, the impurity such as the dust in removing flue gas and tar.
Accordingly, as shown in Figure 2, the present embodiment also in additionally provide a kind of carbonizing method continuously, comprise the following steps:
Step one, lights the gas making point match in vapourizing furnace, produces combustible fumes;
Step 2, opens induced draft fan, and the combustible fumes produced in vapourizing furnace is caused burner;
Step 3, opens rotary carbide furnace, and small part raw material is put into rotary carbide furnace;
Step 4, when rotary carbide furnace temperature reaches 500 DEG C, starts a large amount of charging feedstock;
Step 5, opens the valve near rotary carbide furnace place, after the combustible fumes produced is caused burner stable burning, closes vapourizing furnace in rotary carbide furnace;
Step 6, when rotary carbide furnace temperature raises further and reaches 550 DEG C, by regulating induced draft fan rotating speed size to control the gas quantity entered in burner, makes to keep this temperature in stove;
Step 7, the discharge port refrigerating unit opening rotary carbide furnace cools powdered carbon and collects.
Wherein, the water content of described vapourizing furnace gas making point match is lower than 10%, and the raw material adding rotary carbide furnace is fragmental, and its water content is lower than 20%.
Also comprise in described step 2 and step 5 and combustible fumes is sprayed, remove dust, meanwhile, also comprise the combustible fumes after to spray and carry out condensation and oily water separation, extract and the moisture isolated in combustible fumes and tar.
The utility model specific embodiment is in sum only the utility model preferred embodiment, is not intended to limit the restriction of the utility model protection domain.Therefore, any do within technical characteristic of the present utility model change, modification, substitute, combination or simplify, all should be equivalence substitute mode, be included within protection domain of the present utility model.
Claims (6)
1. a continuous carbonizing device, is characterized in that, comprises rotary carbide furnace (1), vapourizing furnace (2), induced draft fan (6), pipeline (7) and burner (9);
Described rotary carbide furnace (1) is connected with burner (9) by pipeline (7);
Described vapourizing furnace (2) is connected with burner (9) by pipeline (7), for providing combustible gas to burner preheating body of heater during device initialization;
Described induced draft fan (6) is arranged in the duct, and the combustible gas that rotary carbide furnace and vapourizing furnace produce can be extracted out and be delivered to burner combustion for charring furnace provides heat;
Valve (8) is also provided with near rotary carbide furnace (1) place in described pipeline, close time initial, open after producing combustible gas in rotary carbide furnace (1), combustible gas in stove is extracted out and is delivered to burner (9) to light continuation heating furnace body.
2. the continuous carbonizing device of one according to claim 1, it is characterized in that, described rotary carbide furnace (1) comprises opening for feed (12) and body of heater (11), described opening for feed (12) is arranged at body of heater (11) one end, is rotated progressively pushed ahead by material by body of heater (11); Described body of heater (11) is rotationally connected by rolling ring (14) and pedestal (16), described body of heater (11) is provided with gear ring (13), drives gear ring (13) to rotate by motor (15).
3. the continuous carbonizing device of one according to claim 2, is characterized in that, described rotary carbide furnace (1) also comprises discharge port refrigerating unit (17).
4. the continuous carbonizing device of one according to claim 1, is characterized in that, described induced draft fan (6) is adjustable speed blower fan.
5. according to the continuous carbonizing device of the one in claim 1-4 described in any one, it is characterized in that, also include spray column (3), for removing the dust that vapourizing furnace (2) and rotary carbide furnace (1) produce.
6. the continuous carbonizing device of one according to claim 5, is characterized in that, is also provided with cooling tower (4) and oily-water seperating equipment (5) after described spray column (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520843878.1U CN205188207U (en) | 2015-10-28 | 2015-10-28 | Continuous system charcoal device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520843878.1U CN205188207U (en) | 2015-10-28 | 2015-10-28 | Continuous system charcoal device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205188207U true CN205188207U (en) | 2016-04-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520843878.1U Expired - Fee Related CN205188207U (en) | 2015-10-28 | 2015-10-28 | Continuous system charcoal device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205188207U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105176550A (en) * | 2015-10-28 | 2015-12-23 | 湖南炭道新能源科技有限公司 | Continuous carbonizing device and method |
-
2015
- 2015-10-28 CN CN201520843878.1U patent/CN205188207U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105176550A (en) * | 2015-10-28 | 2015-12-23 | 湖南炭道新能源科技有限公司 | Continuous carbonizing device and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160926 Address after: 413414 Yiyang City, Hunan province Heshan District Xin Shi Du Zhen Xinhua community Patentee after: YIMING YONGMING NEW ENERGY TECHNOLOGY CO., LTD. Address before: Tongzi high tech Development Zone in Hunan province Changsha Po Road 410000 No. 408 Lugu Lin language community building E21 Room 608 Patentee before: HUNAN TANDAO NEW ENERGY SCIENCE & TECHNOLOGY CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160427 Termination date: 20161028 |
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| CF01 | Termination of patent right due to non-payment of annual fee |