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CN201284301Y - Dry distillation combined charing kiln - Google Patents

Dry distillation combined charing kiln Download PDF

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Publication number
CN201284301Y
CN201284301Y CNU2008201489354U CN200820148935U CN201284301Y CN 201284301 Y CN201284301 Y CN 201284301Y CN U2008201489354 U CNU2008201489354 U CN U2008201489354U CN 200820148935 U CN200820148935 U CN 200820148935U CN 201284301 Y CN201284301 Y CN 201284301Y
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China
Prior art keywords
jar
tank
charing
kiln
kiln body
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Expired - Fee Related
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CNU2008201489354U
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Chinese (zh)
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赵陆凯
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Individual
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Individual
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Priority to CNU2008201489354U priority Critical patent/CN201284301Y/en
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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Abstract

本实用新型公开了一种干馏式组合炭化窑,包括窑体和设置在该窑体上的燃烧器、燃烧室和炭化罐,所述的炭化罐包括内罐、外罐和罐盖,外罐固定设置在窑体内,内罐置入外罐中,内罐和外罐分体设置,罐盖将内罐和外罐一起封闭;炭化罐上设置有吊装位置;内罐侧壁设置排气口,窑体上设置排气管,排气管一端开口于外罐的管壁上,内罐上的排气口与排气管设置于外罐上的开口位置相对应;本实用新型提高了干馏法制炭的生产效率,适用于工业制炭领域。

Figure 200820148935

The utility model discloses a dry distillation combined carbonization kiln, which comprises a kiln body, a burner arranged on the kiln body, a combustion chamber and a carbonization tank. The carbonization tank includes an inner tank, an outer tank and a tank cover, and the outer tank Fixedly installed in the kiln body, the inner tank is placed in the outer tank, the inner tank and the outer tank are set separately, and the tank cover seals the inner tank and the outer tank together; the carbonization tank is provided with a hoisting position; the side wall of the inner tank is provided with an exhaust port , the kiln body is provided with an exhaust pipe, one end of the exhaust pipe is opened on the pipe wall of the outer tank, and the exhaust port on the inner tank corresponds to the opening position of the exhaust pipe on the outer tank; the utility model improves the dry distillation The production efficiency of legal charcoal is applicable to the field of industrial charcoal.

Figure 200820148935

Description

Dry distillation type combination carbonizing kiln
Technical field
The utility model relates to the energy device field, especially relates to a kind of dry distillation type combination carbonizing kiln.
Background technology
Produce the carbonized charcoal method at present: earth kiln, spontaneous combustion method, dry distillation.Though earth kiln can guarantee charcoal li amount, carbonization time is longer, and production efficiency is lower, generally takes 5~7 days, and it is bigger to produce flue gas during charing, does not meet environmental protection requirement.What manufacturer produced mostly all is to adopt spontaneous combustion method carbonizing kiln, and the spontaneous combustion method produces heat by fuel stick self and goes charing self, and essence is anoxycausis, and the dead angle is arranged when shortcoming is charing, and yield rate is low.Weak point, smokeless and dust free, simple to operate between the dry distillation charing, and quality product is guaranteed, carbonization degree is 100%, and carbide is not pulverized, the visual appearance height, and therefore, the dry distillation charring technology is the charring process of suitable popularization at present.But also there is certain deficiency in present dry distillation type carbonizing kiln, mainly is that cooling time of needing in the carbonization process is oversize, and production efficiency is low, and working strength of workers is big.
The utility model content
In view of this, the purpose of this utility model is to provide a kind of dry distillation type combination carbonizing kiln, improves the production efficiency of dry distillation charcoal processing.
For achieving the above object, the utility model by the following technical solutions:
Dry distillation type combination carbonizing kiln of the present utility model, comprise kiln body and the burner, combustion chamber and the charing jar that are arranged on this kiln body, described charing jar comprises interior jar, outer jar and cover, outer jar is fixedly installed in the kiln body, interior jar is inserted in outer jar, interior jar and outer jar of split setting, cover is with interior jar and the sealing together of outer jar; The charing jar is provided with the lifting position; Interior pot sidewall is provided with venting port, on the kiln body vapor pipe is set, and vapor pipe one end opening is on outer jar tube wall, and the venting port on the interior jar is corresponding with the aperture position that described vapor pipe is arranged on outer jar.
Further, described kiln body is provided with at least two cover burner, combustion chamber and charing jars.
Further, described kiln body is provided with six cover burner, combustion chamber and charing jars.
The beneficial effects of the utility model are: because the charing jar comprises interior jar and outer jar that split is provided with, interior jar can hang out outer jar, adopt this knockdown destructive distillation kiln stove, charing jar as coking chamber can make up more than two, the charing jar can adopt single or double form to carry out assembled arrangement, outside kiln, the firewood rod that processes is put into the charing jar during charing, closing loam cake lifts in the carbonizing kiln, the tank body that charing finishes hangs out body of heater and cools off outside kiln, new clothes charing jar hangs in the charing that circulates in the stove, has improved the production efficiency of charcoal processing so greatly.
Other advantages of the present utility model, target and feature will be set forth to a certain extent in the following description, and to a certain extent, based on being conspicuous to those skilled in the art, perhaps can from practice of the present utility model, obtain instruction to investigating hereinafter.Target of the present utility model and other advantages can be passed through following specification sheets, claims, and the specifically noted structure realizes and obtains in the accompanying drawing.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further described.
Fig. 1 is a carbonizing kiln front view synoptic diagram among the embodiment 1;
Fig. 2 is the synoptic diagram of the vertical view of Fig. 1.
Embodiment
Embodiment 1.
As depicted in figs. 1 and 2, the dry distillation type combination carbonizing kiln of present embodiment comprises kiln body 1 and the burner 3, combustion chamber 2, inflammable gas input tube 4, vapor pipe 9, fluidic device 10 and the charing jar that are arranged on this kiln body when implementing, certainly the dry distillation type carbonizing kiln also comprises other parts, also not shown among the figure, the technician can connect use according to the technical knowledge of the industry.Jar 5b, outer jar 5a and cover 6 in described charing jar comprises, an outer jar 5a is fixedly installed in the kiln body 1, and interior jar of 5b inserts among the outer jar 5a, and interior jar of 5b and outer jar of 5a split are provided with, and the charing jar is provided with hoisting ring 7.The sidewall of interior jar 5b is provided with venting port 8, vapor pipe 9 is set on the kiln body, vapor pipe 9 one end openings are on the tube wall of outer jar of 5a, the other end of vapor pipe 9 links to each other with inflammable gas input unit 4, venting port 8 on the interior jar 5b is corresponding with the aperture position that vapor pipe 9 is arranged on the outer jar 5a, and the inflammable gas that forms in the carbonization process can be guided to combustion chamber 2 internal combustion use like this.The kiln body is provided with six cover burner, combustion chamber and charing jars in the present embodiment, as shown in the figure, adopts two rows to be provided with, and every row is provided with three charing jars.Outside kiln, the firewood rod that processes is put into the jar 5b of charing jar during charing, close cover 6, then interior jar of 5b lifted into outer jar 5a, add the heat supply heat by biomass burner, make firewood rod dry distillation charring in the charing jar, not only carbonization time is short, and after charing finishes, interior jar of 5b hung out kiln to be cooled off outward, in the refrigerative process, can hang in the charing that circulates in the stove to the interior jar that installs the firewood rod, accelerate production schedule like this, day output improves greatly, and the combustible gas that produces in the charing is by vapor pipe 9, fluidic device 10 and inflammable gas input tube 4 draw to return and carry out recycle in the combustion chamber 2.
Embodiment 2.
Textural association was substantially the same manner as Example 1 when the dry distillation type combination carbonizing kiln of present embodiment was implemented, and different is that the charing jar is provided with 8, and every row is provided with 4, and day output can further improve with respect to the carbonizing kiln of embodiment 1.
Explanation is at last, above embodiment is only unrestricted in order to the explanation the technical solution of the utility model, other modifications that those of ordinary skills make the technical solution of the utility model or be equal to replacement, only otherwise break away from the spirit and scope of technical solutions of the utility model, all should be encompassed in the middle of the claim scope of the present utility model.

Claims (3)

1. dry distillation type makes up carbonizing kiln, comprise kiln body and the burner, combustion chamber and the charing jar that are arranged on this kiln body, it is characterized in that: described charing jar comprises interior jar, outer jar and cover, outer jar is fixedly installed in the kiln body, interior jar is inserted in outer jar, interior jar and outer jar of split setting, cover is with interior jar and the sealing together of outer jar; The charing jar is provided with the lifting position; Interior pot sidewall is provided with venting port, on the kiln body vapor pipe is set, and vapor pipe one end opening is on outer jar tube wall, and the venting port on the interior jar is corresponding with the aperture position that described vapor pipe is arranged on outer jar.
2. dry distillation type combination carbonizing kiln according to claim 1 is characterized in that: described kiln body is provided with at least two cover burner, combustion chamber and charing jars.
3. dry distillation type combination carbonizing kiln according to claim 2 is characterized in that: described kiln body is provided with six cover burner, combustion chamber and charing jars.
CNU2008201489354U 2008-09-02 2008-09-02 Dry distillation combined charing kiln Expired - Fee Related CN201284301Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201489354U CN201284301Y (en) 2008-09-02 2008-09-02 Dry distillation combined charing kiln

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201489354U CN201284301Y (en) 2008-09-02 2008-09-02 Dry distillation combined charing kiln

Publications (1)

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CN201284301Y true CN201284301Y (en) 2009-08-05

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103224801A (en) * 2013-04-10 2013-07-31 贝洪毅 Simple self-heat supply dry distillation apparatus
CN104100978A (en) * 2014-07-17 2014-10-15 河南省科学院能源研究所有限公司 Harmless treatment method for organic pollutants and assorted device of harmless treatment method
CN109923192A (en) * 2016-09-26 2019-06-21 莱奥·席尔恩霍费尔 Method and apparatus for producing biochar
CN113061444A (en) * 2021-03-24 2021-07-02 循天能源环境科技有限公司 Double-atmosphere carbonization device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103224801A (en) * 2013-04-10 2013-07-31 贝洪毅 Simple self-heat supply dry distillation apparatus
CN104100978A (en) * 2014-07-17 2014-10-15 河南省科学院能源研究所有限公司 Harmless treatment method for organic pollutants and assorted device of harmless treatment method
CN104100978B (en) * 2014-07-17 2017-02-15 河南省科学院能源研究所有限公司 Harmless treatment method for organic pollutants and assorted device of harmless treatment method
CN109923192A (en) * 2016-09-26 2019-06-21 莱奥·席尔恩霍费尔 Method and apparatus for producing biochar
US10934490B2 (en) 2016-09-26 2021-03-02 Leo SCHIRNHOFER Process for producing biocoal and plant therefor
CN113061444A (en) * 2021-03-24 2021-07-02 循天能源环境科技有限公司 Double-atmosphere carbonization device

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GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090805

Termination date: 20100902