CN106609142A - Intermittent inner container by pyrolysis carbonization kettle - Google Patents
Intermittent inner container by pyrolysis carbonization kettle Download PDFInfo
- Publication number
- CN106609142A CN106609142A CN201710038136.5A CN201710038136A CN106609142A CN 106609142 A CN106609142 A CN 106609142A CN 201710038136 A CN201710038136 A CN 201710038136A CN 106609142 A CN106609142 A CN 106609142A
- Authority
- CN
- China
- Prior art keywords
- kettle
- inner container
- inner bag
- kettle body
- outside
- 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.)
- Withdrawn
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B1/00—Retorts
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
Abstract
The invention discloses an intermittent inner container by pyrolysis carbonization kettle. The intermittent inner container by pyrolysis carbonization kettle comprises an outer kettle body (1), wherein one end of the outer kettle body (1) is connected with a heat channel pipe (4) and the other end of the outer kettle body (1) is connected with a smoke channel pipe (7); the outer kettle body (1) is placed on a base (5); a transmission mechanism is arranged outside the outer kettle body (1); a heat-insulating layer is arranged outside the outer kettle body (1); an inner container (2) is arranged in the outer kettle body (1); a reinforcing rib plate for inner diameter of the outer kettle body (1) is connected with the inner container (2); a gap is formed between the outer kettle body (1) and the inner container (2); an oil gas channel pipe (6) is arranged in the smoke channel pipe (7); one end of the oil gas channel pipe (6) is connected with the inner container (2); a feeding and discharging port (3) is formed in the upper part of the inner container (2) and penetrates through the outer kettle body (1); and a spiral mechanism is arranged on the inner diameter edge part of the inner container (2). The intermittent inner container by pyrolysis carbonization kettle has the advantages of high heating speed, high carbonization efficiency, high heat-insulating performance, short cooling intermittent time and the like.
Description
Technical field
The present invention relates to a kind of batch (-type) inner container type cracks carbonization kettle.
Background technology
Current problem of environmental pollution has become a difficult problem for countries in the world great attention, builds " Health China " increasingly
Become the common recognition and the objective of the struggle of China's most people.Biomass carry out hot tearing to biomass under conditions of anaerobism or anoxybiotic
Solution, can produce combustible gas, many hydrocarbon ils and biomass carbon, and biomass carbon has the features such as bearing carbon emission reduction, improved soil, and production is biological
The biomass material of matter charcoal has waste plastics, scrap rubber, greasy dirt, straw, rice husk, agriculture and forestry organic waste material etc..Biomass are produced at present
The carbonization kettle generally existing potential safety hazard of charcoal, carbonization are inefficient, cool down the shortcomings of intermittent time is long, and stability is poor, constrain
The development of charcoal industry.
The content of the invention
The technical problem to be solved in the present invention is：A kind of batch (-type) inner container type cracking carbonization kettle is provided, original splitting is overcome
The carbonization of solution carbonization kettle generally existing is inefficient, and poor thermal insulation property, cooling intermittent time are long, and safety stability difference etc. lacks
Point.
To solve above-mentioned technical problem, the present invention is adopted the technical scheme that：The batch (-type) inner container type cracks carbonization kettle bag
Outside kettle is included, outside kettle one end connects passage of heat pipe, and other end connection exhaust gases passes pipe, outside kettle are placed in pedestal tugboat
On, drive mechanism is provided with outside outside kettle, outside outside kettle, heat-insulation layer is provided with, and inner bag is provided with outside kettle, it is outside
Kettle is coaxially disposed with inner bag, and outside kettle internal diameter is connected with inner bag with gusset is strengthened, and is provided between outside kettle and inner bag
Gap, is provided with gas channel pipe in exhaust gases passes pipe, and gas channel pipe one end is connected with inner bag, exhaust gases passes pipe gas channel
Pipe is coaxially disposed, and passes outside kettle on inner bag top and is provided with charging discharging opening, is provided with screw mechanism in inner bag inner diameter edge portion.
Further, discharging opening is fed at least provided with one.
Using having the technical effect that for bringing after above-mentioned technical proposal：Heating is quick, and carbonization efficiency high, good heat insulating are cold
But the intermittent time is short, and being blown into cold wind in passage of heat spout part can make cracking carbonization kettle lower the temperature rapidly, be cracked charcoal next time
Metaplasia is produced, and the intermittent time is short, and stably well, whole process is cleaned very much for safety, meets GB/T32662-2016《The useless modeling of scrap rubber
Material cracked oiling complete production unit》Requirement, also with simple structure, easy to operate, cost-effective, energy-conserving and environment-protective etc. are excellent
Point.
Description of the drawings
Fig. 1 is the structural representation of the present invention；
1-outside kettle, 2-inner bag, 3-charging discharging opening, 4-passage of heat pipe,
5-pedestal, 6-gas channel pipe, 7-exhaust gases passes pipe.
Specific embodiment
Below in conjunction with the accompanying drawings the principle and feature of the present invention are described, example is served only for explaining the present invention, and
It is non-for limiting the scope of the present invention.
According to Fig. 1, the batch (-type) inner container type cracking carbonization kettle includes outside kettle 1,1 one end of outside kettle connection heat
Channel 4, other end connection exhaust gases passes pipe 7, outside kettle 1 is placed on pedestal tugboat 5, and transmission is provided with outside outside kettle 1
Mechanism, is provided with heat-insulation layer outside outside kettle 1, in outside kettle 1 is provided with inner bag 2, and outside kettle 1 is coaxially disposed with inner bag 2,
1 internal diameter of outside kettle is strengthened gusset and is connected with inner bag 2, is provided with gap, in exhaust gases passes between outside kettle 1 and inner bag 2
Gas channel pipe 6 is provided with pipe 7,6 one end of gas channel pipe is connected with inner bag 2, and 7 gas channel pipe 6 of exhaust gases passes pipe coaxially sets
Put, outside kettle 1 is passed on 2 top of inner bag and be provided with charging discharging opening 3, when charging discharging opening 3 rotates to 2 top of inner bag, use
In charging, when charging discharging opening 3 rotates to 2 bottom of inner bag, for discharging, screw mechanism is provided with 2 inner diameter edge portion of inner bag.
Preferably, charging discharging opening 3 is at least provided with one.
The operation principle and process of the present invention mainly includes：The kettle of rotating batch-type inner container type cracking carbonization kettle first makes
Charging discharging opening 3 upwards, according to the volume of inner bag 2, biomass cracking raw material is put into into inner bag 2 from charging discharging opening 3, is led to
A dead lift or machinery conveying are crossed, closing charging discharging opening 3 enters thermal vapor stream from passage of heat pipe 4, and thermal vapor stream enters outside kettle
Heating is circulated to the biomass in inner bag 2 in gap between body 1 and inner bag 2, is passed through between outside kettle 1 and inner bag 2
Reinforcement plate shape is welded to connect with gusset segmentation is strengthened indirectly into passage, prevents the expansion of outside kettle 1 and 2 material of inner bag not
Unanimously, thermal vapor stream does not adopt straight channel, it is ensured that the utilization rate of thermal vapor stream is maximized；Inner bag 2 is in cleaved carbide in hot vapour
Rapidly heat up in the presence of stream, transfer heat to processed material, processed material heats up under anaerobic state, reach the cracking carbonization temperature of processed material
Start to crack carbonization when spending, cracking carbonization stops heating immediately after finishing, removes thermal vapor stream supply arrangement, air-cooler is placed in
At thermal vapor stream supply arrangement, by from the import of passage of heat pipe 4 to air blast in the passage of heat, while to prevent inner bag 2 from forming larger
Negative pressure and inner bag 2 receive cold deformation, inject certain nitrogen to inner bag 2, accelerate the fast quickly cooling of outside kettle 1, inner bag 2 and carbide
But, carbide temperature drop to less than 80 degree is made, charging discharging opening 3 is opened, is shed the carbide in inner bag 2, once crack charcoal
Change process terminates.After heating utilization, the flue tail gas discharged from exhaust gases passes pipe 7 enter cleaning system to thermal vapor stream, do not coagulate
Combustible gas returns kettle and carries out second burning, exports oil gas from gas channel pipe 6, after the completion of heating, rotating batch-type cracking carbonization
The kettle of kettle makes charging discharging opening 3 downwards, discharges the charcoal material that cracking carbonization kettle is generated, and in passage of heat pipe, 4 mouthfuls pass through continuously to blow
To inner bag 2, temperature that can be rapidly by outside kettle 1 with inner bag 2 is reduced cold wind, then carries out the life of next kettle again with gap
Produce, can so move in circles has been used up above-mentioned production procedure and produced incessantly.
The basic principles, principal features and advantages of the present invention have been shown and described above.The technical staff of the industry should
Understand, the present invention is not restricted to the described embodiments, the simply explanation present invention's of the description in above-described embodiment and description
Principle, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, and these change and change
Enter to both fall within scope of the claimed invention.
Claims (2)
1. a kind of batch (-type) inner container type cracks carbonization kettle, including outside kettle（1）, it is characterised in that outside kettle（1）One end connects
Connect passage of heat pipe（4）, other end connection exhaust gases passes pipe（7）, outside kettle（1）It is placed in pedestal（5）On, outside kettle（1）Outward
Portion is provided with drive mechanism, outside kettle（1）Outside is provided with heat-insulation layer, in outside kettle（1）Inner bag is provided with inside（2）, outside kettle
（1）With inner bag（2）It is coaxially disposed, outside kettle（1）Internal diameter reinforcement gusset and inner bag（2）Connection, in outside kettle（1）With it is interior
Gallbladder（2）Between be provided with gap, in exhaust gases passes pipe（7）Gas channel pipe is provided with inside（6）, gas channel pipe（6）One end and inner bag
（2）Connection, exhaust gases passes pipe（7）Gas channel pipe（6）It is coaxially disposed, in inner bag（2）Top passes outside kettle（1）Be provided with into
Material discharging opening（3）, in inner bag（2）Inner diameter edge portion is provided with screw mechanism.
2. batch (-type) inner container type according to claim 1 cracks carbonization kettle, it is characterised in that described charging discharging opening
（3）At least provided with one.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710038136.5A CN106609142A (en) | 2017-01-19 | 2017-01-19 | Intermittent inner container by pyrolysis carbonization kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710038136.5A CN106609142A (en) | 2017-01-19 | 2017-01-19 | Intermittent inner container by pyrolysis carbonization kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106609142A true CN106609142A (en) | 2017-05-03 |
Family
ID=58636362
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710038136.5A Withdrawn CN106609142A (en) | 2017-01-19 | 2017-01-19 | Intermittent inner container by pyrolysis carbonization kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106609142A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108913174A (en) * | 2018-09-21 | 2018-11-30 | 商丘瑞新通用设备制造股份有限公司 | The cracker and cracking apparatus of wall are glued in a kind of prevention and treatment coking |
| CN114196426A (en) * | 2021-11-22 | 2022-03-18 | 殷梅芳 | Flue gas heating pipeline in dry distillation kiln |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1872953A (en) * | 2006-06-27 | 2006-12-06 | 姚军辉 | Technique for cracking integral scrap tires |
| CN2931478Y (en) * | 2006-06-27 | 2007-08-08 | 姚军辉 | Cracking kettle for integral waste tyre |
| CN102154019A (en) * | 2011-03-22 | 2011-08-17 | 苏州辰昌新能源技术有限公司 | Spiral push type low temperature pyrolysis carbonation furnace |
| CN105950193A (en) * | 2016-05-13 | 2016-09-21 | 农业部规划设计研究院 | Dual-power rotary poly-generation system for continuous biomass dry distillation |
-
2017
- 2017-01-19 CN CN201710038136.5A patent/CN106609142A/en not_active Withdrawn
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1872953A (en) * | 2006-06-27 | 2006-12-06 | 姚军辉 | Technique for cracking integral scrap tires |
| CN2931478Y (en) * | 2006-06-27 | 2007-08-08 | 姚军辉 | Cracking kettle for integral waste tyre |
| CN102154019A (en) * | 2011-03-22 | 2011-08-17 | 苏州辰昌新能源技术有限公司 | Spiral push type low temperature pyrolysis carbonation furnace |
| CN105950193A (en) * | 2016-05-13 | 2016-09-21 | 农业部规划设计研究院 | Dual-power rotary poly-generation system for continuous biomass dry distillation |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108913174A (en) * | 2018-09-21 | 2018-11-30 | 商丘瑞新通用设备制造股份有限公司 | The cracker and cracking apparatus of wall are glued in a kind of prevention and treatment coking |
| CN114196426A (en) * | 2021-11-22 | 2022-03-18 | 殷梅芳 | Flue gas heating pipeline in dry distillation kiln |
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|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20170503 |