CN109590312A - A kind of organic waste anoxybiotic cracking technology and its equipment - Google Patents
A kind of organic waste anoxybiotic cracking technology and its equipment Download PDFInfo
- Publication number
- CN109590312A CN109590312A CN201811575391.4A CN201811575391A CN109590312A CN 109590312 A CN109590312 A CN 109590312A CN 201811575391 A CN201811575391 A CN 201811575391A CN 109590312 A CN109590312 A CN 109590312A
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- Prior art keywords
- cracking
- anoxybiotic
- bed body
- organic waste
- waste
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- 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
-
- 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
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
-
- 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/02—Multi-step carbonising or coking processes
-
- 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
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/08—Non-mechanical pretreatment of the charge, e.g. desulfurization
- C10B57/10—Drying
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/002—Removal of contaminants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/02—Dust removal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/02—Dust removal
- C10K1/026—Dust removal by centrifugal forces
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
- C10K1/06—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials combined with spraying with water
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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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/78—Recycling of wood or furniture waste
Abstract
The invention discloses a kind of organic waste anoxybiotic cracking technology and its equipment, the method for this processing organic waste compares Other Waste processing mode, and effects of energy saving and emission reduction is good, belongs to typical Mode of Circular.Good to rubbish adaptability, domestic waste is not required to stringent screening, sorting, very strong to the adaptability of biological organism and house refuse, greatly reduces the generation of the harmful substances such as dioxin, pollutant is few.
Description
Technical field
The present invention relates to environment protection field, specially a kind of organic waste anoxybiotic cracking technology and its equipment.
Background technique
Contain a large amount of organic matter in the house refuse in city, such as: all living things stalk, bone class, food waste class, vegetables
Class, pericarp, fruit stone, waste plastics, scrap rubber, paper scrap, wooden, the careless class of tree branches and leaves, inorganic matter etc., containing a large amount of in this type organic
C, the elements such as H, O, N, if do not handled it, this kind of waste can cause the eutrophy of water body in nature natural decomposition
Change pollution.
Pyrolysis is a kind of traditional production technology, is widely used in adding for the fuel such as timber, coal, heavy oil, oil shale
Work processing, has there is very long history.The initial stage seventies, pyrolysis are applied to municipal solid waste, solid waste warp
Cross not only available fuel and chemical products convenient for storage and transport, and institute under the high temperature conditions after this pyrolysis processing
Obtained breeze can also constitute hard and crisp inert solid product with inorganic matters certain in material and heavy metal component, keep its subsequent
Landfill stabilization operation can be safer and advantageously carry out, with the development of modern industry, pyrolysis processing has become
A kind of one of promising solid organic waste substances processing method.It can handle municipal refuse, sludge, waste plastics, rubber of giving up
The organic solid waste with certain energy including the industry such as glue and agricultural waste, human and animal excreta etc..
Summary of the invention
The purpose of the present invention is to provide a kind of organic waste anoxybiotic cracking technologies, solve proposed in background technique
The problem of.
To achieve the above object, the invention provides the following technical scheme: a kind of organic waste anoxybiotic cracking technology, including
Following steps:
S1 is broken, and organic waste is broken into little particle by crusher；
S2 drying introduces hot wind using air-introduced machine and carries out heating, drying to organic waste；
The cracking of S3 anoxybiotic carries out anoxybiotic cracking to organic waste using cracking bed body；
S4 spiral dedusting, the gas generated in cracking process is dusted by spiral dust catcher；
S5 filtering, the gas generated in cracking process is absorbed and filtered；
S6 goes out anoxybiotic fuel, and the solid fuel cooling output that cracking is obtained is collected.
As a kind of preferred embodiment of the invention, the process of the S3 anoxybiotic cracking is divided into 4 stages, first stage
The first section after bed body charging is cracked for anoxybiotic, is warming up to 210 DEG C, organic waste mainly heats up in this stage and drains, the
Two-stage is that anoxybiotic cracks bed body interlude, is warming up to 280 DEG C, which is mainly organic matter gasification, generates a large amount of combustible gas
Body, organic waste start the cracking of preliminary surface anoxybiotic in this stage, and the phase III is the endpiece that anoxybiotic cracks bed body, heating
To 300 DEG C, this stage is that depth anoxybiotic cracks section, and fourth stage is to crack section with the complete anoxybiotic of cooling.
As a kind of preferred embodiment of the invention, organic waste is heated to 120 DEG C by S2 drying, and water content is low
In 1%.
As a kind of preferred embodiment of the invention, in S5 filtering, the gas that cracking process generates after water cooling again
Flow through oil scoop, gas temperature is down to 100-140 DEG C, can liquefied body gas isolate tar and two class of wood vinegar into
Row recycling can not become liquid fuel gas and be back to combustion heating in the heating bed body thorax of cracking bed body.
As a kind of preferred embodiment of the invention, it is filtered in the form of spray in S5 filtering.
As a kind of preferred embodiment of the invention, S6 goes out Fuel Process and is discharged and done at sealing using spiral discharging machine
Reason.
To realize above-mentioned organic waste anoxybiotic cracking technology, design has following cooperating equipment, and one kind is discarded organic
Object anoxybiotic cracking apparatus, including crusher, dryer, cracking bed body, waste fuel collection device, wherein crusher and dryer it
Between by feed screw connect, dryer be equipped with air-introduced machine and hot wind input channel, cracking bed body be horizontal tubular, crack
It is divided into the region of several segments different heating temperature inside bed body, cracking bed body connects waste fuel collection device, and waste fuel collects dress
It sets including waste fuel water cooling plant and closed mucking machine, waste fuel turnover box, cracks and be connected with spiral dust catcher in bed body, spiral is removed
Dirt device connects oil scoop, and oil scoop is divided into two outlets, and one of outlet is return air outlet, is connected to cracking bed
The heating bed body thorax of body, another outlet are that liquid collecting exports.
As a kind of preferred embodiment of the invention, fuel gas is equipped between oil scoop and heating bed body thorax and is hindered
Buddhist nun's purification device.
As a kind of preferred embodiment of the invention, the preferred water tower water circulating cooling of waste fuel water cooling plant.
Compared with prior art, beneficial effects of the present invention are as follows: the cracking of high temperature anoxybiotic is more more scientific than power generation by waste combustion, has
Effect, it may be said that be the ultimate New Method for Processing of rubbish harmless, tasteless, without remnants.Compared to Other Waste processing mode, energy-saving and emission-reduction
Effect is good, belongs to typical Mode of Circular.Good to rubbish adaptability, domestic waste is not required to stringent screening, sorting,
It is very strong to the adaptability of house refuse, the generation of the harmful substances such as dioxin is greatly reduced, pollutant is few, environmentally friendly high temperature anoxybiotic
It is high to crack built-in temperature, dioxin can be decomposed completely.After heavy metal high temperature anoxybiotic cracking in rubbish, with stable chemical combination
State form, which is formed, mixes crystalline solid, realizes stabilization.The heat utilization ratio that the cracking of rubbish anoxybiotic generates is up to 80% or more, waste fuel
Aggregate can be done, can be used as the raw material of production construction material, recycling degree is high, and flameholding, rubbish are burnt in anoxybiotic cracking bed body
Changing thorough, waste heat can recycle.The soil occupied because handling rubbish can be saved to the maximum extent.
Detailed description of the invention
Upon reading the detailed description of non-limiting embodiments with reference to the following drawings, other feature of the invention,
Objects and advantages will become more apparent upon:
Fig. 1 is a kind of overall structure figure of organic waste anoxybiotic cracking apparatus of the present invention；
Fig. 2 is a kind of waste fuel collection device enlarged diagram of organic waste anoxybiotic cracking apparatus of the present invention.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to
Specific embodiment, the present invention is further explained.
Embodiment 1, the present invention provide a kind of technical solution: a kind of organic waste anoxybiotic cracking technology, including following step
It is rapid:
S1 is broken, and organic waste is broken into little particle by crusher；
S2 drying introduces hot wind using air-introduced machine and carries out heating, drying to organic waste；
The cracking of S3 anoxybiotic carries out anoxybiotic cracking to organic waste using cracking bed body；
S4 spiral dedusting, the gas generated in cracking process is dusted by spiral dust catcher；
S5 filtering, the gas generated in cracking process is absorbed and filtered；
S6 goes out carbon, and the solid fuel cooling output that cracking is obtained is collected.
As a kind of preferred embodiment of the invention, the process of S3 anoxybiotic cracking is divided into 4 stages, and the first stage is exhausted
Oxygen cracks the first section after bed body charging, is warming up to 210 DEG C, organic waste mainly heats up in this stage and drains, second-order
Section is that anoxybiotic cracks bed body interlude, is warming up to 280 DEG C, which is mainly organic matter gasification, generates a large amount of fuel gas, is given up
It abandons organic matter and starts the cracking of preliminary surface anoxybiotic in this stage, the phase III is the endpiece that anoxybiotic cracks bed body, is warming up to 300
DEG C, this stage is that depth anoxybiotic cracks section, and fourth stage is to crack section with the complete anoxybiotic of cooling.
Organic waste is heated to 120 DEG C by S2 drying, and water content is lower than 1%.
In S5 filtering, the gas that cracking process generates passes through oil scoop after water cooling, and gas temperature is down to
100-140 DEG C, can the gas of liquefied body isolate tar and two class of wood vinegar is recycled, liquid fuel gas can not be become
It is back to combustion heating in the heating bed body thorax of cracking bed body.
Using being filtered in the form of spraying in S5 filtering, can fast cooling, while it is energy saving.
S6 goes out solid fuel process and is discharged using spiral discharging machine and done encapsulation process, prevents fuel ash from leaking and causes environment
Pollution.
Embodiment 2, with reference to Fig. 1 and Fig. 2, a kind of organic waste anoxybiotic cracking apparatus, it is characterised in that: including crusher
1, dryer 2, cracking bed body 3, waste fuel collection device 4, are wherein connected between crusher 1 and dryer 2 by feed screw 5
It connects, dryer 2 is equipped with air-introduced machine 6 and hot wind input channel 7, and cracking bed body 3 is horizontal tubular, cracks and is divided into inside bed body 3
The region of several segments different heating temperature, cracking bed body 3 connect waste fuel collection device 4, and waste fuel collection device 4 includes fuel
Pulp water device for cooling 41 and closed mucking machine 42, waste fuel turnover box 43 crack and are connected with spiral dust catcher 8, spiral dedusting in bed body 3
Device 8 connects oil scoop 9, and oil scoop 9 is divided to be exported for two, and one of outlet is return air outlet 10, is connected to and splits
The heating bed body thorax 31 of bed body 3 is solved, another outlet is liquid collecting outlet 11.
Oil scoop 9 and heating bed body thorax 31 between be equipped with fuel gas damp purification device 12, can prevent foreign matter into
Enter to heat bed body thorax 31, plays a protective role.
The preferred water tower water circulating cooling of waste fuel water cooling plant 41, can accomplish lasting effective recirculated water cooling.
Beneficial effects of the present invention are as follows: the cracking of high temperature anoxybiotic is more more scientific than power generation by waste combustion, effective, it may be said that is nothing
The ultimate New Method for Processing of rubbish harmful, tasteless, without remnants.Compared to Other Waste processing mode, effects of energy saving and emission reduction is good, belongs to allusion quotation
The Mode of Circular of type.Good to rubbish adaptability, domestic waste is not required to stringent screening, sorting, to house refuse and
The adaptability of biological straw is very strong, greatly reduces the generation of the harmful substances such as dioxin, and pollutant is few, and environmentally friendly high temperature anoxybiotic is split
It is high to solve built-in temperature, dioxin can be decomposed completely.After heavy metal high temperature anoxybiotic cracking in rubbish, with stable compound state
Form, which is formed, mixes crystalline solid, realizes stabilization.The heat utilization ratio that rubbish and the cracking of waste material anoxybiotic generate is fired up to 80% or more
Material residue can do aggregate, can be used as the raw material of production construction material, and recycling degree is high, and anoxybiotic cracks flameholding, rubbish in bed body
Rubbish incinerates thorough, waste heat and can recycle.The soil occupied because handling rubbish can be saved to the maximum extent.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention, for this field skill
For art personnel, it is clear that invention is not limited to the details of the above exemplary embodiments, and without departing substantially from spirit of the invention or
In the case where essential characteristic, the present invention can be realized in other specific forms.Therefore, in all respects, should all incite somebody to action
Embodiment regards exemplary as, and is non-limiting, the scope of the present invention by appended claims rather than on state
Bright restriction, it is intended that including all changes that fall within the meaning and scope of the equivalent elements of the claims in the present invention
It is interior.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (9)
1. a kind of organic waste anoxybiotic cracking technology, which comprises the following steps:
S1 is broken, and organic waste is broken into little particle by crusher；
S2 drying introduces hot wind using air-introduced machine and carries out heating, drying to organic waste；
The cracking of S3 anoxybiotic carries out anoxybiotic cracking to organic waste using cracking bed body；
S4 spiral dedusting, the gas generated in cracking process is dusted by spiral dust catcher；
S5 filtering, the gas generated in cracking process is absorbed and filtered；
S6 goes out anoxybiotic fuel, and the fuel cooling output that cracking is obtained is collected.
2. a kind of organic waste anoxybiotic cracking technology according to claim 1, it is characterised in that: the S3 anoxybiotic cracking
Process be divided into 4 stages, the first stage is that anoxybiotic cracks the first section after bed body charging, is warming up to 210 DEG C, organic waste exists
This stage mainly heats up and drains, and second stage is that anoxybiotic cracks bed body interlude, is warming up to 280 DEG C, which mainly has
The gasification of machine object, generates a large amount of fuel gas, and organic waste starts the cracking of preliminary surface anoxybiotic, phase III in this stage
The endpiece that bed body is cracked for anoxybiotic, is warming up to 300 DEG C, this stage is that depth anoxybiotic cracks section, and fourth stage is with cooling
Complete anoxybiotic cracks section.
3. a kind of organic waste anoxybiotic cracking technology according to claim 1, it is characterised in that: the S2 drying will give up
It abandons organic matter and is heated to 100 DEG C, and water content is lower than 1%.
4. a kind of organic waste anoxybiotic cracking technology according to claim 1, it is characterised in that: in the S5 filtering,
The gas that cracking process generates passes through oil scoop after water cooling, and gas temperature is down to 100-140 DEG C, can liquefied body
Gas isolate tar and two class of wood vinegar is recycled, the heating that liquid fuel gas is back to cracking bed body can not be become
Combustion heating in bed body thorax.
5. a kind of organic waste anoxybiotic cracking technology according to claim 4, it is characterised in that: adopted in the S5 filtering
It is filtered with the form of spray.
6. a kind of organic waste anoxybiotic cracking technology according to claim 1, it is characterised in that: the S6 goes out anoxybiotic combustion
Material process is discharged using spiral discharging machine and is done encapsulation process.
7. a kind of organic waste anoxybiotic cracking apparatus, it is characterised in that: including crusher (1), dryer (2), cracking bed body
(3), waste fuel collection device (4) are wherein connect between crusher (1) and dryer (2) by feed screw (5), described
Dryer (2) is equipped with air-introduced machine (6) and hot wind input channel (7), and the cracking bed body (3) is horizontal tubular, the cracking
It is divided into the region of several segments different heating temperature inside bed body (3), the cracking bed body (3) connects waste fuel collection device (4),
The waste fuel collection device (4) includes waste fuel water cooling plant (41) and closed waste fuel machine (42), waste fuel turnover box out
(43), it is connected with spiral dust catcher (8) on the cracking bed body (3), the spiral dust catcher (8) connects oil scoop (9), institute
It states oil scoop (9) and is divided into two outlets, one of outlet is return air outlet (10), is connected to the cracking bed body (3)
Heating bed body thorax (31), it is another outlet be liquid collecting export (11).
8. a kind of organic waste anoxybiotic cracking apparatus according to claim 1, it is characterised in that: the oil scoop
(9) fuel gas damping purification device (12) is equipped between heating bed body thorax (31).
9. a kind of organic waste anoxybiotic cracking apparatus according to claim 1, it is characterised in that: the waste fuel water cooling
Device (41) is water tower water circulating cooling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811575391.4A CN109590312A (en) | 2018-12-22 | 2018-12-22 | A kind of organic waste anoxybiotic cracking technology and its equipment |
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| CN201811575391.4A CN109590312A (en) | 2018-12-22 | 2018-12-22 | A kind of organic waste anoxybiotic cracking technology and its equipment |
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Cited By (4)
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| CN109575968A (en) * | 2018-12-27 | 2019-04-05 | 湖州南浔盛兴再生资源有限公司 | A kind of organic waste anoxybiotic cracking carbonization technique and its equipment |
| CN112625714A (en) * | 2020-12-22 | 2021-04-09 | 浙江圣沐新能源有限公司 | Environment-friendly production line for producing carbon by using organic wastes and production method thereof |
| CN112662409A (en) * | 2020-12-22 | 2021-04-16 | 浙江圣沐新能源有限公司 | Cracking conversion device for producing carbon and processing technology thereof |
| CN113121251A (en) * | 2019-12-30 | 2021-07-16 | 湖州南浔盛兴再生资源有限公司 | Process for manufacturing pavement bricks |
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Cited By (5)
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