CN105778955A - Dynamic continuous organic solid waste gas-carbon oil cogeneration device - Google Patents
Dynamic continuous organic solid waste gas-carbon oil cogeneration device Download PDFInfo
- Publication number
- CN105778955A CN105778955A CN201610332144.6A CN201610332144A CN105778955A CN 105778955 A CN105778955 A CN 105778955A CN 201610332144 A CN201610332144 A CN 201610332144A CN 105778955 A CN105778955 A CN 105778955A
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- CN
- China
- Prior art keywords
- bed board
- board panel
- solid waste
- organic solid
- pyrolysis
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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
- C10B53/07—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
- 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
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a dynamic continuous organic solid waste gas-carbon oil cogeneration device. The device comprises a sealed reaction main body structure as well as a first bed board panel and a second bed board panel which are distributed in the cavity of the reaction main body structure, the device body is provided with a continuous feeding mechanism used for conveying to-be-treated materials to the first bed board panel to be subjected to pyrolysis treatment, a scraper chain mechanism is arranged inside the reaction main body structure, and an oil gas outlet used for conveying oil gas generated through pyrolysis reaction to a condenser to be condensed into fuel oil and a solid residue outlet used for discharging waste residue produced through pyrolysis out the device body are formed in the reaction main body structure. The device disclosed by the invention is provided with an upper pyrolysis bed board and a lower pyrolysis bed board, and organic solid waste incompletely cracked on a first layer is transferred on to the lower pyrolysis bed board by virtue of a movable scraper chain to be continuously pyrolyzed until pyrolysis is fully completed, so that pyrolysis efficiency is improved, effective length of equipment is shortened, and floor area of the equipment is reduced.
Description
Technical field
The present invention relates to a kind of dynamic serialization organic solid waste coproduction gas carbon oil device being applicable to produce fuel oil.
Background technology
Environment is created two direct harm by organic solid waste after throwing aside: landscape pollution, ecosystem endanger.Organic solid waste cracked oiling technology is a kind of method of " white pollution " in thoroughly elimination environment.The method can make macromolecular chain in organic solid waste crack under heat energy effect, it is thus achieved that relatively small compound molecular weight also finally obtains and the close vapour of oil component, diesel oil or paraffin goods.It is possible not only to solve the pollution problem of organic solid waste, it is also possible to the problem substantially alleviating energy scarcity, reaches the purpose of resource circulation utilization.
In recent years having the organic solid waste liquefying apparatus of various different structure to occur both at home and abroad, but no matter adopt any cleavage method, all ubiquity is long for reaction time, not exclusively, equipment carbon distribution is serious, it is impossible to produce continuously all the year round in reaction, discharge solid residue to be difficult to process, cause the phenomenon of secondary pollution.
Summary of the invention
The purpose of the present invention is contemplated to solve the problems referred to above, it is provided that a kind of dynamically serialization organic solid waste coproduction gas carbon oil device.
nullFor solving above-mentioned technical problem，Embodiments of the present invention provide a kind of dynamically serialization organic solid waste coproduction gas carbon oil device，It includes device body，This device body has Packed reactive agent structure and is distributed in reactive agent structural cavity body and pending thing can carry out the first bed board panel of pyrolysis processing、Second bed board panel，Second bed board panel is arranged at the first bed board lower panels，Device body is provided with and pending thing is delivered to the first bed board panel carries out the continuous feed mechanism of pyrolysis processing，Reactive agent inside configuration is provided with the pending thing that can be pointed to the first bed board panel upper surface and carries out scraping the flight chain mechanism processing and being pushed to by pending thing complete for non-pyrolysis the second bed board panel，Reactive agent structure is provided with the oil gas vent that oil-gas transportation to the condenser that pyrolytic reaction generates is condensed into fuel oil and the solid residue outlet by the waste residue discharger body of pyrolysis generation.
Compared with prior art, embodiment provided by the invention can realize industrial continuous production, and flight chain mechanism can realize the automatic coke cleaning of reactor body structure, and reactor body structure arranges flue gas heat-insulation layer, effectively prevent high-temperature oil gas from condensing at reactor wall, and two-layer flue gas body structure is not changing increase heat exchange area on the basis of reactor volume, increase single machine yield, by access path reserved in device end, maintenance management for the later stage is more convenient, further, whole device can realize self-skimming.
Further, first, second bed board panel is airtight hot-air channel structure, and first, second bed board panel is respectively arranged with respective hot blast and imports and exports, and double-decker can also increase single machine yield while increasing heat exchange area.
Further, the hot-blast outlet of the first bed board panel and/or the second bed board panel is connected to the heat preservation sandwich layer of reactive agent structure, this heat preservation sandwich layer is provided with hot-blast outlet, it is of great advantage for keeping the temperature of reactive agent structure, and for hot blast heat again with, improve heating efficiency.
Further, heat preservation sandwich layer is provided with and makes flue gas that reactive agent structure is carried out the smoke deflector of uniform heating and thermal insulation so that heat preservation sandwich layer can be heated and keep the temperature of reactive agent structure by flue gas uniformly.
Further, flight chain mechanism includes the mobile bed board link chain mechanism around the first bed board panel layout, is installed on the scraper plate of mobile bed board link chain mechanism, drives mobile bed board link chain mechanism to carry out the driving device moved, the scraper plate that mobile bed board link chain mechanism is installed is resisted against the upper surface of the first bed board panel when moving to the first bed board panel upper surface, is resisted against the second bed board panel upper surface when the scraper plate that mobile bed board link chain mechanism is installed moves to the second bed board panel upper surface.
Further, the mobile bed board link chain mechanism of flight chain mechanism is provided with strainer, it is possible to carry out elasticity adjustment as required.
Further, reactive agent structure is removably provided with the black box being positioned at the left and right end of device body, its maintenance being easy to the later stage and installation exercise.
Further, scraper plate is rectangular toothed structure, and material has certain disturbance in the process being pushed into, and is that material can evenly be heated.
Further, the bottom of device body is provided with reactor underframe, and it both can as reactor bottom supporting construction, it is also possible to carry out integral hoisting.
The pyrolysis treatment device of the present invention may be used to junked tire, waste or used plastics, waste and old resin, municipal domestic organic refuse, industrial organic waste, the pyrolysis processing technique of the organic solid castoff such as mud and medical waste.
Accompanying drawing explanation
Fig. 1 is dynamic serialization organic solid waste coproduction gas carbon oil device front view in first embodiment of the invention；
Fig. 2 is dynamic serialization organic solid waste coproduction gas carbon oil device top view in first embodiment of the invention；
Fig. 3 is dynamic serialization organic solid waste coproduction gas carbon oil device side view in first embodiment of the invention.
Fig. 4 is driven shaft strainer fragmentary detail view.
Description of reference numerals: 1, reactor underframe；2, left end black box；3, motor drive train；4, main reactor casing；5, bed board link chain mechanism is moved；6, upper flue gas casing；7, charging cloth device；8, driven shaft strainer；9, right-hand member black box；10, slave drive device；11, lower flue gas casing；12, active actuating device.
Detailed description of the invention
For the technological means making the present invention realize, creation characteristic, reach purpose and effect and be easy to understand, below in conjunction with specific embodiment, the present invention is expanded on further.
nullFirst embodiment of the present invention provides a kind of dynamically serialization organic solid waste coproduction gas carbon oil device，Shown in Fig. 1-3，It includes device body，This device body has reactive agent structure that is Packed and that be made up of main reactor casing 4、It is distributed in reactive agent structural cavity body and pending thing can be carried out the first bed board panel of pyrolysis processing、Second bed board panel，Pending thing herein is melted fluid organic solid waste object，First、Second bed board panel is airtight hot-air channel structure，And first、Second bed board panel is respectively arranged with respective hot blast and imports and exports，Such as，First bed board panel adopts upper flue gas casing 6 as shown in Figure 1，On this, flue gas cabinet arrangement has gas approach B and exhanst gas outlet D，And the second bed board panel adopts lower flue gas casing 11 as depicted，This lower flue gas casing is provided with gas approach C，Lower flue gas casing is arranged at flue gas lower box，And the length of lower flue gas casing is slightly larger than upper flue gas casing，It is easy to can directly drop at the upper surface of lower flue gas casing after the object of upper flue gas tank surface drops，Device body is provided with and pending thing is delivered to the first bed board panel carries out the continuous feed mechanism of pyrolysis processing，Reactive agent inside configuration is provided with the pending thing that can be pointed to flue gas casing upper surface and carries out scraping the flight chain mechanism processing and being pushed to by pending thing complete for non-pyrolysis the second bed board panel，This flight chain mechanism propelling movement direction in the drawings is: pushed from upper flue gas casing upper surface right-to-left by pending thing，After pending thing falls to lower flue gas casing，Pending thing is pushed from left to right from lower flue gas casing upper surface，Reactive agent structure is provided with the oil gas vent G that oil-gas transportation to the condenser that pyrolytic reaction generates is condensed into fuel oil and by the solid residue outlet H of the waste residue discharger body of pyrolysis generation，This solid residue outlet H is generally distributed in the underface of lower flue gas casing right-hand member.
From the discussion above it is seen that, embodiment provided by the invention can realize industrial continuous production, and flight chain structure can realize the automatic coke cleaning of reactor body structure, and reactor body structure arranges flue gas heat-insulation layer, effectively prevent high-temperature oil gas from condensing at reactor wall, and two-layer flue gas body structure is not changing increase heat exchange area on the basis of reactor volume, increase single machine yield, by access path reserved in device end, maintenance management for the later stage is more convenient, and, whole device can realize self-skimming, adopt fixed reaction bed, except driving shaft, all the other sealings are static sealing, sealing effectiveness is good；Entering reactor content is molten state organic solid waste, not only reduces the thermic load of reactor, and molten state organic solid waste can play sealing function, prevents hydrocarbon gas in reactor from overflowing from import.
It is worth mentioning that, the hot-blast outlet of upper flue gas casing and/or lower flue gas casing is connected to the heat preservation sandwich layer of reactive agent structure, this heat preservation sandwich layer is provided with hot-blast outlet, it is of great advantage for keeping the temperature of reactive agent structure, and for hot blast heat again with, improve heating efficiency, for this enforcement, select the exhanst gas outlet C of lower flue gas casing is accessed flue gas heat-insulation layer import E set by main reactor cabinet insulation interlayer, make flue gas form thermodynamic barrier in the interlayer of main reactor casing and keep the temperature of main reactor, finally, exhanst gas outlet F set by flue gas autonomic response device cabinet insulation interlayer drains.
Additionally, flight chain mechanism includes surrounding the mobile bed board link chain mechanism that the first bed board panel is arranged, it is installed on the scraper plate of mobile bed board link chain mechanism, mobile bed board link chain mechanism is driven to carry out the driving device moved, this driving device is motor drive train 3, and this motor drive train drives actively actuating device 12, it is further driven to mobile bed board link chain mechanism, and mobile bed board link chain mechanism is strained by slave drive device 10 by the elasticity moving bed board link chain mechanism by driven shaft strainer 8, the scraper plate that mobile bed board link chain mechanism is installed is resisted against the upper surface of the first bed board panel when moving to the first bed board panel upper surface, it is resisted against the second bed board panel upper surface when the scraper plate that mobile bed board link chain mechanism is installed moves to the second bed board panel upper surface.The effect of flight chain (mobile bed board link chain mechanism) is to be pushed ahead by the material being evenly distributed on upper flue gas casing bed body upper surface, concurrently disinfect the coking of warm air bed upper surface, and the material of not pyrolysis completely is transported on lower flue gas casing bed body upper surface and proceeds pyrolytic reaction.The oil gas that pyrolytic reaction generates is transported to condenser via oil gas vent G and is condensed into fuel oil, is transported to oil depot with oil transfer pump and stores.The waste residue that pyrolysis produces is exported H by solid residue and discharges, and is transported to next process with conveying equipment and carries out processing utilization.
Wherein, charging cloth device 7 main enters flue gas case width on reactor casing tailing edge and arranges multiple material charging aperture A, it is ensured that on upper flue gas case, material is uniform.
Reactive agent structure is removably provided with and is positioned at device body left end black box 2 and right-hand member black box 9, its maintenance being easy to the later stage and installation exercise.
Scraper plate is rectangular toothed structure, and material has certain disturbance in the process being pushed into, and is that material can evenly be heated.
The bottom of device body is provided with reactor underframe 1, and it both can as reactor bottom supporting construction, it is also possible to carry out integral hoisting, and certainly, this lower support structure can arrange lowering or hoisting gear.
Referring to Fig. 4, driven shaft strainer includes: be connected to the first connector S1 of flight chain mechanism slave drive device 10, and its free end is provided with the first securing member S2 of female thread structure；It is installed on the fixed pedestal S3 on fuel oil process units support；Being installed on the tumbler S4 between fixed pedestal and the first securing member, its one end is provided with the helicitic texture coordinated with the first connector, and the other end is connected to described fixed pedestal by rotating axis component；Described first connector, the first securing member, fixed pedestal, tumbler are distributed on same axis.
The fuel oil process units support at described fixed pedestal place is provided with multiple fixed pedestal installing hole, described fixed pedestal is removably installed in the fixed pedestal installing hole of fuel oil process units support by locking bolt, adjustment for fixed pedestal position, it is possible to increase the scope that elasticity adjustment structure adjusts.
The process route that organic solid waste of the present invention processes adopts and is totally different from general traditional pyrolysis method.What pyrolysis reactor adopted is the fixed-bed structure burying scraper plate transmission, flue gas heating, successfully solve equipment continuous prodution and equipment carbon distribution etc., utilize unique blade structure to control organic solid waste liquation and add the thickness on hot tank surface in flue gas, and the stirring action in scraper plate progradation makes material heat uniformly, the problem overcoming the produced response time length that organic solid waste heat conductivity is low.
Second embodiment of the present invention provides a kind of dynamically serialization organic solid waste coproduction gas carbon oil device, it is as the further improvement of the first embodiment, in this second embodiment, heat preservation sandwich layer is provided with and makes flue gas that reactive agent structure is carried out the smoke deflector of uniform heating and thermal insulation so that heat preservation sandwich layer can be heated and keep the temperature of reactive agent structure by flue gas uniformly.
It will be understood by those skilled in the art that the respective embodiments described above are to realize specific embodiments of the invention, and in actual applications, it is possible in the form and details it is done various change, without departing from the spirit and scope of the present invention.
Claims (9)
- null1. dynamic serialization organic solid waste coproduction gas carbon oil device，It includes device body，It is characterized in that，This device body has Packed reactive agent structure and is distributed in reactive agent structural cavity body and pending thing can carry out the first bed board panel of pyrolysis processing、Second bed board panel，Described second bed board panel is arranged at the first bed board lower panels，Described device body is provided with and pending thing is delivered to the first bed board panel carries out the continuous feed mechanism of pyrolysis processing，Described reactive agent inside configuration is provided with the pending thing that can be pointed to the first bed board panel upper surface and carries out scraping the flight chain mechanism processing and being pushed to by pending thing complete for non-pyrolysis the second bed board panel，Described reactive agent structure is provided with the oil gas vent that oil-gas transportation to the condenser that pyrolytic reaction generates is condensed into fuel oil and the solid residue outlet by the waste residue discharger body of pyrolysis generation.
- 2. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 1, it is characterised in that described first, second bed board panel is airtight hot-air channel structure, and first, second bed board panel be respectively arranged with respective hot blast import and export.
- 3. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 1 and 2, it is characterized in that, the hot-blast outlet of described first bed board panel and/or the second bed board panel is connected to the heat preservation sandwich layer of reactive agent structure, and this heat preservation sandwich layer is provided with hot-blast outlet.
- 4. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 3, it is characterised in that described heat preservation sandwich layer is provided with and makes flue gas that reactive agent structure is carried out the smoke deflector of uniform heating and thermal insulation.
- 5. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 1, it is characterized in that, described flight chain mechanism includes surrounding the mobile bed board link chain mechanism that the first bed board panel is arranged, it is installed on the scraper plate of described mobile bed board link chain mechanism, mobile bed board link chain mechanism is driven to carry out the driving device moved, the scraper plate that described mobile bed board link chain mechanism is installed is resisted against the upper surface of described first bed board panel when moving to the first bed board panel upper surface, it is resisted against the second bed board panel upper surface when the scraper plate that mobile bed board link chain mechanism is installed moves to the second bed board panel upper surface.
- 6. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 1 or 5, it is characterised in that the mobile bed board link chain mechanism of described flight chain mechanism is provided with strainer.
- 7. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 1, it is characterised in that described reactive agent structure is removably provided with the black box being positioned at the left and right end of device body.
- 8. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 5, it is characterised in that described scraper plate is rectangular toothed structure.
- 9. dynamic serialization organic solid waste coproduction gas carbon oil device according to claim 1, it is characterised in that the bottom of described device body is provided with reactor underframe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610332144.6A CN105778955A (en) | 2016-05-19 | 2016-05-19 | Dynamic continuous organic solid waste gas-carbon oil cogeneration device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610332144.6A CN105778955A (en) | 2016-05-19 | 2016-05-19 | Dynamic continuous organic solid waste gas-carbon oil cogeneration device |
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| CN105778955A true CN105778955A (en) | 2016-07-20 |
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| CN201610332144.6A Pending CN105778955A (en) | 2016-05-19 | 2016-05-19 | Dynamic continuous organic solid waste gas-carbon oil cogeneration device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107841320A (en) * | 2017-11-06 | 2018-03-27 | 华中农业大学 | A kind of comprehensive resources regeneration Poly-generation circulation furnace apparatus |
| CN113509786A (en) * | 2021-04-29 | 2021-10-19 | 维尔利环保科技集团股份有限公司 | Impurity-removing oil dissolving machine and kitchen waste grease treatment system and method |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
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| CN113509786A (en) * | 2021-04-29 | 2021-10-19 | 维尔利环保科技集团股份有限公司 | Impurity-removing oil dissolving machine and kitchen waste grease treatment system and method |
| CN113509786B (en) * | 2021-04-29 | 2022-05-10 | 维尔利环保科技集团股份有限公司 | Impurity-removing oil dissolving machine and kitchen waste grease treatment system and method |
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