CN204550471U - The device of charcoal, biofuel, combustion gas is produced for agriculture and forestry organic waste material catalytic pyrolysis - Google Patents
The device of charcoal, biofuel, combustion gas is produced for agriculture and forestry organic waste material catalytic pyrolysis Download PDFInfo
- Publication number
- CN204550471U CN204550471U CN201520254564.8U CN201520254564U CN204550471U CN 204550471 U CN204550471 U CN 204550471U CN 201520254564 U CN201520254564 U CN 201520254564U CN 204550471 U CN204550471 U CN 204550471U
- Authority
- CN
- China
- Prior art keywords
- feed
- pyrolysis installation
- pyrolysis
- agriculture
- dust collector
- 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
Links
- 239000000463 material Substances 0.000 title claims abstract description 14
- 239000010815 organic waste Substances 0.000 title claims abstract description 14
- 239000003610 charcoal Substances 0.000 title claims abstract description 13
- 239000002551 biofuel Substances 0.000 title claims abstract description 10
- 238000007233 catalytic pyrolysis Methods 0.000 title claims abstract description 10
- 239000000567 combustion gas Substances 0.000 title claims abstract description 10
- 238000000197 pyrolysis Methods 0.000 claims abstract description 40
- 238000009434 installation Methods 0.000 claims abstract description 34
- 239000000428 dust Substances 0.000 claims abstract description 17
- 238000002485 combustion reaction Methods 0.000 claims abstract description 13
- 239000007789 gas Substances 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims description 10
- 239000000571 coke Substances 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 230000000576 supplementary Effects 0.000 claims description 3
- 239000002994 raw material Substances 0.000 abstract description 4
- 235000002918 Fraxinus excelsior Nutrition 0.000 abstract description 2
- 239000002956 ash Substances 0.000 abstract description 2
- 239000004615 ingredient Substances 0.000 abstract description 2
- 239000010908 plant waste Substances 0.000 abstract description 2
- 239000002028 Biomass Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000002309 gasification Methods 0.000 description 5
- 230000001603 reducing Effects 0.000 description 5
- 238000006722 reduction reaction Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000001590 oxidative Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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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
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or 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
- Y02P20/10—Process efficiency
Abstract
The utility model is open produces charcoal biofuel for agriculture and forestry organic waste material catalytic pyrolysis, the device of combustion gas, comprise: feeding device, pyrolysis installation, tornado dust collector, cleaner, combustion header, described feeding device is arranged on the side of pyrolysis installation, pyrolysis installation side connects tornado dust collector, tornado dust collector connect cleaner, combustion header connects gas pipeline, described feeding device comprises feed barrel, feed barrel is arranged on the side of pyrolysis installation, piston is provided with in described feed barrel, piston side is fixedly connected with piston rod, the opening for feed that described feed barrel wall is arranged, the feed bin arranged above opening for feed, in feed bin, turnover panel is installed.The non-stop run of the utility model energy, must not stop working, and removes ashes, again reinforced, igniting, working efficiency is high, and the utility model is low to ingredient requirement, all dry, wet plant wastes all can be used as raw material, and raw material sources are wide, solve the problem of agriculture and forestry organic waste material pollution, energy-conserving and environment-protective simultaneously.
Description
Technical field
The utility model relates to new forms of energy preparing technical field, is specially the device producing charcoal biofuel, combustion gas for agriculture and forestry organic waste material catalytic pyrolysis.
Background technology
Along with the exhaustion of fossil energy and the mankind are to the concern of global environmental problem, biomass energy substitutes the research and development that fossil energy utilizes, and has become the focus of lot of domestic and foreign scholar's research and concern.
Traditional biomass gasification is produced combustible gas process and is divided into drying, pyrolysis, oxidation and reduction four-stage:
(1) drying process: after biomass enter vapourizing furnace, separates out surface-moisture under the effect of heat, is main drying stage 200 ~ 300 DEG C time;
(2) pyrolytic reaction: start when temperature is elevated to more than 300 DEG C to carry out pyrolytic reaction.300 ~ 400 DEG C time, biomass just can discharge the volatile matter of about 70%, and coal just can discharge the volatile matter of about 30% to 800 DEG C.The volatile matter that pyrolytic reaction is separated out mainly comprises water vapour, H
2, CO, CH
4, tar and other hydrocarbon polymers;
(3) oxidizing reaction: the residue charcoal of pyrolysis and the air of introducing react, and temperature of reaction is about 800 ~ 900 DEG C;
(4) reduction process: reduction process does not have oxygen, in the products of combustion in zone of oxidation and water vapour and reducing zone, charcoal reacts, and generates H
2with CO etc.These gases and volatile matter constitute inflammable gas, complete the conversion process of solid biomass to geseous fuel.
Problems existing in combustible gas process is produced in above-mentioned traditional biomass gasification to be had: in four main phase of gasification, the oxidizing reaction stage releases a large amount of heat energy, owing to failing the heat energy collected wherein in conventional production methods, cause the waste of the energy; Need in reduction process to consume a large amount of heat energy, need the external world to provide corresponding energy for this reason.Therefore, the loss that in reaction, heat energy is a large amount of and consumption, make the thermo-efficiency of whole biomass gasification process greatly reduce.
Utility model content
The technical problem that the utility model solves is to be provided for the device that agriculture and forestry organic waste material catalytic pyrolysis produces charcoal biofuel, combustion gas, to solve the problem proposed in above-mentioned background technology.
The technical problem that the utility model solves realizes by the following technical solutions: produce charcoal biofuel for agriculture and forestry organic waste material catalytic pyrolysis, the device of combustion gas, comprise: feeding device, pyrolysis installation, tornado dust collector, cleaner, combustion header, described feeding device is arranged on the side of pyrolysis installation, pyrolysis installation side connects tornado dust collector, tornado dust collector connect cleaner, combustion header connects gas pipeline, described feeding device comprises feed barrel, feed barrel is arranged on the side of pyrolysis installation, piston is provided with in described feed barrel, piston side is fixedly connected with piston rod, the opening for feed that described feed barrel wall is arranged, the feed bin arranged above opening for feed, in feed bin, turnover panel is installed.
What described cleaner was provided with supplementary coke adds burnt hole and coke discharge port, establishes cooling pool below coke discharge port.
Described pyrolysis installation one end is provided with charging ship lock, the other end is provided with inlet plenum, discharge chamber and for discharging the discharging ship lock of solid active carbon that pyrolysis produces, pyrolysis installation is cydariform roughly, heating pipe line is had along drum axial distribution, the junction of pyrolysis installation charging ship lock and discharging ship lock is provided with the sealed valve of isolated extraneous air, and the discharge chamber of pyrolysis installation connects tornado dust collector.
Compared with prior art, the beneficial effects of the utility model are: the non-stop run of the utility model energy, must not stop working, remove ashes, again reinforced, igniting, working efficiency is high, and the utility model is low to ingredient requirement, all dry, wet plant wastes all can be used as raw material, and raw material sources are wide, solve the problem of agriculture and forestry organic waste material pollution, energy-conserving and environment-protective simultaneously.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is feeding device structural representation of the present utility model.
In figure: 1, feeding device; 2, pyrolysis installation; 3, tornado dust collector; 4, cleaner; 5, combustion header; 6, emergent chimney; 7, chimney; 11, opening for feed; 12, feed barrel; 13, piston; 14, piston rod; 15, feed bin; 16, turnover panel.
Embodiment
In order to make actualizing technology means of the present utility model, creation characteristic, reach object and effect is easy to understand, below in conjunction with concrete diagram, set forth the utility model further.
As Fig. 1, shown in Fig. 2, charcoal biofuel is produced for agriculture and forestry organic waste material catalytic pyrolysis, the device of combustion gas, comprise: feeding device 1, pyrolysis installation 2, tornado dust collector 3, cleaner 4, combustion header 5, described feeding device 1 is arranged on the side of pyrolysis installation 2, pyrolysis installation 2 side connects tornado dust collector 3, tornado dust collector 3 connect cleaner 4, cleaner 4 connects combustion header 5, combustion header 5 connects gas pipeline, described feeding device 1 comprises feed barrel 12, feed barrel 12 is arranged on the side of pyrolysis installation 12, piston 13 is provided with in described feed barrel 12, piston 13 side is fixedly connected with piston rod 14, the opening for feed 11 that described feed barrel 12 wall is arranged, the feed bin 15 arranged above opening for feed 11, turnover panel 16 is installed in feed bin 15.
What described cleaner 4 was provided with supplementary coke adds burnt hole and coke discharge port, establishes cooling pool below coke discharge port.
Described pyrolysis installation 2 one end is provided with charging ship lock, the other end is provided with inlet plenum, discharge chamber and the discharging ship lock for discharging the solid active carbon that pyrolysis produces, pyrolysis installation is cydariform roughly, heating pipe line is had along drum axial distribution, the junction of pyrolysis installation charging ship lock and discharging ship lock is provided with the sealed valve of isolated extraneous air, and the discharge chamber of pyrolysis installation connects tornado dust collector 3.
Principle of work of the present utility model is:
First agriculture and forestry organic waste material is continuously flowed into from feed bin 15 top, overstock to a certain extent, first group, top turnover panel 16 starts, rotate and stop several weeks, rear lower second group of turnover panel is stopped to start, rotate and stop several weeks, through the agriculture and forestry organic waste material of upper and lower two groups of turnover panels twice compacting, pyrolysis installation 2 is entered under the thrust of piston 13, conducted heat by the tube wall of piping system in pyrolysis installation 2, low temperature pyrogenation is carried out under the condition of isolated air, after the combustible gas produced after pyrolytic gasification enters tornado dust collector 3 dedusting via pipeline, cleaner 4 is entered again via pipeline, the rear combustible gas of purification enters combustion header 5 by pipeline and collects, the charcoal produced after biomass pyrolytic, exported by the discharging ship lock in pyrolysis installation 2, in addition, in order to support equipment safety, the discharge chamber of pyrolysis installation 2 is provided with emergent chimney 6, and when breaking down, the pyrolysis gas in pyrolysis installation 2 is imported emergent chimney 6 fast, at high temperature burns.
More than show and describe ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.Claimed scope of the present utility model is defined by appending claims and equivalent thereof.
Claims (3)
1. produce charcoal for agriculture and forestry organic waste material catalytic pyrolysis, biofuel, the device of combustion gas, comprise: feeding device, pyrolysis installation, tornado dust collector, cleaner, combustion header, it is characterized in that: described feeding device is arranged on the side of pyrolysis installation, pyrolysis installation side connects tornado dust collector, tornado dust collector connect cleaner, cleaner connects combustion header, combustion header connects gas pipeline, described feeding device comprises feed barrel, feed barrel is arranged on the side of pyrolysis installation, piston is provided with in described feed barrel, piston side is fixedly connected with piston rod, the opening for feed that described feed barrel wall is arranged, the feed bin arranged above opening for feed, in feed bin, turnover panel is installed.
2. the device producing charcoal, biofuel, combustion gas for agriculture and forestry organic waste material catalytic pyrolysis according to claim 1, is characterized in that: what described cleaner was provided with supplementary coke adds burnt hole and coke discharge port, establishes cooling pool below coke discharge port.
3. the device producing charcoal, biofuel, combustion gas for agriculture and forestry organic waste material catalytic pyrolysis according to claim 1, it is characterized in that: described pyrolysis installation one end is provided with charging ship lock, the other end is provided with inlet plenum, discharge chamber and for discharging the discharging ship lock of solid active carbon that pyrolysis produces, pyrolysis installation is cydariform roughly, heating pipe line is had along drum axial distribution, the junction of pyrolysis installation charging ship lock and discharging ship lock is provided with the sealed valve of isolated extraneous air, and the discharge chamber of pyrolysis installation connects tornado dust collector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520254564.8U CN204550471U (en) | 2015-04-25 | 2015-04-25 | The device of charcoal, biofuel, combustion gas is produced for agriculture and forestry organic waste material catalytic pyrolysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520254564.8U CN204550471U (en) | 2015-04-25 | 2015-04-25 | The device of charcoal, biofuel, combustion gas is produced for agriculture and forestry organic waste material catalytic pyrolysis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204550471U true CN204550471U (en) | 2015-08-12 |
Family
ID=53825607
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520254564.8U Expired - Fee Related CN204550471U (en) | 2015-04-25 | 2015-04-25 | The device of charcoal, biofuel, combustion gas is produced for agriculture and forestry organic waste material catalytic pyrolysis |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204550471U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110293115A (en) * | 2019-06-28 | 2019-10-01 | 新疆中金科瑞新能源发展股份有限公司 | A kind of two-way rapid cooling system of oily waste thermal desorption high temperature tailings |
-
2015
- 2015-04-25 CN CN201520254564.8U patent/CN204550471U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110293115A (en) * | 2019-06-28 | 2019-10-01 | 新疆中金科瑞新能源发展股份有限公司 | A kind of two-way rapid cooling system of oily waste thermal desorption high temperature tailings |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150812 Termination date: 20170425 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |