CN213803640U - Biomass carbonization co-production equipment - Google Patents
Biomass carbonization co-production equipment Download PDFInfo
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- CN213803640U CN213803640U CN202022540110.0U CN202022540110U CN213803640U CN 213803640 U CN213803640 U CN 213803640U CN 202022540110 U CN202022540110 U CN 202022540110U CN 213803640 U CN213803640 U CN 213803640U
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- tank body
- wall
- oleophobic membrane
- membrane net
- carbonization
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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
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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
- 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 relates to biomass carbonization co-production equipment, which comprises a carbonization mechanism, wherein the exhaust end of the carbonization mechanism is detachably provided with one end of a connecting pipe which is convenient for conveying synthesis gas; the device comprises a tank body, a gas inlet pipeline convenient for synthesis gas to enter is spliced on the left side of the tank body, the other end of a connecting pipe is detachably and fixedly connected with the left side of the gas inlet pipeline, a discharge pipe convenient for tar discharge is arranged at the bottom end of the tank body, a valve for controlling synthesis gas discharge is locked at the top end of the tank body through a bolt, and an exhaust pipe convenient for synthesis gas discharge is arranged at the top end of the valve; the steam inlet pipe is inserted at the right side of the top end of the tank body; the supporting plate is inserted into the bottom end of the inner wall of the tank body. The device can effectively separate out tar in the synthesis gas, improves the purity of the synthesis gas, is energy-saving and environment-friendly, and is suitable for popularization and use.
Description
Technical Field
The utility model relates to a biological charcoal production facility technical field especially relates to a living beings carbomorphism coproduction equipment.
Background
Biomass carbonization is a key technology for converting agricultural and forestry wastes into clean fuel gas, the generated synthesis gas can replace fossil fuels such as natural gas and the like, and the supply of fuel gas, heat energy and electric energy is realized, the biomass pyrolysis gasification technology in China is developed for more than 20 years at present, the demonstration and layout of a civil distributed biomass fuel gas supply system are completed, the industrial technical basis of large-scale fuel gas preparation and power generation is preliminarily possessed, and the large-scale, standardized and standardized design and manufacture of equipment for biomass pyrolysis gasification carbonization becomes necessary for industrial development;
traditional living beings carbomorphism all can produce synthetic gas and tar, for the purity that improves the synthetic gas, need carry out the filtration of tar or impurity in the synthetic gas, tar catalytic cracking becomes important research direction in recent years, the method of tar desorption mainly adopts mechanical desorption technique in current actual engineering, mechanical decoking method mainly includes wet-type decoking, wherein wet-type decoking is that partial tar in the water will burn gas is taken away, the capital equipment is the spray column, if adopt wet-type processing, then can additionally increase equipment, and the increase in production cost is unfavorable for carrying out the volume production, and cause the pollution to the environment.
Disclosure of Invention
The utility model aims to solve the defects of the prior art and provide biomass carbonization co-production equipment,
the utility model discloses a realize above-mentioned purpose, adopt following technical scheme:
a biomass carbonization co-production device comprises a carbonization mechanism, wherein the exhaust end of the carbonization mechanism is detachably provided with one end of a connecting pipe which is convenient for conveying synthesis gas;
the device comprises a tank body, a gas inlet pipeline convenient for synthesis gas to enter is spliced on the left side of the tank body, the other end of a connecting pipe is detachably and fixedly connected with the left side of the gas inlet pipeline, a discharge pipe convenient for tar discharge is arranged at the bottom end of the tank body, a valve for controlling synthesis gas discharge is locked at the top end of the tank body through a bolt, and an exhaust pipe convenient for synthesis gas discharge is arranged at the top end of the valve;
the steam inlet pipe is inserted at the right side of the top end of the tank body;
the supporting plate is inserted at the bottom end of the inner wall of the tank body, through holes which are circularly arranged are formed in the supporting plate, a first oleophobic membrane net and a second oleophobic membrane net are detachably and fixedly arranged at the top ends of the through holes respectively, the first oleophobic membrane net is positioned at the inner side of the second oleophobic membrane net, and the outer wall of the air inlet pipeline penetrates through the first oleophobic membrane net and the second oleophobic membrane net;
get rid of dirty mechanism, get rid of dirty mechanism and set up on the outer wall of backup pad.
Preferably, the second oleophobic membrane net has a larger mesh size than the first oleophobic membrane net.
Preferably, the dirt throwing mechanism comprises a shell, a motor, a first conical gear, a sealing bearing, a round rod, a second conical gear, a round plate and blades, the shell is fixedly arranged at the bottom end of the supporting plate, the motor is locked on the inner wall of the right side of the bottom end of the shell through a screw, the first conical gear is detachably and fixedly arranged at the output end of the motor, the two sealing bearings are arranged on the inner wall of the left side of the upper end and the lower end of the shell, the round rod is arranged on the inner rings of the two sealing bearings, the second conical gear is arranged on the outer wall of the round rod, the conical gear II is meshed and connected with the conical gear I, the top end of the round rod penetrates through the supporting plate, the circular plate is arranged on the outer wall of the round rod, and the circular plate is positioned at the top end of the supporting plate, the blades are arranged on the outer wall of the circular rod, and the bottom ends of the blades are fixedly connected with the upper end face of the circular plate.
Preferably, the outer rings of the two sealing bearings are fixedly connected with the inner wall of the shell through bearing seats, and the inner rings of the sealing bearings are in interference fit with the outer wall of the round rod.
Preferably, the blades are distributed on the outer wall of the round rod at intervals of 20 degrees clockwise.
The utility model has the advantages that:
the circular plate and the blades rotate at a high speed and simultaneously drive rising synthesis gas to rotate at a high speed, the synthesis gas can generate huge centrifugal force by the high-speed rotation of the synthesis gas, the synthesis gas and the first oleophobic membrane net and the second oleophobic membrane net rub, when the synthesis gas with tar rubs with the first oleophobic membrane net and the second oleophobic membrane net, oil films containing tar are formed on the surfaces of the first oleophobic membrane net and the second oleophobic membrane net in a certain area, the synthesis gas can throw away the tar in the synthesis gas under the action of the centrifugal force, when the oil films on the surfaces of the first oleophobic membrane net and the second oleophobic membrane net reach a certain area and thickness, the oil films can flow downwards along the surfaces of the first oleophobic membrane net and the second oleophobic membrane net and flow downwards to the bottom of the tank body through the through holes, the oil films are discharged through the discharge pipe, the treated synthesis gas is discharged and collected through the valve and the exhaust pipe, and steam enters the inner cavity of the tank body through the steam inlet pipe, steam cleaning is carried out to the inner chamber of jar body, can effectually go out the tar separation in the synthetic gas, has improved the purity of synthetic gas, controls to use more simple and conveniently, and energy-concerving and environment-protective reduces construction cost and working costs, is fit for using widely.
Drawings
Fig. 1 is a front view of the present invention;
fig. 2 is a sectional view of the housing of the present invention;
fig. 3 is a top cross-sectional view of the tank of the present invention.
In the figure: 1. the device comprises a carbonization mechanism, 2, a tank body, 3, an air inlet pipeline, 4, a discharge pipe, 5, a valve, 6, an exhaust pipe, 7, a steam inlet pipe, 8, a support plate, 9, a through hole, 10, a first oleophobic membrane net, 11, a second oleophobic membrane net, 12, a connecting pipe, 13, a shell, 14, a motor, 15, a first conical gear, 16, a sealing bearing, 17, a round rod, 18, a second conical gear, 19, a round plate, 20 and a blade.
The following detailed description will be made in conjunction with embodiments of the present invention with reference to the accompanying drawings.
Detailed Description
The invention will be further explained with reference to the following figures and examples:
as shown in fig. 1-3, a biomass carbonization co-production device comprises a carbonization mechanism 1, wherein an exhaust end of the carbonization mechanism 1 is detachably provided with one end of a connecting pipe 12 which is convenient for conveying synthesis gas; the device comprises a tank body 2, wherein the tank body 2 is positioned on the right side of a carbonization mechanism 1, an air inlet pipeline 3 convenient for synthetic gas to enter is spliced on the left side of the tank body 2, the other end of a connecting pipe 12 is detachably and fixedly connected with the left side of the air inlet pipeline 3, a discharge pipe 4 convenient for tar discharge is arranged at the bottom end of the tank body 2, a valve 5 for controlling the discharge of the synthetic gas is locked at the top end of the tank body 2 through a bolt, and an exhaust pipe 6 convenient for the discharge of the synthetic gas is arranged at the top end of the valve 5; the steam inlet pipe 7 is inserted at the right side of the top end of the tank body 2; the supporting plate 8 is inserted into the bottom end of the inner wall of the tank body 2, through holes 9 which are circularly arranged are formed in the supporting plate 8, the top ends of the through holes 9 are detachably and fixedly provided with a first oleophobic membrane net 10 and a second oleophobic membrane net 11 respectively, the first oleophobic membrane net 10 is located on the inner side of the second oleophobic membrane net 11, and the outer wall of the air inlet pipeline 3 penetrates through the first oleophobic membrane net 10 and the second oleophobic membrane net 11; get rid of dirty mechanism, get rid of dirty mechanism and set up on the outer wall of backup pad 8.
Preferably, the second oleophobic membrane network 11 has a larger mesh size than the first oleophobic membrane network 10.
Preferably, the dirt throwing mechanism comprises a shell 13, a motor 14, a first conical gear 15, a sealing bearing 16, a circular rod 17, a second conical gear 18, a circular plate 19 and blades 20, the shell 13 is fixedly arranged at the bottom end of the supporting plate 8, the motor 14 is locked on the right inner wall of the bottom end of the shell 13 through screws, the first conical gear 15 is detachably and fixedly arranged at the output end of the motor 14, the two sealing bearings 16 are arranged on the left inner walls of the upper end and the lower end of the shell 13, the circular rod 17 is arranged on the inner rings of the two sealing bearings 16, the second conical gear 18 is arranged on the outer wall of the circular rod 17, and the second conical gear 18 is meshed with the first conical gear 15, the top end of the round rod 17 penetrates through the support plate 8, the round plate 19 is arranged on the outer wall of the round rod 17, the circular plate 19 is located at the top end of the supporting plate 8, the plurality of blades 20 are arranged on the outer wall of the circular rod 17, and the bottom ends of the blades 20 are fixedly connected with the upper end face of the circular plate 19.
Preferably, the outer rings of the two sealed bearings 16 are fixedly connected with the inner wall of the housing 13 through bearing seats, and the inner rings of the sealed bearings 16 are in interference fit with the outer wall of the round rod 17.
Preferably, the blades 20 are distributed on the outer wall of the round bar 17 at every 20 degrees clockwise.
When the utility model is used, the synthesis gas generated during carbonization of the carbonization mechanism 1 is conveyed to the inner cavity of the tank body 2 through the connecting pipe 12 and the air inlet pipeline 3, the conical gear 15 is driven to rotate through the motor 14, the conical gear two 18 is driven to drive the round rod 17 through the conical gear 15, the round plate 19 and the blade 20 are driven to rotate at high speed through the sealing bearing 16, the round rod 17 is fixed through the sealing bearing 16, the round rod 17 is convenient to drive the round plate 19 and the blade 20 to rotate through the sealing bearing 16, the round plate 19 and the blade 20 rotate at high speed and simultaneously drive the rising synthesis gas to rotate at high speed, the synthesis gas generates huge centrifugal force, the synthesis gas and the oleophobic membrane net one 10 and the oleophobic membrane net two 11 generate friction, when the synthesis gas with tar and the oleophobic membrane net one 10 and the oleophobic membrane net two 11 generate friction, tar-containing oil films with certain areas are formed on the surfaces of the oleophobic membrane net one 10 and the oleophobic membrane net two 11, the synthetic gas still can throw away tar among the synthetic gas under centrifugal force, reach certain area and thickness when the surface oil film of oleophobic membrane net one 10 and oleophobic membrane net two 11, will flow downwards along the surface of oleophobic membrane net one 10 and oleophobic membrane net two 11, flow to the bottom of jar body 2 through-hole 9 downwards, arrange outward through arranging material pipe 4, the synthetic gas after handling passes through valve 5 and the collection of 6 dischargings of blast pipe, steam passes through steam intake pipe 7 and gets into the inner chamber of jar body 2, carry out steam cleaning to the inner chamber of jar body 2.
The present invention has been described above with reference to the accompanying drawings, and it is obvious that the present invention is not limited by the above embodiments, and various improvements made by the method concept and technical solution of the present invention or directly applied to other occasions without improvement are all within the protection scope of the present invention.
Claims (5)
1. A biomass carbonization co-production equipment is characterized in that:
the device comprises a carbonization mechanism (1), wherein the exhaust end of the carbonization mechanism (1) is detachably provided with one end of a connecting pipe (12) which is convenient for conveying synthesis gas;
the device comprises a tank body (2), wherein the tank body (2) is positioned on the right side of a carbonization mechanism (1), an air inlet pipeline (3) facilitating the entry of synthetic gas is spliced on the left side of the tank body (2), the other end of a connecting pipe (12) is detachably and fixedly connected with the left side of the air inlet pipeline (3), a discharge pipe (4) facilitating the discharge of tar is arranged at the bottom end of the tank body (2), a valve (5) controlling the discharge of the synthetic gas is locked at the top end of the tank body (2) through a bolt, and an exhaust pipe (6) facilitating the discharge of the synthetic gas is arranged at the top end of the valve (5);
the steam inlet pipe (7), the steam inlet pipe (7) is inserted and connected to the right side of the top end of the tank body (2);
the tank body is characterized by comprising a supporting plate (8), wherein the supporting plate (8) is inserted into the bottom end of the inner wall of the tank body (2), through holes (9) which are circularly arranged are formed in the supporting plate (8), the top ends of the through holes (9) are respectively detachably and fixedly provided with a first oleophobic membrane net (10) and a second oleophobic membrane net (11), the first oleophobic membrane net (10) is located on the inner side of the second oleophobic membrane net (11), and the outer wall of the air inlet pipeline (3) penetrates through the first oleophobic membrane net (10) and the second oleophobic membrane net (11);
get rid of dirty mechanism, get rid of dirty mechanism and set up on the outer wall of backup pad (8).
2. The biomass carbonization co-production equipment as claimed in claim 1, characterized in that: the mesh number of the second oleophobic membrane net (11) is larger than that of the first oleophobic membrane net (10).
3. The biomass carbonization co-production equipment as claimed in claim 1, characterized in that: the sewage throwing mechanism comprises a shell (13), a motor (14), a first conical gear (15), sealing bearings (16), a round rod (17), a second conical gear (18), a circular plate (19) and blades (20), wherein the shell (13) is fixedly arranged at the bottom end of the supporting plate (8), the motor (14) is locked on the right inner wall of the bottom end of the shell (13) through screws, the first conical gear (15) is detachably fixedly arranged at the output end of the motor (14), the two sealing bearings (16) are arranged on the left inner walls of the upper end and the lower end of the shell (13), the round rod (17) is arranged on the inner rings of the two sealing bearings (16), the second conical gear (18) is arranged on the outer wall of the round rod (17), the second conical gear (18) is meshed with the first conical gear (15), the top end of the round rod (17) penetrates through the supporting plate (8), the circular plate (19) is arranged on the outer wall of the circular rod (17), the circular plate (19) is located at the top end of the supporting plate (8), the blades (20) are arranged on the outer wall of the circular rod (17), and the bottom ends of the blades (20) are fixedly connected with the upper end face of the circular plate (19).
4. The biomass carbonization co-production equipment as claimed in claim 3, characterized in that: the outer rings of the two sealing bearings (16) are fixedly connected with the inner wall of the shell (13) through bearing seats, and the inner rings of the sealing bearings (16) are in interference fit with the outer wall of the round rod (17).
5. The biomass carbonization co-production equipment as claimed in claim 3, characterized in that: the blades (20) are distributed on the outer wall of the round rod (17) at intervals of 20 degrees clockwise.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022540110.0U CN213803640U (en) | 2020-11-06 | 2020-11-06 | Biomass carbonization co-production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022540110.0U CN213803640U (en) | 2020-11-06 | 2020-11-06 | Biomass carbonization co-production equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213803640U true CN213803640U (en) | 2021-07-27 |
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ID=76965503
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022540110.0U Active CN213803640U (en) | 2020-11-06 | 2020-11-06 | Biomass carbonization co-production equipment |
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| Country | Link |
|---|---|
| CN (1) | CN213803640U (en) |
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2020
- 2020-11-06 CN CN202022540110.0U patent/CN213803640U/en active Active
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