CN212404019U - Biomass pyrolysis and comprehensive energy utilization device - Google Patents

Biomass pyrolysis and comprehensive energy utilization device Download PDF

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CN212404019U
CN212404019U CN202020096374.9U CN202020096374U CN212404019U CN 212404019 U CN212404019 U CN 212404019U CN 202020096374 U CN202020096374 U CN 202020096374U CN 212404019 U CN212404019 U CN 212404019U
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pyrolysis
gas
chamber
energy utilization
biomass
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高东坡
孙宏伟
曹永强
康延年
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Gansu Huizhong Energy Saving Development Co ltd
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Gansu Huizhong Energy Saving Development Co ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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Abstract

The utility model belongs to the technical field of the living beings pyrolysis, a living beings pyrolysis and comprehensive energy utilization device is disclosed, with the problem that exists among the living beings pyrolysis technology among the solution prior art, the device includes the pyrolysis chamber, the gas heating chamber is equipped with in the outside of pyrolysis chamber, distributing device is equipped with to the bottom of gas heating chamber, and bottom one side of pyrolysis chamber is equipped with the biochar bin outlet, the living beings granule feed bin is equipped with at the top of pyrolysis chamber, the distributing pipe of living beings granule feed bin stretches into the indoor lower part of pyrolysis, the top of pyrolysis chamber still is equipped with pyrolysis gas conveying pipeline, pyrolysis gas conveying pipeline is connected with tar recovery unit, tar recovery unit is connected with gas ejection of compact pipeline, gas ejection of compact pipeline is connected with the compressor, the compressor is connected with the gas. The utility model discloses can effectively acquire biological charcoal and biological tar and gas. At high temperature, the synthesized weather product can be used as fuel for power generation or heating, and the liquid biological tar can be used for refining automobile fuel oil or mineral dressing agent; biochar is a high quality soil improvement additive.

Description

Biomass pyrolysis and comprehensive energy utilization device
Technical Field
The utility model relates to a living beings pyrolysis technical field, concretely relates to living beings pyrolysis and comprehensive energy utilization device.
Background
The amount of solid biomass available in china is huge, mainly based on agricultural waste and wood waste. The biomass is distributed and dispersed, and is difficult to collect and transport, and the large-scale pyrolysis technology is difficult to adopt under the current conditions of China, so the medium-scale and small-scale biomass pyrolysis gasification technology has unique advantages in China. At present, a plurality of biomass power generation and combustion technologies appear in various places to support biomass power generation systems and biomass combustion furnaces. The calorific value of the fuel gas generated by different gasification processes is greatly different, and the statistics of related data are as follows:
Figure DEST_PATH_IMAGE001
the biomass raw materials in the prior art have wide range, and the products of the existing biomass power generation and biomass gas pyrolysis furnaces are single. Unsmooth production and use and the like.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a biomass pyrolysis and comprehensive energy utilization device in order to solve the problem existing in the biomass pyrolysis technology in the prior art.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a living beings pyrolysis and comprehensive energy utilization device, including the pyrolysis chamber, the outside of pyrolysis chamber is equipped with the gas heating chamber, distributing device is equipped with to the bottom of pyrolysis chamber, and bottom one side of pyrolysis chamber is equipped with the biochar bin outlet, the living beings granule feed bin is equipped with at the top of pyrolysis chamber, the distributing pipe of living beings granule feed bin stretches into the indoor lower part of pyrolysis, the top of pyrolysis chamber still is equipped with the defeated material pipeline of pyrolysis gas, the defeated material pipe connection of pyrolysis gas has tar recovery unit, tar recovery unit is connected with gas ejection of compact pipeline, gas ejection of compact pipeline is connected with the compressor, the compressor is connected with the gas.
Further, the distributing device comprises a distributing device which is rotatably arranged at the bottom of the pyrolysis chamber.
Further, the pyrolysis chamber bottom is slope surface, the distributing device is including setting up the rotatable material awl point baffle at slope surface top, and slope surface top is equipped with a plurality ofly along the circumferencial direction equipartition with the fender material scraping bar of slope surface looks adaptation, and the tip of keeping off the material scraping bar is fixed with the lower part of material awl point baffle.
Furthermore, the bottom of the material conical tip baffle is provided with a rotating shaft, and the rotating shaft penetrates through a shaft hole formed in the bottom of the pyrolysis chamber and then is connected with a driving device.
Furthermore, a cavity is arranged below the bottom of the pyrolysis chamber, a driving device is arranged in the cavity, a biochar discharging cavity is arranged on one side of the cavity, the top of the biochar discharging cavity is communicated with a biochar discharging port, and a discharging port is arranged at the bottom of the biochar discharging cavity.
Furthermore, a gas burner is arranged on the side part of the gas heating chamber, a spiral flue is arranged on the upper part of the gas heating chamber, and the top of the spiral flue is connected with a smoke exhaust pipeline arranged on the top of the gas heating chamber.
Further, the tar recovery device is a gas cooler.
Furthermore, the driving device is a driving motor, the driving motor is installed at the bottom of the pyrolysis chamber in the cavity through a connecting frame and a bolt, the shaft end of a driving shaft of the driving motor is installed in a matched mode with a bearing seat fixed at the bottom of the pyrolysis chamber, a driving gear is fixedly installed on the driving shaft of the driving motor, and the driving gear is matched with a driven gear fixedly installed on a rotating shaft.
Furthermore, a temperature sensor is arranged on the pyrolysis chamber, and the temperature sensor is connected with an electric valve arranged on the gas burner through a controller.
Compared with the prior art, the utility model, following beneficial effect has:
the utility model distributes the biomass in the biomass particle bin to the rotatable distributing device at the bottom of the pyrolysis chamber through the distributing pipe, and the gas heating chamber provides enough temperature, so that the biomass is decomposed to generate gas and biochar in the rotation of the rotatable distributing device; the biochar is discharged from the biochar discharge port, synthetic biogas generated by pyrolysis is conveyed to the tar recovery device through the pyrolysis gas conveying pipeline, the gas is cooled, and contained tar is condensed. The cooled synthetic fuel gas is compressed and then is delivered to a gas storage tank for storage. And the compression fan compresses the gas to 0.3Mpa for the user to use.
The utility model discloses can effectively acquire biological charcoal and biological tar gas together. The biomass particles are placed in an anoxic state at a high temperature of 500 to 600 ℃ for controlled pyrolysis thereof. Besides the biochar, the high-temperature decomposition can also generate products such as synthetic natural gas, liquid tar and the like, the synthetic weather product can be used as a fuel for power generation or heating, and the liquid biological tar can be used for refining automobile fuel oil or mineral dressing reagents; biochar is a high quality soil improvement additive.
The utility model discloses a distributing device can make living beings along the slope behind the distributing pipe cloth to the edge in scattering by the pyrolysis, and sets up material awl point baffle at slope surface's center, and firstly convenient fixed fender material scrapes the strip, secondly makes the material be convenient for lay in slope surface. The utility model discloses set up a plurality of fender materials and scrape the strip along the circumferencial direction equipartition on the slope surface, keep off the material and scrape the strip rotatory and drive the material and decompose the back and flow from the biochar bin outlet.
The utility model discloses a bottom below of pyrolysis chamber sets up the cavity for install drive arrangement, biological charcoal ejection of compact chamber is used for accomodating and the biological charcoal of discharging.
The utility model discloses a spiral flue that the upper portion of gas heating chamber set up can make the flue gas that produces in the gas heating chamber flow into exhaust pipe from spiral flue, then discharges after handling.
The gas cooler of the utility model can collect tar while cooling the gas.
The utility model discloses can detect the pyrolysis temperature through the temperature sensor on the pyrolysis chamber, give the controller with temperature signal transmission, utilize the controller to adjust the valve on the gas nozzle, and then adjust the gas volume to the proportion of this temperature control synthetic gas in the control pyrolysis chamber, biochar and tar output.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic view of the distributor of the present invention.
Fig. 3 is a top view of the distributor of the present invention.
Fig. 4 is a schematic view of the gas heating chamber of the present invention.
The reference numerals have the following meanings: 1. a biomass particle bin; 2. a distributing device; 3. a gas heating chamber; 4. a pyrolysis chamber; 5. a gas burner; 6. a biochar discharge port; 7. a biochar discharging cavity; 8. a discharge port; 9. a drive device; 10. a cavity; 11. a smoke exhaust duct; 12. a pyrolysis gas delivery pipeline; 13. a gas cooler; 14. a gas discharge pipeline; 15. a compressor; 16. a fuel gas storage tank; 17. an air supply valve; 18. a gas supply line; 19. a material blocking scraping strip; 20. a spiral flue; 21. a distributing pipe; 22. an inclined slope surface; 23. a material conical tip baffle; 24. a rotating shaft; 25. the motor is driven.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and the following detailed description.
As shown in fig. 1-4, a biomass pyrolysis and comprehensive energy utilization device comprises a pyrolysis chamber 4, a gas heating chamber 3 integrated with the pyrolysis chamber 4 is arranged outside the pyrolysis chamber 4, a gas burner 5 is arranged on the side of the gas heating chamber 3, a spiral flue 20 is arranged on the inner side of the upper portion of the gas heating chamber 3, and the top of the spiral flue 20 is connected with a smoke exhaust pipe 11 arranged on the top of the gas heating chamber 3. The pyrolysis chamber 4 is provided with a temperature sensor which is connected with an electric valve arranged on the gas burner 5 through a controller, and the electric valve can be controlled by a Siemens S71200 series PLC controller.
The bottom of the pyrolysis chamber 4 is provided with a distributing device which comprises a rotatable distributor arranged at the bottom of the pyrolysis chamber 4. The bottom of the pyrolysis chamber 4 is provided with an inclined slope surface 22 integrated with the pyrolysis chamber 4, the distributor 2 comprises a rotatable material cone-point baffle 23 arranged at the top of the inclined slope surface 22, and the bottom of the material cone-point baffle 23 can be provided with a ball at the contact part of the top of the inclined slope surface 22 to ensure flexible rotation. (namely, the bottom of the cone-tip baffle 23 is provided with a ball, the top of the inclined slope surface 22 is provided with a chute matched with the ball along the circumference), the top of the inclined slope surface 22 is uniformly provided with a plurality of material blocking scraping strips 19 matched with the inclined slope surface 22 along the circumferential direction, and the end part of each material blocking scraping strip 19 is fixed with the periphery of the lower part of the material cone-tip baffle 23.
The bottom of the material conical tip baffle 23 is fixed with a rotating shaft 24 which is integrated with the material conical tip baffle 23, and the rotating shaft 24 is connected with a driving device 9 after penetrating through a shaft hole arranged on the inclined slope surface 22.
The driving device 9 is a high-temperature-resistant driving motor 25, the driving motor 25 is installed at the bottom of the pyrolysis chamber 4 in the cavity 10 through a connecting frame and fastening bolts, the shaft end of a driving shaft of the driving motor 25 is installed in a matched mode with a bearing seat fixed at the bottom of the pyrolysis chamber 4, a driving gear is further fixedly installed on the driving shaft of the driving motor 25, and the driving gear is matched with a driven gear fixedly installed on the rotating shaft 24.
The bottom of pyrolysis chamber 4 is equipped with biological charcoal bin outlet 6 promptly on the edge one side of slope surface 22, and the bottom below of pyrolysis chamber 4 is equipped with cavity 10, is equipped with drive arrangement 9 in the cavity 10, and one side of cavity 10 is equipped with biological charcoal ejection of compact chamber 7, and the top of biological charcoal ejection of compact chamber 7 link up with biological charcoal bin outlet 6, and the bottom of biological charcoal ejection of compact chamber 7 is equipped with discharge gate 8. The other side of the cavity 10 is the lower part of the gas heating chamber 3. The bottom of the cavity 10 is provided with a support plate. Fixed welding in top of pyrolysis chamber 4 is equipped with living beings granule feed bin 1, the bottom of living beings granule feed bin 1 is equipped with cloth pipe 21, cloth pipe 21 stretches into pyrolysis chamber 4 inner lower part, the top of pyrolysis chamber 4 still is equipped with pyrolysis gas conveying pipeline 12, pyrolysis gas conveying pipeline 12 is connected with tar recovery unit, tar recovery unit is connected with gas ejection of compact pipeline 14, gas ejection of compact pipeline 14 is connected with compressor 15, compressor 15 is connected with gas storage tank 16, tar recovery unit is gas cooler 13. Valves can be correspondingly arranged on each pipeline.
The process of biomass pyrolysis includes a drying process, a pyrolysis reaction, and a reduction reaction. In the drying process, the biomass enters a gasification furnace hopper, the temperature is raised in a feeding pipe to separate out surface moisture, and the drying stage is carried out at 200-300 ℃. The pyrolysis reaction starts when the temperature rises to above 300 ℃, and about 70% of volatile components can be released from the biomass at 200-300 ℃, wherein the volatile components mainly comprise water vapor, hydrogen, carbon monoxide, methane, tar and other hydrocarbons. Oxygen does not exist in the reduction process, and combustion products and water vapor in the oxidation layer react with charcoal in the reduction layer to generate hydrogen, carbon monoxide and the like. These gases and volatile components constitute a combustible gas.
The during operation, distribute the living beings cloth in the living beings granule feed bin 1 to the pyrolysis chamber 4 bottom through distributing pipe 21 on slope surface 22 that inclines promptly, transmission shaft 24 passes through driving motor 25's drive shaft drive, it rotates to drive material awl point baffle 23 and keep off the integrative of material scraping strip 19, living beings are followed slope surface 22 after distributing pipe 21 cloth and are scattered to the edge in by the pyrolysis, and set up material awl point baffle 23 at slope surface 22's central top and can make the material that falls on slope surface 22 disperse all around, and it scrapes strip 19 rotation to drive to keep off the material, make the material flow out from the charcoal bin outlet 6 after being scraped and rotating the decomposition.
A gas nozzle valve of the gas heating chamber 3 is opened to ensure that enough temperature is provided in the gas heating chamber 3, smoke generated in the gas heating chamber 3 enters a smoke exhaust pipeline 17 along a spiral flue 20 and is exhausted after being processed to reach the standard, and the material blocking scraping strips 19 enable biomass to be decomposed to generate gas and biochar in the process of driving rotation of a driving motor 25; after the biochar discharge opening 6 is discharged, the biochar is discharged from the biochar discharge cavity 7 through the discharge opening 8 and collected, synthetic biogas generated by pyrolysis is conveyed to the gas cooler 13 through the pyrolysis gas conveying pipeline 12, the gas is cooled, and contained tar is condensed. The cooled synthetic fuel gas is compressed by a compressor 15 and then is delivered to a gas storage tank 16 for storage. And the compressor 15 compresses the gas to 0.3Mpa for the user to use.
The utility model discloses can effectively acquire biological charcoal and biological tar. The biomass particles are placed in an anoxic state at a high temperature of 500 to 600 ℃ for controlled pyrolysis thereof. Besides the biochar, the high-temperature decomposition can also generate products such as synthetic natural gas, liquid tar and the like, the synthetic weather product can be used as a fuel for power generation or heating, and the liquid biological tar can be used for refining automobile fuel oil or mineral dressing reagents; biochar is a high quality soil improvement additive.

Claims (9)

1. The utility model provides a comprehensive energy utilization device of biomass pyrolysis, includes pyrolysis chamber (4), characterized by: the outside of pyrolysis chamber (4) is equipped with gas heating chamber (3), the distributing device is equipped with to the bottom of pyrolysis chamber (4), and bottom one side of pyrolysis chamber (4) is equipped with biochar bin outlet (6), biomass particles feed bin (1) is equipped with at the top of pyrolysis chamber (4), the bottom of biomass particles feed bin (1) is equipped with distributing pipe (21), lower part in pyrolysis chamber (4) is stretched into in distributing pipe (21), the top of pyrolysis chamber (4) still is equipped with pyrolysis gas conveying pipeline (12), pyrolysis gas conveying pipeline (12) are connected with tar recovery unit, tar recovery unit is connected with gas ejection of compact pipeline (14), gas ejection of compact pipeline (14) are connected with compressor (15), compressor (15) are connected with gas storage tank (16).
2. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 1, wherein: the distributing device comprises a rotatable distributor (2) arranged at the bottom of the pyrolysis chamber (4).
3. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 2, wherein: pyrolysis chamber (4) bottom is equipped with slope surface (22), distributing device (2) are equipped with a plurality ofly and the fender material of slope surface (22) looks adaptation scrapes strip (19) including setting up at the rotatable material awl point baffle (23) at slope surface (22) top along the circumferencial direction equipartition slope surface (22) top, and the tip of keeping off the material and scraping strip (19) is fixed with the lower part of material awl point baffle (23).
4. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 3, wherein: the bottom of the material conical tip baffle (23) is fixedly provided with a rotating shaft (24), and the rotating shaft (24) is connected with a driving device (9) after penetrating through a shaft hole formed in the inclined slope surface (22).
5. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 2 or 4, wherein: the bottom below of pyrolysis chamber (4) is equipped with cavity (10), is equipped with drive arrangement (9) in cavity (10), and one side of cavity (10) is equipped with biochar unloading chamber (7), and the top and the biochar bin outlet (6) of biochar unloading chamber (7) link up, and the bottom of biochar unloading chamber (7) is equipped with discharge gate (8).
6. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 5, wherein: the side part of the gas heating chamber (3) is provided with a gas burner (5), the upper part of the gas heating chamber (3) is provided with a spiral flue (20), and the top of the spiral flue (20) is connected with a smoke exhaust pipeline (11) arranged at the top of the gas heating chamber (3).
7. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 6, wherein: the tar recovery device is a fuel gas cooler (13).
8. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 5, wherein: drive arrangement (9) are driving motor (25), and driving motor (25) pass through link and bolt and install the bottom in cavity (10) pyrolysis chamber (4), and the axle head of driving motor (25) drive shaft and the bearing frame cooperation installation of fixing pyrolysis chamber (4) bottom still fixedly are equipped with drive gear in the drive shaft of driving motor (25), and drive gear and the driven gear cooperation of fixed mounting on axis of rotation (24).
9. The biomass pyrolysis comprehensive energy utilization device as claimed in claim 8, wherein: and a temperature sensor is arranged on the pyrolysis chamber (4), and the temperature sensor is connected with an electric valve arranged on the gas burner (5) through a controller.
CN202020096374.9U 2020-01-16 2020-01-16 Biomass pyrolysis and comprehensive energy utilization device Active CN212404019U (en)

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Application Number Priority Date Filing Date Title
CN202020096374.9U CN212404019U (en) 2020-01-16 2020-01-16 Biomass pyrolysis and comprehensive energy utilization device

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Publication Number Publication Date
CN212404019U true CN212404019U (en) 2021-01-26

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