CN110747010A - Self-produced gas combustion linkage type pyrolysis gasification device - Google Patents

Self-produced gas combustion linkage type pyrolysis gasification device Download PDF

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Publication number
CN110747010A
CN110747010A CN201911198350.2A CN201911198350A CN110747010A CN 110747010 A CN110747010 A CN 110747010A CN 201911198350 A CN201911198350 A CN 201911198350A CN 110747010 A CN110747010 A CN 110747010A
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CN
China
Prior art keywords
gas
furnace
pyrolysis
self
pyrolysis furnace
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CN201911198350.2A
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Chinese (zh)
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苏钰杰
赵廷林
关树义
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North China University of Water Resources and Electric Power
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North China University of Water Resources and Electric Power
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Priority to CN201911198350.2A priority Critical patent/CN110747010A/en
Publication of CN110747010A publication Critical patent/CN110747010A/en
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07—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
    • C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C5/00—Production of pyroligneous acid distillation of wood, dry distillation of organic waste
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/12—Heating the gasifier
    • C10J2300/1223—Heating the gasifier by burners
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics

Abstract

The invention discloses a combustion linkage type pyrolysis gasification device for self-produced gas, which comprises a pyrolysis furnace, wherein a fire grate is arranged in the pyrolysis furnace, the fire grate is an active fire grate, a feed inlet is formed in the position of the pyrolysis furnace above the fire grate, a closed feeder is arranged at the position of the feed inlet, a discharge outlet is formed in the position of the pyrolysis furnace below the fire grate, and a closed discharger is arranged at the position of the discharge outlet; the pyrolysis furnace is internally provided with a combustible gas collector which is led out to the outside of the pyrolysis furnace through a fuel gas collecting pipeline; a feedback branch pipe is connected to the upper side of the fuel gas collecting pipeline and is connected with an input pipeline of the oxygen-free medium temperature gas source mechanism. The invention realizes that the self-produced gas is burnt to supply oxygen-free medium-temperature flue gas to the pyrolysis furnace, and a medium-temperature field is formed in the pyrolysis furnace, so that the precipitation temperature can be effectively controlled.

Description

Self-produced gas combustion linkage type pyrolysis gasification device
Technical Field
The invention relates to the technical field of biomass pyrolysis, in particular to a self-produced gas combustion linkage type pyrolysis gasification device.
Background
The gasification of biomass is a process of subjecting high polymers of biomass to pyrolysis, oxidation, reduction and reforming reactions under certain thermodynamic conditions by the action of air (or oxygen) and steam, and finally converting the high polymers into combustible gases such as carbon monoxide, hydrogen and low molecular hydrocarbons.
The key point of biomass gasification is a gasification furnace, and the gasification furnaces used at present have an updraft type, a downdraft type, an open type, a fluidized bed and the like. The reaction processes of different biomasses are also different, and the reaction of a common gasification furnace can be divided into an oxidation layer, a reduction layer, a cracking layer and a drying layer:
1) an oxide layer; the main reaction of the biomass in the oxidation layer is an oxidation reaction, a gasifying agent is introduced from the lower part of the grate, absorbs heat through an ash layer and then enters the oxidation layer, and a combustion reaction is carried out through high-temperature carbon to generate a large amount of carbon dioxide and release heat at the same time, wherein the temperature can reach 1000-1300 ℃; the combustion in the oxide layer is exothermic reaction, and the reaction heat provides a heat source for the reduction reaction of the reduction layer, and the cracking and drying of the materials.
2) A reduction layer; carbon dioxide and carbon generated in the oxide layer undergo a reduction reaction with water vapor.
3) A cracking layer; the hot gas generated by the oxidation layer and the reduction layer passes through the cracking layer in the ascending process to heat the biomass, so that the biomass in the cracking zone is subjected to cracking reaction.
4) And drying the layer. The gas products passing through the oxidation layer, the reduction layer and the cracking layer rise to the zone, the biomass raw material is heated, water in the raw material is evaporated, heat is absorbed, the generated temperature is reduced, the outlet temperature of the biomass gasification furnace is generally 100-300 DEG C
The oxidation layer and the reduction layer are collectively called as a gasification zone, and the gasification reaction is mainly carried out in the gasification zone; the pyrolysis zone and the drying zone are collectively referred to as a fuel preparation zone.
The invention discloses a composite biomass graded gasification furnace, which comprises a furnace body, wherein a grate is fixed on the side wall below the inner part of the furnace body, a furnace slag cavity is arranged in the space below the grate, an ash discharge port is arranged on the side wall of the furnace body corresponding to the position of the furnace slag cavity, a filter screen is also fixed on the inner wall of the furnace body, the filter screen is positioned above the grate and forms a pyrolysis cavity with the grate, a fine filter is fixed on the top wall inside the furnace body, a feeding mechanism is fixed on the outer side of the furnace body, a primary filter mechanism is fixed on the feeding mechanism, the primary filter mechanism is connected with the feeding mechanism through a feeding pipe, and the primary filter mechanism is respectively connected with the upper part of the side wall of the furnace body and the fine filter mechanism.
The invention discloses a downdraft carbon gas co-production gasifier with the main structure of CN110452736A, which comprises a feed hopper, a feed bin, a gasification reaction chamber, a double-section bucket-shaped water cooling sleeve, a turnover grate and a settling chamber from top to bottom, wherein a carbon discharging auger is arranged at the bottom of the settling chamber, a bucket-shaped material pulling disc is arranged on the inner side of the lower part of the feed bin, and a bucket-shaped ash disc is superposed on the inner side of the upper part of the double-section bucket-shaped water cooling sleeve; firstly, carrying out pyrolysis gasification reaction on the biomass fuel in a gasification reaction chamber to generate fuel gas, and discharging the fuel gas downwards from a fuel gas outlet on the side wall of a settling chamber; the biomass fuel which is not completely reacted in the gasification reaction chamber to generate fuel gas is carbonized, then falls into the settling chamber and is cooled to form biomass carbon, so that the biomass fuel can simultaneously realize carbon gas co-production.
The invention provides, as in publication No. CN107083257B, a biomass gasification system comprising: the gasification furnace comprises a furnace body and a blanking pipeline, wherein the furnace body comprises an air outlet, a grate and a feed inlet, the air outlet is formed in the side wall of the furnace body, the grate is arranged at the bottom of the furnace body and provided with an air inlet, and the blanking pipeline is arranged at the top end of the furnace body corresponding to the feed inlet; the feeding device comprises a storage bin, a feeding pipeline, a material shifting mechanism, a first sealing door, a second sealing door and a sealing assembly, wherein the feeding pipeline is arranged at the top of the storage bin; the sealing assembly comprises a water tank arranged on the storage bin, a channel used for passing through the driving rod is arranged in the water tank, the channel is tubular, and the sealing cover covers the channel.
The technical scheme adopts a conventional gasification furnace arrangement form of an oxidation layer, a reduction layer, a cracking layer and a drying layer, but in application, the gasification agent generally adopts oxygen-containing normal-temperature air which is introduced into a gasification zone from the lower part of a grate, so that the combustion reaction is not well controlled, the temperature is often too high to exceed the optimal separation temperature of combustible gas separated from biomass, and the separation effect of the combustible gas is finally influenced; and the gas of conventional gasifier is derived and is needed high-power fan cooperation, realizes constantly taking out, and the energy consumption is great.
Disclosure of Invention
The invention aims to provide a self-produced gas combustion linkage type pyrolysis gasification device.
In order to solve the technical problems, the invention adopts the following technical scheme:
a self-produced gas combustion linkage type pyrolysis gasification device comprises a pyrolysis furnace, a fire grate is arranged in the pyrolysis furnace, a feed inlet is arranged at the position of the pyrolysis furnace above the fire grate, a closed feeder is arranged at the position of the feed inlet, a discharge outlet is arranged at the position of the pyrolysis furnace below the fire grate, a closed discharger is arranged at the position of the discharge outlet,
the fire grate is an active fire grate and comprises a plurality of furnace rollers which are horizontally arranged side by side, the furnace rollers are adjacent to each other and are in a group, and the two furnace rollers in the same group alternately rotate in opposite directions and rotate in opposite directions;
the device also comprises an anaerobic medium-temperature gas source mechanism which is arranged outside the pyrolysis furnace and supplies flue gas to the pyrolysis furnace, wherein the anaerobic medium-temperature gas source mechanism comprises a combustor, an inlet of the combustor is connected with an input pipeline for supplying fuel gas to the combustor, the fuel gas is combusted in the combustor to produce the flue gas, an outlet of the combustor is connected with a flue gas output pipeline, and a flue gas conveying pipeline is introduced into the pyrolysis furnace;
the pyrolysis furnace is internally provided with a combustible gas collector which is led out to the outside of the pyrolysis furnace through a fuel gas collecting pipeline;
a feedback branch pipe is connected beside the fuel gas collecting pipeline and is connected with an input pipeline of the oxygen-free medium temperature gas source mechanism, and a feedback control valve is arranged on the feedback branch pipe.
A gas heat value detector is arranged at the tail end of the gas collecting pipeline, a signal output end of the gas heat value detector is connected with the control module, and a signal output end of the control module is connected with the active grate and the closed feeder.
And the gas collecting pipeline is sequentially connected with a dust remover, a cooler and a conveying fan.
And a collecting control valve is arranged at the downstream of the connecting point of the return branch pipe of the fuel gas collecting pipeline.
The combustor is connected with an air supply fan.
The surface of the furnace roller is provided with material poking teeth along the circumferential direction.
The closed feeder comprises a feeding cylinder connected with a feeding port, the cross section of the feeding cylinder is of a rectangular structure, two feeding rollers which are horizontally arranged are arranged in the feeding cylinder in an up-and-down overlapping mode, the feeding rollers are matched with the feeding cylinder in a sealing mode, and the feeding rollers are circumferentially arranged to form a trough which axially extends.
The closed discharging device is a screw conveyer which is connected with the discharging opening and is horizontally arranged.
A distributor is arranged below the feed inlet in the pyrolysis furnace.
The temperature of the flue gas generated by combustion in the combustor is 570-600 ℃.
The invention has the beneficial effects that:
1. the invention provides an oxygen-free medium-temperature heat source for the pyrolysis furnace by using the medium-temperature flue gas which is generated by the burner and has the temperature of about 570-600 ℃, and a medium-temperature (570-600 ℃) temperature field is formed in the pyrolysis furnace, so that the separation temperature can be effectively controlled, the biomass in the pyrolysis furnace is ensured to be at the optimal separation temperature for separating out the combustible gas, and the separation effect of the combustible gas is further ensured. Because the temperature field formed in the pyrolysis furnace is medium temperature (570-600 ℃), the temperature of separated combustible gas is relatively low, and the difficulty of subsequent temperature reduction treatment is reduced.
Under the action of the suction force of the combustible gas collector, the raw materials are gradually subjected to anaerobic medium-temperature pyrolysis to separate out volatile components of the combustible gas, and simultaneously separated out fuel gas enters a fuel gas collecting pipeline from the combustible gas collector under the suction force of a conveying fan and is discharged to the outside of the pyrolysis furnace, and dust removal and temperature reduction treatment are sequentially carried out.
And because the pyrolysis is a boosting process, the requirement on the pumping power of the conveying fan is low, the energy consumption is reduced, and the working efficiency is improved. Meanwhile, the pumping power of the conveying fan is low, less dust is brought out when separated combustible gas is discharged outwards, and the difficulty of subsequent purification treatment is reduced.
Meanwhile, because the pyrolysis furnace is provided with an oxygen-free medium-temperature heat source, carbon in the biomass does not participate in the reaction, the heat value of the separated combustible gas is higher, and the furnace slag after the separation of the combustible gas is carbon furnace slag, falls to a discharge port through a furnace grate, is discharged through a closed type discharging device and can be reused.
2. According to the invention, the feedback branch pipe is connected to the side of the fuel gas collecting pipeline and is connected with the input pipeline of the anaerobic medium-temperature gas source mechanism, and the feedback control valve is arranged on the feedback branch pipe.
3. A gas heat value detector is arranged at the tail end of a gas collecting pipeline, a signal output end of the gas heat value detector is connected with a control module, a signal output end of the control module is connected with an active fire grate and a closed feeder, the combustible gas heat value in the gas collecting pipeline can be detected by the gas heat value detector, if the heat value level is reduced, the active fire grate is controlled to discharge slag to a discharge opening, and the closed feeder is controlled to feed new materials.
4. The grate adopts an active grate which comprises a plurality of horizontally arranged furnace rollers side by side, wherein the furnace rollers are adjacent to each other and are in a group, and the furnace rollers alternately rotate in opposite directions and back to back in time, so that active discharging can be realized, and the uniformity of discharging is ensured.
5. According to the invention, the feed inlet is provided with the closed feeder, and the discharge outlet is provided with the closed discharge device, so that the sealing effect in the pyrolysis furnace is ensured.
6. The gas collecting pipeline is provided with the cooler, the cooler is provided with a plurality of stages, the multistage coolers are sequentially connected in series on the gas collecting pipeline to form a multistage cooling mechanism, the gas is cooled by the cooler to obtain combustible gas which is dried at about 80 ℃ for later use, and chemical substances in the combustible gas are dissolved in liquid in the cooling process to form chemical products such as pyroligneous liquor and the like.
Drawings
FIG. 1 is a schematic diagram of a first embodiment of the present invention;
FIG. 2 is a schematic view of a closed feeder according to an embodiment of the present invention;
FIG. 3 is a schematic view of the active grates being rotated in opposite directions according to one embodiment of the present invention;
FIG. 4 is a schematic view of an active grate in an opposite rotation in accordance with one embodiment of the present invention;
FIG. 5 is a schematic view of a second embodiment of the present invention;
fig. 6 is a schematic diagram of a third embodiment of the present invention.
Detailed Description
The following detailed description of embodiments of the invention refers to the accompanying drawings.
The first embodiment is as follows:
as shown in fig. 1, the anaerobic intermediate temperature downdraft pyrolysis device of the present invention comprises a pyrolysis furnace 1, wherein a grate 2 is arranged in the pyrolysis furnace 1, a feed inlet is arranged at the position of the pyrolysis furnace 1 above the grate 2, a closed feeder 3 is arranged at the feed inlet, a slag bin 4 is formed at the position of the pyrolysis furnace 1 below the grate 2, a discharge outlet is arranged downward at the slag bin, and a closed discharger 5 is arranged at the discharge outlet.
As shown in fig. 2, in this embodiment, the closed feeder 3 includes a feeding cylinder 31 connected to the feeding port, the cross section of the feeding cylinder 31 is a rectangular structure, two feeding rollers 32 horizontally arranged are tangentially arranged in the feeding cylinder 31 up and down, the feeding rollers 32 are matched with the feeding cylinder 31 and are in sealing fit, axially extending troughs 33 are arranged on the feeding rollers 31 along the circumferential direction, and the feeding cylinder 31 is connected to a feeding hopper 34 upward, so as to realize closed feeding. A distributor 35 is arranged below the feed inlet in the pyrolysis furnace 1 to realize uniform distribution.
In this embodiment, the closed discharging device 5 is a screw conveyor connected to the discharge opening and horizontally arranged.
The closed feeder 3 and the closed discharging device 4 are matched, so that the sealing effect in the pyrolysis furnace is ensured.
As shown in fig. 3 and 4, the grate 2 is an active grate, and includes a plurality of furnace rollers horizontally arranged side by side, the surfaces of the furnace rollers 21 are circumferentially arranged with material-poking teeth 22, the furnace rollers 21 are adjacent in pairs and in one group, and two furnace rollers in the same group are alternately rotated in opposite directions and back to back in time.
Taking six furnace rollers as an example for explanation, the furnace rollers are divided into three groups and form five discharging gaps, when the two furnace rollers rotate oppositely, the first, third and fifth discharging gaps discharge materials downwards, and the second and fourth discharging gaps turn materials upwards; when the two furnace rollers rotate oppositely, the first, third and fifth discharging gaps turn upwards, and the second and fourth discharging gaps discharge downwards, so that active discharging is realized, and the uniformity of discharging is ensured.
The invention also comprises an anaerobic medium-temperature gas source mechanism which is arranged outside the pyrolysis furnace 1 and supplies flue gas to the pyrolysis furnace 1, wherein the anaerobic medium-temperature gas source mechanism comprises a combustor 6, an inlet of the combustor 6 is connected with an input pipeline 61 for supplying fuel gas to the combustor 6, and the combustor is also connected with an air supply fan 63. The gas is burnt in the burner 6 to produce oxygen-free medium-temperature flue gas (the flue gas temperature is 570-600 ℃, preferably about 600 ℃), the outlet of the burner 6 is connected with a flue gas output pipeline 62, and the flue gas transmission pipeline 62 is led into the pyrolysis furnace.
The pyrolysis furnace 1 is also provided with a combustible gas collector 7, the combustible gas collector 7 is led out of the pyrolysis furnace 1 through a fuel gas collecting pipeline 71, and the fuel gas collecting pipeline is sequentially connected with a dust remover 8, a cooler 9 and a conveying fan 10. The separated fuel gas enters the fuel gas collecting pipeline 71 from the fuel gas collector 7 under the suction force of the conveying fan 10 and is discharged to the outside of the pyrolysis furnace 1, and dust removal and temperature reduction treatment are sequentially carried out.
In this embodiment, the cooler 9 is the shell and tube cooler, and the cooler 9 is equipped with the level four, and the level four cooler establishes ties in proper order and forms multistage cooling mechanism on the gas collecting pipe way.
The gas collecting pipeline 71 is connected with a feedback branch pipe 12 by the side, the feedback branch pipe 12 is connected with an input pipeline 61 of the oxygen-free medium temperature gas source mechanism, a feedback control valve 13 is arranged on the feedback branch pipe 12, the gas collecting pipeline 71 is provided with a collecting control valve 14 at the downstream of the connection point of the feedback branch pipe 12, through the design, the combustible gas part collected into the gas collecting pipeline 71 is conveyed to the input pipeline 61 for supplying gas to a burner through the feedback branch pipe 12, and the self-produced gas is combusted to supply oxygen-free medium temperature flue gas to the pyrolysis furnace.
And a gas heat value detector 15 is arranged at the tail end of the gas collecting pipeline, the signal output end of the gas heat value detector 15 is connected with the control module, the signal output end of the control module is connected with the active fire grate and the closed feeder 3, the combustible gas heat value in the gas collecting pipeline 71 can be detected through the gas heat value detector 15, if the heat value level is reduced, the active fire grate is controlled to discharge slag to a discharge opening, and the closed feeder 3 is controlled to feed new materials.
The working principle of the invention is as follows: biomass material (refuse, sludge, rubber, etc.) is fed into the pyrolysis furnace 1 by a closed feeder 3, forming a bed indicator as shown at 11 in fig. 1.
The anaerobic middle-temperature flue gas generated by the combustor 6 and with the temperature of about 570-600 ℃ provides an anaerobic middle-temperature heat source for the pyrolysis furnace 1, and a middle-temperature (570-600 ℃) temperature field is formed in the pyrolysis furnace 1, so that the precipitation temperature can be effectively controlled, the biomass in the pyrolysis furnace is ensured to be at the optimal precipitation temperature for precipitating combustible gas, and the precipitation effect of the combustible gas is further ensured. Because a medium-temperature (570-600 ℃) temperature field is formed in the pyrolysis furnace 1, the temperature of the separated combustible gas is relatively low (about 300 ℃), and the difficulty of subsequent temperature reduction treatment is reduced.
Under the action of the suction force of the combustible gas collector 7, the raw materials are gradually subjected to anaerobic medium-temperature pyrolysis to separate out combustible gas volatile matters, and simultaneously separated out fuel gas enters a fuel gas collecting pipeline 71 from the combustible gas collector 7 under the suction force of the conveying fan 10 and is discharged to the outside of the pyrolysis furnace 1, and dust removal and temperature reduction treatment are sequentially carried out. The separated gas is cooled by a cooler 9 to obtain dry combustible gas at about 80 ℃ for later use, and chemical substances in the combustible gas are dissolved in the liquid in the cooling process to form chemical products such as pyroligneous liquor and the like.
And because the pyrolysis is the process of boosting, the requirement on the suction power of the conveying fan 10 is low, the energy consumption is reduced, and the working efficiency is improved. Meanwhile, the pumping power of the conveying fan is low, less dust is brought out when separated combustible gas is discharged outwards, and the difficulty of subsequent purification treatment is reduced.
And because the pyrolysis furnace 1 is provided with an oxygen-free medium-temperature heat source, carbon in the biomass does not participate in the reaction, the heat value of the separated combustible gas is higher, and the furnace slag after the separation of the combustible gas is carbon furnace slag, falls to a discharge port through a furnace grate, is discharged through a closed type discharging device 5 and can be reused.
The invention is completely different from the arrangement form and principle of the conventional gasification furnace, effectively ensures that the biomass in the pyrolysis furnace is at the optimal separation temperature for separating out the combustible gas, further ensures the separation effect of the combustible gas and realizes the comprehensive recycling treatment.
In the embodiment, a downdraft structure is adopted, the flue gas conveying pipe 62 is located above the grate 2 and adjacent to the top of the pyrolysis furnace 1, and preferably, the tail end of the flue gas conveying pipe 62 is located below the indication line 11 at the top of the material layer in the pyrolysis furnace 1. The combustible gas collector 7 is located below the grate 2.
Example two:
the difference between the present embodiment and the first embodiment is: as shown in fig. 5, the embodiment adopts an updraft structure, the flue gas conveying pipe 62 is located below the fire grate 2, and the end of the flue gas conveying pipe 62 is directed upward to the fire grate 2 and is connected with a medium temperature heater 64.
In this embodiment, the medium temperature heat supply device 64 is a cone structure communicated with the end of the flue gas conveying pipeline, the tip of the cone also points upwards to the fire grate, and the side wall of the cone is provided with an exhaust port, so that the uniform supply of the oxygen-free medium temperature flue gas in the pyrolysis furnace 1 is realized, and the uniformity of the medium temperature field formed in the pyrolysis furnace 1 is ensured.
The combustible gas collector 7 is provided with a combustible gas collecting opening which is positioned above the fire grate and adjacent to the top of the pyrolysis furnace. In this embodiment, the combustible gas collection port is located above the indication line 11 at the top of the charge bed in the pyrolysis furnace 1.
Example three:
the difference between the present embodiment and the first embodiment is: as shown in fig. 6, the present embodiment adopts a side draft structure, the flue gas conveying pipe 62 is located below the fire grate 2, and the end of the flue gas conveying pipe 62 is directed upward toward the fire grate 2 and connected with a medium temperature heater 64.
In this embodiment, the medium temperature heat supply device 64 is a cone structure communicated with the end of the flue gas conveying pipeline, the tip of the cone also points upwards to the fire grate, and the side wall of the cone is provided with an exhaust port, so that the uniform supply of the oxygen-free medium temperature flue gas in the pyrolysis furnace 1 is realized, and the uniformity of the medium temperature field formed in the pyrolysis furnace 1 is ensured.
The combustible gas collector 7 is provided with a combustible gas collecting mechanism at the side wall above the fire grate. Combustible gas collection mechanism includes the gas vent that sets up at pyrolysis oven middle part lateral wall, and the gas vent is located pyrolysis oven 1 middle material layer top indicator line 11's top in this embodiment. The exhaust port encircles the pyrolysis oven and arranges and form the exhaust area, and the outside in exhaust area is encircleed to be equipped with the collection cover 72 with its parcel, collects cover 72 and pyrolysis oven 1 sealed fixed, collects the intussuseption of cover 72 and is filled with granule filler 73, collects cover 72 and outwards is connected with gas collection pipeline 71. Adopt above-mentioned structure, the combustible gas volatile that raw materials in the pyrolysis oven 1 were analyzed out is siphoned away by the gas vent of direct follow pyrolysis oven 1 middle part lateral wall, has optimized the combustible gas by the inside outside exhaust route of pyrolysis oven, avoids combustible gas to form the gas pocket and the explosion risk that leads to in the pyrolysis oven.
Meanwhile, as the collecting cover 72 is filled with the particle filler 73, the particle filler 73 is preferably vermiculite, gaps are formed among the particle fillers 73, and the combustible gas enters the particle fillers and then travels along the gaps, so that dust in the combustible gas is absorbed by the particle fillers as much as possible.
Although the present invention has been described in detail with reference to the above embodiments, it should be understood by those skilled in the art that: modifications and equivalents may be made thereto without departing from the spirit and scope of the invention and it is intended to cover in the claims the invention as defined in the appended claims.
In the description of the present invention, it is to be understood that the terms "front", "rear", "upper", "lower", "left", "right", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the scope of the present invention.

Claims (10)

1. The utility model provides a from producing gas combustion coordinated type pyrolysis gasification equipment, includes the pyrolysis oven, is provided with the grate in the pyrolysis oven, and the pyrolysis oven department of grate top is equipped with the feed inlet, and feed inlet department sets closed feeder, and pyrolysis oven department of grate below is equipped with the bin outlet, and the bin outlet department sets closed discharger, its characterized in that:
the fire grate is an active fire grate and comprises a plurality of furnace rollers which are horizontally arranged side by side, the furnace rollers are adjacent to each other and are in a group, and the two furnace rollers in the same group alternately rotate in opposite directions and rotate in opposite directions;
the device also comprises an anaerobic medium-temperature gas source mechanism which is arranged outside the pyrolysis furnace and supplies flue gas to the pyrolysis furnace, wherein the anaerobic medium-temperature gas source mechanism comprises a combustor, an inlet of the combustor is connected with an input pipeline for supplying fuel gas to the combustor, the fuel gas is combusted in the combustor to produce the flue gas, an outlet of the combustor is connected with a flue gas output pipeline, and a flue gas conveying pipeline is introduced into the pyrolysis furnace;
the pyrolysis furnace is internally provided with a combustible gas collector which is led out to the outside of the pyrolysis furnace through a fuel gas collecting pipeline;
a feedback branch pipe is connected beside the fuel gas collecting pipeline and is connected with an input pipeline of the oxygen-free medium temperature gas source mechanism, and a feedback control valve is arranged on the feedback branch pipe.
2. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: a gas heat value detector is arranged at the tail end of the gas collecting pipeline, a signal output end of the gas heat value detector is connected with the control module, and a signal output end of the control module is connected with the active grate and the closed feeder.
3. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: and the gas collecting pipeline is sequentially connected with a dust remover, a cooler and a conveying fan.
4. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: and a collecting control valve is arranged at the downstream of the connecting point of the return branch pipe of the fuel gas collecting pipeline.
5. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: the combustor is connected with an air supply fan.
6. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: the surface of the furnace roller is provided with material poking teeth along the circumferential direction.
7. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: the closed feeder comprises a feeding cylinder connected with a feeding port, the cross section of the feeding cylinder is of a rectangular structure, two feeding rollers which are horizontally arranged are arranged in the feeding cylinder in an up-and-down overlapping mode, the feeding rollers are matched with the feeding cylinder in a sealing mode, and the feeding rollers are circumferentially arranged to form a trough which axially extends.
8. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: the closed discharging device is a screw conveyer which is connected with the discharging opening and is horizontally arranged.
9. The self-produced gas combustion linkage type pyrolysis gasification device according to claim 1, characterized in that: a distributor is arranged below the feed inlet in the pyrolysis furnace.
10. The self-produced gas combustion linkage type pyrolysis gasification device according to any one of claims 1 to 9, characterized in that: the temperature of the flue gas generated by combustion in the combustor is 570-600 ℃.
CN201911198350.2A 2019-11-29 2019-11-29 Self-produced gas combustion linkage type pyrolysis gasification device Pending CN110747010A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111679033A (en) * 2020-05-09 2020-09-18 东华大学 Device and method for detecting pyrolysis gas components of casting molding material
CN111753691A (en) * 2020-06-15 2020-10-09 上海电气集团股份有限公司 Method, equipment and system for detecting and controlling gasification furnace

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111679033A (en) * 2020-05-09 2020-09-18 东华大学 Device and method for detecting pyrolysis gas components of casting molding material
CN111753691A (en) * 2020-06-15 2020-10-09 上海电气集团股份有限公司 Method, equipment and system for detecting and controlling gasification furnace
CN111753691B (en) * 2020-06-15 2024-01-02 上海电气集团股份有限公司 Method, equipment and system for detecting and controlling gasification furnace

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