CN106957704A - Edible fungi residues thermoelectricity fertilizer co-generation system and technique - Google Patents
Edible fungi residues thermoelectricity fertilizer co-generation system and technique Download PDFInfo
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- CN106957704A CN106957704A CN201710303620.6A CN201710303620A CN106957704A CN 106957704 A CN106957704 A CN 106957704A CN 201710303620 A CN201710303620 A CN 201710303620A CN 106957704 A CN106957704 A CN 106957704A
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- thermoelectricity
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/445—Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G65/00—Loading or unloading
- B65G65/30—Methods or devices for filling or emptying bunkers, hoppers, tanks, or like containers, of interest apart from their use in particular chemical or physical processes or their application in particular machines, e.g. not covered by a single other subclass
- B65G65/34—Emptying devices
- B65G65/40—Devices for emptying otherwise than from the top
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G1/00—Mixtures of fertilisers belonging individually to different subclasses of C05
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
- C05G3/60—Biocides or preservatives, e.g. disinfectants, pesticides or herbicides; Pest repellants or attractants
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
- C05G3/80—Soil conditioners
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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
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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
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/10—Treating solid fuels to improve their combustion by using additives
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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
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1603—Integration of gasification processes with another plant or parts within the plant with gas treatment
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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
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1603—Integration of gasification processes with another plant or parts within the plant with gas treatment
- C10J2300/1606—Combustion processes
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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
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1671—Integration of gasification processes with another plant or parts within the plant with the production of electricity
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/02—Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
- C10L2200/0204—Metals or alloys
- C10L2200/0213—Group II metals: Be, Mg, Ca, Sr, Ba, Ra, Zn, Cd, Hg
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/02—Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
- C10L2200/0254—Oxygen containing compounds
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/02—Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
- C10L2200/0272—Silicon containing compounds
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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
- 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
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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
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Abstract
The invention discloses a kind of fertile co-generation system of edible fungi residues thermoelectricity, including be sequentially connected in series bacterium bag disintegrating machine, separator, cylindrical drier, the medium entrance of cylindrical drier is connected with hot-blast stove, it is characterised in that:The material outlet of cylindrical drier is connected by screw(-type) feeder and elevator with rotary discharge bin; the discharge gate of one additive conveying worm is also connected with the charging aperture of this screw(-type) feeder; rotary derivatived fuel comminutor, cooler, gasification furnace of the discharge bin again with rear is sequentially connected in series, and the outlet of gasification furnace is connected by decanter type clarifier, air-introduced machine with gas burning waste heat boiler;The invention also discloses a kind of fertile joint production process of edible fungi residues thermoelectricity;The present invention, which can be industrialized, handle in time bacteria residue, prevent the pollution to environment, and resource consumption is small, output object value is high, and realize continuous production and long-term normal operation, improve overall economic efficiency, the recycling of achievable bacteria residue.
Description
Technical field
The present invention relates to a kind of fertile co-generation system of thermoelectricity for edible fungi residues and technique.Edible fungi residues thermoelectricity fertilizer coproduction system
System and technique.
Background technology
Edible mushroom is only second to grain, cotton, oil, dish, fruit in China's agricultural economy, occupies the 6th, cultivates the bacterium of edible mushroom
Include the bacteria residue such as polybag and Qi Nei strain, powder of straw, peanut shell, corncob and cotton seed hull, be biomass, current bacterium
Field is arbitrarily deposited in more than slag, river levee, irrigation canals and ditches is poured over or even is burned, only Heilongjiang Province year bacteria residue amount is up to 100
Many ten thousand tons, immense pressure is brought to agricultural environment, causes the abnormal serious, quality of air environment of Rural Plane Source Pollution continuous worsening,
Industry faces the bottlenecks of " develop more, more pollute ";Because the average moisture content of bacteria residue is higher than 40%, such as it is used as biological organic
, it is necessary to which substantial amounts of nitrogen source organic matter makees dispensing during fertile base-material, a large amount of utilizations of bacteria residue are limited, when such as mushroom dreg feed raw material
Substantial amounts of feedstuff culture medium is also required to, resource consumption is big, and corresponding input cost is also higher, and overall economic efficiency is poor,
The recycling of bacteria residue can not be realized.
The content of the invention
The purpose of the present invention is that not enough there is provided a kind of fertile co-generation system of the thermoelectricity of edible fungi residues for prior art above-mentioned
And technique, it, which can be industrialized, handle in time bacteria residue, prevent the pollution to environment, and resource consumption is small, output object value is high, and in fact
Existing continuous production and long-term normal operation, improve overall economic efficiency, and the recycling of bacteria residue can be achieved.
In order to achieve the above object, the fertile co-generation system of edible fungi residues thermoelectricity of the invention, including the bacterium bag being sequentially connected in series are broken
Broken machine, separator, cylindrical drier, the medium entrance of cylindrical drier are connected with hot-blast stove, it is characterised in that:Drum-type
The material outlet of drying machine is connected by screw(-type) feeder and elevator with rotary discharge bin, an additive conveying worm
Discharge gate is also connected with the charging aperture of this screw(-type) feeder, rotary discharge bin derivatived fuel comminutor again with rear, cooling
Device, gasification furnace are sequentially connected in series, and the outlet of gasification furnace is connected by decanter type clarifier, air-introduced machine with gas burning waste heat boiler;
As the further improvement of said system, the slag-drip opening of the gasification furnace passes through carbon output machine and the ecological composite heat transfer of charcoal base
System feeding mouthful;Being easy to breeze is used for the preparation of the ecological composite fertilizer of follow-up charcoal base;
As the further improvement of said system, rotary discharge bin is connected with derivatived fuel comminutor by conveying worm,
Derivatived fuel comminutor is connected with cooler by elevator, and cooler passes through elevator, Bunker, helical feed with gasification furnace
Machine is connected;Material transfer efficiency can be improved, continuous production is realized;
As the further improvement of said system, rotary discharge bin includes fixation feed bin, the support being sequentially connected from top to bottom
And stationary hopper, hollow rotation distribution cabins, the top suit of rotation distribution cabins are provided between fixed feed bin and stationary hopper
Outside the bottom of fixed feed bin, the bottom of rotation distribution cabins is placed in stationary hopper, and canine tooth is fixedly connected with the outside of rotation distribution cabins
The little gear engaged with bull gear is associated with circle, the output shaft of a motor, in the lower surface of bull gear and the upper end of stationary hopper
Face is equipped with corresponding rolling groove, and several balls are placed in corresponding rolling groove, and the bottom centre in stationary hopper sets
There is material distributing cone, one piece is provided with rotation distribution cabins inwall provided with discharging opening with material distributing cone bias in stationary hopper bottom
Material scraping plate above;The smoothly blanking such as biomass material of lightweight can be made, be not in block, meanwhile, it is capable to realize uniform
The effect of blanking, it is ensured that the continuity of production;
As the further improvement of said system, annular groove is provided with the lower surface of the bull gear, the rolling groove of bull gear is located at
This annular groove;The upper surface of stationary hopper is located in this annular groove;Can be spacing to ball progress, prevent that it from coming off, it is ensured that normal work;
The present invention uses the fertile joint production process of the edible fungi residues thermoelectricity of said system, it is characterised in that comprise the following steps:1)Broken bag:
Waste mushroom packet input bacterium bag disintegrating machine is crushed, material includes plastic sheet and the bacteria residue particle of biomass after crushing;2)Sorting:
Broken material is sent into separator, plastic sheet is discharged, and bacteria residue particle is admitted to cylindrical drier;3)Dry:Bacteria residue
Grain is in cylindrical drier through heated-air drying, and its moisture content is less than 20%;4)Batch mixing:Bacteria residue particle is discharged into after screw(-type) feeder,
Mixed with the carbon sequestration additive added by additive conveying worm, carbon sequestration additive is 5-8% with the mass ratio of bacteria residue particle,
Carbon sequestration additive includes 50-60% diatomite, 20-30% calcium oxide and 15-20% magnesium slag, is quality percentage
Than, and the particle diameter of three kinds of components is 60-80 mesh;5)Granulation:By mixed bacteria residue particle and the feeding rotation of carbon sequestration additive
Formula discharge bin, enter after discharging and be extruded, granulate, obtained graininess derivatived fuel in derivatived fuel comminutor;6)Cooling:
Graininess derivatived fuel is sent to cooler and cooled down;7)Gasification:Graininess derivatived fuel is in gasification furnace at 600 DEG C -800
DEG C, air equivalent than under the micro-oxygen conditions between 0.18-0.25 be pyrolyzed, gasify, obtain the biomass fuel containing partial impurities
Gas, the breeze after burning is discharged by the slag-drip opening of gasification furnace;8)Purification:Biological fuel gas is sent sedimentation in the presence of air-introduced machine
In formula clarifier, abjection wood tar and pyrolkigneous liquid;9)Combustion power generation:Biological fuel gas burns into gas burning waste heat boiler after purification
After generate electricity;
The present invention need to only use a small amount of carbon sequestration additive to add in bacteria residue, and resource consumption is small, its suction of the diatomite in additive
Attached performance is strong, unit weight light, and fineness is uniform, and pH value neutrality is nontoxic, and mixing uniformity is good, can turn into concentrated fertilizer, promote crops
Growth, act in terms of improved soil, add that particle diameter is smaller, porosity is big, and absorption property is strong, the titanium dioxide in adsorbable combustion gas
Carbon, add calcium oxide and magnesium slag gasification when with the carbon dioxide reaction in combustion gas, can be by the dioxy in biological fuel gas
Change carbon component to be solidificated in breeze, greatly increase the content of carbon component in breeze, be the effective effectively sufficient using ensureing of breeze
Charcoal composition, as production charcoal base ecological fertilizer raw material, obtain high value output object, while reduce biological fuel gas burning
When CO2 emissions;During granulation, mixed material is extruded heating, can be further backing out moisture, its bulk density and energy
Metric density is also improved, and can improve gasification efficiency;Particle can be solidified during cooling, increase hardness, it is real in order to convey
Existing continuous production, while sloughing 3-5% moisture again;It is strict during gasification to control air equivalent ratio between 0.18-0.25,
The carbon content for making recrement after gasification while realizing production biological fuel gas is 30-60%, is the effective effective using ensureing of breeze
Sufficient charcoal composition, biological fuel gas contains the fuel gas such as hydrogen, carbon monoxide, methane;Deviate from wood tar and wood during purification
Vinegar liquid, can avoid a large amount of cokings during combustion power generation from having a strong impact on the heat exchange efficiency of boiler and normal operation, and prevent that moisture is high
Cause to damage big in boiler, realize the recycling of normal operation for a long time and bacteria residue;
One kind as the fertile joint production process of edible fungi residues thermoelectricity of the present invention is preferred, and its carbon content of the breeze produced in gasification process is
30-60%, it is used for the ecological compound fertilizer of production charcoal base, the flue gas of gas burning waste heat boiler is used to produce the dry of charcoal base ecological fertilizer
It is dry;Reduce thermal loss and improve overall economic efficiency;
One kind as the fertile joint production process of edible fungi residues thermoelectricity of the present invention is preferred, and wood tar and pyrolkigneous liquid quilt are deviate from cleaning procedure
Additive for producing the ecological composite fertilizer of charcoal base;Wood tar and pyrolkigneous liquid can make plant nutrient regulation auxin, have to plant
Effect is grown, desinsection is splendid, be conducive to granulating and forming to act on again as the ecological fertilizer additive of charcoal base, the growth factor in pyrolkigneous liquid
There is regulation to promote the function of plant growth;
In summary, the present invention, which can be industrialized, handle in time bacteria residue, prevent the pollution to environment, and resource consumption is small, output object
Value is high, and realizes continuous production and long-term normal operation, improves overall economic efficiency, the recycling of bacteria residue can be achieved
Utilize.
Brief description of the drawings
Fig. 1 is the structure diagram of the fertile co-generation system embodiment of edible fungi residues thermoelectricity of the present invention.
Fig. 2 is the front view of rotary discharge bin in Fig. 1.
Fig. 3 is bull gear and stationary hopper junction structure chart in Fig. 2.
Embodiment
Below in conjunction with the accompanying drawings, the present invention is further detailed explanation.
As shown in figure 1, the fertile co-generation system of the edible fungi residues thermoelectricity of the present embodiment, including be sequentially connected in series by belt feeder 2 and 4
Bacterium bag disintegrating machine 1, rotary screen formula separator 3, cylindrical drier 5, the medium entrance of cylindrical drier 5 and hot-blast stove 6
It is connected, the material outlet of cylindrical drier 5 is connected by screw(-type) feeder 7 and elevator 8 with rotary discharge bin 9, and one adds
Plus charging aperture of the discharge gate of agent conveying worm 10 also with screw(-type) feeder 7 is connected, rotary discharge bin 9 spreads out with rear again
Raw fuel comminutor 11 is connected by conveying worm 12, and derivatived fuel comminutor 11 passes through elevator 13 with counter-current cooler 14
It is connected, cooler 14 is connected with gasification furnace 18 by elevator 15, Bunker 16, conveying worm 17, the outlet of gasification furnace 18
It is connected by decanter type clarifier 19, air-introduced machine 20 with gas burning waste heat boiler 21;The slag-drip opening of gasification furnace 18 passes through carbon output machine 22
It is connected with the charging aperture of the ecological composite heat transfer system 23 of charcoal base;
Wherein rotary discharge bin 9 as shown in Figure 2 and Figure 3, including be sequentially connected from top to bottom fixation feed bin 31, the and of support 32
Stationary hopper 33, is provided with hollow rotation distribution cabins 34 between fixed feed bin 31 and stationary hopper 33, rotation distribution cabins 34
Top is sleeved on outside the bottom of fixed feed bin 31, and the bottom of rotation distribution cabins 34 is placed in stationary hopper 33, in rotation distribution cabins
34 outside welding, which are fixedly connected with bull gear 35, the output shaft of a motor 37, is associated with the little gear 36 engaged with bull gear 35, motor
37 are fixedly connected on support 32;Annular groove 38 is provided with the lower surface of bull gear 35, the upper surface of stationary hopper 33 is located at this ring
In groove, corresponding rolling groove is equipped with the upper surface of the end face of annular groove 38 and stationary hopper 33, several balls 39 are placed in relatively
In the rolling groove answered, the bottom centre in stationary hopper 33 is provided with material distributing cone 40, in the bottom of stationary hopper 33 and material distributing cone 40
Eccentric is provided with discharging opening 41, and several piece material scraping plate 42 is provided with the rotation inwall of distribution cabins 34;Fixed in use, material enters
Feed bin 31, startup motor 37, are rotated distribution cabins 34 and are rotated, material distributing cone 40 pushes away material by little gear 36, bull gear 35
Laterally, tapping channel is formed between material distributing cone 40 and stationary hopper 33, material scraping plate 42 promotes material to be incited somebody to action when passing through discharging opening 41
It is discharged;In use, material enters fixed feed bin 31, starts motor 37, cloth is rotated by little gear 36, bull gear 35
Storehouse 34 is rotated, and material distributing cone 40 pushes material to outside, and tapping channel, material scraping plate 42 are formed between material distributing cone 40 and stationary hopper 33
Material is promoted to be discharged it when passing through discharging opening 41;The device can make the biomass of lightweight by using rotation distribution cabins 34
The smooth blanking of material, is not in block, meanwhile, it is capable to realize the effect of uniform blanking, it is ensured that the continuity of granulation, realizes system
Unite prolonged normal work;
Edible fungi residues thermoelectricity fertile joint production process of the present invention for said system, comprises the following steps:1)Broken bag:Waste mushroom packet is thrown
Enter bacterium bag disintegrating machine 1 to be crushed, the material after crushing includes plastic sheet and the bacteria residue particle of biomass;2)Sorting:Will be broken
Material feeding rotary screen formula separator 3, plastic sheet is discharged, and bacteria residue particle is admitted to cylindrical drier 5;3)Dry:Bacterium
Solid impurity particle is through heated-air drying in cylindrical drier 5, and its moisture content is less than 20%;4)Batch mixing:Bacteria residue particle be discharged into spiral to
Mixed after material machine 7, with the carbon sequestration additive added by additive conveying worm 10, the quality of carbon sequestration additive and bacteria residue particle
Than for 5-8%, carbon sequestration additive includes 50-60% diatomite, 20-30% calcium oxide and 15-20% magnesium slag, is
Mass percent, and the particle diameter of three kinds of components is 60-80 mesh;5)Granulation:By mixed bacteria residue particle and carbon sequestration additive
Boosted machine 8 sends into rotary discharge bin 9, enters after discharging and is extruded, granulates, while being risen in derivatived fuel comminutor 11
Temperature, obtained graininess derivatived fuel;6)Cooling:Graininess derivatived fuel is sent to cooler 14 and cooled down;7)Gasification:
The granular boosted machine 15 of derivatived fuel, Bunker 16, in conveying worm 17 to gasification furnace 18, work as in 600 DEG C -800 DEG C, air
Amount obtains the biological fuel gas containing partial impurities, after burning than pyrolysis, gasification under the micro-oxygen conditions between 0.18-0.25
Breeze discharged by the slag-drip opening of gasification furnace 18, into carbon output machine 22, be used for the ecological composite fertilizer of production charcoal base;8)Purification:It is raw
Substance combustible gas is sent in decanter type clarifier 19 in the presence of air-introduced machine 20, wood tar and wooden vinegar in abjection biological fuel gas
Liquid, the additive for producing charcoal base ecological fertilizer;9)Combustion power generation:Biological fuel gas enters gas burning waste heat boiler 21 after purification
Generated electricity after burning, the flue gas of gas burning waste heat boiler is used for the drying for producing charcoal base ecological fertilizer;
The present invention need to only use a small amount of carbon sequestration additive to add in bacteria residue, and resource consumption is small;Diatomaceousization in additive
A point mainly SiO2 is studied, containing a small amount of Al2O3, Fe2O3, CaO, MgO etc. and organic matter, SiO2 rises stable to active component
Effect;Its absorption property of diatomite is strong, unit weight light, and fineness is uniform, and pH value neutrality is nontoxic, and mixing uniformity is good, will not when using
Agricultural machinery pipeline is blocked, moisturizing, loose soil property, extension drug effect fertilizer efficiency time can be played in soil, crop growth effect is encouraged,
Concentrated fertilizer can be turned into, promote effect in terms of crop growth, improved soil, add that particle diameter is smaller, porosity is big, adsorptivity
Can be strong, absorbing carbon dioxide can be played a part of in pyrolytic gasification, calcium oxide and magnesium slag is added in gasification and combustion gas
In carbon dioxide reaction, calcium carbonate, carbon and magnesia are generated respectively, the dioxide component in biological fuel gas can be solidified
In breeze, the content of carbon component in breeze is greatly increased, is the effective using effectively sufficient charcoal composition is ensured of breeze, turns into
Produce the raw material of the ecological composite fertilizer of charcoal base, charcoal base manure be one kind using biomass carbon as matrix, according to different zones land characteristics, no
The ecological environment-friendly type fertilizer being formulated with plant growth feature and the principle that applies fertilizers scientifically, addition organic matter or/and inanimate matter;
Charcoal base manure basic theories is clay fertilizer charcoal base-organism, that is, increases the content of charcoal base-organic matter in soil, quick transformation soil knot
Structure, balance salt and moisture, the soil environment for being conducive to plant health to grow is created by rapid aging, so as to increase soil fertilizer
Power, promotes plant growth, referred to as " geobiont bridge technology ", can improve the crumb structure of soil, improves soil water-reataining fertilizer-keeping
Ability, improve utilization rate of fertilizer, with higher-value;Increase the content of carbon component in breeze simultaneously, biomass fuel can be reduced
CO2 emissions when gas burns;During granulation, mixed material is extruded, heated up, and can be further backing out moisture, its heap ratio
Weight and energy density are also improved, and can improve gasification efficiency;Material is warmed, softened after granulation, and cooling can be carried out to particle
Cooling, solidification, increase hardness, in order to convey, realizes continuous production, while sloughing 3-5% moisture again;It is strict during gasification
Air equivalent ratio is controlled between 0.18-0.25, the carbon content of recrement after making gasification while production biological fuel gas is realized
It is the effective using effectively sufficient charcoal composition is ensured of breeze, biological fuel gas contains hydrogen, carbon monoxide, first for 30-60%
The fuel gas such as alkane;Deviate from wood tar and pyrolkigneous liquid during purification, a large amount of cokings during combustion power generation can be avoided to have a strong impact on boiler
It is normal to run and heat exchange efficiency, and prevent that moisture height from causing to damage big in boiler, realize the resource of normal operation for a long time and bacteria residue
Change and utilize;Wood tar and pyrolkigneous liquid can make plant nutrient regulation auxin, have growth effect to plant, desinsection is splendid, as charcoal
Base ecology fertilizer additive is conducive to granulating and forming to act on, and the growth factor in pyrolkigneous liquid has the function of regulation promotion plant growth.
Claims (8)
1. a kind of fertile co-generation system of edible fungi residues thermoelectricity, including be sequentially connected in series bacterium bag disintegrating machine, separator, drum-type drying
Machine, the medium entrance of cylindrical drier is connected with hot-blast stove, it is characterised in that:The material outlet of cylindrical drier passes through spiral shell
Rotation batcher and elevator are connected with rotary discharge bin, the discharge gate of an additive conveying worm also with this screw(-type) feeder
Charging aperture be connected, rotary discharge bin is sequentially connected in series with the derivatived fuel comminutor, cooler, gasification furnace at rear again, gasification
The outlet of stove is connected by decanter type clarifier, air-introduced machine with gas burning waste heat boiler.
2. the fertile co-generation system of edible fungi residues thermoelectricity according to claim 1, it is characterised in that:The slag-drip opening of the gasification furnace
It is connected by the ecological composite heat transfer system feeding mouthful of carbon output machine and charcoal base.
3. the fertile co-generation system of the edible fungi residues thermoelectricity stated according to claim 1 or 2, it is characterised in that:Rotary discharge bin is with spreading out
Raw fuel comminutor is connected by conveying worm, and derivatived fuel comminutor is connected with cooler by elevator, cooler and
Gasification furnace is connected by elevator, Bunker, conveying worm.
4. the fertile co-generation system of edible fungi residues thermoelectricity according to claim 3, it is characterised in that:Rotary discharge bin include by
On the fixation feed bin, support and the stationary hopper that are sequentially connected downwards, be provided with hollow rotation between fixed feed bin and stationary hopper
Turn distribution cabins, the top of rotation distribution cabins is sleeved on outside the bottom of fixed feed bin, and the bottom of rotation distribution cabins is placed in stationary hopper
It is interior, it is fixedly connected with the outside of rotation distribution cabins on bull gear, the output shaft of a motor and is associated with the little gear engaged with bull gear, big
The lower surface of gear ring and the upper surface of stationary hopper are equipped with corresponding rolling groove, and several balls are placed in corresponding rolling groove
In, bottom centre in stationary hopper is provided with material distributing cone, stationary hopper bottom and material distributing cone it is eccentric be provided with discharging opening,
More than one piece of material scraping plate is provided with rotation distribution cabins inwall.
5. the fertile co-generation system of edible fungi residues thermoelectricity according to claim 4, it is characterised in that:In the lower end of the bull gear
Face is provided with annular groove, and the rolling groove of bull gear is located at this annular groove;The upper surface of stationary hopper is located in this annular groove.
6. use the fertile joint production process of the edible fungi residues thermoelectricity of system as claimed in claim 1, it is characterised in that comprise the following steps:
1)Broken bag:Waste mushroom packet input bacterium bag disintegrating machine is crushed, material includes plastic sheet and the bacteria residue particle of biomass after crushing;
2)Sorting:Broken material is sent into separator, plastic sheet is discharged, and bacteria residue particle is admitted to cylindrical drier;3)Dry:
Bacteria residue particle is in cylindrical drier through heated-air drying, and its moisture content is less than 20%;4)Batch mixing:Bacteria residue particle be discharged into spiral to
Mixed after material machine, with the carbon sequestration additive added by additive conveying worm, the mass ratio of carbon sequestration additive and bacteria residue particle
For 5-8%, carbon sequestration additive includes 50-60% diatomite, 20-30% calcium oxide and 15-20% magnesium slag, is matter
Percentage is measured, and the particle diameter of three kinds of components is 60-80 mesh;5)Granulation:Mixed bacteria residue particle and carbon sequestration additive are sent
Enter rotary discharge bin, enter after discharging and be extruded, granulate, obtained graininess derivatived fuel in derivatived fuel comminutor;
6)Cooling:Graininess derivatived fuel is sent to cooler and cooled down(Solidification, increase hardness, are easy to conveying, while sloughing 3-5%
Moisture);7)Gasification:Graininess derivatived fuel in gasification furnace 600 DEG C -800 DEG C, air equivalent ratio 0.18-0.25 it
Between micro-oxygen conditions under pyrolysis, gasification, obtain the biological fuel gas containing partial impurities, the breeze after burning by gasification furnace row
Cinder notch is discharged, into the ecological composite fertilizer's fertilizer producing system of charcoal base;8)Purification:Biological fuel gas is sent sedimentation in the presence of air-introduced machine
In formula clarifier, abjection tar and pyrolkigneous liquid;9)Combustion power generation:Biological fuel gas enters after gas burning waste heat boiler burning after purification
Generate electricity.
7. the fertile joint production process of edible fungi residues thermoelectricity according to claim 6, it is characterised in that:The charcoal produced in gasification process
The carbon content of slag reaches 30-60%, is extraordinary charcoal base manure raw material, is used for the ecological composite fertilizer of production charcoal base, waste heat gas
The flue gas of boiler is used for the drying for producing charcoal base ecological fertilizer.
8. the fertile joint production process of edible fungi residues thermoelectricity according to claim 7, it is characterised in that:Deviate from wood in cleaning procedure burnt
Oil and pyrolkigneous liquid are used for the additive for producing the ecological composite fertilizer of charcoal base.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107365614A (en) * | 2017-08-15 | 2017-11-21 | 四川雷鸣环保装备有限公司 | Cigarette stalk biology shaped fuel resource recycling Application way |
CN109628147A (en) * | 2019-01-16 | 2019-04-16 | 天津大学 | A method of using mushroom bran vaporizing system for synthesis gas |
CN113319109A (en) * | 2021-05-12 | 2021-08-31 | 杨西建 | Resource utilization and treatment device for agricultural and livestock wastes |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105368496A (en) * | 2015-11-30 | 2016-03-02 | 南京林业大学 | Process method for cogenerating electricity, charcoal, heat and fertilizer through gasified gas supply of biomass |
CN106582444A (en) * | 2016-12-19 | 2017-04-26 | 四川雷鸣环保装备有限公司 | Granulating-tempering system for biomass derived fuel |
CN206721153U (en) * | 2017-05-03 | 2017-12-08 | 四川雷鸣环保装备有限公司 | Edible fungi residues thermoelectricity fertilizer co-generation system |
-
2017
- 2017-05-03 CN CN201710303620.6A patent/CN106957704A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105368496A (en) * | 2015-11-30 | 2016-03-02 | 南京林业大学 | Process method for cogenerating electricity, charcoal, heat and fertilizer through gasified gas supply of biomass |
CN106582444A (en) * | 2016-12-19 | 2017-04-26 | 四川雷鸣环保装备有限公司 | Granulating-tempering system for biomass derived fuel |
CN206721153U (en) * | 2017-05-03 | 2017-12-08 | 四川雷鸣环保装备有限公司 | Edible fungi residues thermoelectricity fertilizer co-generation system |
Non-Patent Citations (1)
Title |
---|
乔春珍: "《化石能源走向零排放的关键 制氢与CO2捕捉》", 30 June 2011, 冶金工业出版社 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107365614A (en) * | 2017-08-15 | 2017-11-21 | 四川雷鸣环保装备有限公司 | Cigarette stalk biology shaped fuel resource recycling Application way |
CN109628147A (en) * | 2019-01-16 | 2019-04-16 | 天津大学 | A method of using mushroom bran vaporizing system for synthesis gas |
CN113319109A (en) * | 2021-05-12 | 2021-08-31 | 杨西建 | Resource utilization and treatment device for agricultural and livestock wastes |
CN113319109B (en) * | 2021-05-12 | 2023-12-26 | 杨西建 | Resource utilization treatment device for farm animal waste |
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