CN103936470B - Industrial and agricultural production waste residue biological fermentation, furnace drying method and special integral system - Google Patents
Industrial and agricultural production waste residue biological fermentation, furnace drying method and special integral system Download PDFInfo
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- CN103936470B CN103936470B CN201410150102.1A CN201410150102A CN103936470B CN 103936470 B CN103936470 B CN 103936470B CN 201410150102 A CN201410150102 A CN 201410150102A CN 103936470 B CN103936470 B CN 103936470B
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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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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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
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
The invention belongs to the technical field of biological fermentation, be specifically related to a kind of industrial and agricultural production waste residue biological fermentation, furnace drying method, also relate to integral system special in above-mentioned fermentation, furnace drying method.Method of the present invention comprises following step: material is delivered to fermenter and ferments, and is delivered in drying tank and dries after fermentation ends.Beneficial effect of the present invention is; adopt method of the present invention and dedicated system processing power is large, production efficiency is high; to the waste residue biological fermentation of industrial and agricultural production; not only increase the protein content of product; add value-added content of product; improve economic benefit, and avoid industrial or agricultural waste residue to environment generation pollution, provide protection is served to environment.
Description
Technical field
The invention belongs to the technical field of biological fermentation, be specifically related to a kind of industrial and agricultural production waste residue biological fermentation, furnace drying method, also relate to integral system special in above-mentioned furnace drying method.
Background technology
Solid-state fermentation technology is in occupation of consequence in the development history of human civilization, in the production of the drinks of China, vinegar class, seasonings and edible mushrooms, occupy very consequence always.Conventional solid-state fermentation adopts the fermentation of heap fermentation, cellar, the fermentation of wine cylinder, cement pit or the fermentation of stainless steel tank, and modern conventional solid-state fermentation reactor has the reactors such as packed-bed reactor, tray formula reactor, rotating drum type reactor.The shortcomings such as these solid state fermentation equipments and technology ubiquity production efficiency is low, low, the easy microbiological contamination of fermentation equipment utilization ratio, labor strength are large, bad environments, be not suitable for utilizing these technical finesse industrial and agricultural production waste residues, present people are to industrial and agricultural production waste residue many employings natural packing fermentative processing, this processing mode fermentation is not thorough, treatment capacity is little, environment is poor, is not suitable for the requirement of people for cleaner production equally.The natural packing fermentation of outdoor formula, the gas produced in fermenting process is directly dispersed in air, causes ill effect to surrounding enviroment.Existing solid substances drying plant has drying baker, drying kiln etc. to be interrupted drying plant, there is polytype continuous drying equipment such as roller drying machine, pipe bundle drier, the equipment such as drying kiln are for being interrupted charging, being interrupted discharging, although the equipment such as pipe bundle drier can accomplish continuously feeding, continuous discharge, but all ubiquity processing power is little, bake out temperature is high, be not suitable for the dry shortcoming of the higher material of thermo-sensitivity, material dead angle is also more.
Therefore need to improve for above-mentioned method and apparatus, design a kind of can continuously feeding, continuous discharge and treatment capacity large, dry thoroughly and be suitable for the method and apparatus of suitability for industrialized production.
Summary of the invention
In order to solve above-mentioned technical problem, the invention provides a kind of processing power large, can continuously feeding and discharging, by fermentation and the method and system of drying being combined as a whole, single cover system of the present invention process waste residue per hour can reach more than 400 cubes; Whole system adopts mechanize conveying, mechanical stirring, alleviates the labour intensity of workman greatly; Ferment in fermenter due to material and dry, production area environment cleans.
Industrial and agricultural production waste residue biological fermentation of the present invention, furnace drying method solve above technical problem by following technical scheme:
Industrial and agricultural production waste residue biological fermentation, furnace drying method, the method comprises following step:
The fermentation of material and oven dry;
(1) mixture is through the feed chute I that lift promotes, transfer roller delivers into fermentor tank, and under the promotion of spreader I, material is evenly distributed on the sieve plate of fermenter, carries out fermentative production;
(2) temperature, the humidity of fermentation materials is tested; When the temperature of material, humidity and processing condition are not inconsistent, the temperature of adjustment material and humidity, start fermentation blower fan, fermentation cooling system, humidification system, start tripper I stirring, regulate the temperature in fermenter, humidity;
(3) after fermentation ends, discharging sleeve pipe mechanism I is carried, start spreader discharging, fermentation materials is flowed down by the space formed between column and discharging cannula system, and bleeder valve discharging at the bottom of tank, falls into discharging belt conveyer and transfer roller is transported to outside fermenter;
(4) material of drying is needed to send into material drying transfer roller by lift after fermentation, drying tank is entered through feed chute II, in drying tank, fermentation materials material under the promotion of spreader is evenly distributed on the sieve plate of drying tank, start to dry hot blast generation system and dry blower fan and material is dried, in drying course, start tripper II pair of material loosening, oven dry terminates rear discharging sleeve pipe mechanism II is carried, start spreader II discharging, material drying is flowed down by the space formed between column and discharging sleeve pipe mechanism II, bleeder valve discharging at the bottom of tank, by material drying discharging machine transmitting system.
In above-mentioned industrial and agricultural production waste residue biological fermentation, furnace drying method, special system comprises fermentation system and drying system;
Above-mentioned fermentation system comprises following device:
Fermenter, mixed fermentation materials delivers to the lift of fermenter, and embedded scraper transporter delivered to by lift, has fermenter material-feeding plugboard valve between described embedded scraper transporter and fermenter;
Fermenter is connected with fermentation blower fan, fermentation cooling system, humidification system;
Fermenter comprises feed chute I, column I, bleeder valve I, frame I, spreader I, tripper I, sieve end pillar I, the sieve end I, cell body I, discharging sleeve pipe mechanism I; The sieve end I, is arranged at the bottom of the cell body I of described fermenter, the sieve end I, is supported at the bottom of fermenter by sieve end pillar I, there is column I centre of the cell body I of fermenter, there is the discharging sleeve pipe mechanism I that can upwards promote the outside of column I, there is the frame I can rotated around column between the top of column I and cell body I outer wall, frame I is equipped with multiple tripper I installed up and down; When frame I rotates around pillar, tripper I starts, and completes stirring work;
There is spreader I moving up and down at the rear that frame I and tripper I run, when charging, material enters fermenter by feed chute I, by spreader I, the material entering fermenter is shakeout, fermentation ends, discharging sleeve pipe mechanism I is carried, and start spreader I discharging, fermentation materials is flowed down by the space formed between column I and discharging sleeve pipe mechanism I, bleeder valve discharging at the bottom of tank, material is delivered to next operation by discharging belt conveyer and outfeed belt conveyor;
Fermentation system comprises at least one group of above-mentioned device, if fermentation system is organize above-mentioned device more, then often organizes between fermentation system parallel with one another;
Drying system comprises following device:
Fermentation materials lift, hot blast produce system, oven dry blower fan, drying tank, feed chute II, column II, bleeder valve II, frame II, tripper II, spreader II, sieve end pillar II, the sieve end II, cell body II, discharging sleeve pipe mechanism II, material drying discharging machine;
Drying tank is supporting has hot blast to produce system;
Drying tank comprises cell body II, feed chute II, column II, bleeder valve II, frame II, spreader II, tripper II, sieve end pillar II, the sieve end II, discharging sleeve pipe mechanism II; The sieve end II, is arranged at the bottom of the cell body II of described drying tank, the sieve end II, is supported at the bottom of drying tank by sieve end pillar II, there is column II centre of the cell body II of drying tank, the discharging sleeve pipe mechanism II that can upwards promote is had outside column II, there is the frame II can rotated around column between the top of column II and cell body II outer wall, frame II is equipped with multiple tripper II installed up and down; When frame II rotates around column II, tripper II starts, and completes stirring work; The rear that frame II and tripper II run is provided with spreader II moving up and down, and when charging, material enters drying tank by feed chute II, and the material entering drying tank shakeouts by spreader II; Start hot blast and produce system to drying materials;
After oven dry terminates, the discharging sleeve pipe mechanism II outside column II promotes, and the bleeder valve II of bottom is opened, and spreader II completes and material is transported to discharge port;
Drying system comprises at least one group of above-mentioned device, if drying unit is organize above-mentioned device more, then often organizes between drying system parallel with one another.
Transfer roller embedded scraper transporter in step (1), the transfer roller in step (3) is rubber conveyer.
Preferably, above-mentioned fermentation system is four groups.
Lift in fermentation system is chapelet.
Lift in drying system is also chapelet.
The application of above-mentioned method and system in multiple fermentable industrial or agricultural waste residue biological fermentations such as process Chinese liquor distiller grains, beer vinasse, vinegar grain is also invention which is intended to be protected.
Solid-state fermentation technology is in occupation of consequence in the development history of human civilization, in the production of the drinks of China, vinegar class, seasonings and mould, edible mushrooms, occupy very consequence always.Conventional solid-state fermentation adopts the fermentation of heap fermentation, cellar, the fermentation of wine cylinder, cement pit or the fermentation of stainless steel tank, and modern conventional solid-state fermentation reactor has the reactors such as packed-bed reactor, tray formula reactor, rotating drum type reactor.The shortcomings such as these solid state fermentation equipments and technology ubiquity production efficiency is low, low, the easy microbiological contamination of fermentation equipment utilization ratio, labor strength are large, bad environments, be not suitable for utilizing these technical finesse industrial and agricultural production waste residues, present people are to industrial and agricultural production waste residue many employings natural packing fermentative processing, this processing mode fermentation is not thorough, treatment capacity is little, environment is poor, is not suitable for the requirement of people for cleaner production equally.
In the present invention, first the raw and auxiliary material of fermentation will be needed, thalline fully mixes before entering this device, mixed raw material enters fermentation unit and ferments, fermentation, drying integrated device adopts and comprises chapelet (or rotary conveyor), fermentation blower fan, fermentation cooling system, humidification system, fermenter, discharging belt conveyer, rubber conveyer, fermentation materials chapelet, hot blast produces system, dry blower fan, drying tank, dry feeding conveyor, air preheater, fermenter material-feeding plugboard valve, embedded scraper transporter, material drying discharging machine forms.Wherein fermenter is by feed chute, column, bleeder valve, frame, spreader, tripper, sieve end pillar, the sieve end, cell body and discharging cannula system composition.Drying tank is by chute, and Zhi Lizhu, bleeder valve, frame, tripper, spreader, sieve end pillar, sieves the end, the technical scheme of cell body and discharging cannula system composition.
System primary structure of the present invention is explained further:
Fermenter is by feed chute, and column, bleeder valve, frame, spreader, tripper, sieve end pillar, the sieve end, cell body and discharging cannula system form.The sieve end, is equipped with in the bottom of cell body, the sieve end, is by sieving end shore supports on bottom land, there is column the centre of cell body, there is discharging cannula system the outside of column, and be provided with frame between the top of column and cell body outer wall, frame can rotate around column, several tripper installed up and down frame is equipped with, frame rotates around pillar, and tripper starts, and completes stirring work.The rear that frame and tripper run is provided with spreader moving up and down, and when charging, material enters fermenter (drying tank) by chute, and spreader completes and shakeout by the material entering fermenter (drying tank), makes the bed of material even.Fermentation (oven dry) terminates, and the discharging cannula system of column sidewall promotes, and the bleeder valve of bottom is opened, and spreader completes the gap being transported to by material and being formed between column and discharging sleeve pipe, and material drains into the transfer roller of bottom through bleeder valve.
Fermenting mixed raw material enters fermentor tank feed chute through lift, embedded scraper transporter, under the promotion of spreader, material is evenly distributed on the sieve plate of fermenter, owing to can produce a large amount of heats in fermenting process, when the cooling of material needs and oxygenation, startup is fermented, and blower fan is lowered the temperature to material, oxygenation.When cooling and oxygenation, a large amount of wind can make fermentation materials moisture distribute, be unfavorable for the further fermentation of material, start humidification system, moisturizing is carried out to fermentation materials, along with the carrying out of fermentation, storeroom can produce bonding, ventilation property is deteriorated, starts tripper and carry out loose to material, prevent material from luming, make fermentation thorough, Uniform Ventilation, fermentation ends discharging cannula system promotes, start spreader (now spreader uses as discharging machine in fermenter) discharging, bleeder valve at the bottom of tank, fermentation materials is transported to outside fermenter by discharging belt conveyer and rubber conveyer, for the material needing to dry, through fermentation materials lift, material drying transfer roller, chute enters drying tank, in drying tank, fermentation materials material under the promotion of spreader is evenly distributed on the sieve plate of drying tank, hot air producing apparatus is dried in startup and blower fan is dried material, for making oven dry uniform and complete, according to scheduling of production, starting tripper carries out loose to material, dry and terminate to start spreader (now spreader uses as discharging machine in drying tank) discharging, bleeder valve at the bottom of tank, fermentation materials is by material drying discharging machine transmitting system.
System of the present invention adopts jumbo solid state fermentation groove, and the quantity of fermenter is suitably selected according to fermentation period.The quantity of drying tank carrys out doses according to fermentation and the oven dry cycle suitably selects.System of the present invention is specially adapted to industrial or agricultural waste residue biological fermentation and produces biological fodder, bio-feritlizer project.Continuously feeding accomplished by system mixed fermentation raw material of the present invention, mechanical stirring shakeouts, mechanical discharging, production efficiency is high, leavening temperature is appropriate controlled, when fermentation ends, for the material needing to dry, drying tank can be utilized to dry, system of the present invention dramatically reduces the labour intensity of workman, improve operating environment, for Appropriate application industrial or agricultural waste residue, reduction industrial or agricultural waste residue environmental pollution provide a set of practicality, efficiently device and technology.
Adopt above-mentioned industrial and agricultural production waste residue biological fermentation, furnace drying method and special integral system; can the waste residue of biological fermentation for what produce in industrial and agricultural production; to add after nutrition agent and yeast after mushroom; ferment through Homogeneous phase mixing; Fermentable substrate matter in material can be carried out bio-transformation through biological fermentation; improve the protein content of product, improve value-added content of product and be conducive to protection of the environment.For Chinese liquor distiller grains, the protein content being separated powder when steaming Chinese liquor distiller grains dry state is after drinking approximately about 17%, owing to being of low nutritive value, sell at a low price peasant to do fuel or sell feed factory doping and made feed, owing to be of low nutritive value and rice husk is not suitable for non-ruminant animal, material injury is caused to Swine non-ruminant animal.By this material after biological fermentation again, protein content is greatly improved, after oven dry through being separated further, be separated the protein content of powder more than 27%, be good poultry and livestock feed, namely improve the attached value of product, additionally reduce the infringement to environment.
The invention belongs to technical field of biological fermentation, be specifically related to a kind of industrial and agricultural production waste residue biological fermentation, drying integrated device and method.Employing comprises chapelet, fermentation blower fan, fermentation cooling system, humidification system, fermenter, discharging belt conveyer, rubber conveyer, fermentation materials chapelet, hot blast produces system, dry blower fan, drying tank, dries feeding conveyor, air preheater, fermenter material-feeding plugboard valve, embedded scraper transporter, material drying discharging machine.Described fermenter is by feed chute, and column, bleeder valve, frame, spreader, tripper, sieve end pillar, sieve the end, cell body, composition.Described drying tank is by chute, and column, bleeder valve, frame, tripper, spreader, sieve end pillar, sieves the end, the technical scheme of cell body discharging cannula system composition.This device first time adopts jumbo solid state fermentation groove, drying tank, and the quantity of fermenter is suitably selected according to fermentation period.The quantity of drying tank carrys out doses according to fermentation and the oven dry cycle suitably selects.
This device is specially adapted to industrial or agricultural waste residue biological fermentation and produces biological fodder, bio-feritlizer project.Continuously feeding accomplished by this device mixed fermentation raw material, mechanical stirring shakeouts, mechanical discharging, production efficiency is high, leavening temperature is appropriate controlled, when fermentation ends, for the material needing to dry, drying tank can be utilized to dry, this device dramatically reduces the labour intensity of workman, improve operating environment, for Appropriate application industrial or agricultural waste residue, reduction industrial or agricultural waste residue environmental pollution provide a set of practicality, efficiently device and technology.
Accompanying drawing explanation
Fig. 1 is the structural representation of industrial or agricultural waste residue biological fermentation of the present invention, drying integrated device;
Fig. 2 is the structural representation that the fermentation system of accompanying drawing 1 in the present invention amplifies;
Fig. 3 is the structural representation that the drying system of accompanying drawing 1 in the present invention is amplified;
In figure, 1-chapelet, 2-fermentation blower fan, 3-fermentation cooling system, 4-humidification system, 5-fermenter,
501-feed chute I, 502-column I, 503-bleeder valve I, 504-frame I, 505-spreader I, 506-tripper I, 507-sieve end pillar, I, 508-sieve end I, 509-cell body I, 510-discharging sleeve pipe mechanism I;
6-discharging belt conveyer, 7-rubber conveyer, 8-fermentation materials chapelet, 9-hot blast produces system, 10-dry blower fan, 11-drying tank;
1101-feed chute II, 1102-column II, 1103-bleeder valve II, 1104-frame II, 1105-tripper II, 1106-spreader II, 1107-sieve end pillar, II, 1108-sieve end II, 1109-cell body II, 1110-discharging sleeve pipe mechanism II;
12-dry feeding conveyor, 13-air preheater, 14-fermenter material-feeding plugboard valve, 15-embedded scraper transporter, 16-material drying discharging machine.
Embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is further described, so that those skilled in the art more understands the present invention, but does not limit the present invention with this.
Embodiment 1
Industrial and agricultural production waste residue biological fermentation, furnace drying method, the method comprises following step:
The fermentation of material and oven dry;
(1) feed chute I 501 that mixture promotes through chapelet 1, embedded scraper transporter 15 delivers into fermentor tank, under the promotion of spreader I 505, material is evenly distributed on the sieve plate of fermenter 5, carries out fermentative production; Mixture is Chinese liquor distiller grains;
(2) temperature, the humidity of fermentation materials is tested; When the temperature of material, humidity and processing condition are not inconsistent, the temperature of adjustment material and humidity, start fermentation blower fan 2, fermentation cooling system 3, humidification system 4, start tripper I 506 stirring, regulate the temperature in fermenter 5, humidity;
(3) after fermentation ends, discharging sleeve pipe mechanism I 510 is carried, start spreader discharging, fermentation materials is flowed down by the space formed between column and discharging cannula system, bleeder valve discharging at the bottom of tank, falls into discharging belt conveyer 6 and rubber conveyer 7 is transported to outside fermenter 5;
(4) material of drying is needed to send into material drying transfer roller by lift after fermentation, drying tank 11 is entered through feed chute II 1101, in drying tank 11, fermentation materials material under the promotion of spreader is evenly distributed on the sieve plate of drying tank 11, start to dry hot blast generation system 9 and dry blower fan 10 pairs of materials and dry, in drying course, start tripper II 1105 pairs of material loosenings, oven dry terminates rear discharging sleeve pipe mechanism II 1110 is carried, start spreader II 1106 discharging, material drying is flowed down by the space formed between column and discharging sleeve pipe mechanism II 1110, bleeder valve discharging at the bottom of tank, by material drying discharging machine 16 transmitting system.
In above-mentioned industrial and agricultural production waste residue biological fermentation, furnace drying method, special system comprises fermentation system and drying system;
Above-mentioned fermentation system comprises following device:
Fermenter 5, mixed fermentation materials delivers to the lift of fermenter 5, and embedded scraper transporter 15 delivered to by lift, has fermenter material-feeding plugboard valve 14 between embedded scraper transporter 15 and fermenter 5;
Fermenter 5 is connected with fermentation blower fan 2, fermentation cooling system 3, humidification system 4;
Fermenter 5 comprises feed chute I 501, column I 502, bleeder valve I 503, frame I 504, spreader I 505, tripper I 506, sieve end pillar I 507, the sieve end I 508, cell body I 509, discharging sleeve pipe mechanism I 510; The sieve end I 508, is arranged at the bottom of the cell body I 509 of described fermenter 5, the sieve end I 508, is supported in by sieve end pillar I 507 at fermenter 5 the end, there is column I 502 centre of the cell body I 509 of fermenter 5, there is the discharging sleeve pipe mechanism I 510 that can upwards promote the outside of column I 502, there is the frame I 504 can rotated around column between the top of column I 502 and cell body I 509 outer wall, frame I 504 is equipped with multiple tripper I 506 installed up and down; When frame I 504 rotates around pillar, tripper I 506 starts, and completes stirring work;
There is spreader I 505 moving up and down at the rear that frame I 504 and tripper I 506 run, when charging, material enters fermenter 5 by feed chute I 501, by spreader I 505, the material entering fermenter 5 is shakeout, fermentation ends, discharging sleeve pipe mechanism I 510 is carried, start spreader I 505 discharging, fermentation materials is flowed down by the space formed between column I 502 and discharging sleeve pipe mechanism I 510, bleeder valve discharging at the bottom of tank, material is delivered to next operation by discharging belt conveyer 6 and outfeed belt conveyor;
Fermentation system comprises four groups of above-mentioned devices, often organizes between fermentation system parallel with one another;
Drying tank is supporting hot-air system.
Fermenter, drying tank are middle discharging, discharging sleeve pipe mechanism lifts during discharging, and material is flowed down, through bleeder valve discharging by discharging sleeve pipe mechanism I and the space between discharging sleeve pipe mechanism II and column.
In fermenter, drying tank, discharge mechanism is made up of discharging sleeve pipe mechanism and bleeder valve, and discharging sleeve pipe mechanism I and the discharging sleeve pipe mechanism II of two cover systems are positioned at outside column, is pneumatic or motor drive mechanism drive unit.
Drying system comprises following device:
Fermented product chapelet 8, oven dry feeding conveyor 12, air preheater 13, hot blast produce system 9, oven dry blower fan 10, drying tank 11, feed chute II 1101, column II 1102, bleeder valve II 1103, frame II 1104, tripper II 1105, spreader II 1106, sieve end pillar II 1107, the sieve end II 1108, cell body II 1109, discharging sleeve pipe mechanism II 1110, material drying discharging machine 16;
Drying tank 11 is supporting has hot blast to produce system 9;
Drying tank 11 comprises cell body II 1109, feed chute II 1101, column II 1102, bleeder valve II 1103, frame II 1104, spreader II 1106, tripper II 1105, sieve end pillar II 1107, the sieve end II 1108, discharging sleeve pipe mechanism II 1110; The sieve end II 1108, is arranged at the bottom of the cell body II 1109 of drying tank 11, the sieve end II 1108, is supported in by sieve end pillar II 1107 at drying tank 11 the end, there is column II 1102 centre of the cell body II 1109 of drying tank 11, the discharging sleeve pipe mechanism II 1110 that can upwards promote is had outside column II 1102, there is the frame II 1104 can rotated around column between the top of column II 1102 and cell body II 1109 outer wall, frame II 1104 is equipped with multiple tripper II 1105 installed up and down; When frame II 1104 rotates around column II 1102, tripper II 1105 starts, and completes stirring work; The rear that frame II 1104 and tripper II 1105 run is provided with spreader II 1106 moving up and down, and when charging, material enters drying tank 11 by feed chute II 1101, and the material entering drying tank 11 shakeouts by spreader II 1106; Start hot blast and produce system 9 pairs of drying materials;
After oven dry terminates, the discharging sleeve pipe mechanism II 1110 outside column II 1102 promotes, and the bleeder valve II 1103 of bottom is opened, and spreader II 1106 completes and material is transported to discharge port;
Drying system can comprise the above-mentioned device of many groups, often organizes between drying system parallel with one another.
Claims (9)
1. industrial and agricultural production waste residue biological fermentation, furnace drying method, the method comprises following step:
The fermentation of material and oven dry;
(1) mixture is through the feed chute I that lift promotes, transfer roller delivers into fermentor tank, and under the promotion of spreader I, material is evenly distributed on the sieve plate of fermenter, carries out fermentative production;
(2) temperature, the humidity of fermentation materials is tested; When the temperature of material, humidity and processing condition are not inconsistent, the temperature of adjustment material and humidity, start fermentation blower fan, fermentation cooling system, humidification system, start tripper I stirring, regulate the temperature in fermenter, humidity;
(3) after fermentation ends, discharging sleeve pipe mechanism I is carried, start spreader discharging, fermentation materials is flowed down by the space formed between column and discharging cannula system, and bleeder valve discharging at the bottom of tank, falls into discharging belt conveyer and transfer roller is transported to outside fermenter;
(4) material of drying is needed to send into material drying transfer roller by lift after fermentation, drying tank is entered through feed chute II, in drying tank, fermentation materials material under the promotion of spreader is evenly distributed on the sieve plate of drying tank, start to dry hot blast generation system and dry blower fan and material is dried, in drying course, start tripper II pair of material loosening, oven dry terminates rear discharging sleeve pipe mechanism II is carried, start spreader II discharging, material drying is flowed down by the space formed between column and discharging sleeve pipe mechanism II, bleeder valve discharging at the bottom of tank, by material drying discharging machine transmitting system.
2. integral system special in industrial and agricultural production waste residue biological fermentation as claimed in claim 1, furnace drying method, it is characterized in that, described system comprises fermentation system and drying system;
Described fermentation system comprises following device:
Fermenter, mixed fermentation materials delivers to the lift of fermenter, and embedded scraper transporter delivered to by lift, has fermenter material-feeding plugboard valve between described embedded scraper transporter and fermenter;
Described fermenter is connected with fermentation blower fan, fermentation cooling system, humidification system;
Described fermenter comprises feed chute I, column I, bleeder valve I, frame I, spreader I, tripper I, sieve end pillar I, the sieve end I, cell body I, discharging sleeve pipe mechanism I; The sieve end I, is arranged at the bottom of the cell body I of described fermenter, the sieve end I, is supported at the bottom of fermenter by sieve end pillar I, there is column I centre of the cell body I of fermenter, there is the discharging sleeve pipe mechanism I that can upwards promote the outside of column I, there is the frame I can rotated around column between the top of column I and cell body I outer wall, frame I is equipped with multiple tripper I installed up and down; When frame I rotates around pillar, tripper I starts, and completes stirring work;
There is spreader I moving up and down at the rear that frame I and tripper I run, when charging, material enters fermenter by feed chute I, by spreader I, the material entering fermenter is shakeout, fermentation ends, discharging sleeve pipe mechanism I is carried, and start spreader I discharging, fermentation materials is flowed down by the space formed between column I and discharging sleeve pipe mechanism I, bleeder valve discharging at the bottom of tank, material is delivered to next operation by discharging belt conveyer and outfeed belt conveyor;
Described fermentation system comprises at least one group of above-mentioned device, if fermentation system is organize above-mentioned device more, then often organizes between fermentation system parallel with one another;
Described drying system comprises following device:
Fermentation materials lift, hot blast produce system, oven dry blower fan, drying tank, feed chute II, column II, bleeder valve II, frame II, tripper II, spreader II, sieve end pillar II, the sieve end II, cell body II, discharging sleeve pipe mechanism II, material drying discharging machine;
Described drying tank is supporting has hot blast to produce system;
Described drying tank comprises cell body II, feed chute II, column II, bleeder valve II, frame II, spreader II, tripper II, sieve end pillar II, the sieve end II, discharging sleeve pipe mechanism II; The sieve end II, is arranged at the bottom of the cell body II of described drying tank, the sieve end II, is supported at the bottom of drying tank by sieve end pillar II, there is column II centre of the cell body II of drying tank, the discharging sleeve pipe mechanism II that can upwards promote is had outside column II, there is the frame II can rotated around column between the top of column II and cell body II outer wall, frame II is equipped with multiple tripper II installed up and down; When frame II rotates around column II, tripper II starts, and completes stirring work; The rear that frame II and tripper II run is provided with spreader II moving up and down, and when charging, material enters drying tank by feed chute II, and the material entering drying tank shakeouts by spreader II; Start hot blast and produce system to drying materials;
After oven dry terminates, the discharging sleeve pipe mechanism II outside column II promotes, and the bleeder valve II of bottom is opened, and spreader II completes and material is transported to discharge port;
Described drying system comprises at least one group of above-mentioned device, if drying unit is organize above-mentioned device more, then often organizes between drying system parallel with one another.
3. industrial and agricultural production waste residue biological fermentation, furnace drying method as claimed in claim 1, it is characterized in that, the transfer roller in described step (1) is embedded scraper transporter.
4. industrial and agricultural production waste residue biological fermentation, furnace drying method as claimed in claim 1, it is characterized in that, the transfer roller in described step (3) is rubber conveyer.
5. integral system special in industrial and agricultural production waste residue biological fermentation as claimed in claim 2, furnace drying method, it is characterized in that, described fermentation system is four groups.
6. integral system special in industrial and agricultural production waste residue biological fermentation as claimed in claim 2, furnace drying method, it is characterized in that, the lift in described fermentation system is chapelet.
7. integral system special in industrial and agricultural production waste residue biological fermentation as claimed in claim 2, furnace drying method, it is characterized in that, the lift in described drying system is chapelet.
8. integral system special in industrial and agricultural production waste residue biological fermentation as claimed in claim 2, furnace drying method, is characterized in that, the application of described system in process Chinese liquor distiller grains, beer vinasse, vinegar grain industrial or agricultural waste residue biological fermentation.
9. integral system special in industrial and agricultural production waste residue biological fermentation as claimed in claim 2, furnace drying method, is characterized in that, the application of described system in process Chinese liquor distiller grains.
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| CN104478512B (en) * | 2014-12-26 | 2017-05-03 | 朱明江 | Fermentation, turnover and drying all-in-one machine of organic fertilizer |
| CN104725092A (en) * | 2015-04-02 | 2015-06-24 | 浙江明佳环保科技有限公司 | Fermenting, reversing and drying all-in-one machine for organic fertilizer |
| CN112425706A (en) * | 2020-11-30 | 2021-03-02 | 天水师范学院 | Method for treating waste by utilizing microbial fermentation |
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| CN1113695A (en) * | 1994-05-26 | 1995-12-27 | 杨发 | Distiller's grains modifying technology and equipment |
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| CN202730021U (en) * | 2012-07-02 | 2013-02-13 | 徐州汉高酒业有限公司 | Novel device for producing grain stillage bio-organic fertilizer |
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| CN1113695A (en) * | 1994-05-26 | 1995-12-27 | 杨发 | Distiller's grains modifying technology and equipment |
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