CN109321438A - Production system of aerobic and then anaerobic biological feed additives - Google Patents
Production system of aerobic and then anaerobic biological feed additives Download PDFInfo
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- CN109321438A CN109321438A CN201811423531.6A CN201811423531A CN109321438A CN 109321438 A CN109321438 A CN 109321438A CN 201811423531 A CN201811423531 A CN 201811423531A CN 109321438 A CN109321438 A CN 109321438A
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- 239000003674 animal food additive Substances 0.000 title abstract description 3
- 239000000463 material Substances 0.000 claims abstract description 147
- 238000010564 aerobic fermentation Methods 0.000 claims abstract description 87
- 239000002994 raw material Substances 0.000 claims abstract description 61
- 238000000855 fermentation Methods 0.000 claims abstract description 55
- 241000894006 Bacteria Species 0.000 claims abstract description 34
- 238000007599 discharging Methods 0.000 claims abstract description 26
- 238000001035 drying Methods 0.000 claims description 98
- 238000002156 mixing Methods 0.000 claims description 71
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 64
- 239000004615 ingredient Substances 0.000 claims description 52
- 238000001816 cooling Methods 0.000 claims description 49
- 239000004744 fabric Substances 0.000 claims description 43
- 239000011344 liquid material Substances 0.000 claims description 34
- 238000005201 scrubbing Methods 0.000 claims description 32
- 238000010438 heat treatment Methods 0.000 claims description 29
- 239000000203 mixture Substances 0.000 claims description 29
- 241000406668 Loxodonta cyclotis Species 0.000 claims description 26
- 239000000843 powder Substances 0.000 claims description 23
- 238000005406 washing Methods 0.000 claims description 23
- 239000012530 fluid Substances 0.000 claims description 22
- 241001148470 aerobic bacillus Species 0.000 claims description 21
- 239000013535 sea water Substances 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 17
- 239000000498 cooling water Substances 0.000 claims description 10
- 238000009826 distribution Methods 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 239000000428 dust Substances 0.000 claims description 7
- 239000007921 spray Substances 0.000 claims description 7
- 241001148471 unidentified anaerobic bacterium Species 0.000 claims description 6
- 238000005243 fluidization Methods 0.000 claims description 2
- 238000005096 rolling process Methods 0.000 claims description 2
- 238000010025 steaming Methods 0.000 claims 2
- 230000004151 fermentation Effects 0.000 abstract description 28
- 239000000872 buffer Substances 0.000 abstract description 7
- 235000015097 nutrients Nutrition 0.000 abstract description 4
- 239000010410 layer Substances 0.000 description 59
- 239000007789 gas Substances 0.000 description 19
- 241001465754 Metazoa Species 0.000 description 10
- 230000006872 improvement Effects 0.000 description 10
- 239000002207 metabolite Substances 0.000 description 9
- 229920002472 Starch Polymers 0.000 description 8
- 235000021050 feed intake Nutrition 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000000926 separation method Methods 0.000 description 6
- 235000019698 starch Nutrition 0.000 description 6
- 239000008107 starch Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
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- 230000009286 beneficial effect Effects 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
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- 239000003205 fragrance Substances 0.000 description 4
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 4
- 239000006041 probiotic Substances 0.000 description 4
- 235000018291 probiotics Nutrition 0.000 description 4
- 108090000623 proteins and genes Proteins 0.000 description 4
- 102000004169 proteins and genes Human genes 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
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- 244000005700 microbiome Species 0.000 description 3
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- 239000000126 substance Substances 0.000 description 3
- 235000019890 Amylum Nutrition 0.000 description 2
- 241000193830 Bacillus <bacterium> Species 0.000 description 2
- 241000235342 Saccharomycetes Species 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 235000004458 antinutrient Nutrition 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
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- 238000000605 extraction Methods 0.000 description 2
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- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 230000036039 immunity Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 235000014655 lactic acid Nutrition 0.000 description 2
- 239000004310 lactic acid Substances 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
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- 108090000765 processed proteins & peptides Proteins 0.000 description 2
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- 238000004806 packaging method and process Methods 0.000 description 1
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- 238000011084 recovery Methods 0.000 description 1
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- 239000002356 single layer Substances 0.000 description 1
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Classifications
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M25/00—Means for supporting, enclosing or fixing the microorganisms, e.g. immunocoatings
- C12M25/16—Particles; Beads; Granular material; Encapsulation
- C12M25/20—Fluidized bed
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/20—Degassing; Venting; Bubble traps
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/04—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus by injection or suction, e.g. using pipettes, syringes, needles
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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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Abstract
本发明涉及一种先好氧后厌氧生物饲料添加剂的生产系统，包括配料装置、好氧发酵机和厌氧发酵罐，投料斗的底部与原料提升机相连，原料提升机与多个配料仓的上端入口相连，各配料仓的底部分别与配料秤的入口相连，配料秤与原料缓冲仓的入口相连，原料缓冲仓底部出口与投料提升机相连，投料提升机的出口与投料缓冲仓相连，投料缓冲仓的出口与原料混合机相连，原料混合机的出口与混合料缓冲仓相连，混合料缓冲仓的出口与调质器的进料口相连，调质器的出料口与保质器的进料口相连，保质器的出料口与风冷机的进料口相连，风冷机的出料口通过配料关风器与配料风送管道相连。该系统兼顾好氧和厌氧发酵，饲料的营养平衡丰富，且发酵过程不易染杂菌。
The invention relates to a production system for an aerobic and then anaerobic biological feed additive, which comprises a batching device, an aerobic fermentation machine and an anaerobic fermentation tank. The bottom of each batching bin is connected to the inlet of the batching scale, the batching scale is connected to the inlet of the raw material buffer bin, the bottom outlet of the raw material buffer bin is connected to the feeding hoist, and the outlet of the feeding hoist is connected to the feeding buffer bin. The outlet of the feeding buffer silo is connected to the raw material mixer, the outlet of the raw material mixer is connected to the mixed material buffer silo, the outlet of the mixed material buffer silo is connected to the inlet of the conditioner, and the outlet of the conditioner is connected to the outlet of the quality preserver. The feeding port is connected, the discharging port of the quality preserver is connected with the feeding port of the air cooler, and the discharging port of the air cooler is connected with the batching air supply pipeline through the batching air shutoff device. The system takes into account both aerobic and anaerobic fermentation, the nutrient balance of the feed is rich, and the fermentation process is not easy to contaminate miscellaneous bacteria.
Description
Technical field
The present invention relates to a kind of production system of fermented feed, in particular to anaerobic organism feed addition after a kind of elder generation is aerobic
The production system of agent belongs to fermented feed production technical field.
Background technique
Traditional biological fermentation feed production technology is fairly simple, generally feed intake, be inoculated with, anaerobic fermentation, high temperature drying,
Packaging.Raw material, only with a kind of raw material, does not pass through ingredient, boiling, more without the utilization technique of boiling waste heat without ingredient.It is single
One raw material makes the nutritional imbalance of raw material, and not conditioned sterilizing is so that easily contaminate miscellaneous bacteria in subsequent fermentation process.
The probiotics and biological metabolite quantity that fermentation generates are few, and drying temperature height makes probiotics and biological metabolite portion
Point inactivation, reduces the bioactivity of biological fermentation feed, also reduces the value of biological fermentation feed, product quality it is consistent
Property is poor.Single layer fermentation machine is generally used, is taken up a large area；Using manually-operated mode, large labor intensity, small scale cannot
Realize industrialization；Tail gas is without processing direct emission, environmental pollution.
Summary of the invention
It is an object of the present invention to overcome problems of the prior art, a kind of aerobic rear anaerobic organism of elder generation is provided and is raised
The production system of feed additives can carry out mix to plurality of raw materials, make the nutrient balance of feed, and fermentation process is not easy
Contaminate miscellaneous bacteria.
In order to solve the above technical problems, the production system of anaerobic organism feed addictive after a kind of elder generation of the invention is aerobic,
Including proportioner, aerobic fermentation machine and anaerobic fermentation tank, the proportioner includes cast hopper and raw material elevator, the throwing
The outlet at bottom of hopper is connected with the lower inlet of raw material elevator, and the upper end outlet of raw material elevator is upper with multiple batch bins
End entrance is connected, and the bottom of each batch bin is respectively equipped with ingredient spiral, the outlet of each ingredient spiral respectively with the entrance of burden balance
It is connected, the outlet of burden balance is connected with the entrance of raw material surge bunker, and the feeding serew of raw material surge bunker bottom is exported and mentioned with feeding intake
The entrance of the machine of liter is connected, and the outlet for the elevator that feeds intake is connected with the entrance for the surge bunker that feeds intake, the outlet for the surge bunker that feeds intake and raw material
The entrance of mixing machine is connected, and the outlet of raw material mixing machine is connected with the entrance of mixture surge bunker, the outlet of mixture surge bunker
It is connected with the feed inlet of quality-adjusting device, the discharge port of the quality-adjusting device is connected with the feed inlet for device of guaranteeing the quality, the quality-adjusting device and described
The guarantee the quality steam inlet of device is connected with raw steam pipe respectively, and the discharge port of the device of guaranteeing the quality is connected with the feed inlet of Air cooler, institute
The discharge port for stating Air cooler is connected by ingredient airlock with ingredient air delivery pipe.
Compared with the existing technology, the present invention achieves following the utility model has the advantages that various raw materials can pour into cast hopper respectively,
It is promoted to high-order by raw material elevator and is entered in corresponding batch bin and store, when ingredient, each raw material is successively by corresponding ingredient
Spiral is sent into burden balance Weighing, and the raw material after metering is sent into raw material surge bunker and keeps in and mix, and mix to ferment
The nutrient balance of product.After each raw material weighs, mixed raw material enters through the feeding serew of raw material surge bunker bottom to feed intake
Elevator after the mixed raw material after promotion is kept in into the surge bunker that feeds intake, is sent into the mixing of raw material mixing machine, and mixed raw material, which enters, mixes
It is temporary to close material surge bunker, subsequently into quality-adjusting device, raw steam enters the inner cavity of quality-adjusting device from raw steam pipe and raw material mixes realization
It is quenched, by the uncooked amylum high-temperature maturing in raw material, the microstructure of starch is destroyed, hydrogen bond is interrupted and reaches gelatinization, change to play
Kind feed nutrition structure, the effect for killing bacterium reduce aerobic fermentation in the process due to the microbial contamination that raw material has, together
When protein, starch etc. in material are denaturalized, be conducive to aerobic fermentation；Mixture after quenched sterilizing is discharged into device of guaranteeing the quality, and guarantees the quality
Device is kept the temperature using steam indirect heating, and it is cooling to be sent into Air cooler after guaranteeing the quality, ingredient after cooling by ingredient airlock into
Enter ingredient air delivery pipe, from the compressed air that roots blower one bloats to fermentation workshop section's feeding.
As an improvement of the present invention, the top outlet inlet of the Air cooler is connected with the air inlet of air-cooled deduster, described
The bottom discharging mouth of air-cooled deduster is connected by closing wind blow-off valve with the entrance of the ingredient airlock, the air-cooled deduster
The exhaust outlet at top is connected with the entrance of ingredient exhaust fan, and the outlet of the ingredient exhaust fan is communicated with atmosphere.From Air cooler top
The fines that portion flies out separates under the swabbing action of ingredient exhaust fan into air-cooled deduster, and fines enters through ingredient airlock
The recycling of ingredient air delivery pipe.
As a further improvement of the present invention, the outlet of the ingredient air delivery pipe and aerobic bacteria liquid pipe access liquid material jointly
The discharge end top of the feed end of blending transportation machine, the liquid material blending transportation machine is connected with the outlet at bottom of aerobic bacteria powder cabin,
It is connected below the discharge end of the liquid material blending transportation machine with the feed inlet of the bacterium powder material mixing machine；The bacterium powder material is mixed
The discharge port of conjunction machine is connected with the aerobic center expects pipe of the aerobic fermentation machine, the aerobic center expects pipe and aerobic fermentation machine
Each layer aerobic fermentation bed is connected to, and is respectively equipped with water heater funnel, the aerobic center expects pipe in the top plate of each aerobic fermentation layer
Lower port be connected with aerobic discharge pipe.Material by quenched sterilizing enters liquid material from ingredient air delivery pipe and three-way distributing
The arrival end of blending transportation machine, aerobic bacterium solution flow out the arrival end for also entering liquid material blending transportation machine, material from aerobic bacteria liquid pipe
It is sufficiently mixed while advancing along liquid material blending transportation machine with aerobic bacterium solution, cold water can also be injected by aerobic layer liquid injection pipe
Make the water capacity 45% or so of material；Aerobic bacteria powder is discharged from aerobic bacteria powder cabin under the action of bacterium powder feeding auger, enters
The outlet end of liquid material blending transportation machine, then enters bacterium powder material mixing machine jointly with material, enters after mixing with material
The aerobic center expects pipe of aerobic fermentation machine enters each layer aerobic fermentation bed by aerobic center expects pipe.Cold material can be led to
The hot water that aerobic bacteria liquid pipe injects 70 DEG C or so is crossed, hot water, which is first uniformly mixed with material, in liquid material blending transportation machine proposes material temperature
Up to 35 DEG C or so, then mixed with aerobic bacteria powder；Avoiding hot water from directly contacting with aerobic bacteria powder causes aerobic bacteria to be killed by boiling hot.By
The material of aerobic fermentation is discharged from the lower end of aerobic center expects pipe into aerobic discharge pipe.Aerobic fermentation is first used, micro- life is made
Object (mainly mould) generates a large amount of biological metabolite.Operator is sometimes for entering in fermentation machine in fermentation process, no
It is avoidable ground can bring miscellaneous bacteria into, miscellaneous bacteria endangers less in air, but the aerobic fermentation machine ceiling of steel construction be easy to produce it is cold
Condensate, condensed water instill material and can also bring miscellaneous bacteria in material into, cause living contaminants.The top tape recirculated water of every layer of fermentation layer
Heating function makes ceiling be maintained at dew-point temperature or more, can prevent the formation of top plate condensed water, avoids under top plate condensing drip
Bring miscellaneous bacteria, contaminated material into.
As a further improvement of the present invention, the tower body wall side above each layer aerobic fermentation bed is equipped with aerobic layer exhaust outlet
And aerobic layer exhaust door is installed, the tower body wall other side above each layer aerobic fermentation bed is equipped with aerobic layer return air inlet and pacifies
Door is adjusted equipped with aerobic layer return air；Tower body wall below each aerobic fermentation bed is equipped with aerobic layer air inlet, the aerobic layer into
The inside in air port is equipped with atomizer, and the entrance of the atomizer is connected with humidification pipeline；Outside the aerobic layer air inlet
End is connected with the air outlet of aerobic fermentation heat exchanger, the air inlet of the aerobic fermentation heat exchanger and going out for aerobic fermentation blower
Air port is connected, and the air inlet of the aerobic fermentation blower is new with aerobic fermentation backwind tube and aerobic fermentation respectively by three-way pipeline
Air hose is connected, and the aerobic fermentation backwind tube is connected with the external port that the aerobic layer return air adjusts door, and the aerobic fermentation is new
Air hose adjusts door by aerobic layer fresh air and communicates with atmosphere.Pass through aerobic layer air inlet to aerobic fermentation by aerobic fermentation blower
Air is sent into bed lower section, and the temperature of air is adjusted by aerobic fermentation heat exchanger, and the suitable air of temperature passes through aerobic fermentation
The eyelet of bed is uniformly blown out upwards, is supplied oxygen to material, and air a part across the bed of material is discharged from aerobic layer exhaust door, separately
A part adjusts door discharge by aerobic layer return air, enters jointly with the fresh air entered from aerobic layer fresh air adjusting door aerobic
The entrance of fermentation blower changes the adjustable return air amount of aperture that aerobic layer return air adjusts door；Change aerobic layer fresh air and adjusts door
The adjustable fresh air volume of aperture.It is mixed using fresh air and return air, can not only guarantee the oxygen content of aerobic layer, but also can recycle
Partial heat is with energy saving.Fresh air can be followed to humidify material by atomizer, made relatively wet in fermentation tower
Degree is maintained at 90% or more, is conducive to microorganism growth.
As a further improvement of the present invention, the upper end interface of the aerobic fermentation heat exchanger be connected separately with steam valve and
Cooling sea water outlet valve, the entrance of the steam valve are connected with raw steam pipe, and outlet and the cooling water of the cooling sea water outlet valve go out
Water pipe is connected；The lower end interface of the aerobic fermentation heat exchanger is connected separately with condensate water discharging valve and cooling sea water inlet valve, institute
The outlet for stating condensate water discharging valve is connected with condensate pipe, and the entrance of the cooling sea water inlet valve is connected with cooling water inlet pipe.
When the air of aerobic layer needs to heat, steam valve and condensate water discharging valve are opened simultaneously, closes cooling sea water inlet valve and cooling water
Outlet valve, steam enter aerobic fermentation heat exchanger, become condensed water from the discharge of condensate water discharging valve after heating air.Aerobic layer
When air needs cooling, cooling sea water inlet valve and cooling sea water outlet valve, steam off valve and condensate water discharging valve are opened simultaneously, it is cold
But water enters aerobic fermentation heat exchanger, is discharged after cooling air from cooling sea water outlet valve.
As a further improvement of the present invention, the outlet and the entrance phase of aerobic material conveyor of the aerobic discharge pipe
Even, the outlet of the aerobic material conveyor is connected by airlock with aerobic material pneumatic conveying pipe, the aerobic material pneumatic conveying pipe
Outlet the entrance of anaerobism liquid material mixing machine is accessed by hauling-chain frame with the outlet of anaerobic bacteria liquid pipe, the anaerobism liquid material mixes
Machine is located on the shared cloth track above each anaerobic fermentation tank feed inlet, can translate along shared cloth track and to each anaerobism
The feed inlet cloth of fermentor；The discharge port of each anaerobic fermentation tank is connected with anaerobism material belt conveyor respectively, the anaerobism
The discharge end of material belt conveyor is connected with anaerobism discharge pipe.Material through aerobic fermentation enters aerobic material conveyor, then
The entrance for entering anaerobism liquid material mixing machine through aerobic material pneumatic conveying pipe, the anaerobism bacterium solution being discharged from anaerobic bacteria liquid pipe also enter anaerobism
The entrance of liquid material mixing machine.In anaerobism liquid material mixing machine, material is discharged after evenly mixing with anaerobism bacterium solution, subsequently into anaerobism
The feed inlet of fermentor.Anaerobism liquid material mixing machine is moved along cloth track is shared, and can be fed, be reduced to more anaerobic fermentation tanks
The quantity of mixing machine.Into anaerobic fermentation tank material after anaerobic fermentation, use lactic acid bacteria, saccharomycete, bacillus etc. produce
Raw biological metabolite and the fragrance and fragrance for inducing feed intake, increase the probiotics and biological metabolism species that fermentation generates
Class, beneficial bacterium are improved the intracorporal beneficial flora of body of animal, are improved the immunity of animal by feed intake, improve the strong of animal
Kang Shuiping further improves the effect of biological fermentation feed.The aerobic biological metabolite generated with anaerobic fermentation is sent out in anaerobism
Harmful substance, anti-nutrient substance in fermentation tank in decomposition raw material；Simultaneously by protein, starch resolve into small peptide, amino acid, with it is small
Molecular polysaccharide helps animal digestion, improves digestibility and animal feed utilization efficiency.Material after anaerobic fermentation directly comes anaerobism
Expect on belt conveyor, after the discharge of the discharge end of anaerobism material belt conveyor, is slipped under anaerobism discharge pipe.
As a further improvement of the present invention, the entrance phase of the outlet of the anaerobism discharge pipe and dry and wet material mixing machine
Even, the outlet of the dry and wet material mixing machine is connected by airlock with mixture air delivery pipe, the mixture air delivery pipe
It exports and is connected with the feed inlet on state drying tower top living, hot wind inlet and the drying tower heater of the state drying tower living lower part
Air outlet is connected；The discharge port of the dry tower bottom of state living is connected with the dry elephant trunk of level-one；At the top of the state drying tower living
Exhaust outlet is connected with the air inlet of drying tower cyclone, and discharge gate and the level-one drying of drying tower cyclone bottom are slipped
Pipe is connected, and the exhaust outlet at the top of the drying tower cyclone is connected by drying tower cyclone exhaust fan with washing blast pipe, institute
It states washing blast pipe to be connected with the lower entrances of scrubbing tower, the entrance phase of the outlet at bottom and scrubbing tower circulating pump of the scrubbing tower
Even, the outlet of the scrubbing tower circulating pump is connected by scrubbing tower circulation pipe with the spray tube on the scrubbing tower top, described to wash
The exhaust outlet for washing top of tower is communicated with atmosphere.The wet stock being discharged from anaerobism discharge pipe is easy bonding, does with a certain proportion of
Material enters dry and wet material mixing machine jointly and mixes, and reduces water capacity, improves and can transport property, and moisture content is 25~30% after mixing,
Into mixture air delivery pipe, it is sent into the upper layer of state drying tower living by mixture air delivery pipe, and flows from above to below；Air quilt
Become hot wind after the heating of drying tower heater, hot wind from the lower part of state drying tower living enters air by drying tower and upwards and material
Reverse flow, the material water ratio after state drying tower living is dry drop to 18~25%, from the discharge port of the dry tower bottom of state living
It is discharged into the dry elephant trunk of level-one.State drying tower living is dry using counter flow flash, and since dry moisture content is high, the higher sky of temperature can be used
Gas is dry, while being able to maintain the microbial activity and biological metabolite activity of fermentation materials.Due to using the sky of higher temperature
Gas, is arranged two layers of drying bed in state drying tower living, and the cascade utilization energy reduces total energy consumption.From discharge at the top of state drying tower living
The tail gas containing tiny material enter the air inlet of drying tower cyclone, it is tiny by centrifuge separation in drying tower cyclone
Material is deposited in the bottom of drying tower cyclone, is also discharged into level-one by airlock from the bottom discharging mouth of drying tower cyclone and does
Dry elephant trunk enables tiny material to recycle.The cleaner tail gas being discharged from the top vent of drying tower cyclone, which enters, to be washed
Blast pipe is washed, the lower entrances of scrubbing tower are entered from washing blast pipe, air-flow flows up in scrubbing tower, wash tower bottoms
Water is washed the extraction of tower circulating pump, and washed tower circulation pipe enters spray tube and uniformly sprays downwards, washs to tail gas, clean
Net tail gas is discharged from the top vent of scrubbing tower, substantially increases environmental benefit.
As a further improvement of the present invention, the dry elephant trunk of the level-one is connected with the entrance of pneumatic conveying drying feeder, gas
The outlet for flowing dry feeder is connected with the air delivery pipe entrance of pneumatic drier, the air delivery pipe entrance of the pneumatic drier
Also it is connected with the outlet of dispersing device, the lower inlet of the dispersing device is connected with the air outlet of pneumatic conveying drying heater；Institute
The air delivery pipe outlet for stating pneumatic drier is connected with the air inlet of big cloth envelop collector, and the bottom of the big cloth envelop collector is set
There are two drier outlets, one of them is connected by siccative reflux elephant trunk with the entrance of the dry and wet material mixing machine, another is dry
Material outlet is connected by secondary drying elephant trunk with the entrance of roller cooler, the roller cooler outlet and product discharge pipe phase
Even；The exhaust outlet on the big cloth envelop collector top is connected with big cloth envelop collector exhaust fan, the big cloth envelop collector exhausting
The outlet of machine is connected with the washing blast pipe；The air inlet of air outlet and beanbag filter at the top of the roller cooler
It is connected, the air outlet of beanbag filter top is connected with beanbag filter exhaust fan, the beanbag filter exhaust fan
Outlet be connected with the washing blast pipe.Enter pneumatic conveying drying feeding from the dry elephant trunk of level-one by the dry material of level-one
Device, the air delivery pipe entrance of pneumatic drier is entered from pneumatic conveying drying feeder, and air is heated as by pneumatic conveying drying heater
Hot wind, hot wind enter from the lower section of dispersing device, and granule materials are pushed by hot wind and flowed up along pneumatic conveying drying hot air pipe, conglomeration
Material fall, smashed by dispersing device, also flowed up with hot wind, hot wind and material carry out hot wet friendship in flow process
It changes, drops to 10~12% by the material water ratio of secondary drying, into being separated in big cloth envelop collector, material is from big
The bottom drier outlet of cloth envelop collector is discharged, small part siccative by siccative reflux elephant trunk return to dry and wet material mixing machine with stick it is wet
Material mixing, improves the transportation performance of material, prevents from being bonded on the way；Most of siccative enters the cooling of roller cooler, after cooling
Finished product be discharged and pack through product discharge pipe.Through the filtered secondary drying tail gas of big cloth envelop collector from big cloth envelop collector
Upper air vent extracted out by big cloth envelop collector exhaust fan, and by from washing blast pipe be sent into scrubbing tower washing.From roller
The cooling wind tail gas of the top discharge of cooler, separates, fine particle also enters product discharge pipe, tail into beanbag filter
Gas is extracted out through beanbag filter exhaust fan, is sent into scrubbing tower washing also by from washing blast pipe.
As a further improvement of the present invention, the drying tower heater and pneumatic conveying drying heater are along the flowing side of air
To hot water and steam heating unit is successively arranged, the medium inlet on the steam heating unit top is connected with raw steam pipe, institute
The media outlet for stating steam heating unit lower part is connected with the medium inlet of hot water heating unit lower part, the hot water heating unit
The media outlet on top is connected with condensate pipe.Air is in drying tower heater and pneumatic conveying drying heater along hot water and steam
When heating unit flow forward, temperature is gradually risen.Raw steam enters steam heating unit and adds to the higher hot wind of temperature
Heat, discharge the latent heat of vaporization steam become condensed water from steam heating unit flow out, enter back into hot water heating unit to temperature compared with
Low air is heated, and is discharged after discharging sensible heat from condensate pipe.
As another improvement of the invention, the outlet and the entrance phase of chain belt conveyer of the anaerobism discharge pipe
Even, the outlet of the chain belt conveyer is connected with the feed inlet of fluid bed dryer, the discharging of the fluid bed dryer
Mouth is connected with product discharge pipe；The lower section of the fluid bed dryer is equipped with multiple fluidized bed air inlets, close to the more of feed end
A fluidized bed air inlet is high temperature air inlet, and the high temperature air inlet is gone out by high-temperature hot-air pipe and fluidized bed high temperature heater (HTH)
Air port is connected, and the air inlet of fluidized bed high temperature heater (HTH) is connected with the outlet of fluidized bed high temperature pressure fan；Close to the stream of discharge end
Change bed air inlet be cooling air inlet, between high temperature air inlet and cooling air inlet be low temperature air inlet, the low temperature into
Air port is connected by low temperature hot air pipe with the air outlet of fluidized bed low-temperature heater, the air inlet of the fluidized bed low-temperature heater
Be connected with the outlet of fluidized bed cold air distribution machine, the outlet of the fluidized bed cold air distribution machine also pass through cooling air supply tube with it is described
Cooling air inlet is connected, and the entrance of the fluidized bed cold air distribution machine and fluidized bed high temperature pressure fan is communicated with atmosphere.From detesting
The wet stock of oxygen discharge pipe discharge is sent into the feed inlet of fluid bed dryer through chain belt conveyer, mobile to discharge port
In the process, material is constantly blown afloat by the hot wind being blown into below fluid bed dryer, and the humidity of materials for having just enter into fluidized bed is higher,
The high-temperature hot-air sent out with high-temperature hot-air pipe contacts, and dries out rapidly；As material is mobile to discharge port, moisture content gradually drops
Low, material is contacted with the low temperature hot wind that low temperature hot air pipe is sent out at this time, further dries out, moisture content is made to meet the requirements；When
The cooling wind that cooled air supply tube is sent into when material is moved to close to discharge port cools, and finally dried material goes out from product
Expects pipe discharge.
As a further improvement of the present invention, the top of the fluid bed dryer is equipped with multiple fluidized bed air outlets, respectively
Fluidized bed air outlet is connected with the air inlet of fluidized bed cyclone respectively, and the air outlet of each fluidized bed cyclone is removed with cloth bag respectively
The air inlet of dirt device is connected, and the discharge gate of each fluidized bed cyclone and bag filter passes through two-stage dust removal pipeline and second level respectively
The air inlet of cyclone is connected, and the discharge gate of second level cyclone passes through the discharge end phase of fluidized bed feed back pipe and fluid bed dryer
Even, the air outlet of second level cyclone is connected with the air inlet of the bag filter, and the air outlet of the bag filter passes through
Deduster exhaust fan is communicated with atmosphere.The material for following hot wind to fly out at the top of fluid bed dryer enters each fluidized bed cyclone
Middle carry out cyclonic separation, material are deposited in the bottom of each fluidized bed cyclone, and hot wind is discharged from the top of fluidized bed cyclone, into
Enter bag filter and further retains material；From the material of bag filter and each fluidized bed cyclone bottom discharge, with air-flow
Enter second level cyclone through two-stage dust removal pipeline, carry out cyclonic separation again, isolated material is returned from fluidized bed feed back pipe
It is recycled into fluid bed dryer, the air being discharged at the top of second level cyclone is again introduced into bag filter filtering, clean
Net air is extracted out by deduster exhaust fan, environmental-friendly.
Detailed description of the invention
The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments, attached drawing only provide with reference to
Illustrate to use, it is non-to limit the present invention.
Fig. 1 is the flow chart of ingredient station in the present invention.
Fig. 2 is the flow chart of fermentation one separate unit aerobic fermentation machine of workshop section's embodiment in the present invention.
Fig. 3 is the flow chart of fermentation 2 two aerobic fermentation machines of workshop section's embodiment in the present invention.
Fig. 4 is the flow chart of anaerobic fermentation in present invention fermentation workshop section.
Fig. 5 is the flow chart of drying section embodiment one in the present invention.
Fig. 6 is the flow chart of drying section embodiment two in the present invention.
In figure: 1. cast hoppers；2. raw material elevator；3. batch bin；3a. ingredient spiral；4. burden balance；5. raw material buffers
Storehouse；6. feed intake elevator；7. feed intake surge bunker；8. raw material mixing machine；9. mixture surge bunker；10. quality-adjusting device；11. device of guaranteeing the quality；
12. Air cooler；13. ingredient airlock；14. air-cooled deduster；15. ingredient exhaust fan；16. aerobic bacteria powder cabin；17. liquid material mixes
Conveyer；18. bacterium powder material mixing machine；19. aerobic fermentation bed；19a. aerobic layer air inlet；19b. aerobic layer exhaust door；19c.
Aerobic fermentation heat exchanger；19d. aerobic fermentation blower；19e. atomizer；19f. aerobic layer return air adjusts door；19g. aerobic layer
Fresh air adjusts door；20. aerobic material conveyor；21. hauling-chain frame；22. anaerobism liquid material mixing machine；23. anaerobic fermentation tank；24. detesting
Oxygen discharging spiral；25. anaerobism material belt conveyor；26. dry and wet material mixing machine；27. state drying tower living；28. drying tower cyclone；
29. scrubbing tower；30. pneumatic drier；30a. pneumatic conveying drying feeder；31. dispersing device；32. big cloth envelop collector；33. rolling
Cylinder cooler；34. beanbag filter；35. chain belt conveyer；36. fluid bed dryer；37. fluidized bed cyclone；
38. bag filter；39. second level cyclone；L1. roots blower one；L2. roots blower two；L3. roots blower three；B1. it washs
Tower circulating pump；F1. big cloth envelop collector exhaust fan；F2. beanbag filter exhaust fan；F3. drying tower cyclone exhaust fan；
F4. fluidized bed high temperature pressure fan；F5. fluidized bed cold air distribution machine；F6. deduster exhaust fan；H1. drying tower heater；H2. gas
Flow drying heater；H3. fluidized bed high temperature heater (HTH)；H4. fluidized bed low-temperature heater；G1. steam pipe is given birth to；G2. ingredient wind is sent
Pipeline；G3. aerobic bacteria liquid pipe；G4. pipeline is humidified；G5. aerobic discharge pipe；G6. condensate pipe；G7. cooling water inlet pipe；
G8. cooling water outlet pipe；G9. hot water circuit water inlet pipe；G10. hot water circuit outlet pipe；G11. anaerobic bacteria liquid pipe；G12. aerobic
Material pneumatic conveying pipe；G13. anaerobism discharge pipe；G14. mixture air delivery pipe；G15. the dry elephant trunk of level-one；G16. washing air inlet
Pipe；G17. scrubbing tower circulation pipe；G18. siccative reflux elephant trunk；G19. secondary drying elephant trunk；G20. product discharge pipe；G21. it cools down
Air supply tube；G22. two-stage dust removal pipeline；G23. fluidized bed feed back pipe；G24. high-temperature hot-air pipe；G25. low temperature hot air pipe.
Specific embodiment
As shown in Figure 1, after the present invention is first aerobic anaerobic organism feed addictive production system, including it is proportioner, good
Aerobe fermentation machine and anaerobic fermentation tank 23.Proportioner includes cast hopper 1 and raw material elevator 2, the outlet at bottom and original of cast hopper 1
Expect that the lower inlet of elevator 2 is connected, the upper end outlet of raw material elevator 2 is connected with the upper end entrance of multiple batch bins 3, respectively matches
The bottom of feed bin 3 is respectively equipped with ingredient spiral 3a, and the outlet of each ingredient spiral 3a is connected with the entrance of burden balance 4 respectively, ingredient
The outlet of scale 4 is connected with the entrance of raw material surge bunker 5, feeding serew outlet and the elevator 6 that feeds intake of 5 bottom of raw material surge bunker
Entrance is connected, and the outlet for the elevator 6 that feeds intake is connected with the entrance for the surge bunker 7 that feeds intake, and the outlet for the surge bunker 7 that feeds intake is mixed with raw material
The entrance of machine 8 is connected, and the outlet of raw material mixing machine 8 is connected with the entrance of mixture surge bunker 9, the outlet of mixture surge bunker 9
It is connected with the feed inlet of quality-adjusting device 10, the discharge port of quality-adjusting device 10 is connected with the feed inlet for device 11 of guaranteeing the quality, and quality-adjusting device 10 and guarantees the quality
The steam inlet of device 11 is connected with raw steam pipe G1 respectively, and the discharge port for device 11 of guaranteeing the quality is connected with the feed inlet of Air cooler 12, wind
The discharge port of cold 12 is connected by ingredient airlock 13 with ingredient air delivery pipe G2.
Various raw materials can pour into respectively in cast hopper 1, be promoted to high-order by raw material elevator 2 and enter corresponding ingredient
It is stored in storehouse 3, when ingredient, each raw material is successively sent into 4 Weighing of burden balance by corresponding ingredient spiral 3a, the raw material after metering
It is sent into raw material surge bunker 5 to keep in and mix, mix makes the nutrient balance of fermented product.After each raw material weighs,
Mixed raw material enters the elevator 6 that feeds intake through the feeding serew of 5 bottom of raw material surge bunker, and the mixed raw material after promotion is slow into feeding intake
Rush storehouse 7 it is temporary after, be sent into raw material mixing machine 8 and mix, it is temporary that mixed raw material enters mixture surge bunker 9, subsequently into quality-adjusting device
10, raw steam from raw steam pipe G1 enter the inner cavity of quality-adjusting device 10 mix with raw material realize it is quenched, by the uncooked amylum height in raw material
Temperature curing, destroys the microstructure of starch, interrupts hydrogen bond and reach gelatinization, so that playing improves feed nutrition structure, kills bacterium
Effect, reduce the microbial contamination being had during aerobic fermentation due to raw material, while by protein, starch etc. in material
Denaturation, is conducive to aerobic fermentation；Mixture after quenched sterilizing is discharged into device 11 of guaranteeing the quality, device 11 of guaranteeing the quality using steam indirect heating into
The cooling of Air cooler 12 is sent into row heat preservation after guaranteeing the quality, ingredient after cooling enters ingredient air delivery pipe G2 by ingredient airlock 13,
From one L1 of roots blower bloat compressed air to fermentation workshop section's feeding.
The top outlet inlet of Air cooler 12 is connected with the air inlet of air-cooled deduster 14, the bottom discharging of air-cooled deduster 14
Mouth is connected by closing wind blow-off valve with the entrance of ingredient airlock 13, the exhaust outlet and ingredient exhaust fan at air-cooled 14 top of deduster
15 entrance is connected, and the outlet of ingredient exhaust fan 15 is communicated with atmosphere.The fines to fly out at the top of Air cooler 12 is in ingredient exhausting
It under the swabbing action of machine 15, is separated into air-cooled deduster 14, fines enters ingredient air delivery pipe G2 through ingredient airlock 13 and returns
It receives.
As shown in Figure 2 and Figure 3, the outlet of ingredient air delivery pipe G2 and aerobic bacteria liquid pipe G3 access liquid material blending transportation jointly
The discharge end top of the feed end of machine 17, liquid material blending transportation machine 17 is connected with the outlet at bottom of aerobic bacteria powder cabin 16, and liquid material is mixed
It closes and is connected below the discharge end of conveyer 17 with the feed inlet of bacterium powder material mixing machine 18；The discharge port of bacterium powder material mixing machine 18
It is connected with the aerobic center expects pipe of aerobic fermentation machine, each layer aerobic fermentation bed 19 of aerobic center expects pipe and aerobic fermentation machine connects
Logical, the lower port of aerobic center expects pipe is connected with aerobic discharge pipe G5.
Material by quenched sterilizing enters entering for liquid material blending transportation machine 17 from ingredient air delivery pipe G2 and three-way distributing
Mouth end, aerobic bacterium solution flow out the arrival end for also entering liquid material blending transportation machine 17 from aerobic bacteria liquid pipe G3, and material is mixed along liquid material
It closes while conveyer 17 advances and is sufficiently mixed with aerobic bacterium solution, can also inject cold water by aerobic layer liquid injection pipe makes material
Water capacity is 45% or so；Aerobic bacteria powder is discharged from aerobic bacteria powder cabin 16 under the action of bacterium powder feeding auger, mixed into liquid material
The outlet end for closing conveyer 17, then enters bacterium powder material mixing machine 18 jointly with material, enters after mixing with material
The aerobic center expects pipe of aerobe fermentation machine enters each layer aerobic fermentation bed 19 by aerobic center expects pipe.
The hot water that 70 DEG C or so can be injected by aerobic bacteria liquid pipe G3 for cold material, in liquid material blending transportation machine 17
Hot water, which is first uniformly mixed with material, improves material temperature to 35 DEG C or so, then mixes with aerobic bacteria powder；Avoid hot water directly with it is aerobic
The contact of bacterium powder causes aerobic bacteria to be killed by boiling hot.Enter aerobic discharging from the lower end of aerobic center expects pipe by the material of aerobic fermentation to slip
Pipe G5 discharge.
Water heater funnel, the top tape circulating water heating of every layer of fermentation layer are respectively equipped in the top plate of each aerobic fermentation layer
Function, hot water enter from hot water circuit water inlet pipe G9, flow out from hot water circuit outlet pipe G10, ceiling is made to be maintained at dew-point temperature
More than, the formation of top plate condensed water can be prevented, avoids bringing miscellaneous bacteria under top plate condensing drip, pollutes aerobic material.
The tower body wall side of each 19 top of layer aerobic fermentation bed is equipped with aerobic layer exhaust outlet and is equipped with aerobic layer air draft
Door 19b, the tower body wall other side of each 19 top of layer aerobic fermentation bed are equipped with aerobic layer return air inlet and are equipped with aerobic layer return air
Adjust door 19f；The tower body wall of each 19 lower section of aerobic fermentation bed is equipped with aerobic layer air inlet 19a, and aerobic layer air inlet 19a's is interior
Side is equipped with atomizer 19e, and the entrance of atomizer 19e is connected with humidification pipeline G4；The external end head of aerobic layer air inlet 19a with
The air outlet of aerobic fermentation heat exchanger 19c is connected, the air inlet of aerobic fermentation heat exchanger 19c and going out for aerobic fermentation blower 19d
Air port is connected, and the air inlet of aerobic fermentation blower 19d is new with aerobic fermentation backwind tube and aerobic fermentation respectively by three-way pipeline
Air hose is connected, and aerobic fermentation backwind tube is connected with the external port that aerobic layer return air adjusts door 19f, and aerobic fermentation fresh wind tube passes through
Oxygen layer fresh air adjusts door 19g and communicates with atmosphere.
By aerobic fermentation blower 19d by aerobic layer air inlet 19a to being sent into air, air below aerobic fermentation bed 19
Temperature be adjusted by aerobic fermentation heat exchanger 19c, the suitable air of temperature by the eyelet of aerobic fermentation bed 19 uniformly to
Upper blowout, is supplied oxygen to material, and air a part across the bed of material is discharged from aerobic layer exhaust door 19b, and another part passes through
Aerobic layer return air adjusts door 19f discharge, enters aerobic fermentation jointly with the fresh air that door 19g enters is adjusted from aerobic layer fresh air
The entrance of blower 19d changes the adjustable return air amount of aperture that aerobic layer return air adjusts door 19f；Change aerobic layer fresh air to adjust
The adjustable fresh air volume of aperture of door 19g.It is mixed using fresh air and return air, can not only guarantee the oxygen content of aerobic layer, but also can
With recovery section heat with energy saving.Fresh air can be followed to humidify material by atomizer 19e, made in fermentation tower
Relative humidity be maintained at 90% or more, be conducive to microorganism growth.
The upper end interface of aerobic fermentation heat exchanger 19c is connected separately with steam valve and cooling sea water outlet valve, and steam valve enters
Mouth is connected with raw steam pipe G1, and the outlet of cooling sea water outlet valve is connected with cooling water outlet pipe G8；Aerobic fermentation heat exchanger 19c's
Lower end interface is connected separately with condensate water discharging valve and cooling sea water inlet valve, outlet and the condensate pipe G6 phase of condensate water discharging valve
Even, the entrance of cooling sea water inlet valve is connected with cooling water inlet pipe G7.
When the air of aerobic layer needs to heat, steam valve and condensate water discharging valve are opened simultaneously, closes cooling sea water inlet valve
And cooling sea water outlet valve, steam enter aerobic fermentation heat exchanger 19c, become condensed water from condensate water discharging valve row after heating air
Out.When the air of aerobic layer needs cooling, cooling sea water inlet valve and cooling sea water outlet valve, steam off valve and condensation are opened simultaneously
Water drain valve, cooling water enter aerobic fermentation heat exchanger 19c, are discharged after cooling air from cooling sea water outlet valve.
As shown in figure 4, the outlet of aerobic discharge pipe G5 is connected with the entrance of aerobic material conveyor 20, aerobic material is defeated
The outlet of machine 20 is sent to be connected by airlock with aerobic material pneumatic conveying pipe G12, the air inlet of aerobic material pneumatic conveying pipe G12 and Roots
The outlet of two L2 of blower is connected, and the outlet of aerobic material pneumatic conveying pipe G12 and the outlet of anaerobic bacteria liquid pipe G11 pass through hauling-chain frame 21
The entrance of anaerobism liquid material mixing machine 22 is accessed, anaerobism liquid material mixing machine 22 is located at sharing above each 23 feed inlet of anaerobic fermentation tank
On cloth track, it can be translated along shared cloth track and to the feed inlet cloth of each anaerobic fermentation tank 23；Each anaerobic fermentation tank
23 discharge port is connected with anaerobism material belt conveyor 25 respectively, and the discharge end and anaerobism of anaerobism material belt conveyor 25 discharge
Elephant trunk G13 is connected.
Material through aerobic fermentation enters aerobic material conveyor 20, then enters anaerobism liquid through aerobic material pneumatic conveying pipe G12
The entrance for expecting mixing machine 22, the anaerobism bacterium solution being discharged from anaerobic bacteria liquid pipe G11 also enter the entrance of anaerobism liquid material mixing machine 22.?
In anaerobism liquid material mixing machine 22, material is discharged after evenly mixing with anaerobism bacterium solution, subsequently into the feed inlet of anaerobic fermentation tank 23.
Anaerobism liquid material mixing machine 22 is moved along shared cloth track, can be fed to more anaerobic fermentation tanks 23, be reduced the number of mixing machine
Amount.Into anaerobic fermentation tank 23 material after anaerobic fermentation, increase fermentation generate probiotics and biological metabolism species,
Further improve the effect of biological fermentation feed.Material after anaerobic fermentation directly comes anaerobism material by anaerobism discharging spiral 24
On belt conveyor 25, after the discharge of the discharge end of anaerobism material belt conveyor 25, slipped under anaerobism discharge pipe G13.
Aerobic fermentation is first used, microorganism (mainly mould) is made to generate a large amount of biological metabolite；Anaerobism hair is carried out again
Ferment generates biological metabolite using lactic acid bacteria, saccharomycete, bacillus etc. and induces the fragrance and fragrance of feed intake, beneficial
Bacterium is improved the intracorporal beneficial flora of body of animal, is improved the immunity of animal, improve the general level of the health of animal by feed intake.
The aerobic biological metabolite generated with anaerobic fermentation decomposes harmful substance in raw material, anti-nutrients in anaerobic fermentation tank 23
Matter；Protein, starch are resolved into small peptide, amino acid and micromolecular polysaccharide simultaneously, help animal digestion, improve digestibility with
Animal feed utilization efficiency.
The embodiment one of drying section is as shown in figure 5, the outlet of anaerobism discharge pipe G13 and entering for dry and wet material mixing machine 26
Mouth is connected, and the outlet of dry and wet material mixing machine 26 is connected by airlock with mixture air delivery pipe G14, mixture air delivery pipe
G14 air inlet is connected with the air outlet of three L3 of roots blower, the outlet of mixture air delivery pipe G14 and 27 top of state drying tower living
Feed inlet be connected, the hot wind inlet of 27 lower part of state drying tower living is connected with the air outlet of drying tower heater H1, and drying tower adds
The air inlet of hot device H1 is communicated with atmosphere.The discharge port of 27 bottom of state drying tower living is connected with the dry elephant trunk G15 of level-one；State living is dry
The exhaust outlet at dry 27 top of tower is connected with the air inlet of drying tower cyclone 28, the discharge gate and one of 28 bottom of drying tower cyclone
The dry elephant trunk G15 of grade is connected, the exhaust outlet at 28 top of drying tower cyclone by drying tower cyclone exhaust fan F3 and wash into
Air hose G16 is connected, and washing blast pipe G16 is connected with the lower entrances of scrubbing tower 29, the outlet at bottom and scrubbing tower of scrubbing tower 29
The entrance of circulating pump B1 is connected, and the outlet of scrubbing tower circulating pump B1 passes through the spray of scrubbing tower circulation pipe G17 and 29 top of scrubbing tower
Shower pipe is connected, and the exhaust outlet at 29 top of scrubbing tower is communicated with atmosphere.
The wet stock being discharged from anaerobism discharge pipe G13 is easy bonding, enters dry and wet material jointly with a certain proportion of siccative
Mixing machine 26 mixes, and reduces water capacity, improves and can transport property, and moisture content is 25~30% after mixing, send into mixture wind
Pipeline G14, the upper layer of state drying tower 27 living is sent by mixture air delivery pipe G14, and is flowed from above to below；Air is by drying tower
Become hot wind after heater H1 heating, it is by drying tower and inverse with material upwards that hot wind from the lower part of state drying tower 27 living enters air
To flowing, the material water ratio after state drying tower 27 living is dry drops to 18~25%, the discharging from 27 bottom of state drying tower living
Mouth is discharged into the dry elephant trunk G15 of level-one.
The tail gas containing tiny material being discharged at the top of state drying tower 27 living enters the air inlet of drying tower cyclone 28,
By centrifuge separation in drying tower cyclone 28, tiny material is deposited in the bottom of drying tower cyclone 28, from drying tower picogram
The bottom discharging mouth of dragon 28 is also discharged into the dry elephant trunk G15 of level-one by airlock, and tiny material is enable to recycle.From dry tassor
The cleaner tail gas of the top vent discharge of cron 28 enters washing blast pipe G16, enters washing from washing blast pipe G16
The lower entrances of tower 29, air-flow flow up in scrubbing tower 29, and the water of 29 bottom of scrubbing tower is washed tower circulating pump B1 and takes out
Out, washed tower circulation pipe G17 enters spray tube and uniformly sprays downwards, washs to tail gas, and clean tail gas is from scrubbing tower
29 top vent discharge.
The dry elephant trunk G15 of level-one is connected with the entrance of pneumatic conveying drying feeder 30a, the outlet of pneumatic conveying drying feeder 30a
Be connected with the air delivery pipe entrance of pneumatic drier 30, the air delivery pipe entrance of pneumatic drier 30 also with dispersing device 31 go out
Mouth is connected, and the lower inlet of dispersing device 31 is connected with the air outlet of pneumatic conveying drying heater H2, pneumatic conveying drying heater H2's
Air inlet is communicated with atmosphere；The air delivery pipe outlet of pneumatic drier 30 is connected with the air inlet of big cloth envelop collector 32, big cloth
The bottom of bag type filter 32 is set there are two drier outlet, one of them passes through siccative reflux elephant trunk G18 and dry and wet material mixing machine 26
Entrance be connected, another drier outlet is connected by secondary drying elephant trunk G19 with the entrance of roller cooler 33, and roller cools down
The outlet of device 33 is connected with product discharge pipe G20.
Enter pneumatic conveying drying feeder 30a from the dry elephant trunk G15 of level-one by the dry material of level-one, is fed from pneumatic conveying drying
Glassware 30a enters the air delivery pipe entrance of pneumatic drier 30, and air is heated as hot wind, hot wind by pneumatic conveying drying heater H2
Enter from the lower section of dispersing device 31, granule materials are pushed by hot wind and flowed up along pneumatic conveying drying hot air pipe, the material of conglomeration
It falls, is smashed by dispersing device 31, also flowed up with hot wind, hot wind and material carry out hot and humid area in flow process, warp
The material water ratio for crossing secondary drying drops to 10~12%, and into being separated in big cloth envelop collector 32, material is from big cloth bag
The bottom drier outlet of filter 32 is discharged, small part siccative by siccative reflux elephant trunk G18 return to dry and wet material mixing machine 26 with
Glutinous wet stock mixing, improves the transportation performance of material, prevents from being bonded on the way；Most of siccative enters the cooling of roller cooler 33,
Finished product after cooling is discharged and packs through product discharge pipe G20.
The exhaust outlet on big 32 top of cloth envelop collector is connected with big cloth envelop collector exhaust fan F1, big cloth envelop collector exhausting
The outlet of machine F1 is connected with washing blast pipe G16；The air outlet at 33 top of roller cooler and the air inlet of beanbag filter 34
Mouth is connected, and the air outlet at 34 top of beanbag filter is connected with beanbag filter exhaust fan F2, beanbag filter exhausting
The outlet of machine F2 is connected with washing blast pipe G16.
Upper air vent through big cloth envelop collector 32 filtered secondary drying tail gas from big cloth envelop collector 32 is big
Cloth envelop collector exhaust fan F1 extraction, and washed by being sent into scrubbing tower 29 from washing blast pipe G16.From roller cooler 33
The cooling wind tail gas of top discharge, separates into beanbag filter 34, and fine particle also enters product discharge pipe G20, tail gas
It extracts out through beanbag filter exhaust fan F2, is washed also by scrubbing tower 29 is sent into from washing blast pipe G16.
Drying tower heater H1 and pneumatic conveying drying heater H2 is successively arranged hot water along the flow direction of air and steam adds
Hot cell, the medium inlet on steam heating unit top are connected with raw steam pipe G1, the media outlet of steam heating unit lower part
It is connected with the medium inlet of hot water heating unit lower part, the media outlet on hot water heating unit top is connected with condensate pipe G6.
Air in drying tower heater H1 and pneumatic conveying drying heater H2 along hot water and steam heating unit flow forward when, temperature by
Edge up height.Raw steam enters steam heating unit and heats to the higher hot wind of temperature, and the steam for discharging the latent heat of vaporization becomes
Condensed water is flowed out from steam heating unit, is entered back into hot water heating unit and is heated to the lower air of temperature, and sensible heat is discharged
It is discharged afterwards from condensate pipe G6.
The embodiment two of drying section is as shown in fig. 6, the outlet of anaerobism discharge pipe and entering for chain belt conveyer 35
Mouth is connected, and the outlet of chain belt conveyer 35 is connected with the feed inlet of fluid bed dryer 36, and fluid bed dryer 36 goes out
Material mouth is connected with product discharge pipe；The lower section of fluid bed dryer 36 is equipped with multiple fluidized bed air inlets, close to the more of feed end
A fluidized bed air inlet is high temperature air inlet, and high temperature air inlet passes through high-temperature hot-air pipe G24's and fluidized bed high temperature heater (HTH) H3
Air outlet is connected, and the air inlet of fluidized bed high temperature heater (HTH) H3 is connected with the outlet of fluidized bed high temperature pressure fan F4；Close to discharging
The fluidized bed air inlet at end is cooling air inlet, is low temperature air inlet, low temperature between high temperature air inlet and cooling air inlet
Air inlet is connected by low temperature hot air pipe G25 with the air outlet of fluidized bed low-temperature heater H4, fluidized bed low-temperature heater H4's
Air inlet is connected with the outlet of fluidized bed cold air distribution machine F5, and the outlet of fluidized bed cold air distribution machine F5 also passes through cooling air supply tube
G21 is connected with cooling air inlet, and the entrance of fluidized bed cold air distribution machine F5 and fluidized bed high temperature pressure fan F4 are communicated with atmosphere.
The wet stock being discharged from anaerobism discharge pipe is sent into the charging of fluid bed dryer 36 through chain belt conveyer 35
Mouthful, into discharge port moving process, material is constantly blown afloat by the hot wind being blown into below fluid bed dryer 36, has just enter into stream
The humidity of materials for changing bed is higher, contacts with the high-temperature hot-air pipe G24 high-temperature hot-air sent out, dries out rapidly；With material to
Discharge port is mobile, and moisture content gradually decreases, and material is contacted with the low temperature hot air pipe G25 low temperature hot wind sent out at this time, further loses
Moisture is removed, moisture content is made to meet the requirements；The cooling that cooled air supply tube G21 is sent into when material is moved to close to discharge port is air-cooled
But cool down, finally dried material is discharged from product discharge pipe.
The top of fluid bed dryer 36 be equipped with multiple fluidized bed air outlets, each fluidized bed air outlet respectively with fluidisation bed material
The air inlet of cron 37 is connected, and the air outlet of each fluidized bed cyclone 37 is connected with the air inlet of bag filter 38 respectively, respectively
The discharge gate of fluidized bed cyclone 37 and bag filter 38 pass through respectively two-stage dust removal pipeline G22 and second level cyclone 39 into
Air port is connected, and the discharge gate of second level cyclone 39 is connected by fluidized bed feed back pipe G23 with the discharge end of fluid bed dryer 36,
The air outlet of second level cyclone 39 is connected with the air inlet of bag filter 38, and the air outlet of bag filter 38 passes through deduster
Exhaust fan F6 is communicated with atmosphere.
It follows hot wind to enter in each fluidized bed cyclone 37 from the material to fly out at the top of fluid bed dryer 36 and carries out whirlwind
Separation, material are deposited in the bottom of each fluidized bed cyclone 37, and hot wind is discharged from the top of fluidized bed cyclone 37, into cloth bag
Deduster 38 further retains material；From the material of bag filter 38 and each 37 bottom discharge of fluidized bed cyclone, with air-flow
Enter second level cyclone 39 through two-stage dust removal pipeline G22, carry out cyclonic separation again, isolated material is from fluidized bed feed back
Pipe G23 is returned in fluid bed dryer 36 and is recycled, and the air being discharged at the top of second level cyclone 39 is again introduced into cloth bag and removes
Dirt device 38 filters, and clean air is extracted out by deduster exhaust fan F6.
The foregoing is merely the preferable possible embodiments of the present invention, non-therefore limitation patent protection model of the invention
It encloses.In addition to the implementation, the present invention can also have other embodiments, all skills formed using equivalent substitution or equivalent transformation
Art scheme, is all fallen within the protection domain of application claims.Technical characteristic of the present invention without description can be by or using now
There is technology realization, details are not described herein.
Claims (11)
- The production system of anaerobic organism feed addictive after 1. a kind of elder generation is aerobic, including proportioner, aerobic fermentation machine and anaerobism Fermentor, it is characterised in that: the proportioner includes cast hopper and raw material elevator, the outlet at bottom and original of the cast hopper Expect that the lower inlet of elevator is connected, the upper end outlet of raw material elevator is connected with the upper end entrance of multiple batch bins, each ingredient The bottom in storehouse is respectively equipped with ingredient spiral, and the outlet of each ingredient spiral is connected with the entrance of burden balance respectively, the outlet of burden balance It is connected with the entrance of raw material surge bunker, the feeding serew outlet of raw material surge bunker bottom is connected with the entrance for the elevator that feeds intake, and throws The outlet of material elevator is connected with the entrance for the surge bunker that feeds intake, and the outlet for the surge bunker that feeds intake is connected with the entrance of raw material mixing machine, The outlet of raw material mixing machine is connected with the entrance of mixture surge bunker, the outlet and the feed inlet phase of quality-adjusting device of mixture surge bunker Even, the discharge port of the quality-adjusting device is connected with the feed inlet for device of guaranteeing the quality, the steam inlet point of the quality-adjusting device and the device of guaranteeing the quality It is not connected with raw steam pipe, the discharge port of the device of guaranteeing the quality is connected with the feed inlet of Air cooler, and the discharge port of the Air cooler is logical Ingredient airlock is crossed to be connected with ingredient air delivery pipe.
- The production system of anaerobic organism feed addictive after 2. elder generation according to claim 1 is aerobic, it is characterised in that: described The top outlet inlet of Air cooler is connected with the air inlet of air-cooled deduster, and the bottom discharging mouth of the air-cooled deduster is by closing wind Blow-off valve is connected with the entrance of the ingredient airlock, the exhaust outlet of the air-cooled dust remover roof and the entrance of ingredient exhaust fan It is connected, the outlet of the ingredient exhaust fan is communicated with atmosphere.
- The production system of anaerobic organism feed addictive after 3. elder generation according to claim 1 is aerobic, it is characterised in that: described The outlet of ingredient air delivery pipe and aerobic bacteria liquid pipe access the feed end of liquid material blending transportation machine, the liquid material blending transportation jointly Be connected above the discharge end of machine with the outlet at bottom of aerobic bacteria powder cabin, the discharge end lower section of the liquid material blending transportation machine with it is described The feed inlet of bacterium powder material mixing machine is connected；The discharge port of the bacterium powder material mixing machine and the aerobic fermentation machine it is aerobic in Heart expects pipe is connected, and the aerobic center expects pipe is connected to each layer aerobic fermentation bed of aerobic fermentation machine, the top of each aerobic fermentation layer Water heater funnel is respectively equipped in plate, the lower port of the aerobic center expects pipe is connected with aerobic discharge pipe.
- The production system of anaerobic organism feed addictive after 4. elder generation according to claim 3 is aerobic, it is characterised in that: each layer Tower body wall side above aerobic fermentation bed is equipped with aerobic layer exhaust outlet and is equipped with aerobic layer exhaust door, each layer aerobic fermentation The tower body wall other side of bed top, which is equipped with aerobic layer return air inlet and is equipped with aerobic layer return air, adjusts door；Under each aerobic fermentation bed The tower body wall of side is equipped with aerobic layer air inlet, and the inside of the aerobic layer air inlet is equipped with atomizer, the atomizer Entrance with humidification pipeline be connected；The external end head of the aerobic layer air inlet is connected with the air outlet of aerobic fermentation heat exchanger, institute The air inlet for stating aerobic fermentation heat exchanger is connected with the air outlet of aerobic fermentation blower, and the air inlet of the aerobic fermentation blower is logical Three-way pipeline is crossed to be connected with aerobic fermentation backwind tube and aerobic fermentation fresh wind tube respectively, the aerobic fermentation backwind tube with it is described good The external port that oxygen layer return air adjusts door is connected, and the aerobic fermentation fresh wind tube adjusts door by aerobic layer fresh air and communicates with atmosphere.
- The production system of anaerobic organism feed addictive after 5. elder generation according to claim 4 is aerobic, it is characterised in that: described The upper end interface of aerobic fermentation heat exchanger is connected separately with steam valve and cooling sea water outlet valve, the entrance of the steam valve and raw steaming Steam pipe is connected, and the outlet of the cooling sea water outlet valve is connected with cooling water outlet pipe；The lower termination of the aerobic fermentation heat exchanger Mouth is connected separately with condensate water discharging valve and cooling sea water inlet valve, and the outlet of the condensate water discharging valve is connected with condensate pipe, The entrance of the cooling sea water inlet valve is connected with cooling water inlet pipe.
- The production system of anaerobic organism feed addictive after 6. elder generation according to claim 3 is aerobic, it is characterised in that: described The outlet of aerobic discharge pipe is connected with the entrance of aerobic material conveyor, and the outlet of the aerobic material conveyor is by closing wind Device is connected with aerobic material pneumatic conveying pipe, and the outlet of the aerobic material pneumatic conveying pipe and the outlet of anaerobic bacteria liquid pipe pass through hauling-chain frame The entrance of anaerobism liquid material mixing machine is accessed, the anaerobism liquid material mixing machine is located at the shared cloth above each anaerobic fermentation tank feed inlet Expect on track, can be translated along shared cloth track and to the feed inlet cloth of each anaerobic fermentation tank；Each anaerobic fermentation tank Discharge port is connected with anaerobism material belt conveyor respectively, discharge end and the anaerobism discharge pipe phase of the anaerobism material belt conveyor Even.
- The production system of anaerobic organism feed addictive after 7. elder generation according to claim 6 is aerobic, it is characterised in that: described The outlet of anaerobism discharge pipe is connected with the entrance of dry and wet material mixing machine, the outlet of the dry and wet material mixing machine by airlock with Mixture air delivery pipe is connected, and the outlet of the mixture air delivery pipe is connected with the feed inlet on state drying tower top living, described The hot wind inlet of state drying tower lower part living is connected with the air outlet of drying tower heater；The discharge port of the dry tower bottom of state living It is connected with the dry elephant trunk of level-one；Exhaust outlet at the top of the state drying tower living is connected with the air inlet of drying tower cyclone, described The discharge gate of drying tower cyclone bottom is connected with the dry elephant trunk of the level-one, and the exhaust outlet at the top of the drying tower cyclone is logical It crosses dry tassor cron exhaust fan to be connected with washing blast pipe, the washing blast pipe is connected with the lower entrances of scrubbing tower, institute The outlet at bottom for stating scrubbing tower is connected with the entrance of scrubbing tower circulating pump, and the outlet of the scrubbing tower circulating pump is followed by scrubbing tower Endless tube is connected with the spray tube on the scrubbing tower top, and the exhaust outlet at the top of the scrubbing tower is communicated with atmosphere.
- The production system of anaerobic organism feed addictive after 8. elder generation according to claim 7 is aerobic, it is characterised in that: described The dry elephant trunk of level-one is connected with the entrance of pneumatic conveying drying feeder, and the outlet of pneumatic conveying drying feeder and the wind of pneumatic drier are sent Entrance is connected, and the air delivery pipe entrance of the pneumatic drier is also connected with the outlet of dispersing device, the dispersing device Lower inlet be connected with the air outlet of pneumatic conveying drying heater；Air delivery pipe outlet and the big cloth bag mistake of the pneumatic drier The air inlet of filter is connected, and the bottom of the big cloth envelop collector is set there are two drier outlet, one of them is flowed back by siccative Elephant trunk is connected with the entrance of the dry and wet material mixing machine, another drier outlet passes through secondary drying elephant trunk and roller cooler Entrance is connected, and the roller cooler outlet is connected with product discharge pipe；The exhaust outlet on the big cloth envelop collector top and big Cloth envelop collector exhaust fan is connected, and the outlet of the big cloth envelop collector exhaust fan is connected with the washing blast pipe；The rolling Air outlet at the top of cylinder cooler is connected with the air inlet of beanbag filter, the air outlet of beanbag filter top and small cloth Bag type filter exhaust fan is connected, and the outlet of the beanbag filter exhaust fan is connected with the washing blast pipe.
- The production system of anaerobic organism feed addictive after 9. elder generation according to claim 8 is aerobic, it is characterised in that: described Drying tower heater and pneumatic conveying drying heater are successively arranged hot water and steam heating unit, the steaming along the flow direction of air The medium inlet on vapour heating unit top is connected with raw steam pipe, and the media outlet of the steam heating unit lower part adds with hot water The medium inlet of hot cell lower part is connected, and the media outlet on hot water heating unit top is connected with condensate pipe.
- The production system of anaerobic organism feed addictive after 10. elder generation according to claim 6 is aerobic, it is characterised in that: institute The outlet for stating anaerobism discharge pipe is connected with the entrance of chain belt conveyer, the outlet and fluidisation of the chain belt conveyer The feed inlet of bed dryer is connected, and the discharge port of the fluid bed dryer is connected with product discharge pipe；The fluidized bed drying The lower section of machine is equipped with multiple fluidized bed air inlets, and multiple fluidized bed air inlets close to feed end are high temperature air inlet, the height Warm air inlet is connected by high-temperature hot-air pipe with the air outlet of fluidized bed high temperature heater (HTH), the air inlet of fluidized bed high temperature heater (HTH) It is connected with the outlet of fluidized bed high temperature pressure fan；Close to discharge end fluidized bed air inlet be cooling air inlet, between high temperature into It is low temperature air inlet between air port and cooling air inlet, the low temperature air inlet passes through low temperature hot air pipe and fluidized bed low-temperature heat The air outlet of device is connected, and the air inlet of the fluidized bed low-temperature heater is connected with the outlet of fluidized bed cold air distribution machine, described The outlet of fluidized bed cold air distribution machine also passes through cooling air supply tube and is connected with the cooling air inlet, the fluidized bed cold air distribution Machine and the entrance of fluidized bed high temperature pressure fan are communicated with atmosphere.
- The production system of anaerobic organism feed addictive after 11. elder generation according to claim 10 is aerobic, it is characterised in that: institute The top for stating fluid bed dryer is equipped with multiple fluidized bed air outlets, each fluidized bed air outlet respectively with fluidized bed cyclone into Air port be connected, the air outlet of each fluidized bed cyclone is connected with the air inlet of bag filter respectively, each fluidized bed cyclone and The discharge gate of bag filter passes through two-stage dust removal pipeline respectively and is connected with the air inlet of second level cyclone, the row of second level cyclone Material mouth is connected by fluidized bed feed back pipe with the discharge end of fluid bed dryer, and the air outlet of second level cyclone is removed with the cloth bag The air inlet of dirt device is connected, and the air outlet of the bag filter is communicated by deduster exhaust fan with atmosphere.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111457670A (en) * | 2020-03-13 | 2020-07-28 | 江苏丰尚智能科技有限公司 | Novel divide storehouse formula to stabilize cooler |
| CN115152901A (en) * | 2022-07-07 | 2022-10-11 | 山东香驰粮油有限公司 | A production process for improving the rumen rate of ruminant protein |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101690554A (en) * | 2009-10-12 | 2010-04-07 | 哈尔滨牛旺牧业管理有限公司 | Method of producing animal feed from straw |
| CN103126042A (en) * | 2013-03-20 | 2013-06-05 | 张有聪 | Production device and method of biological feeds |
| CN206380654U (en) * | 2016-10-10 | 2017-08-08 | 迈安德集团有限公司 | A kind of automatic aerobic fermentation system |
| CN207519590U (en) * | 2017-08-17 | 2018-06-22 | 迈安德集团有限公司 | A kind of solid state fermentation system |
-
2018
- 2018-11-27 CN CN201811423531.6A patent/CN109321438B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101690554A (en) * | 2009-10-12 | 2010-04-07 | 哈尔滨牛旺牧业管理有限公司 | Method of producing animal feed from straw |
| CN103126042A (en) * | 2013-03-20 | 2013-06-05 | 张有聪 | Production device and method of biological feeds |
| CN206380654U (en) * | 2016-10-10 | 2017-08-08 | 迈安德集团有限公司 | A kind of automatic aerobic fermentation system |
| CN207519590U (en) * | 2017-08-17 | 2018-06-22 | 迈安德集团有限公司 | A kind of solid state fermentation system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111457670A (en) * | 2020-03-13 | 2020-07-28 | 江苏丰尚智能科技有限公司 | Novel divide storehouse formula to stabilize cooler |
| CN115152901A (en) * | 2022-07-07 | 2022-10-11 | 山东香驰粮油有限公司 | A production process for improving the rumen rate of ruminant protein |
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