CN205774166U - Utilize mud and the complete set of equipments of organic solid waste batch production ecoalimental base - Google Patents
Utilize mud and the complete set of equipments of organic solid waste batch production ecoalimental base Download PDFInfo
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- CN205774166U CN205774166U CN201620444368.1U CN201620444368U CN205774166U CN 205774166 U CN205774166 U CN 205774166U CN 201620444368 U CN201620444368 U CN 201620444368U CN 205774166 U CN205774166 U CN 205774166U
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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
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Abstract
This utility model belongs to waste processing arts, relates to a kind of complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base.It includes mud conveying mechanism and organic solid waste conveying mechanism; described mud conveying mechanism and organic solid waste conveying mechanism connect hydrolytic decomposition pot respectively; described hydrolytic decomposition pot connects drying device; the air outlet of described drying device connects air purifier; the discharging opening of drying device connects material conveyer, and material conveyer connects fermentation tank, and fermentation tank connects vibrosieve; vibrosieve connects comminutor, and comminutor connects finished product storage tank.This utility model is reasonable in design, reliable operation, safety, and production efficiency is high, it is easy to popularization and application.
Description
Technical field
This utility model belongs to waste processing arts, relates to a kind of waste treatment equipment, particularly relates to a kind of complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base.
Background technology
Along with China's level of urbanization improves constantly, sewage treatment facility construction has obtained high speed development, more than 2500 has been had according to " the specific resistance to filtration degree of depth investigation of 2013-2017 China is reported with investment strategy planning application " statistics China's urban wastewater treatment firm in 2010, municipal sewage treatment ability has reached every day 1.22 hundred million tons, emission reduction targets and water environment for realizing country improve, and are made that tremendous contribution.But a large amount of excess sludge has been supervened in the construction of Sewage Plant and operation, in terms of moisture content 80%, the whole nation year total aquifer yield of mud will quickly break through 30,000,000 tons, and Treatment of Sludge situation is the severeest.Owing to China's Sewage Plant is in process of construction, for a long time " the light mud of heavy water ", China's urban wastewater treatment firm achieves the preliminary minimizing of mud substantially, but the stabilizing treatment of unrealized mud.According to statistics, about 80% Sewage Plant has the thickening facility of mud, has reached a certain degree of minimizing；There are about the mud of 80% without stabilizing treatment, mud transfers to land containing pollutant such as odorant, pathogen, persistent organisms from sewage, pollutant are caused to spread further so that the environment reduction of discharging benefit having built up the big sewage treatment facility put into operation is had a greatly reduced quality.According to statistics, in current disposal options, landfill accounts for 63.0%, sludge aerobic fermentation+agricultural accounts for 13.5%, mud nature mummification comprehensive utilization accounts for 5.4%, sludge incineration accounts for 1.8%, mud air storage and outward transport and respectively accounts for 1.8% and 14.4%.It is true that the mud overwhelming majority of landfill, air storage and outward transport belongs to arbitrarily disposal, really realize the ratio of safe disposal less than 20%.
Additionally, the quantity of urban garden and green space system area garden waste also gets more and more, the two becomes one of mainly comprising of municipal solid wastes.The common disposal options of both solid organic castoffs is landfill or burns, and this not only adds government's cost to garbage disposal, also wastes the land resource of preciousness, pollutes environment.Containing substantial amounts of organic matter in municipal sludge and garden waste, being not added with utilizing also is greatly to waste resource simultaneously.
On the other hand, the most wide variety of cultivation matrix is peat at present, yet with exhaustive exploitation, mud and charcoal greatly reduces, Wetland ecological can be caused serious destruction by exploitation peat simultaneously, and peat is the most non-renewable, the pressure therefore limiting peat use is increasing, in the urgent need to developing the succedaneum of peat
In order to overcome the deficiencies in the prior art, people are through constantly exploring, have employed various method, such as Chinese patent literature discloses a kind of method and device [application number: 201510133600X] utilizing urban waste to prepare novel ecological cultivation matrix, comprise the following steps: (a) is by garden waste thing Mechanical Crushing that moisture content is 10%～35% to particle diameter≤3cm, and be stirred mixing with first mummification, the rear municipal sludge sheared, obtain mixing raw material；The moisture content of the municipal sludge after drying and other treatment is 60%～90%, and the mass ratio that municipal sludge mixes with garden waste is 1: 0.3～2；B described mixing raw material is sent into and is carried out Steam explosion treatment in steam explosion tank by (), the temperature 180 in control steam explosion tank～260 DEG C, pressure 0.8MPa～2.6MPa, heat-insulation pressure keeping time 10min～20min；Material after Steam explosion treatment is cooled to 50 DEG C～65 DEG C；Material after process carries out cooling down and reclaim its waste heat, obtains hot-air；(c) material after cooling add account for its 0.2～0.5% the aerobic fermentation microbial inoculum of mass carry out aerobic fermentation as Inoculant, be passed through hot-air to keep fermentation temperature required simultaneously, controlling fermentation temperature is 55 DEG C～65 DEG C, fermentation time 5～10 days；Described Inoculant is aerobic fermentation microbial inoculum；D material after described fermentation is carried out sieving, is dried by (), pelletize, obtains ecological cultivation substrate.
Such scheme, by the high temperature high pressure process of steam explosion pretreating process, various pathogen in raw material, parasitic ovum etc. can thoroughly be killed, thus realize environment innoxious.But steam explosion processing pressure is high, temperature is high, has certain danger and complex treatment process.
Utility model content
The purpose of this utility model is for the problems referred to above, it is provided that a kind of complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base.
For reaching above-mentioned purpose, this utility model have employed following technical proposal: a kind of complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, including mud conveying mechanism and organic solid waste conveying mechanism, described mud conveying mechanism and organic solid waste conveying mechanism connect hydrolytic decomposition pot respectively, described hydrolytic decomposition pot connects drying device, the air outlet of described drying device connects air purifier, the discharging opening of drying device connects material conveyer, material conveyer connects fermentation tank, fermentation tank connects vibrosieve, vibrosieve connects comminutor, comminutor connects finished product storage tank.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, described mud conveying mechanism includes sludge storage tank and the cutting machine being connected with the discharging opening of sludge storage tank, the discharging opening of described cutting machine connects hydrolytic decomposition pot, described organic solid waste conveying mechanism includes the auger machine that organic solid waste storage tank and the discharging opening with organic solid waste storage tank are connected, and the discharging opening of described auger machine connects hydrolytic decomposition pot.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, described organic solid waste conveying mechanism also includes the pulverizer being arranged on organic solid waste tank top, and the ribbon conveyer being connected with pulverizer, the first mass flowmenter it is provided with between described cutting machine and hydrolytic decomposition pot, being provided with the second mass flowmenter between described auger machine and hydrolytic decomposition pot, described vibrosieve is also connected with bulky grain storage tank.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, described drying device includes mummification storehouse and the conveyer belt assembly being arranged in mummification storehouse, below conveyer belt assembly, it is provided with the filter assemblies being connected with mummification storehouse inner wall sealing, below filter assemblies, is provided with the turner structure that the material in mummification storehouse can be turned over throwing.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, described conveyer belt assembly includes some conveyer belts, the conveying direction of two the most adjacent conveyer belts is contrary, described filter assemblies includes drainage screen, described turner structure includes the rotating shaft that is rotationally connected with mummification storehouse and the driver with rotating shaft drive connection, described rotating shaft is fixed with some be crisscross arranged turn over throwing spoon.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, the air inlet in described mummification storehouse is sequentially connected with heater and aerator.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, the air outlet in described mummification storehouse connects and connects air purifier successively after heat exchange tank, gas-liquid separator, air-introduced machine, the liquid outlet of gas-liquid separator connects infusion pump, and infusion pump connects coolant storage tank.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, described heat exchange tank includes heat exchange tank body and the spiral heat exchange coil being arranged in heat exchange tank body, described heat exchange coil one end connects the air outlet in mummification storehouse, and the other end of heat exchange coil connects the charging aperture of gas-liquid separator.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, the shaft in hollow it is provided with in described fermentation tank, it is fixedly connected with on shaft and connects with shaft and the stirring paddle of hollow, the end of stirring paddle is provided with the stirring block removably connected with stirring paddle, stirring block is provided with liquid outlet, fermentation tank is provided with and adds flow container, the described two ends adding flow container are fixing with the driver on fermentation tank and shaft respectively to be connected, described add flow container connection shaft it is thus possible to flow out in allowing the liquid adding in flow container enter into shaft and from liquid outlet.
In the above-mentioned complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base, described fermenter base is provided with aeration cover, aeration cover top is rotationally connected with shaft, aeration cover sidepiece is densely covered with solarization air cap, aeration tube it is provided with in fermentation tank, this aeration tube one end is extended outside fermentation tank, and the other end is inserted in aeration cover.
Compared with prior art, the utility model has the advantage of: reasonable in design, reliable operation, safety, production efficiency is high, it is easy to popularization and application.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of drying device；
Fig. 3 is the structural representation of fermentation tank.
nullIn figure: mud conveying mechanism 1、Organic solid waste conveying mechanism 2、Hydrolytic decomposition pot 3、Drying device 4、Air purifier 5、Material conveyer 6、Fermentation tank 7、Vibrosieve 8、Comminutor 9、Finished product storage tank 10、Sludge storage tank 11、Cutting machine 12、Organic solid waste storage tank 13、Auger machine 14、Pulverizer 15、Ribbon conveyer 16、First mass flowmenter 17、Second mass flowmenter 18、Bulky grain storage tank 19、Mummification storehouse 20、Conveyer belt assembly 21、Filter assemblies 22、Turner structure 23、Conveyer belt 24、Drainage screen 25、Rotating shaft 26、Driver 27、Turn over throwing spoon 28、Heater 29、Aerator 30、Heat exchange tank 31、Gas-liquid separator 32、Air-introduced machine 33、Infusion pump 34、Coolant storage tank 35、Heat exchange tank body 36、Heat exchange coil 37、Shaft 38、Stirring paddle 39、Stirring block 40、Liquid outlet 41、Add flow container 42、Aeration cover 43、Aeration tube 44.
Detailed description of the invention
The utility model is described in more detail with detailed description of the invention below in conjunction with the accompanying drawings.
nullAs shown in Figure 1，A kind of complete set of equipments utilizing mud and organic solid waste batch production ecoalimental base，Including mud conveying mechanism 1 and organic solid waste conveying mechanism 2，Described mud conveying mechanism 1 and organic solid waste conveying mechanism 2 connect hydrolytic decomposition pot 3 respectively，Described hydrolytic decomposition pot 3 connects drying device 4，Drying device 4 can select commercially available prod，By the moisture in heating evaporation mud thus improve the solid content of mud，The air outlet of described drying device 4 connects air purifier 5，Air purifier 5 can select cloth-bag type air purifier or electrostatic precipitator，The discharging opening of drying device 4 connects material conveyer 6，Carrier 6 can be auger、Belt type conveyer or feeding engine etc.，Material conveyer 6 connects fermentation tank 7，Fermentation tank 7 can select commercially available prod，Fermentation tank 7 connects vibrosieve 8，Vibrosieve 8 plays sieving actoion，For separating bulky grain mud or vegetation pruning thing etc.，Vibrosieve 8 connects comminutor 9，Comminutor 9 connects finished product storage tank 10.
nullThis utility model，Respectively mud and organic solid waste are carried by mud conveying mechanism 1 and organic solid waste conveying mechanism 2，In the present embodiment，Mud can be municipal sludge、Riverway sludge、In lake silt and other municipal sludge any one or several，Organic solid waste can be straw、Caulis et Folium Oryzae、Urban path tree lop、Afforestation rubbish、Chicken and duck cattle manure、Plant Humus and other cellulosic biological waste etc.，Mixing and hydrolysis is realized in hydrolytic decomposition pot 3，Also will mix and complete with hydrolysing step one step，Mud after hydrolysis is dehydrated by drying device 4 with organic solid waste，Improve solid content，It is known that，Gas-liquid mixture can be produced in dehydration，Then can be to environment as being directly discharged into air，Therefore gas-liquid mixture is passed into after air purifier 5 purifies and discharges，Environment is played a protective role.Material conveyer 6 can select enclosed auger; the conveying making material completes under an air-tight state; prevent the excessive of dust or gas; also play protected effect; being fermented by fermentation tank 7, with comminutor 9 pelletize after vibrosieve 8 classification, product is sent directly into finished product storage tank 10 again; technical process is simple and reliable, it is easy to promote.
Mud conveying mechanism 1 includes the cutting machine 12 that sludge storage tank 11 and the discharging opening with sludge storage tank 11 are connected, preferably, rabbling mechanism can be set in sludge storage tank 11, the discharging opening of described cutting machine 12 connects hydrolytic decomposition pot 3, described organic solid waste conveying mechanism 2 includes the auger machine 14 that organic solid waste storage tank 13 and the discharging opening with organic solid waste storage tank 13 are connected, auger machine 14 belongs to common knowledge, here is omitted, can also arrange rabbling mechanism in organic solid waste storage tank 13, the discharging opening of described auger machine 14 connects hydrolytic decomposition pot 3.nullPreferred version，Organic solid waste conveying mechanism 2 also includes the pulverizer 15 being arranged on organic solid waste storage tank 13 top，And the ribbon conveyer 16 being connected with pulverizer 15，Organic solid waste can first be placed on ribbon conveyer 16，It is sent to pulverizer 15 pulverize，The pulverized particles of pulverizer can be formulated by actual technological parameter，As organic solid waste is ground into below 3mm，The first mass flowmenter 17 it is provided with between described cutting machine 12 and hydrolytic decomposition pot 3，The second mass flowmenter 18 it is provided with between described auger machine 14 and hydrolytic decomposition pot 3，Described vibrosieve 8 is also connected with bulky grain storage tank 19，Operator can directly learn the inlet amount of mud and organic solid waste by the first mass flowmenter 17 and the second mass flowmenter 18，Thus regulate the proportioning of mud and organic solid waste，Therefore regulation inlet amount can realize proportioning，Improve work efficiency，From without the proportioning readjusting content component etc. hydrolytic decomposition pot 3 again.
Shown in Fig. 2, drying device 4 includes mummification storehouse 20 and the conveyer belt assembly 21 being arranged in mummification storehouse 20, below conveyer belt assembly 21, it is provided with the filter assemblies 22 being connected with mummification storehouse 20 inner wall sealing, below filter assemblies 22, is provided with the turner structure 23 that the material in mummification storehouse 20 can be turned over throwing.
Specifically, conveyer belt assembly 21 includes some conveyer belts 24, the conveying direction of two the most adjacent conveyer belts 24 is contrary, namely, material is successively from the conveyer belt 24 that the conveyer belt 24 of the top enters into lower section, the transport path of material can be extended namely extend drying time, work efficiency significantly improves, described filter assemblies 22 includes drainage screen 25, drainage screen 25 is preferably stainless steel filtering net, aperture of filter screen does not limits, can be 10 mesh, 20 mesh, 30 mesh etc., preferably, some elastic components can be set below drainage screen 25, elastic component is fixed on the inwall of mummification storehouse 20, in drainage screen 25 filter process, elastic component makes drainage screen 25 vertical tremor, filter efficiency significantly improves.
In the present embodiment, turner structure 23 includes the rotating shaft 26 that is rotationally connected with mummification storehouse 20 and the driver 27 with rotating shaft 26 drive connection, driver 27 can be motor or oil cylinder etc., be fixed with in described rotating shaft 26 some be crisscross arranged turn over throwing spoon 28, turn over throwing spoon 28 in spoon shape, the snatch rate of material can be improved, improve mummification effect the most further.
The air inlet in mummification storehouse 20 is sequentially connected with heater 29 and aerator 30.Aerator 30 provides air for mummification storehouse 20 is internal, forms hot-air by heater 29 after being heated, as too high in mummification storehouse 20 internal temperature, it is also possible to close down heater 29, only drive aerator 30.
As shown in Figure 1, the air outlet in mummification storehouse 20 connects and connects air purifier 5 successively after heat exchange tank 31, gas-liquid separator 32, air-introduced machine 33, the liquid outlet of gas-liquid separator 32 connects infusion pump 34, infusion pump 34 can be turbine pump, gear pump, plunger displacement pump etc., and infusion pump 34 connects coolant storage tank 35.
Heat exchange tank 31 includes heat exchange tank body 36 and the spiral heat exchange coil 37 being arranged in heat exchange tank body 36, skilled artisan would appreciate that, heat transferring medium such as water, heat exchange oil etc. it is filled with in heat exchange tank body 36, hot mixture in heat exchanging coil pipe 37 carries out heat exchange, after heat transferring medium absorbs heat, temperature rises, can be used for other needing, in the operation heated, to play the effect of energy recovery.Described heat exchange coil 37 one end connects the air outlet in mummification storehouse 20, the other end of heat exchange coil 37 connects the charging aperture of gas-liquid separator 32, it should also be appreciated by one skilled in the art that gas-liquid separator 32 can be shell and tube condenser, finned cooler or cyclone separator etc..
Shown in Fig. 3, the shaft 38 in hollow it is provided with in fermentation tank 7, it is fixedly connected with on shaft 38 and connects with shaft 38 and the stirring paddle 39 of hollow, stirring paddle 39 can be several, upper, middle and lower arranges, the end of stirring paddle 39 is provided with the stirring block 40 removably connected with stirring paddle 39, stirring block 40 is provided with liquid outlet 41, fermentation tank 7 is provided with and adds flow container 42, the described two ends adding flow container 42 are fixed be connected with the drivers on fermentation tank 7 and shaft 38 respectively, the described flow container 42 that adds connects shaft 38 it is thus possible in allowing the liquid added in flow container 42 enter into shaft 38 and flow out from liquid outlet 41.Being provided with aeration cover 43 bottom fermentation tank 7, aeration cover 43 top is rotationally connected with shaft 38, and aeration cover 43 sidepiece is densely covered with solarization air cap, is provided with aeration tube 44 in fermentation tank 7, and this aeration tube 44 one end is extended outside fermentation tank 7, and the other end is inserted in aeration cover 43.
It is known that, during the fermentation, need to add specific fermentation liquid, conditioner, acid solution etc., owing to mud has higher viscosity, the liquid added is not easy rapid dispersion, namely refining weak effect, thus reduce ferment effect, the structure of fermentation tank 7 of the present utility model, when needs add liquid in fermentation tank, can first liquid be joined in flow container 42, liquid flows out from liquid outlet 41 after the shaft 38 of hollow flows through stirring paddle 39, owing to stirring paddle 39 is in rotary state, therefore liquid feeding process is also to carry out in lasting rotary state, the liquid added is disperseed rapidly, dispersion efficiency is fabulous.
nullWork process of the present utility model is: joined by mud in sludge storage tank 11，Bulking agent and ferrous sulfate can be added in sludge storage tank 11、Polyacrylamide etc.，Mud is cut by cutting machine 12，Bulk is shredded，It is continuously fed in hydrolytic decomposition pot 3 after being measured by the first mass flowmenter 17，Organic solid waste first passes through pulverizer 15 and is ground into little granule，Particle diameter stores after being typically smaller than 3mm in organic solid waste storage tank 13，Hydrolytic decomposition pot 3 inside is entered into by auger machine 14 and after the second mass flowmenter 18 is quantitative，Hydrolytic decomposition pot 3 carries out mix and blend to material，And add oxalic acid，Wherein mud、Organic solid waste、Ferrous sulfate、The mass ratio of polyacrylamide and oxalic acid can be 500:1000:500-1000:0.1-1:0.1-1:0.1-1，It is preferably 500:500:0.2:0.3:0.2.
nullThe hydrolysis temperature of hydrolytic decomposition pot 3 is 90-160 DEG C，Hydrolysis time is 0.5-5hr，It is preferably 1hr，Steam or compressed air pressurize can be passed through in hydrolytic decomposition pot 3，Pressurize is between 0.2-0.6MPa，Obtain hydrolysate，The cooperation of heater 29 and aerator 30 produces hot-air and enters into inside, mummification storehouse 20，Hydrolysate enters on the conveyer belt 24 in mummification storehouse 20，Conveyer belt 24 obtains mummification for the first time，By entering into bottom mummification storehouse 20 after drainage screen 25，Turned over throwing spoon 28 and turned over throwing，Carry out second time mummification，Hydrolyzed solution after mummification is entered in fermentation tank 7 by material conveyer 6 and ferments，Fermentation tank 7 temperature 50-65 DEG C，Fermentation time 5-8 days，Obtain fermentation material，After fermentation material is sieved by vibrosieve 8，Large particulate matter is removed and is sent in bulky grain storage tank 19，Can be as the raw material produced next time，Material after sieving is sent to pelletize in comminutor 9，Product after pelletize is ecoalimental base，It is sent in finished product storage tank 10 store.
Specific embodiment described herein is only to this utility model spirit explanation for example.Described specific embodiment can be made various amendment or supplements or use similar mode to substitute by this utility model person of ordinary skill in the field, but without departing from spirit of the present utility model or surmount scope defined in appended claims.
nullAlthough the most more employing mud conveying mechanism 1、Organic solid waste conveying mechanism 2、Hydrolytic decomposition pot 3、Drying device 4、Air purifier 5、Material conveyer 6、Fermentation tank 7、Vibrosieve 8、Comminutor 9、Finished product storage tank 10、Sludge storage tank 11、Cutting machine 12、Organic solid waste storage tank 13、Auger machine 14、Pulverizer 15、Ribbon conveyer 16、First mass flowmenter 17、Second mass flowmenter 18、Bulky grain storage tank 19、Mummification storehouse 20、Conveyer belt assembly 21、Filter assemblies 22、Turner structure 23、Conveyer belt 24、Drainage screen 25、Turn over throwing spoon 28、Heater 29、Aerator 30、Heat exchange tank 31、Gas-liquid separator 32、Air-introduced machine 33、Infusion pump 34、Coolant storage tank 35、Heat exchange tank body 36、Heat exchange coil 37、Shaft 38、Stirring paddle 39、Stirring block 40、Liquid outlet 41、Add flow container 42、Aeration cover 43、Aeration tube 44 term such as grade，But it is not precluded from using the probability of other term.Use these terms to be only used to more easily and describe and explain essence of the present utility model；It is all contrary with this utility model spirit for being construed as any additional restriction.
Claims (10)
1. one kind utilize mud and organic solid waste batch production ecoalimental base become sheathed
Standby, including mud conveying mechanism (1) and organic solid waste conveying mechanism (2), its feature exists
In, described mud conveying mechanism (1) and organic solid waste conveying mechanism (2) connect respectively
Connecing hydrolytic decomposition pot (3), described hydrolytic decomposition pot (3) connects drying device (4), described mummification
The air outlet of device (4) connects air purifier (5), and the discharging opening of drying device (4) is even
Connecing material conveyer (6), material conveyer (6) connects fermentation tank (7), fermentation tank (7)
Connecting vibrosieve (8), vibrosieve (8) connects comminutor (9), and comminutor (9) is even
Connect finished product storage tank (10).
The most according to claim 1 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that described mud conveying mechanism (1) bag
Include sludge storage tank (11) and cutting machine (12) that the discharging opening with sludge storage tank (11) is connected,
The discharging opening of described cutting machine (12) connects hydrolytic decomposition pot (3), described organic solid waste
Conveying mechanism (2) include organic solid waste storage tank (13) and with organic solid waste storage tank (13)
The auger machine (14) that connects of discharging opening, the discharging opening of described auger machine (14) connects
Hydrolytic decomposition pot (3).
The most according to claim 2 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that described organic solid waste conveying mechanism (2)
Also include the pulverizer (15) being arranged on organic solid waste storage tank (13) top, and with pulverizing
The ribbon conveyer (16) that machine (15) connects, described cutting machine (12) and hydrolytic decomposition pot
(3) be provided with the first mass flowmenter (17) between, described auger machine (14) and
The second mass flowmenter (18), described vibrosieve (8) it is provided with between hydrolytic decomposition pot (3)
It is also connected with bulky grain storage tank (19).
The most according to claim 1 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that described drying device (4) includes mummification
Storehouse (20) and the conveyer belt assembly (21) being arranged in mummification storehouse (20), at conveyer belt
Assembly (21) lower section is provided with the filter assemblies (22) being connected with mummification storehouse (20) inner wall sealing,
Filter assemblies (22) lower section is provided with and the material in mummification storehouse (20) can be turned over throwing
Turner structure (23).
The most according to claim 4 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that described conveyer belt assembly (21) bag
Including some conveyer belts (24), the conveying direction of two the most adjacent conveyer belts (24) is contrary,
Described filter assemblies (22) includes drainage screen (25), described turner structure (23)
Drive including the rotating shaft (26) being rotationally connected with mummification storehouse (20) and with rotating shaft (26)
The driver (27) connected, described rotating shaft (26) is fixed with some being crisscross arranged
Turn over throwing spoon (28).
The most according to claim 4 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that the air intake in described mummification storehouse (20)
Mouth is sequentially connected with heater (29) and aerator (30).
The most according to claim 4 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that the air-out in described mummification storehouse (20)
Mouth connects heat exchange tank (31), gas-liquid separator (32), air-introduced machine successively and connects after (33)
Connecing air purifier (5), the liquid outlet of gas-liquid separator (32) connects infusion pump (34),
Infusion pump (34) connects coolant storage tank (35).
The most according to claim 7 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that described heat exchange tank (31) includes changing
Hot tank body (36) and the spiral heat exchange coil being arranged in heat exchange tank body (36)
(37), described heat exchange coil (37) one end connects the air outlet in mummification storehouse (20),
The other end of heat exchange coil (37) connects the charging aperture of gas-liquid separator (32).
The most according to claim 1 utilize mud and organic solid waste batch production raw
The complete set of equipments of state Nutrient medium, it is characterised in that be provided with in described fermentation tank (7) in
The shaft (38) of hollow, shaft (38) is fixedly connected with and shaft (38)
Connection and the stirring paddle (39) of hollow, the end of stirring paddle (39) is provided with and stirring paddle (39)
The stirring block (40) removably connected, stirring block (40) is provided with liquid outlet (41),
Fermentation tank (7) is provided with and adds flow container (42), the described two ends adding flow container (42)
Fix with the driver on fermentation tank (7) and shaft (38) respectively and be connected, described
Add flow container (42) connection shaft (38) it is thus possible to allow the liquid added in flow container (42)
Flow out in entering into shaft (38) and from liquid outlet (41).
The most according to claim 9 utilize mud and organic solid waste batch production
The complete set of equipments of ecoalimental base, it is characterised in that described fermentation tank (7) bottom sets
There are aeration cover (43), aeration cover (43) top to be rotationally connected with shaft (38), expose
Gas hood (43) sidepiece is densely covered with solarization air cap, is provided with aeration tube (44) in fermentation tank (7),
Fermentation tank (7) is extended outward in this aeration tube (44) one end, and the other end is inserted into aeration cover
(43) in.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620444368.1U CN205774166U (en) | 2016-05-16 | 2016-05-16 | Utilize mud and the complete set of equipments of organic solid waste batch production ecoalimental base |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620444368.1U CN205774166U (en) | 2016-05-16 | 2016-05-16 | Utilize mud and the complete set of equipments of organic solid waste batch production ecoalimental base |
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| CN205774166U true CN205774166U (en) | 2016-12-07 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111849728A (en) * | 2020-07-28 | 2020-10-30 | 袁见英 | High-temperature fermentation equipment for treating urban organic solid waste |
-
2016
- 2016-05-16 CN CN201620444368.1U patent/CN205774166U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111849728A (en) * | 2020-07-28 | 2020-10-30 | 袁见英 | High-temperature fermentation equipment for treating urban organic solid waste |
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Effective date of registration: 20200825 Address after: Room 408, Xiaoshan entrepreneurship service center, Hangzhou, Zhejiang Province Patentee after: Hangzhou Emerson Environmental Protection Technology Co.,Ltd. Address before: 311213, No. 98, Qin Li Cun, Yi Qiao Town, Xiaoshan District, Zhejiang, Hangzhou Patentee before: Hu Weijiang |