CN106007818A - Full-automatic-temperature-control refuse fermentation apparatus and operating method thereof - Google Patents
Full-automatic-temperature-control refuse fermentation apparatus and operating method thereof Download PDFInfo
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- CN106007818A CN106007818A CN201610348687.7A CN201610348687A CN106007818A CN 106007818 A CN106007818 A CN 106007818A CN 201610348687 A CN201610348687 A CN 201610348687A CN 106007818 A CN106007818 A CN 106007818A
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F9/00—Fertilisers from household or town refuse
- C05F9/02—Apparatus for the manufacture
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F9/00—Fertilisers from household or town refuse
- C05F9/04—Biological compost
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
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Abstract
The invention discloses a full-automatic-temperature-control refuse fermentation apparatus and an operating method thereof. The fermentation apparatus is composed of a supporting frame, a fermentation plant, a temperature control system, a fermentation liquid discharge pipe, a fermentation liquid storage pool and a control system. The refuse waste for fermentation is added into the fermentation plant from a feed port of the fermentation plant; microbes in the fermentation plant perform fermentation treatment on the refuse waste; meanwhile, the control system starts the temperature control system to provide the proper fermentation temperature for the fermentation process; the fermentation liquid after fermentation is discharged from a fermentation liquid discharge pipe on the bottom of the fermentation plant; and humus after fermentation is discharged from a discharge port of the fermentation plant. The full-automatic-temperature-control refuse fermentation apparatus and operating method thereof have the advantages of novel and reasonable structure, high fermentation efficiency and wide application range.
Description
Technical field
The invention belongs to garbage waste material processing means field, be specifically related to a kind of Full-automatic temp-control formula style refuse fermenter and
Its method of work.
Background technology
At present, conventional in the world rubbish fermentation technique buries (Landfill) and aerobic compost based on hole.Since the eighties,
Along with the generation of " giving energy by burning refuse ", waste resources is reclaimed pay attention to day by day, the conventional anaerobic digestion techniques of rubbish and high speed and detests
Oxygen composting technology has obtained developing on a large scale very much.
Promote Harmless and Comprehensive Disposal of Municipal Refuse method in China, engineering needs solve three aspects
Key technology: (1) refuse breaking and sorting sorting technique；(2) rubbish fermentation composting technology；(3) garbage incineration technology.?
At the Technique Popularizing initial stage, the technology in terms of these three should meet substantially wanting of the aspects such as construction investment, operating cost and environmental effect
Ask, step up and perfect along with the expansion in the face of popularization.
Rubbish fermentation composting technology common name garbage compost (garbage composting) technology, refers under controlled conditions,
Organic substance in rubbish forms the process of humus through microbial biochemical degraded.By the aerobic degree of biochemical degradation process, rubbish
Composting technology can be divided into aerobic fermentation and anaerobic fermentation two kinds.
Aerobic fermentation: by the difference of fermentation temperature, aerobic fermentation process is divided into middle temperature, high temperature and cooling three phases.?
Middle thermophase, mesophile growth and breeding enlivens, and hot stage mesophile is suppressed, and Thermophilic Bacteria is enlivened, and temperature-fall period is mesophilic
Bacterium enlivens once again, makes sweat enter stable becoming thoroughly decomposed the stage.
Anaerobic fermentation: at the anaerobic fermentation initial stage, zymogenous bacteria utilizes exoenzyme that Organic substance is carried out external enzymolysis, makes solid
Material becomes water-soluble material, and then, antibacterial re-absorption is dissolved in the material of water, and its zymolysis becomes different product.Logical
The primary product crossing anaerobe decomposition organic has organic acid, alcohol, carbon dioxide, ammonia, hydrogen etc..Increasing along with organic acid
Adding, pH value declines therewith, and this stage is referred to as producing acid phase, and the antibacterial of participation is referred to as acidogenic bactria.In the anaerobic fermentation later stage,
Due to the neutralization of ammonia, pH value gradually gos up, and methanogen starts to decompose organic acid and alcohol, and primary product has methane and two
Carbonoxide, along with the breeding of methanogen, organic acid decomposes rapidly, and pH value rises rapidly.
Existing style refuse fermenter, complex process, floor space is big, and fermentation efficiency is low, and prior art cannot meet
The process of substantial amounts of rubbish.
Summary of the invention
In order to solve above-mentioned technical problem, the present invention provides a kind of Full-automatic temp-control formula style refuse fermenter, including: fermentation
Equipment support 1, Zymolysis Equipment 2, temperature control system 3, fermentation liquid draining pipe 4, fermentation liquid storage pool 5, control system 6；
Described Zymolysis Equipment bracing frame 1 upper face is provided with Zymolysis Equipment 2 and control system 6, and described Zymolysis Equipment 2 top is provided with temperature
Ore-controlling Role 3, is provided with fermentation liquid draining pipe 4, is provided with fermentation liquid below described fermentation liquid draining pipe 4 bottom described Zymolysis Equipment 2
Storage pool 5；
Electrically-controlled valve on described fermentation liquid draining pipe 4 is connected with control system 6 polygon control survey.
Further, described Zymolysis Equipment 2 includes: fermentation cabin 2-1, charging aperture 2-2, charging aperture case lid 2-3, microorganism
Depend on bent plate 2-4, adjustable sliding plate 2-5, sliding plate angle adjustment motor 2-6, synchronous rotating shaft 2-7, discharge port 2-8, unload
Material mouth case lid 2-9, fermentation liquid transitional storehouse 2-10, angle measurement and control instrument 2-11, fermentability measurement and control instrument 2-12, temperature measurement-control instrument 2-
13；Described fermentation cabin 2-1 profile is rectangular-shaped, and fermentation cabin 2-1 is welded by corrosion resistant plate bending；Described charging aperture 2-
2 are positioned at above the sidewall of fermentation cabin 2-1 front, and charging aperture 2-2 is rectangular aperture shape；Described charging aperture case lid 2-3 is positioned at charging
Mouth 2-2 side, charging aperture case lid 2-3 profile size is consistent with charging aperture 2-2, and charging aperture case lid 2-3 passes through hinge and fermentation
Storehouse 2-1 is rotationally connected；Described microbial adherence bent plate 2-4 is positioned at inside fermentation cabin 2-1, microbial adherence bent plate 2-4 with send out
Ferment storehouse 2-1 inwall seamless welding is fixed, microbial adherence bent plate 2-4 profile in " Serpentis " shape, microbial adherence bent plate 2-4
Quantity is no less than 2 pieces, and adjacent two microbial adherence bent plate 2-4 spacing are not less than 30cm；Described discharge port 2-8 is positioned at fermentation
2-1 sidewall bottom position, storehouse, discharge port 2-8 is rectangular aperture shape structure；Described discharge port case lid 2-9 is positioned at discharge port 2-8
Side, discharge port case lid 2-9 profile size is consistent with discharge port 2-8, and discharge port case lid 2-9 is by hinge and fermentation cabin 2-1
It is rotationally connected；Described fermentation liquid transitional storehouse 2-10 is positioned at immediately below fermentation cabin 2-1, fermentation liquid transitional storehouse 2-10 and fermentation cabin 2-1
Being welded and fixed, fermentation liquid transitional storehouse 2-10 is separated by adjustable sliding plate 2-5 with fermentation cabin 2-1；Described adjustable sliding plate
2-5 surface distributed has substantial amounts of filtrate hole, and filtrate hole quantity is no less than 100, and filtrate hole pore diameter range value is at 1mm～3
Between mm, adjustable sliding plate 2-5 and horizontal plane angle are α, and described α value range is between 15 °～60 °；Described
Sliding plate angle adjustment motor 2-6 is positioned at outside fermentation cabin 2-1, and sliding plate angle adjustment motor 2-6 passes through synchronous rotating shaft 2-7
Fixing with adjustable sliding plate 2-5 and be connected, sliding plate angle adjustment motor 2-6 is connected with control system 6 polygon control survey；Described
Angle measurement and control instrument 2-11 is positioned at adjustable sliding plate 2-5 surface, and angle measurement and control instrument 2-11 is connected with control system 6 polygon control survey；
Described fermentability measurement and control instrument 2-12 is positioned at inside fermentation cabin 2-1, fermentability measurement and control instrument 2-12 and control system 6 wire control
System connects；Described temperature measurement-control instrument 2-13 is positioned at inside fermentation cabin 2-1, temperature measurement-control instrument 2-13 and control system 6 wire control
System connects.
Further, described temperature control system 3 includes: solar panel 3-1, heat energy evaporimeter 3-2, thermal energy transfer duct
3-3, heat energy conveying electrically-controlled valve 3-4；Described solar panel 3-1 is connected with control system 6 polygon control survey；Described heat energy steams
Sending out instrument 3-2 and be positioned at below solar panel 3-1, heat energy evaporimeter 3-2 is connected with control system 6 polygon control survey；Described heat
Can carry pipe 3-3 and be positioned at heat energy evaporimeter 3-2 both sides, thermal energy transfer duct 3-3 is mutually communicated inside heat energy evaporimeter 3-2；
Described heat energy conveying electrically-controlled valve 3-4 is positioned at thermal energy transfer duct 3-3 external diameter surface, heat energy conveying electrically-controlled valve 3-4 and control system 6
Polygon control survey connects.
Further, described microbial adherence bent plate 2-4 by macromolecular material pressing mold molding, microbial adherence bent plate 2-4's
Constituent and manufacture process are as follows:
One, microbial adherence bent plate 2-4 constituent:
Count by weight, a tetramethylene xylene diisocyanate 45～125 parts, 1,6-hexamethylene diisocyanate 60～
105 parts, dimethylene phenylene diisocyanate 110～175 parts, di-2-ethylhexylphosphine oxide butyl dithiocarbamate 83～166 parts,
N, N "-(methylene two-4,1-phenylene) two (N', N'-dimethyl urea) 55～177 parts, 3,5-double (acetamido)-2,4,6-triiodo-benzene first
Acid 120～330 parts, concentration is N-propyl group-N-(formyl chloride)-2-(2,4, the 6-Trichlorophenoxy) ethamine of 50ppm～90ppm
60～150 parts, 3-amino-2,4,6-Triiodobenzoic acids 75～135 parts, N-nitro-N-(N'-is to acetylphenyl)-carbamyl-
2,4,6-trichloroanilines 70～160 parts, cross-linking agent 90～165 parts, 3,5-biacetyl amino-2,4,6-Triiodobenzoic acid salt 55～
130 parts, 5-amino-3-carboxyl-2,4,6-tri-iodo-N-methyl-benzamides 80～170 parts, N-acetyl group-3,5-bis-iodo-O-(4-first
Oxygen phenyl)-TYR ethyl ester 40～75 parts, 6-(3,5-diaminobenzene formamido group) n-caproic acid hydrochlorate 45～120 parts；
Described cross-linking agent is 5-amino-2,4,6-triiodo m-phthaloyl chloride, 1,2-dichloroethanes-3,5-double (trifluoromethyl) bromobenzene, N-(3,5-
Dichlorobenzene base) any one in-1,2-dimethylcyclopropane-1,2-diformyl imines；
Two, the manufacture process of microbial adherence bent plate 2-4, comprises the steps of
1st step: add ultra-pure water 610～1200 parts that electrical conductivity is 0.45 μ S/cm～0.75 μ S/cm in a kettle., start
Agitator in reactor, rotating speed is 93rpm～233rpm, start heat pump, make reactor temperature rise to 66 DEG C～
73℃；It is sequentially added into a tetramethylene xylene diisocyanate, 1,6-hexamethylene diisocyanate, dimethylene benzene two different
Cyanate, stirring is to being completely dissolved, and regulation pH value is 2.3～7.3, and agitator speed is adjusted to 123rpm～243rpm,
Temperature is 83 DEG C～153 DEG C, esterification 23～33 hours；
2nd step: take di-2-ethylhexylphosphine oxide butyl dithiocarbamate, N, N "-(methylene two-4,1-phenylene) two (N', N'-dimethyl urea)
Pulverizing, powder diameter is 303～1130 mesh；Add 3, double (acetamido)-2 of 5-, 4,6-Triiodobenzoic acid mix homogeneously are flat
Being laid in pallet, tiling thickness is 13mm～53mm, and employing dosage is 2.3kGy～10.3kGy, energy is 6.3
The alpha ray irradiation 53 of MeV～13MeV～133 minutes, and the β x ray irradiation x 73 of Isodose～163 minutes；
3rd step: the mixed-powder processed through the 2nd step is dissolved in N-propyl group-N-(formyl chloride)-2-(2,4,6-Trichlorophenoxy) ethamine, adds
Entering reactor, agitator speed is 83rpm～193rpm, and temperature is 93 DEG C～143 DEG C, starts vacuum pump and makes reactor
Vacuum reach-0.43MPa～-0.83MPa, keep this state response 13～53 hours；Pressure release is also passed through nitrogen, makes anti-
Answering pressure in still is 0.33MPa～0.73MPa, and insulation stands 13～23 hours；Agitator speed be promoted to 113rpm～
253rpm, simultaneous reactions still pressure release to 0MPa；Be sequentially added into 3-amino-2,4,6-Triiodobenzoic acid, (N'-is to second for N-nitro-N-
Aminosulfonylphenyl)-carbamyl-2, after 4,6-trichloroanilines are completely dissolved, add cross-linking agent stirring mixing so that reactor solution
Hydrophile-lipophile balance value is 4.3～7.3, and insulation stands 13～23 hours；
4th step: when agitator speed is 133rpm～263rpm, is sequentially added into 3,5-biacetyl amino-2,4,6-Triiodobenzoic acids
Salt, the 5-amino iodo-N-methyl-benzamide of-3-carboxyl-2,4,6-three, N-acetyl group-3,5-two iodo-O-(4-anisyl)-L-cheese ammonia
Acetoacetic ester, 6-(3,5-diaminobenzene formamido group) n-caproic acid hydrochlorate, promote reactor pressure so that it is reach 0.83MPa～
1.63MPa, temperature is 133 DEG C～273 DEG C, polyreaction 13～33 hours；After having reacted, reacting kettle inner pressure is dropped
To 0MPa, it is cooled to 33 DEG C～43 DEG C, discharging, enter molding press and can be prepared by microbial adherence bent plate 2-4.
The invention also discloses the method for work of a kind of Full-automatic temp-control formula style refuse fermenter, the method includes following
Step:
1st step: open charging aperture case lid 2-3, renders to fermentation cabin 2-1 by the rubbish heap gurry of required fermentation from charging aperture 2-2,
Rubbish heap gurry in fermentation cabin 2-1 is carried out decomposing oxidation processes by the microorganism of microbial adherence bent plate 2-4 surface attachment；
2nd step: control system 6 starts solar panel 3-1 and carries out light energy collecting and luminous energy changes into heat energy, heat energy is heat energy
Evaporimeter 3-2 provides thermal source, and control system 6 starts heat energy evaporimeter 3-2 and heat energy is flashed to high-temperature vapor, now, and control
High-temperature steam in heat energy evaporimeter 3-2 is carried by heat energy conveying electrically-controlled valve 3-4 that system 6 processed is opened in thermal energy transfer duct 3-3
Temperature environment to fermentation cabin 2-1, needed for providing for sweat；
3rd step: during the fermentation, the temperature conditions in fermentation cabin 2-1 is carried out by control system 6 start-up temperature measurement and control instrument 2-13
Monitoring in real time, when the temperature that temperature measurement-control instrument 2-13 detects in fermentation cabin 2-1 reaches between 30 DEG C～50 DEG C, temperature
Measurement and control instrument 2-13 sends feedback signal to control system 6, and control system 6 closes heat energy conveying electrically-controlled valve 3-4, stops to fermentation
Storehouse 2-1 carries high-temperature steam；
4th step: during the fermentation, control system 6 starts fermentability measurement and control instrument 2-12 and sends out microorganism in fermentation cabin 2-1
Ferment ability monitors in real time, when fermentability measurement and control instrument 2-12 detects that in fermentation cabin 2-1, the fermentability of microorganism is less than
When 30%～60%, fermentability measurement and control instrument 2-12 sends feedback signal the 40s that reports to the police to control system 6, points out work people
Member strengthens the injected volume of microorganism in fermentation cabin 2-1；
5th step: until this plant running 2～after 7 days, one time fermentation process completes, opens discharge port case lid 2-9, by the corruption after fermentation
Growing matter to take out from discharge port 2-8, if this process feeding difficulty, control system 6 starts sliding plate angle adjustment motor 2-6,
The synchronous rotating shaft 2-7 of sliding plate angle adjustment motor 2-6 drives adjustable sliding plate 2-5 to rotate, in rotation process, and angle
Measurement and control instrument 2-11 monitors adjustable sliding plate 2-5 rotational angle in real time, when angle measurement and control instrument 2-11 detects that rotational angle reaches
Time between 15 °～60 °, angle measurement and control instrument 2-11 sends feedback signal to control system 6, and control system 6 controls lubricating substance
Plate angle adjustment motor 2-6 stop motion, the fermentation liquid produced in the sweat filtrate by adjustable sliding plate 2-5 surface
Hole flows in fermentation liquid transitional storehouse 2-10, and control system 6 is opened the electrically-controlled valve on fermentation liquid draining pipe 4 and entered by fermentation liquid and send out
In ferment liquid storage pool 5.
A kind of Full-automatic temp-control formula style refuse fermenter and method of work thereof disclosed in patent of the present invention, have an advantage in that:
(1) this device increases temperature control system, makes the sweat moment keep preference temperature；
(2) this apparatus structure is reasonable in design compact, and integrated level is high；
(3) this device microbial adherence bent plate uses macromolecular material to prepare, and fermenting speed promotes notable.
A kind of Full-automatic temp-control formula style refuse fermenter of the present invention and method of work novel and reasonable structure thereof, fermentation effect
Rate is efficient, and the scope of application is wide.
Accompanying drawing explanation
Fig. 1 is heretofore described a kind of Full-automatic temp-control formula style refuse fermenter schematic diagram.
Fig. 2 is heretofore described Zymolysis Equipment internal structure schematic diagram.
Fig. 3 is heretofore described temperature control system structural representation.
Fig. 4 is microbial adherence bent plate material of the present invention and fermenting speed enhancing rate graph of a relation.
In figure 1 above～Fig. 3, Zymolysis Equipment bracing frame 1, Zymolysis Equipment 2, fermentation cabin 2-1, charging aperture 2-2, charging
Mouth case lid 2-3, microbial adherence bent plate 2-4, adjustable sliding plate 2-5, sliding plate angle adjustment motor 2-6, synchronous rotating shaft
2-7, discharge port 2-8, discharge port case lid 2-9, fermentation liquid transitional storehouse 2-10, angle measurement and control instrument 2-11, fermentability measurement and control instrument
2-12, temperature measurement-control instrument 2-13, temperature control system 3, solar panel 3-1, heat energy evaporimeter 3-2, thermal energy transfer duct 3-3,
Heat energy conveying electrically-controlled valve 3-4, fermentation liquid draining pipe 4, fermentation liquid storage pool 5, control system 6.
Detailed description of the invention
A kind of Full-automatic temp-control formula style refuse fermenter provided the present invention with embodiment below in conjunction with the accompanying drawings is carried out further
Explanation.
As it is shown in figure 1, be the schematic diagram of a kind of Full-automatic temp-control formula style refuse fermenter that the present invention provides.Figure is found out,
Including Zymolysis Equipment bracing frame 1, Zymolysis Equipment 2, temperature control system 3, fermentation liquid draining pipe 4, fermentation liquid storage pool 5, control
System 6；Described Zymolysis Equipment bracing frame 1 upper face is provided with Zymolysis Equipment 2 and control system 6, and described Zymolysis Equipment 2 is pushed up
Portion is provided with temperature control system 3, is provided with fermentation liquid draining pipe 4, sets below described fermentation liquid draining pipe 4 bottom described Zymolysis Equipment 2
There is fermentation liquid storage pool 5；
Electrically-controlled valve on described fermentation liquid draining pipe 4 is connected with control system 6 polygon control survey.
As in figure 2 it is shown, be heretofore described Zymolysis Equipment internal structure schematic diagram.Find out from Fig. 2 or Fig. 1,
Described Zymolysis Equipment 2 includes: fermentation cabin 2-1, charging aperture 2-2, charging aperture case lid 2-3, and microbial adherence bent plate 2-4 can
Mode sliding plate 2-5, sliding plate angle adjustment motor 2-6, synchronous rotating shaft 2-7, discharge port 2-8, discharge port case lid 2-9, sends out
Ferment liquid transitional storehouse 2-10, angle measurement and control instrument 2-11, fermentability measurement and control instrument 2-12, temperature measurement-control instrument 2-13；Described fermentation cabin
2-1 profile is rectangular-shaped, and fermentation cabin 2-1 is welded by corrosion resistant plate bending；Described charging aperture 2-2 is positioned at fermentation cabin 2-1
Above the sidewall of front, charging aperture 2-2 is rectangular aperture shape；Described charging aperture case lid 2-3 is positioned at charging aperture 2-2 side, charging
Mouth case lid 2-3 profile size is consistent with charging aperture 2-2, and charging aperture case lid 2-3 is rotationally connected with fermentation cabin 2-1 by hinge；
Described microbial adherence bent plate 2-4 is positioned at inside fermentation cabin 2-1, microbial adherence bent plate 2-4 and wall seamless in fermentation cabin 2-1
Being welded and fixed, microbial adherence bent plate 2-4 profile is in " Serpentis " shape, and microbial adherence bent plate 2-4 quantity is no less than 2 pieces,
Adjacent two microbial adherence bent plate 2-4 spacing are not less than 30cm；Described discharge port 2-8 is positioned at fermentation cabin 2-1 sidewall bottom position
Putting, discharge port 2-8 is rectangular aperture shape structure；Described discharge port case lid 2-9 is positioned at discharge port 2-8 side, discharge port case lid
2-9 profile size is consistent with discharge port 2-8, and discharge port case lid 2-9 is rotationally connected with fermentation cabin 2-1 by hinge；Described fermentation
Liquid transitional storehouse 2-10 is positioned at immediately below fermentation cabin 2-1, and fermentation liquid transitional storehouse 2-10 is welded and fixed with fermentation cabin 2-1, fermentation liquid
Transitional storehouse 2-10 is separated by adjustable sliding plate 2-5 with fermentation cabin 2-1；Described adjustable sliding plate 2-5 surface distributed has greatly
Amount filtrate hole, filtrate hole quantity be no less than 100, filtrate hole pore diameter range value between 1mm～3mm, adjustable cunning
Flitch 2-5 and horizontal plane angle are α, and described α value range is between 15 °～60 °；Described sliding plate angle adjustment motor
2-6 is positioned at outside fermentation cabin 2-1, and sliding plate angle adjustment motor 2-6 is solid by synchronous rotating shaft 2-7 and adjustable sliding plate 2-5
Fixed connection, sliding plate angle adjustment motor 2-6 is connected with control system 6 polygon control survey；Described angle measurement and control instrument 2-11 is positioned at can
Mode sliding plate 2-5 surface, angle measurement and control instrument 2-11 is connected with control system 6 polygon control survey；Described fermentability measurement and control instrument
2-12 is positioned at inside fermentation cabin 2-1, and fermentability measurement and control instrument 2-12 is connected with control system 6 polygon control survey；Described temperature is surveyed
Control instrument 2-13 is positioned at inside fermentation cabin 2-1, and temperature measurement-control instrument 2-13 is connected with control system 6 polygon control survey.
As it is shown on figure 3, be heretofore described temperature control system structural representation.Find out from Fig. 3 or Fig. 1, described
Temperature control system 3 includes: solar panel 3-1, heat energy evaporimeter 3-2, thermal energy transfer duct 3-3, heat energy conveying electrically-controlled valve 3-
4；Described solar panel 3-1 is connected with control system 6 polygon control survey；Described heat energy evaporimeter 3-2 is positioned at solar energy and receives
Below collection plate 3-1, heat energy evaporimeter 3-2 is connected with control system 6 polygon control survey；Described thermal energy transfer duct 3-3 is positioned at heat energy
Evaporimeter 3-2 both sides, thermal energy transfer duct 3-3 is mutually communicated inside heat energy evaporimeter 3-2；Described heat energy conveying electrically-controlled valve 3-4
Being positioned at thermal energy transfer duct 3-3 external diameter surface, heat energy conveying electrically-controlled valve 3-4 is connected with control system 6 polygon control survey.
The work process of a kind of Full-automatic temp-control formula style refuse fermenter of the present invention is:
1st step: open charging aperture case lid 2-3, renders to fermentation cabin 2-1 by the rubbish heap gurry of required fermentation from charging aperture 2-2,
Rubbish heap gurry in fermentation cabin 2-1 is carried out decomposing oxidation processes by the microorganism of microbial adherence bent plate 2-4 surface attachment；
2nd step: control system 6 starts solar panel 3-1 and carries out light energy collecting and luminous energy changes into heat energy, heat energy is heat energy
Evaporimeter 3-2 provides thermal source, and control system 6 starts heat energy evaporimeter 3-2 and heat energy is flashed to high-temperature vapor, now, and control
High-temperature steam in heat energy evaporimeter 3-2 is carried by heat energy conveying electrically-controlled valve 3-4 that system 6 processed is opened in thermal energy transfer duct 3-3
Temperature environment to fermentation cabin 2-1, needed for providing for sweat；
3rd step: during the fermentation, the temperature conditions in fermentation cabin 2-1 is carried out by control system 6 start-up temperature measurement and control instrument 2-13
Monitoring in real time, when the temperature that temperature measurement-control instrument 2-13 detects in fermentation cabin 2-1 reaches between 30 DEG C～50 DEG C, temperature
Measurement and control instrument 2-13 sends feedback signal to control system 6, and control system 6 closes heat energy conveying electrically-controlled valve 3-4, stops to fermentation
Storehouse 2-1 carries high-temperature steam；
4th step: during the fermentation, control system 6 starts fermentability measurement and control instrument 2-12 and sends out microorganism in fermentation cabin 2-1
Ferment ability monitors in real time, when fermentability measurement and control instrument 2-12 detects that in fermentation cabin 2-1, the fermentability of microorganism is less than
When 30%～60%, fermentability measurement and control instrument 2-12 sends feedback signal the 40s that reports to the police to control system 6, points out work people
Member strengthens the injected volume of microorganism in fermentation cabin 2-1；
5th step: until this plant running 2～after 7 days, one time fermentation process completes, opens discharge port case lid 2-9, by the corruption after fermentation
Growing matter to take out from discharge port 2-8, if this process feeding difficulty, control system 6 starts sliding plate angle adjustment motor 2-6,
The synchronous rotating shaft 2-7 of sliding plate angle adjustment motor 2-6 drives adjustable sliding plate 2-5 to rotate, in rotation process, and angle
Measurement and control instrument 2-11 monitors adjustable sliding plate 2-5 rotational angle in real time, when angle measurement and control instrument 2-11 detects that rotational angle reaches
Time between 15 °～60 °, angle measurement and control instrument 2-11 sends feedback signal to control system 6, and control system 6 controls lubricating substance
Plate angle adjustment motor 2-6 stop motion, the fermentation liquid produced in the sweat filtrate by adjustable sliding plate 2-5 surface
Hole flows in fermentation liquid transitional storehouse 2-10, and control system 6 is opened the electrically-controlled valve on fermentation liquid draining pipe 4 and entered by fermentation liquid and send out
In ferment liquid storage pool 5.
A kind of Full-automatic temp-control formula style refuse fermenter of the present invention and method of work novel and reasonable structure thereof, fermentation effect
Rate is efficient, and the scope of application is wide.
The following is the embodiment of the manufacture process of microbial adherence bent plate 2-4 of the present invention, embodiment is in order to furtherly
Bright present disclosure, but should not be construed as limitation of the present invention.Without departing from the spirit and substance of the case in the present invention, right
Amendment that the inventive method, step or condition are made and replacement, belong to the scope of the present invention.
If not specializing, the conventional means that technological means used in embodiment is well known to those skilled in the art.
Embodiment 1
According to following steps manufacture microbial adherence bent plate 2-4 of the present invention, and mark meter by weight:
1st step: add the ultra-pure water 610 parts that electrical conductivity is 0.45 μ S/cm in a kettle., start agitator in reactor, turn
Speed is 93rpm, starts heat pump, makes reactor temperature rise to 66 DEG C；It is sequentially added into a tetramethylene xylene two different
Cyanate 45 parts, 1,6-hexamethylene diisocyanate 60 parts, dimethylene phenylene diisocyanate 110 parts, stirring to completely
Dissolving, regulation pH value is 2.3, and agitator speed is adjusted to 123rpm, and temperature is 83 DEG C, esterification 23 hours；
2nd step: take di-2-ethylhexylphosphine oxide butyl dithiocarbamate 83 parts, N, N "-(methylene two-4,1-phenylene) two (N', N'-bis-
MU) 55 parts pulverize, powder diameter is 303 mesh；Add double (the acetamido)-2,4,6-Triiodobenzoic acid 120 parts of 3,5-
Mix homogeneously, is laid in pallet, and tiling thickness is 13mm, and employing dosage is 2.3kGy, energy is the α of 6.3MeV
X ray irradiation x 53 minutes, and the β x ray irradiation x of Isodose 73 minutes；
3rd step: the mixed-powder processed through the 2nd step is dissolved in N-propyl group-N-(formyl chloride)-2-(the 2,4,6-trichloro-benzenes that concentration is 50ppm
Epoxide) in 60 parts of ethamine, add reactor, agitator speed is 83rpm, and temperature is 93 DEG C, starts vacuum pump and makes reaction
The vacuum of still reaches-0.43MPa, keeps this state response 13 hours；Pressure release is also passed through nitrogen, makes the reacting kettle inner pressure be
0.33MPa, insulation stands 13 hours；Agitator speed is promoted to 113rpm, simultaneous reactions still pressure release to 0MPa；Successively
Add 3-amino-2,4,6-Triiodobenzoic acid 75 parts, N-nitro-N-(N'-is to acetylphenyl)-carbamyl-2,4,6-trichloroaniline
After 70 parts are completely dissolved, add cross-linking agent 90 parts stirring mixing so that the hydrophile-lipophile balance value of reactor solution is 4.3,
Insulation stands 13 hours；
4th step: when agitator speed is 133rpm, is sequentially added into 3,5-biacetyl amino-2,4,6-Triiodobenzoic acid salt 55 parts,
5-amino-3-carboxyl-2,4,6-three iodo-N-methyl-benzamide 80 parts, N-acetyl group-3,5-two iodo-O-(4-anisyl)-L-cheese ammonia
Acetoacetic ester 40 parts, 6-(3,5-diaminobenzene formamido group) n-caproic acid hydrochlorate 45 parts, promote reactor pressure so that it is reach
0.83MPa, temperature is 133 DEG C, polyreaction 13 hours；After having reacted, reacting kettle inner pressure is down to 0MPa, cooling
To 33 DEG C, discharging, enter molding press and can be prepared by microbial adherence bent plate 2-4；
Described cross-linking agent is 5-amino-2,4,6-triiodo m-phthaloyl chloride.
Embodiment 2
According to following steps manufacture microbial adherence bent plate 2-4 of the present invention, and mark meter by weight:
1st step: add the ultra-pure water 1200 parts that electrical conductivity is 0.75 μ S/cm in a kettle., start agitator in reactor,
Rotating speed is 233rpm, starts heat pump, makes reactor temperature rise to 73 DEG C；It is sequentially added into a tetramethylene xylene
Diisocyanate 125 parts, 1,6-hexamethylene diisocyanate 105 parts, dimethylene phenylene diisocyanate 175 parts, stirring
To being completely dissolved, regulation pH value is 7.3, and agitator speed is adjusted to 243rpm, and temperature is 153 DEG C, esterification 33
Hour；
2nd step: take di-2-ethylhexylphosphine oxide butyl dithiocarbamate 166 parts, N, N "-(methylene two-4,1-phenylene) two (N', N'-bis-
MU) 177 parts pulverize, powder diameter is 1130 mesh；Add double (the acetamido)-2,4,6-Triiodobenzoic acid 330 of 3,5-
Part mix homogeneously, is laid in pallet, and tiling thickness is 53mm, and employing dosage is 10.3kGy, energy is 13MeV's
Alpha ray irradiation 133 minutes, and the β x ray irradiation x of Isodose 163 minutes；
3rd step: the mixed-powder processed through the 2nd step is dissolved in N-propyl group-N-(formyl chloride)-2-(the 2,4,6-trichloro-benzenes that concentration is 90ppm
Epoxide) in 150 parts of ethamine, add reactor, agitator speed is 193rpm, and temperature is 143 DEG C, starts vacuum pump and makes
The vacuum of reactor reaches-0.83MPa, keeps this state response 53 hours；Pressure release is also passed through nitrogen, makes reactor intrinsic pressure
Power is 0.73MPa, and insulation stands 23 hours；Agitator speed is promoted to 253rpm, simultaneous reactions still pressure release to 0MPa；
It is sequentially added into 3-amino-2,4,6-Triiodobenzoic acid 135 parts, N-nitro-N-(N'-is to acetylphenyl)-carbamyl-2,4,6-trichlorine
After aniline 160 parts is completely dissolved, add cross-linking agent 165 parts stirring mixing so that the hydrophile-lipophile balance value of reactor solution is
7.3, insulation stands 23 hours；
4th step: when agitator speed is 263rpm, is sequentially added into 3,5-biacetyl amino-2,4,6-Triiodobenzoic acid salt 130 parts,
5-amino-3-carboxyl-2,4,6-three iodo-N-methyl-benzamide 170 parts, N-acetyl group-3,5-two iodo-O-(4-anisyl)-L-cheese
Propylhomoserin ethyl ester 75 parts, 6-(3,5-diaminobenzene formamido group) n-caproic acid hydrochlorate 120 parts, promote reactor pressure so that it is reach
To 1.63MPa, temperature is 273 DEG C, polyreaction 33 hours；After having reacted, reacting kettle inner pressure is down to 0MPa,
It is cooled to 43 DEG C, discharging, enter molding press and can be prepared by microbial adherence bent plate 2-4；
Described cross-linking agent is N-(3,5-Dichlorobenzene base)-1,2-dimethylcyclopropane-1,2-diformyl imines.
Embodiment 3
According to following steps manufacture microbial adherence bent plate 2-4 of the present invention, and mark meter by weight:
1st step: add the ultra-pure water 900 parts that electrical conductivity is 0.65 μ S/cm in a kettle., start agitator in reactor, turn
Speed is 133rpm, starts heat pump, makes reactor temperature rise to 70 DEG C；It is sequentially added into a tetramethylene xylene two
Isocyanates 85 parts, 1,6-hexamethylene diisocyanate 95 parts, dimethylene phenylene diisocyanate 135 parts, stirring is to the completeest
CL, regulation pH value is 4.3, and agitator speed is adjusted to 183rpm, and temperature is 123 DEG C, esterification 28 hours；
2nd step: take di-2-ethylhexylphosphine oxide butyl dithiocarbamate 126 parts, N, N "-(methylene two-4,1-phenylene) two (N', N'-bis-
MU) 137 parts pulverize, powder diameter is 880 mesh；Add double (the acetamido)-2,4,6-Triiodobenzoic acid 230 of 3,5-
Part mix homogeneously, is laid in pallet, and tiling thickness is 33mm, and employing dosage is 6.3kGy, energy is the α of 9MeV
X ray irradiation x 100 minutes, and the β x ray irradiation x of Isodose 93 minutes；
3rd step: the mixed-powder processed through the 2nd step is dissolved in N-propyl group-N-(formyl chloride)-2-(the 2,4,6-trichloro-benzenes that concentration is 70ppm
Epoxide) in 110 parts of ethamine, add reactor, agitator speed is 123rpm, and temperature is 113 DEG C, starts vacuum pump and makes instead
The vacuum answering still reaches-0.63MPa, keeps this state response 43 hours；Pressure release is also passed through nitrogen, makes reacting kettle inner pressure
For 0.53MPa, insulation stands 20 hours；Agitator speed is promoted to 153rpm, simultaneous reactions still pressure release to 0MPa；Depend on
Secondary addition 3-amino-2,4,6-Triiodobenzoic acid 115 parts, N-nitro-N-(N'-is to acetylphenyl)-carbamyl-2,4,6-trichloro-benzenes
After amine 120 parts is completely dissolved, add cross-linking agent 115 parts stirring mixing so that the hydrophile-lipophile balance value of reactor solution is
5.3, insulation stands 20 hours；
4th step: when agitator speed is 163rpm, is sequentially added into 3,5-biacetyl amino-2,4,6-Triiodobenzoic acid salt 90 parts,
5-amino-3-carboxyl-2,4,6-three iodo-N-methyl-benzamide 120 parts, N-acetyl group-3,5-two iodo-O-(4-anisyl)-L-cheese
Propylhomoserin ethyl ester 55 parts, 6-(3,5-diaminobenzene formamido group) n-caproic acid hydrochlorate 80 parts, promote reactor pressure so that it is reach
1.23MPa, temperature is 173 DEG C, polyreaction 23 hours；After having reacted, reacting kettle inner pressure is down to 0MPa, fall
Warm to 40 DEG C, discharging, enter molding press and can be prepared by microbial adherence bent plate 2-4；
Described cross-linking agent is double (trifluoromethyl) bromobenzene of 1,2-dichloroethanes-3,5-.
Reference examples
Reference examples is the microbial adherence bent plate service condition for garbage waste material sweat of certain brand commercially available.
Embodiment 4
Microbial adherence bent plate described in microbial adherence bent plate 2-4 embodiment 1～3 prepared and reference examples is used for rubbish and gives up
The process contrast of the service condition of gurry sweat.Respectively the parameters of garbage waste material sweat is entered after fermentation ends
Row detection, result is as shown in table 1.
Table 1 is the property in garbage waste material sweat of the microbial adherence bent plate described in embodiment 1～3 and reference examples
The impact of energy parameter, as seen from Table 1, microbial adherence bent plate 2-4 of the present invention, its oxidation Decomposition degree of polymerization, oxidation
Decomposition intensity enhancing rate, oxidation Decomposition yield enhancing rate, fermenting speed enhancing rate are above the product that prior art produces.
Additionally, as shown in Figure 4, it is microbial adherence bent plate 2-4 material of the present invention and fermenting speed enhancing rate relation
Figure.Find out in figure, macromolecular material the microbial adherence bent plate 2-4 material manufactured is evenly distributed, and material surface amasss and volume
Bigger, Dispersion on surface is good, and the concentration relative comparison example of dispersible carrier free in continuous phase is high；Use micro-life of the present invention
Thing depends on bent plate 2-4, makes garbage waste material be prone to assemble agglomerating, forms the humus of paradigmatic structure；Use of the present invention micro-
Biology depends on bent plate 2-4, and its fermenting speed enhancing rate is superior to existing product.
Claims (5)
1. a Full-automatic temp-control formula style refuse fermenter, including: Zymolysis Equipment bracing frame (1), Zymolysis Equipment (2), temperature control system
System (3), fermentation liquid draining pipe (4), fermentation liquid storage pool (5), control system (6)；It is characterized in that, described fermentation sets
Standby bracing frame (1) upper face is provided with Zymolysis Equipment (2) and control system (6), and described Zymolysis Equipment (2) top is provided with
Temperature control system (3), described Zymolysis Equipment (2) bottom is provided with fermentation liquid draining pipe (4), under described fermentation liquid draining pipe (4)
Side is provided with fermentation liquid storage pool (5)；
Electrically-controlled valve on described fermentation liquid draining pipe (4) is connected with control system (6) polygon control survey.
A kind of Full-automatic temp-control formula style refuse fermenter the most according to claim 1, it is characterised in that described Zymolysis Equipment (2)
Including: fermentation cabin (2-1), charging aperture (2-2), charging aperture case lid (2-3), microbial adherence bent plate (2-4), adjustable
Sliding plate (2-5), sliding plate angle adjustment motor (2-6), synchronous rotating shaft (2-7), discharge port (2-8), discharge port case lid
(2-9), fermentation liquid transitional storehouse (2-10), angle measurement and control instrument (2-11), fermentability measurement and control instrument (2-12), temperature measurement-control instrument
(2-13)；Wherein said fermentation cabin (2-1) profile is rectangular-shaped, and fermentation cabin (2-1) is welded by corrosion resistant plate bending；
Described charging aperture (2-2) is positioned at above the sidewall of fermentation cabin (2-1) front, and charging aperture (2-2) is rectangular aperture shape；Described enter
Material mouth case lid (2-3) is positioned at charging aperture (2-2) side, charging aperture case lid (2-3) profile size and charging aperture (2-2)
Causing, charging aperture case lid (2-3) is rotationally connected with fermentation cabin (2-1) by hinge；Described microbial adherence bent plate (2-4) position
Internal in fermentation cabin (2-1), microbial adherence bent plate (2-4) is fixed with fermentation cabin (2-1) inwall seamless welding, microorganism
Depending on bent plate (2-4) profile in " Serpentis " shape, microbial adherence bent plate (2-4) quantity is no less than 2 pieces, adjacent two micro-lifes
Thing depends on bent plate (2-4) spacing not less than 30cm；Described discharge port (2-8) is positioned at fermentation cabin (2-1) sidewall bottom position,
Discharge port (2-8) is rectangular aperture shape structure；Described discharge port case lid (2-9) is positioned at discharge port (2-8) side, discharge port
Case lid (2-9) profile size is consistent with discharge port (2-8), and discharge port case lid (2-9) is by hinge and fermentation cabin (2-1)
It is rotationally connected；Described fermentation liquid transitional storehouse (2-10) is positioned at immediately below fermentation cabin (2-1), fermentation liquid transitional storehouse (2-10) with
Fermentation cabin (2-1) is welded and fixed, and fermentation liquid transitional storehouse (2-10) and fermentation cabin (2-1) are by adjustable sliding plate (2-5)
Separate；Described adjustable sliding plate (2-5) surface distributed has substantial amounts of filtrate hole, and filtrate hole quantity is no less than 100, filter
Fluid apertures pore diameter range value is between 1mm～3mm, and adjustable sliding plate (2-5) and horizontal plane angle are α, described α model
Enclosing value is between 15 °～60 °；Described sliding plate angle adjustment motor (2-6) is positioned at fermentation cabin (2-1) outside, lubricating substance
Plate angle adjustment motor (2-6) is connected by synchronous rotating shaft (2-7) and adjustable sliding plate (2-5) are fixing, sliding plate angle
Adjust motor (2-6) to be connected with control system (6) polygon control survey；Described angle measurement and control instrument (2-11) is positioned at adjustable lubricating substance
Plate (2-5) surface, angle measurement and control instrument (2-11) is connected with control system (6) polygon control survey；Described fermentability measurement and control instrument
(2-12) being positioned at fermentation cabin (2-1) internal, fermentability measurement and control instrument (2-12) is connected with control system (6) polygon control survey；
It is internal that described temperature measurement-control instrument (2-13) is positioned at fermentation cabin (2-1), and temperature measurement-control instrument (2-13) is led with control system (6)
Line traffic control connects.
A kind of Full-automatic temp-control formula style refuse fermenter the most according to claim 1, it is characterised in that described temperature control system (3)
Including: solar panel (3-1), heat energy evaporimeter (3-2), thermal energy transfer duct (3-3), heat energy conveying electrically-controlled valve (3-
4)；Wherein said solar panel (3-1) is connected with control system (6) polygon control survey；Described heat energy evaporimeter (3-2)
Being positioned at solar panel (3-1) lower section, heat energy evaporimeter (3-2) is connected with control system (6) polygon control survey；Described
Thermal energy transfer duct (3-3) is positioned at heat energy evaporimeter (3-2) both sides, thermal energy transfer duct (3-3) and heat energy evaporimeter (3-2)
Inside is mutually communicated；Described heat energy conveying electrically-controlled valve (3-4) is positioned at thermal energy transfer duct (3-3) external diameter surface, heat energy conveying electricity
Control valve (3-4) is connected with control system (6) polygon control survey.
A kind of Full-automatic temp-control formula style refuse fermenter the most according to claim 2, it is characterised in that described microbial adherence
Bent plate (2-4) is by macromolecular material pressing mold molding, and constituent and the manufacture process of microbial adherence bent plate (2-4) are as follows:
One, microbial adherence bent plate (2-4) constituent:
Count by weight, a tetramethylene xylene diisocyanate 45～125 parts, 1,6-hexamethylene diisocyanate 60～
105 parts, dimethylene phenylene diisocyanate 110～175 parts, di-2-ethylhexylphosphine oxide butyl dithiocarbamate 83～166 parts,
N, N "-(methylene two-4,1-phenylene) two (N', N'-dimethyl urea) 55～177 parts, 3,5-double (acetamido)-2,4,6-triiodo-benzene first
Acid 120～330 parts, concentration is N-propyl group-N-(formyl chloride)-2-(2,4, the 6-Trichlorophenoxy) ethamine of 50ppm～90ppm
60～150 parts, 3-amino-2,4,6-Triiodobenzoic acids 75～135 parts, N-nitro-N-(N'-is to acetylphenyl)-carbamyl-
2,4,6-trichloroanilines 70～160 parts, cross-linking agent 90～165 parts, 3,5-biacetyl amino-2,4,6-Triiodobenzoic acid salt 55～
130 parts, 5-amino-3-carboxyl-2,4,6-tri-iodo-N-methyl-benzamides 80～170 parts, N-acetyl group-3,5-bis-iodo-O-(4-first
Oxygen phenyl)-TYR ethyl ester 40～75 parts, 6-(3,5-diaminobenzene formamido group) n-caproic acid hydrochlorate 45～120 parts；
Described cross-linking agent is 5-amino-2,4,6-triiodo m-phthaloyl chloride, 1,2-dichloroethanes-3,5-double (trifluoromethyl) bromobenzene, N-(3,5-
Dichlorobenzene base) any one in-1,2-dimethylcyclopropane-1,2-diformyl imines；
Two, the manufacture process of microbial adherence bent plate (2-4), comprises the steps of
1st step: add ultra-pure water 610～1200 parts that electrical conductivity is 0.45 μ S/cm～0.75 μ S/cm in a kettle., start
Agitator in reactor, rotating speed is 93rpm～233rpm, start heat pump, make reactor temperature rise to 66 DEG C～
73℃；It is sequentially added into a tetramethylene xylene diisocyanate, 1,6-hexamethylene diisocyanate, dimethylene benzene two different
Cyanate, stirring is to being completely dissolved, and regulation pH value is 2.3～7.3, and agitator speed is adjusted to 123rpm～243rpm,
Temperature is 83 DEG C～153 DEG C, esterification 23～33 hours；
2nd step: take di-2-ethylhexylphosphine oxide butyl dithiocarbamate, N, N "-(methylene two-4,1-phenylene) two (N', N'-dimethyl urea)
Pulverizing, powder diameter is 303～1130 mesh；Add 3, double (acetamido)-2 of 5-, 4,6-Triiodobenzoic acid mix homogeneously are flat
Being laid in pallet, tiling thickness is 13mm～53mm, and employing dosage is 2.3kGy～10.3kGy, energy is 6.3
The alpha ray irradiation 53 of MeV～13MeV～133 minutes, and the β x ray irradiation x 73 of Isodose～163 minutes；
3rd step: the mixed-powder processed through the 2nd step is dissolved in N-propyl group-N-(formyl chloride)-2-(2,4,6-Trichlorophenoxy) ethamine, adds
Entering reactor, agitator speed is 83rpm～193rpm, and temperature is 93 DEG C～143 DEG C, starts vacuum pump and makes reactor
Vacuum reach-0.43MPa～-0.83MPa, keep this state response 13～53 hours；Pressure release is also passed through nitrogen, makes anti-
Answering pressure in still is 0.33MPa～0.73MPa, and insulation stands 13～23 hours；Agitator speed be promoted to 113rpm～
253rpm, simultaneous reactions still pressure release to 0MPa；Be sequentially added into 3-amino-2,4,6-Triiodobenzoic acid, (N'-is to second for N-nitro-N-
Aminosulfonylphenyl)-carbamyl-2, after 4,6-trichloroanilines are completely dissolved, add cross-linking agent stirring mixing so that reactor solution
Hydrophile-lipophile balance value is 4.3～7.3, and insulation stands 13～23 hours；
4th step: when agitator speed is 133rpm～263rpm, is sequentially added into 3,5-biacetyl amino-2,4,6-Triiodobenzoic acids
Salt, the 5-amino iodo-N-methyl-benzamide of-3-carboxyl-2,4,6-three, N-acetyl group-3,5-two iodo-O-(4-anisyl)-L-cheese ammonia
Acetoacetic ester, 6-(3,5-diaminobenzene formamido group) n-caproic acid hydrochlorate, promote reactor pressure so that it is reach 0.83MPa～
1.63MPa, temperature is 133 DEG C～273 DEG C, polyreaction 13～33 hours；After having reacted, reacting kettle inner pressure is dropped
To 0MPa, it is cooled to 33 DEG C～43 DEG C, discharging, enter molding press and can be prepared by microbial adherence bent plate (2-4).
5. the method for work of a Full-automatic temp-control formula style refuse fermenter, it is characterised in that the method includes following step:
1st step: open charging aperture case lid (2-3), renders to fermentation cabin by the rubbish heap gurry of required fermentation from charging aperture (2-2)
(2-1), in, the rubbish heap gurry in fermentation cabin (2-1) is carried out by the microorganism of microbial adherence bent plate (2-4) surface attachment
Decompose oxidation processes；
2nd step: control system (6) starts solar panel (3-1) and carries out light energy collecting and luminous energy is changed into heat energy, heat energy
Thering is provided thermal source for heat energy evaporimeter (3-2), control system (6) starts heat energy evaporimeter (3-2) and heat energy is flashed to high temperature
Steam, now, control system (6) opens heat energy conveying electrically-controlled valve (3-4) in thermal energy transfer duct (3-3) by heat energy
High-temperature steam in evaporimeter (3-2) is delivered in fermentation cabin (2-1), the temperature environment needed for providing for sweat；
3rd step: during the fermentation, control system (6) start-up temperature measurement and control instrument (2-13) is to the temperature in fermentation cabin (2-1)
Situation monitors in real time, and the temperature in temperature measurement-control instrument (2-13) detects fermentation cabin (2-1) reaches 30 DEG C～50 DEG C
Between time, temperature measurement-control instrument (2-13) to control system (6) send feedback signal, control system (6) close heat energy conveying
Electrically-controlled valve (3-4), stops conveying high-temperature steam in fermentation cabin (2-1)；
4th step: during the fermentation, control system (6) starts fermentability measurement and control instrument (2-12) to micro-in fermentation cabin (2-1)
Biological fermentability monitors in real time, microorganism in fermentability measurement and control instrument (2-12) detects fermentation cabin (2-1)
Fermentability less than 30%～60% time, fermentability measurement and control instrument (2-12) to control system (6) send feedback signal also
Warning 40s, prompting staff strengthens the injected volume of microorganism in fermentation cabin (2-1)；
5th step: until this plant running 2～after 7 days, one time fermentation process completes, opens discharge port case lid (2-9), after fermenting
Humus take out from discharge port (2-8), if this process feeding difficulty, control system (6) starts sliding plate angle adjustment
Motor (2-6), the synchronous rotating shaft (2-7) of sliding plate angle adjustment motor (2-6) drives adjustable sliding plate (2-5) to rotate,
In rotation process, angle measurement and control instrument (2-11) monitoring adjustable sliding plate (2-5) rotational angle in real time, when angle measurement and control instrument
(2-11) detect that, when rotational angle reaches between 15 °～60 °, angle measurement and control instrument (2-11) is to control system (6)
Sending feedback signal, control system (6) controls sliding plate angle adjustment motor (2-6) stop motion, produces in sweat
Fermentation liquid flow in fermentation liquid transitional storehouse (2-10) by the filtrate hole on adjustable sliding plate (2-5) surface, control system
(6) fermentation liquid is entered in fermentation liquid storage pool (5) by the electrically-controlled valve opened on fermentation liquid draining pipe (4).
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| CN107748514B (en) * | 2017-09-30 | 2019-06-04 | 贵州松桃嘟嘟食品有限公司 | A kind of travelling fermentation case control system |
| CN108821816A (en) * | 2018-07-04 | 2018-11-16 | 合肥欧语自动化有限公司 | A kind of automated production equipment of liquid state organic fertilizer |
| CN109467460A (en) * | 2018-11-16 | 2019-03-15 | 四川锐源能环科技有限公司 | A kind of agriculture and food and drink waste resource recovery processing method |
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