CN108911396A - A kind of residents in rural community agent-feeding treatment device - Google Patents
A kind of residents in rural community agent-feeding treatment device Download PDFInfo
- Publication number
- CN108911396A CN108911396A CN201810809811.4A CN201810809811A CN108911396A CN 108911396 A CN108911396 A CN 108911396A CN 201810809811 A CN201810809811 A CN 201810809811A CN 108911396 A CN108911396 A CN 108911396A
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- China
- Prior art keywords
- water
- methyl
- chemicals dosing
- dosing plant
- parts
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
- C02F3/342—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the enzymes used
-
- 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
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
The invention discloses a kind of residents in rural community agent-feeding treatment device, chemicals dosing plant includes：Drug-feeding tube, peep hole, drug discharging tube, DC electric field cathode, agitating shaft, DC electric field anode；The chemicals dosing plant housings close structure, the agitating shaft in portion disposed thereon are connect by gear with external motor, and agitating shaft lower part is equipped with impeller；It is equipped with drug-feeding tube in chemicals dosing plant shell side, drug-feeding tube top is equipped with DC electric field anode, and DC electric field anode is inserted into chemicals dosing plant enclosure interior；It is equipped with drug discharging tube in the chemicals dosing plant shell other side, drug discharging tube top is equipped with DC electric field cathode, and DC electric field cathode is inserted into chemicals dosing plant enclosure interior；DC electric field cathode is connect with DC electric field anode outside with DC power supply；Peep hole is equipped in chemicals dosing plant shell side.A kind of residents in rural community agent-feeding treatment device of the present invention, the plant automation degree is high, stable and reliable operation, convenient later maintenance.
Description
Technical field
The invention belongs to field of garbage disposal equipment, and in particular to a kind of residents in rural community agent-feeding treatment device.
Background technique
Currently, various regions domestic rubbish disposal is by the way of burning mostly, due to containing in house refuse, there are many organic
The smog of object, burning pollutes atmosphere, harmful to human body and crops；Also using fill out hole bury by the way of handle
House refuse, but contain many kinds of substance such as plastics in house refuse, it cannot degrade for a long time in the soil, pollution is generated to soil；
Besides classification processing house refuse, it is larger to the plastics in house refuse, paper, metal class mainly by artificial mode
Material sieved, recycling and reusing.The selectivity of conventional garbage processing is small, amount of application is big, at high cost, there are environmental risks
The features such as all limit the more extensive utilization of itself.
Summary of the invention
In order to solve the above technical problem, the present invention provides a kind of residents in rural community agent-feeding treatment device, rubbish dosings
Mixing arrangement 21, including：Discharge port 21-1, auger 21-2, separating sieve 21-3 crush motor 21-4, feed hopper 21-5, pulverization roller
21-6, dust removing tube 21-7, dispersion plate 21-8, blanking tube 21-9, horizontal push plate 21-10, push plate crankshaft 21-11, discharge quantity control
Device 21-12, blanking slideway 21-13, chemicals dosing plant 21-14, mixing chamber 21-15, can not fragmenting bulk export 21-16, water of compaction
Outer comb 21-17；
Feed hopper 21-5 positioned at top is passed through with blanking tube 21-9, blanking slideway 21-13, mixing chamber 21-15, discharge port 21-1
Logical, the lower part feed hopper 21-5 is equipped with pulverization roller 21-6, and pulverization roller 21-6 quantity is 2, arranged opposite, 2 pulverization roller 21-6 with
Outside crushes motor 21-4 mechanical connection；The lower part pulverization roller 21-6 is equipped with dispersion plate 21-8, is equipped with level in the middle part of dispersion plate 21-8
Axis, dispersion plate 21-8 swing along trunnion axis, and the surface dispersion plate 21-8 is equipped with a large amount of through-holes；The lower part dispersion plate 21-8, which is equipped with, to be divided
It is equipped with horizontal push plate 21-10 on the left of choosing sieve 21-3, separating sieve 21-3, horizontal push plate 21-10 passes through push plate crankshaft 21-11 and motor
Connection；Being equipped on the right side of separating sieve 21-3 can not fragmenting bulk outlet 21-16；The lower part separating sieve 21-3 is equipped with blanking amount controller
21-12；Blanking amount controller 21-12 is horizontal push-pull configuration, and blanking amount controller 21-12 controls blanking velocity；Discharge quantity control
The lower part device 21-12 processed be equipped with blanking slideway 21-13, the lower part blanking slideway 21-13 be equipped with mixing chamber 21-15, mixing chamber 21-15 with
Chemicals dosing plant 21-14 connection；The lower part mixing chamber 21-15 is equipped with auger 21-2, and the lower part of the auger 21-2 other end is equipped with discharge port
21-1；The outer comb 21-17 of water of compaction is located at auger 21-2 bottom side；
The outer comb 21-17 of water of compaction is connected to cesspool 1；
Discharge port 21-1 is connected to extruder loading hopper 22-1.
Further, this section is the explanation to heretofore described chemicals dosing plant 21-14 structure.Chemicals dosing plant 21-14 packet
It includes：Drug-feeding tube 21-14-1, peep hole 21-14-2, drug discharging tube 21-14-3, DC electric field cathode 21-14-4, agitating shaft 21-14-
5, DC electric field anode 21-14-6；
The chemicals dosing plant 21-14 housings close structure, the agitating shaft 21-14-5 in portion disposed thereon pass through gear and external electrical
Machine connection, the lower part agitating shaft 21-14-5 are equipped with impeller；It is equipped with drug-feeding tube 21-14-1 in chemicals dosing plant 21-14 shell side, into
The top pencil 21-14-1 is equipped with DC electric field anode 21-14-6, and DC electric field anode 21-14-6 is inserted into chemicals dosing plant 21-14 shell
Internal portion；It is equipped with drug discharging tube 21-14-3 in the chemicals dosing plant 21-14 shell other side, the top drug discharging tube 21-14-3 is equipped with direct current
Field cathode 21-14-4, DC electric field cathode 21-14-4 are inserted into chemicals dosing plant 21-14 enclosure interior；DC electric field cathode 21-14-
4 connect with outside DC electric field anode 21-14-6 with DC power supply；Peep hole 21- is equipped in chemicals dosing plant 21-14 shell side
14-2。
Further, this section is the explanation to heretofore described 22 structure of squeezing device for solid waste.Squeezing device for solid waste 22
Including：Extruder loading hopper 22-1 squeezes capstan winch 22-2, counter-force pallet 22-3, expressed water comb 22-4, sluicing pipe 22-5,
Squeeze water collecting tank 22-6, counter-force supporting plate 22-7, garbage emission mouth 22-8, lower compression water comb 22-9, capstan winch motor 22-
10；
Extruder loading hopper 22-1 positioned at top, its underpart are equipped with counter-force pallet 22-3, counter-force pallet 22-3 concave, center
Hatch frame, counter-force pallet 22-3 quantity are 2；The counter-force side pallet 22-3 is equipped with expressed water comb 22-4；Expressed water comb
22-4 is connected to the extruding water collecting tank 22-6 of lower part, is squeezed water collecting tank 22-6 and is connected to lower compression water comb 22-9；Instead
Be equipped at power pallet 22-3 king and squeeze capstan winch 22-2, run through 2 counter-force pallet 22-3 up and down, squeeze capstan winch 22-2 with
External capstan winch motor 22-10 mechanical connection；It squeezes the bottom capstan winch 22-2 and is equipped with counter-force supporting plate 22-7, be inclined design, length
Rectangular, surface is equipped with a large amount of through-holes, and the counter-force side supporting plate 22-7 is equipped with garbage emission mouth 22-8；The bottom counter-force supporting plate 22-7 is equipped with
Lower compression water comb 22-9；Sluicing pipe 22-5 is equipped on the extruder top loading hopper 22-1；
Lower compression water comb 22-9 is connected to cesspool 1.
Further, this section is the explanation to heretofore described water of compaction after-treatment system structure.Water of compaction post-processing
System includes：Cesspool 1, reaction tower 2, anaerobic pond 3, drainage tube 4, grid 5, filler 6, aerobic tank 7, air blower 8, blender
9, control cabinet 10；
2 side of reaction tower is equipped with cesspool 1, and the other side is equipped with anaerobic pond 3, cesspool 1 and anaerobic pond 3 by pipeline with
Reaction tower 2 connects；The control cabinet 10 is located at 2 front side of reaction tower；The 3 top both ends of anaerobic pond are equipped with blender 9, blender
9 altogether there are two, blender 9 is controlled by conducting wire and control cabinet 10 to be connected；3 side of anaerobic pond is equipped with drainage tube 4, drainage tube
4 quantity are not less than 12, and wherein 4 one end of drainage tube and anaerobic pond 3 penetrate through, and the other end and aerobic tank 7 penetrate through；The air blower 8
Positioned at 7 bottom both ends of aerobic tank, 8 quantity of air blower is two, and air blower 8 and aerobic tank 7 penetrate through；It is set inside the aerobic tank 7
There is filler 6；The grid 5 is located at 7 inner tip of aerobic tank, and grid 5 is fixedly connected with aerobic tank 7.
Further, this section is the explanation to heretofore described 2 structure of reaction tower.The reaction tower 2 includes：Aspiration pump
2-1, filter vat 2-2, sewage pump 2-3, sewage pipe 2-4, reaction chamber 2-5, tracheae 2-6, outlet pipe 2-7, exhaust pipe 2-8；
The reaction chamber 2-5 bottom side be equipped with filter vat 2-2 and sewage pump 2-3, wherein filter vat 2-2 and reaction chamber 2-5 it
Between penetrated through by tracheae 2-6；Sewage pipe 2-4 is equipped on the sewage pump 2-3, sewage pipe 2-4 shape is handstand U-typed；It is described
The side filter vat 2-2 is equipped with aspiration pump 2-1, and aspiration pump 2-1 is penetrated through by pipeline and filter vat 2-2, wherein set on aspiration pump 2-1
There is exhaust pipe 2-8；The top reaction chamber 2-5 side is penetrated through equipped with outlet pipe 2-7, outlet pipe 2-7 and reaction chamber 2-5；It is described
Aspiration pump 2-1 and sewage pump 2-3 passes through conducting wire and is connected with the control of control cabinet 10.
Further, this section is the explanation to heretofore described reaction chamber 2-5 structure.The reaction chamber 2-5 includes：Point
Flow tube 2-5-1, spray head 2-5-2, partition 2-5-3, water outlet 2-5-4, gas chamber 2-5-5 collect air column 2-5-6；
The reaction chamber 2-5 inner bottom is equipped with isocon 2-5-1, is equipped with spray head 2-5-2, spray head 2-5-2 on isocon 2-5-1
Quantity is 6；The reaction chamber 2-5 inner tip is equipped with gas chamber 2-5-5, and wherein the bottom end gas chamber 2-5-5 is equipped with collection air column 2-5-
6, collection air column 2-5-6 quantity is not less than 10, and collection air column 2-5-6 and gas chamber 2-5-5 are penetrated through；Run through on the collection air column 2-5-6
There are partition 2-5-3, partition 2-5-3 mono- to be divided into two layers, is fixedly connected inside partition 2-5-3 and reaction chamber 2-5；The water outlet
2-5-4 is located at reaction chamber 2-5 top side, and water outlet 2-5-4 is welded and fixed with outlet pipe 2-7.
Further, this section is the explanation to heretofore described collection air column 2-5-6 structure.The collection air column 2-5-6 packet
It includes：Gas outlet 2-5-6-1, catalyst jet pipe 2-5-6-2, steam jet 2-5-6-3, organic matter adsorbent material 2-5-6-4, water row
Pipe 2-5-6-5 is put, air column partition 2-5-6-6, air inlet 2-5-6-7, detection hole 2-5-6-8 are collected；
Positioned at the gas outlet 2-5-6-1 on top, uncovered structure, treated, and gas is discharged from gas outlet 2-5-6-1；The catalysis
Agent jet pipe 2-5-6-2 is located at the gas outlet lower part 2-5-6-1, the two spacing 20cm~40cm, and the top catalyst jet pipe 2-5-6-2 is set
There is valve, valve and supervisor connect, and supervisor lower part connects multiple branch pipes, and the quantity of branch pipe is 2~8, and the end of branch pipe is equipped with
Spray head, spray head spray into catalyst in collection air column 2-5-6, and catalyst promotes the degradation of organic matter in gas；The steam jet
2-5-6-3 is located at the lower part catalyst jet pipe 2-5-6-2, the two spacing 20cm~40cm, steam jet 2-5-6-3 circular hollow knot
Structure, steam jet 2-5-6-3 and external steam supervisor connect, and main steam header is equipped with valve, the lower part cyclic annular steam jet 2-5-6-3
Equipped with lotus spray-head, the two is communicated, and lotus spray-head sprays high-temperature steam, and high-temperature steam promotes catalyst to react with organic matter；Institute
It states organic matter adsorbent material 2-5-6-4 and is located at the lower part steam jet 2-5-6-3, the two spacing 20cm~40cm, organic matter absorption
The cellular porous reticular structure of material 2-5-6-4, organic matter adsorbent material 2-5-6-4 are that multilayer is laid out, interlamellar spacing 2cm~4cm,
Organic matter adsorbent material 2-5-6-4 adsorbs organic matter in exhaust gas；The collection air column partition 2-5-6-6 is located in collection air column 2-5-6
Portion and bottom, quantity be 2, collect air column partition 2-5-6-6 stainless steel material, surface be equipped with a large amount of through-hole, collection air column every
The side plate 2-5-6-6 is equipped with water discharge spout 2-5-6-5, for condensed water, excessive catalyst to be collected reprocessing；The collection air column
The bottom 2-5-6 is equipped with air inlet 2-5-6-7, and exhaust gas enters from there；Collect and be equipped with detection hole 2-5-6-8 in the middle part of air column 2-5-6, uses
In overhaul of the equipments.
Further, the partition 2-5-3 is formed by high molecular material pressing mold, the constituent and manufacture of partition 2-5-3
Process is as follows：
One, partition 2-5-3 constituent：
According to parts by weight, 19~89 parts of benzoic acid of 4- (3- formoxyl -1H- indoles -5- base), 4- (2- (amino methyl) -4- nitre
Base phenyl) 129~206 parts of piperazine -1- carboxylic acid tert-butyl ester, 2- cyano -2- (1,2- dihydro -2- Yang Dai quinoxaline -3- base) acetic acid
67~147 parts of ethyl ester, 140~180 parts of methyl acetate of 2- [4- (2- acetyl bromide) -3- methylphenoxy], 3- (5- formoxyl furan
Mutter -2- base) 78~176 parts of -4- methyl benzoic acid, [2- [2- (2,5- dihydro -2,5- dioxo -1H- pyrroles -1- base) ethoxy
Base] ethyl] carbamic acid 1,221~296 parts of 1- dimethylethyl esters, concentration is 5- [(the chloro- 1H- pyrrole of 4- of 57ppm~87ppm
Azoles -1- base) methyl] 155~243 parts of -2- formic acid, 37~80 parts of propionic acid of 3- (1,3,5- trimethyl -1H- pyrazoles -4- base), N-
[2- [4- [(methyl sulphonyl) amino] phenyl] ethyl] carbamic acid 1,127~188 parts of 1- dimethylethyl esters, crosslinking agent 129
~196 parts, 221~334 parts of carboxylate methyl ester of -1H- pyrazoles -5- of -4- nitro of 1- ((ethoxy carbonyl) methyl), 3- (5- acetyl group -
2- thiophene) 218~281 parts of methyl benzoate, 2- (n- methyl-1 H- pyrazoles -1- carboxylic acid amides) ethyl methylcarbamic acid tert-butyl ester
87~169 parts；
The crosslinking agent is 4- (4- hydroxyphenoxy) ethyl butyrate, 3,4- dihydroxypiperdine -1- benzyl carboxylate, 2- (3- amyl)
Any one in dimethyl malenate；
Two, the manufacturing process of partition 2-5-3, comprises the steps of：
Step 1：2755~3655 parts of ultrapure water that conductivity is 5.33 μ of μ S/cm~8.23 S/cm, starting are added in a kettle
Blender in reaction kettle, revolving speed are 76rpm~131rpm, start heat pump, reactor temperature is made to rise to 77 DEG C~129
℃；Sequentially add 4- (3- formoxyl -1H- indoles -5- base) benzoic acid, 4- (2- (amino methyl) -4- nitrobenzophenone) piperazine -1-
Carboxylic acid tert-butyl ester, 2- cyano -2- (1,2- dihydro -2- Yang Dai quinoxaline -3- base) ethyl acetate, stirring and adjusting pH value is 5.8
~7.7, agitator speed is adjusted to 141rpm~233rpm, temperature is 115 DEG C~169 DEG C, is chemically reacted 21~33 hours；
Step 2：Take 2- [4- (2- acetyl bromide) -3- methylphenoxy] methyl acetate, 3- (5- formylfuran -2- base) -4-
Methyl benzoic acid is crushed, and powder diameter is 1050~1250 mesh；[2- [2- (2,5- dihydro -2,5- dioxo -1H- is added
Pyrroles -1- base) ethyoxyl] ethyl] carbamic acid 1,1- dimethylethyl esters be uniformly mixed, be laid in pallet, tiling with a thickness of
29mm~45mm uses the alpha ray irradiation 135~225 that dosage is 6.9MeV~9.1MeV for 8.9kGy~12.8kGy, energy
Minute and the same dose of β x ray irradiation xs 135~225 minutes；
Step 3：The mixed-powder handled through step 2 is added in 5- [(the chloro- 1H- pyrazol-1-yl of 4-) methyl] -2- formic acid, is added
Enter reaction kettle, agitator speed is 137rpm~182rpm, and temperature is 132 DEG C~201 DEG C, and booster air pump makes the pressure of reaction kettle
Reach 1.03MPa~2.27MPa, keeps this state response 15~27 hours；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure
1.14MPa~1.81MPa, heat preservation stand 17~25 hours；Agitator speed is promoted to 221rpm~269rpm, simultaneous reactions kettle
Pressure release is to 0MPa；Sequentially add 3- (1,3,5- trimethyl -1H- pyrazoles -4- base) propionic acid, N- [2- [4- [(methyl sulphonyl) ammonia
Base] phenyl] ethyl] carbamic acid 1, after 1- dimethylethyl esters are completely dissolved, crosslinking agent is added and is stirred, heat preservation standing 19~
29 hours；
Step 4：When agitator speed is 233rpm~298rpm, 1- ((ethoxy carbonyl) methyl) -4- nitro-is sequentially added
1H- pyrazoles -5- carboxylate methyl ester, 3- (5- acetyl group -2- thiophene) methyl benzoate and 2- (n- methyl-1 H- pyrazoles -1- carboxylic acid amides)
The ethyl methylcarbamic acid tert-butyl ester promotes reactor pressure, reaches 2.60MPa~4.1MPa, and temperature is 188 DEG C~
253 DEG C, polymerization reaction 25~35 hours；Reacting kettle inner pressure is down to 0MPa after the reaction was completed, is cooled to 29 DEG C~33 DEG C, out
Material, entering molding press can be prepared by partition 2-5-3.
A kind of residents in rural community agent-feeding treatment device of the present invention, the plant automation degree is high, stable
Reliably, convenient later maintenance；Device treatment effeciency is high, reduces labor intensity, while to producing in sewage disposal process
Raw exhaust gas carries out concentration purification filtering, avoids the pollution to air.
Detailed description of the invention
Fig. 1 is heretofore described 21 structural schematic diagram of rubbish medicine mixing device.
Fig. 2 is heretofore described chemicals dosing plant 21-14 structural schematic diagram.
Fig. 3 is heretofore described 22 structural schematic diagram of squeezing device for solid waste.
Fig. 4 is heretofore described water of compaction after-treatment system structural schematic diagram.
Fig. 5 is heretofore described 2 structural schematic diagram of reaction tower.
Fig. 6 is heretofore described reaction chamber 2-5 structural schematic diagram.
Fig. 7 is heretofore described collection air column 2-5-6 schematic diagram.
Fig. 8 is that heretofore described partition 2-5-3 fatigue strength changes over time figure.
Specific embodiment
With reference to the accompanying drawings and examples to a kind of residents in rural community agent-feeding treatment device provided by the invention carry out into
One step explanation.
As shown in Figure 1, being a kind of heretofore described residents in rural community agent-feeding treatment apparatus structure schematic diagram.From figure
In find out, rubbish medicine mixing device 21, including：Discharge port 21-1, auger 21-2, separating sieve 21-3 crush motor 21-4, into
Hopper 21-5, pulverization roller 21-6, dust removing tube 21-7, dispersion plate 21-8, blanking tube 21-9, horizontal push plate 21-10, push plate crankshaft
21-11, blanking amount controller 21-12, blanking slideway 21-13, chemicals dosing plant 21-14, mixing chamber 21-15, can not fragmenting bulk
Export 21-16, the outer comb 21-17 of water of compaction；
Feed hopper 21-5 positioned at top is passed through with blanking tube 21-9, blanking slideway 21-13, mixing chamber 21-15, discharge port 21-1
Logical, the lower part feed hopper 21-5 is equipped with pulverization roller 21-6, and pulverization roller 21-6 quantity is 2, arranged opposite, 2 pulverization roller 21-6 with
Outside crushes motor 21-4 mechanical connection；The lower part pulverization roller 21-6 is equipped with dispersion plate 21-8, is equipped with level in the middle part of dispersion plate 21-8
Axis, dispersion plate 21-8 swing along trunnion axis, and the surface dispersion plate 21-8 is equipped with a large amount of through-holes；The lower part dispersion plate 21-8, which is equipped with, to be divided
It is equipped with horizontal push plate 21-10 on the left of choosing sieve 21-3, separating sieve 21-3, horizontal push plate 21-10 passes through push plate crankshaft 21-11 and motor
Connection；Being equipped on the right side of separating sieve 21-3 can not fragmenting bulk outlet 21-16；The lower part separating sieve 21-3 is equipped with blanking amount controller
21-12；Blanking amount controller 21-12 is horizontal push-pull configuration, and blanking amount controller 21-12 controls blanking velocity；Discharge quantity control
The lower part device 21-12 processed be equipped with blanking slideway 21-13, the lower part blanking slideway 21-13 be equipped with mixing chamber 21-15, mixing chamber 21-15 with
Chemicals dosing plant 21-14 connection；The lower part mixing chamber 21-15 is equipped with auger 21-2, and the lower part of the auger 21-2 other end is equipped with discharge port
21-1；The outer comb 21-17 of water of compaction is located at auger 21-2 bottom side；
The outer comb 21-17 of water of compaction is connected to cesspool 1.
As shown in Fig. 2, being heretofore described chemicals dosing plant 21-14 structural schematic diagram.As seen from the figure, chemicals dosing plant
21-14 includes：Drug-feeding tube 21-14-1, peep hole 21-14-2, drug discharging tube 21-14-3, DC electric field cathode 21-14-4, stirring
Axis 21-14-5, DC electric field anode 21-14-6；
The chemicals dosing plant 21-14 housings close structure, the agitating shaft 21-14-5 in portion disposed thereon pass through gear and external electrical
Machine connection, the lower part agitating shaft 21-14-5 are equipped with impeller；It is equipped with drug-feeding tube 21-14-1 in chemicals dosing plant 21-14 shell side, into
The top pencil 21-14-1 is equipped with DC electric field anode 21-14-6, and DC electric field anode 21-14-6 is inserted into chemicals dosing plant 21-14 shell
Internal portion；It is equipped with drug discharging tube 21-14-3 in the chemicals dosing plant 21-14 shell other side, the top drug discharging tube 21-14-3 is equipped with direct current
Field cathode 21-14-4, DC electric field cathode 21-14-4 are inserted into chemicals dosing plant 21-14 enclosure interior；DC electric field cathode 21-14-
4 connect with outside DC electric field anode 21-14-6 with DC power supply；Peep hole 21- is equipped in chemicals dosing plant 21-14 shell side
14-2。
As shown in figure 3, being heretofore described 22 structural schematic diagram of squeezing device for solid waste.As seen from the figure, rubbish squeezes
Pressure device 22 includes：Extruder loading hopper 22-1 squeezes capstan winch 22-2, counter-force pallet 22-3, expressed water comb 22-4, washing
Pipe 22-5 squeezes water collecting tank 22-6, counter-force supporting plate 22-7, garbage emission mouth 22-8, lower compression water comb 22-9, capstan winch electricity
Machine 22-10；
Extruder loading hopper 22-1 positioned at top, its underpart are equipped with counter-force pallet 22-3, counter-force pallet 22-3 concave, center
Hatch frame, counter-force pallet 22-3 quantity are 2；The counter-force side pallet 22-3 is equipped with expressed water comb 22-4；Expressed water comb
22-4 is connected to the extruding water collecting tank 22-6 of lower part, is squeezed water collecting tank 22-6 and is connected to lower compression water comb 22-9；Instead
Be equipped at power pallet 22-3 king and squeeze capstan winch 22-2, run through 2 counter-force pallet 22-3 up and down, squeeze capstan winch 22-2 with
External capstan winch motor 22-10 mechanical connection；It squeezes the bottom capstan winch 22-2 and is equipped with counter-force supporting plate 22-7, be inclined design, length
Rectangular, surface is equipped with a large amount of through-holes, and the counter-force side supporting plate 22-7 is equipped with garbage emission mouth 22-8；The bottom counter-force supporting plate 22-7 is equipped with
Lower compression water comb 22-9；Sluicing pipe 22-5 is equipped on the extruder top loading hopper 22-1；
Lower compression water comb 22-9 is connected to cesspool 1.
As shown in figure 4, being heretofore described water of compaction after-treatment system structural schematic diagram.As seen from the figure, including：
Cesspool 1, reaction tower 2, anaerobic pond 3, drainage tube 4, grid 5, filler 6, aerobic tank 7, air blower 8, including：Cesspool 1, instead
Answer tower 2, anaerobic pond 3, drainage tube 4, grid 5, filler 6, aerobic tank 7, air blower 8, blender 9, control cabinet 10；
2 side of reaction tower is equipped with cesspool 1, and the other side is equipped with anaerobic pond 3, cesspool 1 and anaerobic pond 3 by pipeline with
Reaction tower 2 connects；The control cabinet 10 is located at 2 front side of reaction tower；The 3 top both ends of anaerobic pond are equipped with blender 9, blender
9 altogether there are two, blender 9 is controlled by conducting wire and control cabinet 10 to be connected；3 side of anaerobic pond is equipped with drainage tube 4, drainage tube
4 quantity are not less than 12, and wherein 4 one end of drainage tube and anaerobic pond 3 penetrate through, and the other end and aerobic tank 7 penetrate through；The air blower 8
Positioned at 7 bottom both ends of aerobic tank, 8 quantity of air blower is two, and air blower 8 and aerobic tank 7 penetrate through；It is set inside the aerobic tank 7
There is filler 6；The grid 5 is located at 7 inner tip of aerobic tank, and grid 5 is fixedly connected with aerobic tank 7.
As shown in figure 5, being heretofore described 2 structural schematic diagram of reaction tower.As seen from the figure, the reaction tower 2 wraps
It includes：Aspiration pump 2-1, filter vat 2-2, sewage pump 2-3, sewage pipe 2-4, reaction chamber 2-5, tracheae 2-6, outlet pipe 2-7, exhaust pipe
2-8；
The reaction chamber 2-5 bottom side be equipped with filter vat 2-2 and sewage pump 2-3, wherein filter vat 2-2 and reaction chamber 2-5 it
Between penetrated through by tracheae 2-6；Sewage pipe 2-4 is equipped on the sewage pump 2-3, sewage pipe 2-4 shape is handstand U-typed；It is described
The side filter vat 2-2 is equipped with aspiration pump 2-1, and aspiration pump 2-1 is penetrated through by pipeline and filter vat 2-2, wherein set on aspiration pump 2-1
There is exhaust pipe 2-8；The top reaction chamber 2-5 side is penetrated through equipped with outlet pipe 2-7, outlet pipe 2-7 and reaction chamber 2-5；It is described
Aspiration pump 2-1 and sewage pump 2-3 passes through conducting wire and is connected with the control of control cabinet 10.
As shown in fig. 6, being heretofore described reaction chamber 2-5 structural schematic diagram.As seen from the figure, the reaction chamber 2-
5 include：Isocon 2-5-1, spray head 2-5-2, partition 2-5-3, water outlet 2-5-4, gas chamber 2-5-5 collect air column 2-5-6；
The reaction chamber 2-5 inner bottom is equipped with isocon 2-5-1, is equipped with spray head 2-5-2, spray head 2-5-2 on isocon 2-5-1
Quantity is 6；The reaction chamber 2-5 inner tip is equipped with gas chamber 2-5-5, and wherein the bottom end gas chamber 2-5-5 is equipped with collection air column 2-5-
6, collection air column 2-5-6 quantity is not less than 10, and collection air column 2-5-6 and gas chamber 2-5-5 are penetrated through；Run through on the collection air column 2-5-6
There are partition 2-5-3, partition 2-5-3 mono- to be divided into two layers, is fixedly connected inside partition 2-5-3 and reaction chamber 2-5；The water outlet
2-5-4 is located at reaction chamber 2-5 top side, and water outlet 2-5-4 is welded and fixed with outlet pipe 2-7.
As shown in fig. 7, being heretofore described collection air column 2-5-6 structural schematic diagram.As seen from the figure, the collection air column
2-5-6 includes：Gas outlet 2-5-6-1, catalyst jet pipe 2-5-6-2, steam jet 2-5-6-3, organic matter adsorbent material 2-5-
6-4, water discharge spout 2-5-6-5 collect air column partition 2-5-6-6, air inlet 2-5-6-7, detection hole 2-5-6-8；
Positioned at the gas outlet 2-5-6-1 on top, uncovered structure, treated, and gas is discharged from gas outlet 2-5-6-1；The catalysis
Agent jet pipe 2-5-6-2 is located at the gas outlet lower part 2-5-6-1, the two spacing 20cm~40cm, and the top catalyst jet pipe 2-5-6-2 is set
There is valve, valve and supervisor connect, and supervisor lower part connects multiple branch pipes, and the quantity of branch pipe is 2~8, and the end of branch pipe is equipped with
Spray head, spray head spray into catalyst in collection air column 2-5-6, and catalyst promotes the degradation of organic matter in gas；The steam jet
2-5-6-3 is located at the lower part catalyst jet pipe 2-5-6-2, the two spacing 20cm~40cm, steam jet 2-5-6-3 circular hollow knot
Structure, steam jet 2-5-6-3 and external steam supervisor connect, and main steam header is equipped with valve, the lower part cyclic annular steam jet 2-5-6-3
Equipped with lotus spray-head, the two is communicated, and lotus spray-head sprays high-temperature steam, and high-temperature steam promotes catalyst to react with organic matter；Institute
It states organic matter adsorbent material 2-5-6-4 and is located at the lower part steam jet 2-5-6-3, the two spacing 20cm~40cm, organic matter absorption
The cellular porous reticular structure of material 2-5-6-4, organic matter adsorbent material 2-5-6-4 are that multilayer is laid out, interlamellar spacing 2cm~4cm,
Organic matter adsorbent material 2-5-6-4 adsorbs organic matter in exhaust gas；The collection air column partition 2-5-6-6 is located in collection air column 2-5-6
Portion and bottom, quantity be 2, collect air column partition 2-5-6-6 stainless steel material, surface be equipped with a large amount of through-hole, collection air column every
The side plate 2-5-6-6 is equipped with water discharge spout 2-5-6-5, for condensed water, excessive catalyst to be collected reprocessing；The collection air column
The bottom 2-5-6 is equipped with air inlet 2-5-6-7, and exhaust gas enters from there；Collect and be equipped with detection hole 2-5-6-8 in the middle part of air column 2-5-6, uses
In overhaul of the equipments.
Following embodiment further illustrates the contents of the present invention, and as partition 2-5-3, it is significant components of the invention,
Due to its presence, the service life of integral device is increased, it plays crucial work for the safety of integral device, even running
With.For this purpose, by it is following be embodiment, further verify partition 2-5-3 of the present invention, shown be higher than other phases
Close the physical characteristic of patent.
Embodiment 1
Partition 2-5-3 of the present invention is manufactured according to the following steps, and according to parts by weight：
Step 1：2755 parts of ultrapure water that conductivity is 5.33 μ S/cm are added in a kettle, start blender in reaction kettle, turn
Speed is 76rpm, starts heat pump, reactor temperature is made to rise to 77 DEG C；Sequentially add 4- (3- formoxyl -1H- indoles -5-
Base) 19 parts of benzoic acid, 4- (2- (amino methyl) -4- nitrobenzophenone) 129 parts of piperazine -1- carboxylic acid tert-butyl ester, 2- cyano -2- (1,
2- dihydro -2- Yang Dai quinoxaline -3- base) 67 parts of ethyl acetate, stirring and adjusting pH value is 5.8, and agitator speed is adjusted to
141rpm, temperature are 115 DEG C, are chemically reacted 21 hours；
Step 2：Take 2- [4- (2- acetyl bromide) -3- methylphenoxy] 140 parts of methyl acetate, 3- (5- formylfuran -2-
Base) 78 parts of -4- methyl benzoic acid crushed, powder diameter be 1050 mesh；[2- [2- (2,5- dihydro -2,5- dioxo-is added
1H- pyrroles -1- base) ethyoxyl] ethyl] carbamic acid 1,221 parts of 1- dimethylethyl esters are uniformly mixed, and are laid in pallet, put down
With a thickness of 29mm, the alpha ray for using dosage to be 6.9MeV for 8.9kGy, energy irradiates 135 minutes and the same dose of β paving
X ray irradiation x 135 minutes；
Step 3：The mixed-powder handled through step 2 is dissolved in the 5- [(the chloro- 1H- pyrazol-1-yl of 4-) methyl]-that concentration is 57ppm
In 155 parts of 2- formic acid, reaction kettle, agitator speed 137rpm is added, temperature is 132 DEG C, and starting vacuum pump makes reaction kettle
Vacuum degree reaches -1.03MPa, keeps this state response 15 hours；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure
1.14MPa, heat preservation stand 17 hours；Agitator speed is promoted to 221rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 3-
(1,3,5- trimethyl -1H- pyrazoles -4- base) 37 parts of propionic acid, N- [2- [4- [(methyl sulphonyl) amino] phenyl] ethyl] amino
Formic acid 1 after 127 parts of 1- dimethylethyl esters are completely dissolved, are added 129 parts of crosslinking agent and are stirred, so that the parent of reaction kettle solution
Hydrophile-lipophile balance value is 6.1, and heat preservation stands 19 hours；
Step 4：When agitator speed is 233rpm, 1- ((ethoxy carbonyl) methyl) -4- nitro -1H- pyrazoles-is sequentially added
221 parts of 5- carboxylate methyl ester, 218 parts of 3- (5- acetyl group -2- thiophene) methyl benzoate and 2- (n- methyl-1 H- pyrazoles -1- carboxylic acyl
Amine) 87 parts of the ethyl methylcarbamic acid tert-butyl ester, reactor pressure is promoted, 2.60MPa is reached, temperature is 188 DEG C, polymerization
Reaction 25 hours；Reacting kettle inner pressure is down to 0MPa after the reaction was completed, is cooled to 29 DEG C, discharging, entering molding press can be prepared by
Partition 2-5-3.
The crosslinking agent is 4- (4- hydroxyphenoxy) ethyl butyrate.
Embodiment 2
Partition 2-5-3 of the present invention is manufactured according to the following steps, and according to parts by weight：
Step 1：3205 parts of ultrapure water that conductivity is 6.78 μ S/cm are added in a kettle, start blender in reaction kettle, turn
Speed is 103rpm, starts heat pump, reactor temperature is made to rise to 103 DEG C；Sequentially add 4- (3- formoxyl -1H- indoles -
5- yl) 54 parts of benzoic acid, 4- (2- (amino methyl) -4- nitrobenzophenone) 164 parts of piperazine -1- carboxylic acid tert-butyl ester, 2- cyano -2-
107 parts of ethyl acetate of (1,2- dihydro -2- Yang Dai quinoxaline -3- base), stirring and adjusting pH value is 6.8, by agitator speed tune
To 187rpm, temperature is 141 DEG C, is chemically reacted 28 hours；
Step 2：Take 2- [4- (2- acetyl bromide) -3- methylphenoxy] 159 parts of methyl acetate, 3- (5- formylfuran -2-
Base) 127 parts of -4- methyl benzoic acid crushed, powder diameter be 1150 mesh；[2- [2- (2,5- dihydro -2,5- dioxy is added
Generation -1H- pyrroles -1- base) ethyoxyl] ethyl] carbamic acid 1,258 parts of 1- dimethylethyl esters are uniformly mixed, it is laid in pallet,
With a thickness of 37mm, the alpha ray for using dosage to be 8.0MeV for 10.9kGy, energy irradiates 180 minutes and Isodose for tiling
β x ray irradiation x 180 minutes；
Step 3：The mixed-powder handled through step 2 is dissolved in the 5- [(the chloro- 1H- pyrazol-1-yl of 4-) methyl]-that concentration is 72ppm
In 199 parts of 2- formic acid, reaction kettle, agitator speed 158rpm is added, temperature is 167 DEG C, and starting vacuum pump makes reaction kettle
Vacuum degree reaches 0.80MPa, keeps this state response 21 hours；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure
1.47MPa, heat preservation stand 21 hours；Agitator speed is promoted to 237rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 3-
(1,3,5- trimethyl -1H- pyrazoles -4- base) 58 parts of propionic acid, N- [2- [4- [(methyl sulphonyl) amino] phenyl] ethyl] amino
Formic acid 1 after 157 parts of 1- dimethylethyl esters are completely dissolved, are added 161 parts of crosslinking agent and are stirred, so that the parent of reaction kettle solution
Hydrophile-lipophile balance value is 8.0, and heat preservation stands 24 hours；
Step 4：When agitator speed is 265rpm, 1- ((ethoxy carbonyl) methyl) -4- nitro -1H- pyrazoles-is sequentially added
277 parts of 5- carboxylate methyl ester, 249 parts of 3- (5- acetyl group -2- thiophene) methyl benzoate and 2- (n- methyl-1 H- pyrazoles -1- carboxylic acyl
Amine) 128 parts of the ethyl methylcarbamic acid tert-butyl ester, reactor pressure is promoted, 3.53MPa is reached, temperature is 220 DEG C, is gathered
Close reaction 30 hours；Reacting kettle inner pressure is down to 0MPa after the reaction was completed, is cooled to 31 DEG C, discharging, entering molding press can make
Obtain partition 2-5-3.
The crosslinking agent is 3,4- dihydroxypiperdine -1- benzyl carboxylate.
Embodiment 3
Partition 2-5-3 of the present invention is manufactured according to the following steps, and according to parts by weight：
Step 1：3655 parts of ultrapure water that conductivity is 8.23 μ S/cm are added in a kettle, start blender in reaction kettle, turn
Speed is 131rpm, starts heat pump, reactor temperature is made to rise to 129 DEG C；Sequentially add 4- (3- formoxyl -1H- indoles -
5- yl) 89 parts of benzoic acid, 4- (2- (amino methyl) -4- nitrobenzophenone) 206 parts of piperazine -1- carboxylic acid tert-butyl ester, 2- cyano -2-
147 parts of ethyl acetate of (1,2- dihydro -2- Yang Dai quinoxaline -3- base), stirring and adjusting pH value is 7.7, by agitator speed tune
To 233rpm, temperature is 169 DEG C, is chemically reacted 33 hours；
Step 2：Take 2- [4- (2- acetyl bromide) -3- methylphenoxy] 180 parts of methyl acetate, 3- (5- formylfuran -2-
Base) 176 parts of -4- methyl benzoic acid crushed, powder diameter be 1241 mesh；[2- [2- (2,5- dihydro -2,5- dioxy is added
Generation -1H- pyrroles -1- base) ethyoxyl] ethyl] carbamic acid 1,296 parts of 1- dimethylethyl esters are uniformly mixed, it is laid in pallet,
With a thickness of 45mm, the alpha ray for using dosage to be 9.1MeV for 12.8kGy, energy irradiates 225 minutes and Isodose for tiling
β x ray irradiation x 225 minutes；
Step 3：The mixed-powder handled through step 2 is dissolved in the 5- [(the chloro- 1H- pyrazol-1-yl of 4-) methyl]-that concentration is 87ppm
In 243 parts of 2- formic acid, reaction kettle, agitator speed 182rpm is added, temperature is 201 DEG C, and starting vacuum pump makes reaction kettle
Vacuum degree reaches 1.90MPa, keeps this state response 27 hours；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure
1.81MPa, heat preservation stand 25 hours；Agitator speed is promoted to 269rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 3-
(1,3,5- trimethyl -1H- pyrazoles -4- base) 80 parts of propionic acid, N- [2- [4- [(methyl sulphonyl) amino] phenyl] ethyl] amino
Formic acid 1 after 188 parts of 1- dimethylethyl esters are completely dissolved, are added 196 parts of crosslinking agent and are stirred, so that the parent of reaction kettle solution
Hydrophile-lipophile balance value is 9.8, and heat preservation stands 28 hours；
Step 4：When agitator speed is 297rpm, 1- ((ethoxy carbonyl) methyl) -4- nitro -1H- pyrazoles-is sequentially added
334 parts of 5- carboxylate methyl ester, 281 parts of 3- (5- acetyl group -2- thiophene) methyl benzoate and 2- (n- methyl-1 H- pyrazoles -1- carboxylic acyl
Amine) 169 parts of the ethyl methylcarbamic acid tert-butyl ester, reactor pressure is promoted, 4.1MPa is reached, temperature is 253 DEG C, polymerization
Reaction 35 hours；Reacting kettle inner pressure is down to 0MPa after the reaction was completed, is cooled to 33 DEG C, discharging, entering molding press can be prepared by
Partition 2-5-3.
The crosslinking agent is 2- (3- amyl) dimethyl malenate.
Reference examples
Reference examples are certain commercially available brand component same as the application partition 2-5-3, are tested for the property test.
Embodiment 4
The partition 2-5-3 and reference examples that Examples 1 to 3 is prepared same component obtained carry out using effect comparison.
The two heat distortion temperature, compression strength, Air permenbility, corrosion rate are counted, the results are shown in Table 1.
As seen from Table 1, partition 2-5-3 of the present invention, heat distortion temperature, compression strength, Air permenbility, corrosion rate
Etc. indexs be superior to the prior art production product.
In addition, finding out from the statistical chart that heretofore described partition 2-5-3 fatigue strength changes over time, embodiment
Partition 2-5-3 used in 1~3, fatigue of materials intensity are substantially better than existing product with using time change degree.
Claims (10)
1. a kind of residents in rural community agent-feeding treatment device, which is characterized in that chemicals dosing plant (21-14) includes：Drug-feeding tube (21-
14-1), peep hole (21-14-2), drug discharging tube (21-14-3), DC electric field cathode (21-14-4), agitating shaft (21-14-5),
DC electric field anode (21-14-6)；
Chemicals dosing plant (21-14) the housings close structure, the agitating shaft (21-14-5) in portion disposed thereon, by gear and outside
The connection of portion's motor, the agitating shaft lower part (21-14-5) are equipped with impeller；Drug-feeding tube is equipped in chemicals dosing plant (21-14) shell side
(21-14-1), the drug-feeding tube top (21-14-1) are equipped with DC electric field anode (21-14-6), DC electric field anode (21-14-6)
It is inserted into chemicals dosing plant (21-14) enclosure interior；It is equipped with drug discharging tube (21-14-3) in chemicals dosing plant (21-14) the shell other side, out
The pencil top (21-14-3) is equipped with DC electric field cathode (21-14-4), and DC electric field cathode (21-14-4) is inserted into chemicals dosing plant
(21-14) enclosure interior；DC electric field cathode (21-14-4) and the outside DC electric field positive (21-14-6) connect with DC power supply
It connects；Peep hole (21-14-2) is equipped in chemicals dosing plant (21-14) shell side；
It is internal that the chemicals dosing plant (21-14) is located at rubbish medicine mixing device (21).
2. a kind of residents in rural community agent-feeding treatment device according to claim 1, which is characterized in that rubbish dosing mixing
Device (21), including：Discharge port (21-1), auger (21-2), separating sieve (21-3) crush motor (21-4), feed hopper (21-
5), pulverization roller (21-6), dust removing tube (21-7), dispersion plate (21-8), blanking tube (21-9), horizontal push plate (21-10), push plate are bent
Axis (21-11), blanking amount controller (21-12), blanking slideway (21-13), chemicals dosing plant (21-14), mixing chamber (21-15),
Can not fragmenting bulk outlet (21-16), the outer comb (21-17) of water of compaction；
Feed hopper (21-5) positioned at top, with blanking tube (21-9), blanking slideway (21-13), mixing chamber (21-15), discharging
Mouthful (21-1) perforation, the feed hopper lower part (21-5) are equipped with pulverization roller (21-6), and pulverization roller (21-6) quantity is 2, arranged opposite,
2 pulverization rollers (21-6) and external crush motor (21-4) are mechanically connected；The pulverization roller lower part (21-6) is equipped with dispersion plate (21-8),
Trunnion axis is equipped in the middle part of dispersion plate (21-8), dispersion plate (21-8) swings along trunnion axis, and the surface dispersion plate (21-8) is equipped with
A large amount of through-holes；The dispersion plate lower part (21-8) is equipped with separating sieve (21-3), and horizontal push plate (21- is equipped on the left of separating sieve (21-3)
10), horizontal push plate (21-10) is connected to motor by push plate crankshaft (21-11)；Being equipped on the right side of separating sieve (21-3) can not crush
Bulk exports (21-16)；The separating sieve lower part (21-3) is equipped with blanking amount controller (21-12)；Blanking amount controller (21-12) is
Horizontal push-pull configuration, blanking amount controller (21-12) control blanking velocity；The blanking amount controller lower part (21-12) is equipped with blanking
Slideway (21-13), the blanking slideway lower part (21-13) are equipped with mixing chamber (21-15), mixing chamber (21-15) and chemicals dosing plant (21-
14) it is connected to；The mixing chamber lower part (21-15) is equipped with auger (21-2), and the lower part of auger (21-2) other end is equipped with discharge port (21-
1)；The outer comb (21-17) of water of compaction is located at auger (21-2) bottom side；
The outer comb (21-17) of water of compaction is connected to cesspool (1)；
Discharge port (21-1) is connected to extruder loading hopper (22-1).
3. a kind of residents in rural community agent-feeding treatment device according to claim 2, which is characterized in that squeezing device for solid waste
(22) include：Extruder loading hopper (22-1) squeezes capstan winch (22-2), counter-force pallet (22-3), expressed water comb (22-4),
Sluicing pipe (22-5) squeezes water collecting tank (22-6), counter-force supporting plate (22-7), garbage emission mouth (22-8), lower compression water row
It manages (22-9), capstan winch motor (22-10)；
Extruder loading hopper (22-1) positioned at top, its underpart are equipped with counter-force pallet (22-3), and counter-force pallet (22-3) is recessed
Type, central opening structure, counter-force pallet (22-3) quantity are 2；The counter-force pallet side (22-3) is equipped with expressed water comb (22-
4)；Expressed water comb (22-4) is connected to the extruding water collecting tank (22-6) of lower part, squeezes water collecting tank (22-6) and lower part is squeezed
Press water comb (22-9) connection；It is equipped at counter-force pallet (22-3) king and squeezes capstan winch (22-2), run through 2 up and down instead
Power pallet (22-3), squeezes capstan winch (22-2) and external capstan winch motor (22-10) is mechanically connected；Squeeze the bottom capstan winch (22-2)
It is inclined design, rectangle, surface equipped with a large amount of through-holes, the side counter-force supporting plate (22-7) is set equipped with counter-force supporting plate (22-7)
There is garbage emission mouth (22-8)；The counter-force supporting plate bottom (22-7) is equipped with lower compression water comb (22-9)；It feeds and leaks in extruder
The top (22-1) struggle against equipped with sluicing pipe (22-5)；
The lower compression water comb (22-9) is connected to cesspool (1).
4. a kind of residents in rural community agent-feeding treatment device according to claim 3, which is characterized in that after its water of compaction
Reason system includes：Cesspool (1), reaction tower (2), anaerobic pond (3), drainage tube (4), grid (5), filler (6), aerobic tank
(7), air blower (8), blender (9), control cabinet (10)；
Reaction tower (2) side is equipped with cesspool (1), and the other side is equipped with anaerobic pond (3), and cesspool (1) and anaerobic pond (3) are equal
It is connect by pipeline with reaction tower (2)；The control cabinet (10) is located on front side of reaction tower (2)；Both ends at the top of the anaerobic pond (3)
Equipped with blender (9), blender (9) altogether there are two, blender (9), which is controlled by conducting wire with control cabinet (10), to be connected；It is described to detest
Oxygen pond (3) side is equipped with drainage tube (4), and drainage tube (4) quantity is not less than 12, wherein drainage tube (4) one end and anaerobic pond (3)
Perforation, the other end and aerobic tank (7) penetrate through；The air blower (8) is located at aerobic tank (7) bottom both ends, and air blower (8) quantity is
Two, air blower (8) and aerobic tank (7) penetrate through；Filler (6) are equipped with inside the aerobic tank (7)；The grid (5) is located at
Aerobic tank (7) inner tip, grid (5) are fixedly connected with aerobic tank (7), and aerobic tank (7) side is equipped with outlet pipe.
5. a kind of residents in rural community agent-feeding treatment device according to claim 4, which is characterized in that the reaction tower
(2) include：Aspiration pump (2-1), filter vat (2-2), sewage pump (2-3), sewage pipe (2-4), reaction chamber (2-5), tracheae (2-
6), outlet pipe (2-7), exhaust pipe (2-8)；
Reaction chamber (2-5) bottom side is equipped with filter vat (2-2) and sewage pump (2-3), wherein filter vat (2-2) and reaction
It is penetrated through between room (2-5) by tracheae (2-6)；It is equipped with sewage pipe (2-4) on the sewage pump (2-3), sewage pipe (2-4) shape
For handstand U-typed；The filter vat side (2-2) is equipped with aspiration pump (2-1), and aspiration pump (2-1) passes through pipeline and filter vat (2-
2) it penetrates through, is wherein equipped with exhaust pipe (2-8) on aspiration pump (2-1)；Reaction chamber (2-5) the top side is equipped with outlet pipe (2-
7), outlet pipe (2-7) and reaction chamber (2-5) are penetrated through；
The aspiration pump (2-1) and sewage pump (2-3) are connected by conducting wire with control cabinet (10) control.
6. a kind of residents in rural community agent-feeding treatment device according to claim 5, which is characterized in that the reaction chamber
(2-5) includes：Isocon (2-5-1), spray head (2-5-2), partition (2-5-3), water outlet (2-5-4), gas chamber (2-5-5), collection
Air column (2-5-6)；
Reaction chamber (2-5) inner bottom is equipped with isocon (2-5-1), is equipped with spray head (2-5-2) on isocon (2-5-1),
Spray head (2-5-2) quantity is 6；Reaction chamber (2-5) inner tip is equipped with gas chamber (2-5-5), wherein the bottom gas chamber (2-5-5)
End is equipped with collection air column (2-5-6), and collection air column (2-5-6) quantity is not less than 10, and collection air column (2-5-6) is passed through with gas chamber (2-5-5)
It is logical；Through having partition (2-5-3) on the collection air column (2-5-6), partition (2-5-3) one is divided into two layers, partition (2-5-3) with
It is fixedly connected inside reaction chamber (2-5)；The water outlet (2-5-4) is located at reaction chamber (2-5) top side, water outlet (2-5-
4) it is welded and fixed with outlet pipe (2-7).
7. a kind of residents in rural community agent-feeding treatment device according to claim 6, which is characterized in that the collection air column
(2-5-6) includes：Gas outlet (2-5-6-1), catalyst jet pipe (2-5-6-2), steam jet (2-5-6-3), organic matter absorption
Material (2-5-6-4), water discharge spout (2-5-6-5) collect air column partition (2-5-6-6), air inlet (2-5-6-7), detection hole (2-
5-6-8)；
Positioned at the gas outlet (2-5-6-1) on top, uncovered structure, treated, and gas is discharged from gas outlet (2-5-6-1)；It is described
Catalyst jet pipe (2-5-6-2) is located at the lower part gas outlet (2-5-6-1), the two spacing 20cm~40cm, catalyst jet pipe (2-5-
6-2) top is equipped with valve, and valve and supervisor connect, and supervisor lower part connects multiple branch pipes, and the quantity of branch pipe is 2~8, branch pipe
End be equipped with spray head, spray head by catalyst spray into collection air column (2-5-6) in, catalyst promote gas in organic matter degradation；
The steam jet (2-5-6-3) is located at the lower part catalyst jet pipe (2-5-6-2), the two spacing 20cm~40cm, steam jet
(2-5-6-3) circular hollow structure, steam jet (2-5-6-3) and external steam supervisor connect, and main steam header is equipped with valve, ring
The shape steam jet lower part (2-5-6-3) is equipped with lotus spray-head, and the two communicates, and lotus spray-head sprays high-temperature steam, and high-temperature steam promotees
It is reacted into catalyst with organic matter；The organic matter adsorbent material (2-5-6-4) is located at the lower part steam jet (2-5-6-3), and two
Person spacing 20cm~40cm, organic matter adsorbent material (2-5-6-4) cellular porous reticular structure, organic matter adsorbent material (2-
It 5-6-4) is laid out for multilayer, interlamellar spacing 2cm~4cm, organic matter adsorbent material (2-5-6-4) adsorbs organic matter in exhaust gas；It is described
Collect air column partition (2-5-6-6) and be located at collection air column (2-5-6) middle part and bottom, quantity is 2, collects air column partition (2-5-6-
6) stainless steel material, surface are equipped with a large amount of through-hole, and the collection air column partition side (2-5-6-6) is equipped with water discharge spout (2-5-6-5),
For condensed water, excessive catalyst to be collected reprocessing；The collection air column bottom (2-5-6) is equipped with air inlet (2-5-6-7), gives up
Gas enters from there；Collect and be equipped with detection hole (2-5-6-8) in the middle part of air column (2-5-6), is used for overhaul of the equipments.
8. a kind of residents in rural community agent-feeding treatment device according to claim 7, which is characterized in that the partition (2-
It 5-3) is formed by high molecular material pressing mold, the constituent of partition (2-5-3) is as follows：
According to parts by weight, 19~89 parts of benzoic acid of 4- (3- formoxyl -1H- indoles -5- base), 4- (2- (amino methyl) -4- nitre
Base phenyl) 129~206 parts of piperazine -1- carboxylic acid tert-butyl ester, 2- cyano -2- (1,2- dihydro -2- Yang Dai quinoxaline -3- base) acetic acid
67~147 parts of ethyl ester, 140~180 parts of methyl acetate of 2- [4- (2- acetyl bromide) -3- methylphenoxy], 3- (5- formoxyl furan
Mutter -2- base) 78~176 parts of -4- methyl benzoic acid, [2- [2- (2,5- dihydro -2,5- dioxo -1H- pyrroles -1- base) ethoxy
Base] ethyl] carbamic acid 1,221~296 parts of 1- dimethylethyl esters, concentration is 5- [(the chloro- 1H- pyrrole of 4- of 57ppm~87ppm
Azoles -1- base) methyl] 155~243 parts of -2- formic acid, 37~80 parts of propionic acid of 3- (1,3,5- trimethyl -1H- pyrazoles -4- base), N-
[2- [4- [(methyl sulphonyl) amino] phenyl] ethyl] carbamic acid 1,127~188 parts of 1- dimethylethyl esters, crosslinking agent 129
~196 parts, 221~334 parts of carboxylate methyl ester of -1H- pyrazoles -5- of -4- nitro of 1- ((ethoxy carbonyl) methyl), 3- (5- acetyl group -
2- thiophene) 218~281 parts of methyl benzoate, 2- (n- methyl-1 H- pyrazoles -1- carboxylic acid amides) ethyl methylcarbamic acid tert-butyl ester
87~169 parts；
The crosslinking agent is 4- (4- hydroxyphenoxy) ethyl butyrate, 3,4- dihydroxypiperdine -1- benzyl carboxylate, 2- (3- amyl)
Any one in dimethyl malenate.
9. a kind of residents in rural community agent-feeding treatment device according to claim 8, which is characterized in that the partition (2-
It 5-3) is formed by high molecular material pressing mold, the manufacturing process of partition (2-5-3) comprises the steps of：
Step 1：2755~3655 parts of ultrapure water that conductivity is 5.33 μ of μ S/cm~8.23 S/cm, starting are added in a kettle
Blender in reaction kettle, revolving speed are 76rpm~131rpm, start heat pump, reactor temperature is made to rise to 77 DEG C~129
℃；Sequentially add 4- (3- formoxyl -1H- indoles -5- base) benzoic acid, 4- (2- (amino methyl) -4- nitrobenzophenone) piperazine -1-
Carboxylic acid tert-butyl ester, 2- cyano -2- (1,2- dihydro -2- Yang Dai quinoxaline -3- base) ethyl acetate, stirring and adjusting pH value is 5.8
~7.7, agitator speed is adjusted to 141rpm~233rpm, temperature is 115 DEG C~169 DEG C, is chemically reacted 21~33 hours；
Step 2：Take 2- [4- (2- acetyl bromide) -3- methylphenoxy] methyl acetate, 3- (5- formylfuran -2- base) -4-
Methyl benzoic acid is crushed, and powder diameter is 1050~1250 mesh；[2- [2- (2,5- dihydro -2,5- dioxo -1H- is added
Pyrroles -1- base) ethyoxyl] ethyl] carbamic acid 1,1- dimethylethyl esters be uniformly mixed, be laid in pallet, tiling with a thickness of
29mm~45mm uses the alpha ray irradiation 135~225 that dosage is 6.9MeV~9.1MeV for 8.9kGy~12.8kGy, energy
Minute and the same dose of β x ray irradiation xs 135~225 minutes；
Step 3：The mixed-powder handled through step 2 is added in 5- [(the chloro- 1H- pyrazol-1-yl of 4-) methyl] -2- formic acid, is added
Enter reaction kettle, agitator speed is 137rpm~182rpm, and temperature is 132 DEG C~201 DEG C, and booster air pump makes the pressure of reaction kettle
Reach 1.03MPa~2.27MPa, keeps this state response 15~27 hours；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure
1.14MPa~1.81MPa, heat preservation stand 17~25 hours；Agitator speed is promoted to 221rpm~269rpm, simultaneous reactions kettle
Pressure release is to 0MPa；Sequentially add 3- (1,3,5- trimethyl -1H- pyrazoles -4- base) propionic acid, N- [2- [4- [(methyl sulphonyl) ammonia
Base] phenyl] ethyl] carbamic acid 1, after 1- dimethylethyl esters are completely dissolved, crosslinking agent is added and is stirred, heat preservation standing 19~
29 hours；
Step 4：When agitator speed is 233rpm~298rpm, 1- ((ethoxy carbonyl) methyl) -4- nitro-is sequentially added
1H- pyrazoles -5- carboxylate methyl ester, 3- (5- acetyl group -2- thiophene) methyl benzoate and 2- (n- methyl-1 H- pyrazoles -1- carboxylic acid amides)
The ethyl methylcarbamic acid tert-butyl ester promotes reactor pressure, reaches 2.60MPa~4.1MPa, and temperature is 188 DEG C~
253 DEG C, polymerization reaction 25~35 hours；Reacting kettle inner pressure is down to 0MPa after the reaction was completed, is cooled to 29 DEG C~33 DEG C, out
Material, entering molding press can be prepared by partition (2-5-3).
10. a kind of working method of residents in rural community agent-feeding treatment device, which is characterized in that this method includes following step
Suddenly：
Step 1：In rubbish medicine mixing device 21, rubbish to be processed is entered by feed hopper (21-5), and pulverization roller (21-6) exists
It crushes and rubbish is crushed under the drive of motor (21-4), dispersion plate (21-8), which will grind up the refuse, carries out homogeneous, dispersion, passes through
Separating sieve (21-3) and blanking amount controller (21-12) control blanking velocity under the premise of, fine powder falls into blanking slideway (21-
13) enter mixing chamber (21-15)；Can not fragmenting bulk fragmenting bulk will be unable to from can not crush by horizontal push plate (21-10)
Bulk exports (21-16) discharge；Rubbish fine powder is mixed in mixing chamber (21-15) with the medicament from chemicals dosing plant (21-14),
Under the stirring action of auger (21-2), realize that the homogeneous of medicament and rubbish fine powder, final rubbish are discharged from discharge port (21-1), into
Enter squeezing device for solid waste (22)；Water of compaction comb (21-17) outside water of compaction is discharged；The water of compaction of discharge enters cesspool (1)；
Step 2：At chemicals dosing plant (21-14), medicament is flowed into from drug-feeding tube (21-14-1), in chemicals dosing plant (21-14) shell
Portion, agitating shaft (21-14-5) carry out mixing homogeneous to medicament by internal impeller, while under the action of DC electric field, removal
Polar substances, treated, and medicament is finally discharged from drug discharging tube (21-14-3)；Operator is right by peep hole (21-14-2)
Agent-feeding treatment process is monitored；
Step 3：In squeezing device for solid waste (22), rubbish enters from extruder loading hopper (22-1), is squeezing capstan winch (22-2)
Under the combination of extrusion effect of counter-force pallet (22-3), moisture in rubbish is squeezed out, expressed water is flowed from expressed water comb (22-4)
Out, into squeezing in water collecting tank (22-6), rubbish continues to fall, and through squeezing capstan winch (22-2) and counter-force supporting plate (22-7)
Combination of extrusion effect, again extrusion dehydration, water of compaction are discharged from lower compression water comb (22-9), and dry rubbish is from garbage emission mouth
(22-8) discharge；When equipment for washing, clear water is flowed out from sluicing pipe (22-5), implements to clean to equipment；
Step 4：In water of compaction after-treatment system, staff puts water of compaction to cesspool (1), and passes through control cabinet (10)
Sewage pump (2-3) starting is controlled, treatment sewage is delivered in reaction tower (2)；After reaction tower (2) processing, sewage is logical
It crosses outlet pipe (2-7) and enters aerobic tank (7) into anaerobic pond (3), then by drainage tube (4), be finally expelled to after the completion of processing
Designated position；
Step 5：In reaction tower (2), sewage enter reaction tower (2) it is interior when, sewage pass through isocon (2-5-1) and spray head (2-
It 5-2) enters in reaction chamber (2-5), is chemically reacted by anaerobic mud bed effect, while generating bulk gas；In dirt
During water reacts, the gas of generation passes through the effect of aspiration pump (2-1), reaches gas chamber (2-5- by collection air column (2-5-6)
5) internal, filter vat (2-2) inside is entered using tracheae (2-6), is discharged finally by exhaust pipe (2-8)；
Step 6：In collection air column (2-5-6), exhaust gas enters from air inlet (2-5-6-7), in multilayer organic matter adsorbent material (2-5-
6-4) under suction-operated, the organic matter in removing exhaust gas is removed, while with organic matter adsorbent material (2-5-6-4) for carrier, in steam
Under the high-temperature steam facilitation that jet pipe (2-5-6-3) sprays, catalyst that exhaust gas and catalyst jet pipe (2-5-6-2) spray into
Row reacts, organic matter in gas of degrading；Condensed water and extra catalyst are discharged from the water of collection side air column partition (2-5-6-6)
It manages (2-5-6-5) and collects reuse；Treated, and gas is discharged from top gas outlet (2-5-6-1)；
Step 7：In water of compaction after-treatment system, when sewage enter anaerobic pond (3) it is internal when, be now placed in anaerobic pond (3) top
Blender (9) start under the manipulation of operator, by sewage stir acceleration its purification；When sewage enter it is aerobic
When pond (7) is internal, it is located at the content of aerobic tank (7) internal oxygen content sensor real-time monitoring aerobic tank (7) internal oxygen,
When oxygen content is lower than its setting value, oxygen content sensor generates electric signal transmission to control cabinet (10), control cabinet (10)
Air blower (8) starting is controlled, oxygen injection aerobic tank (7) is internal, guarantee that aerobic tank (7) internal oxygen stable content is being set
Near.
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| CN201810809811.4A CN108911396A (en) | 2018-07-23 | 2018-07-23 | A kind of residents in rural community agent-feeding treatment device |
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|---|---|---|---|
| CN201810809811.4A CN108911396A (en) | 2018-07-23 | 2018-07-23 | A kind of residents in rural community agent-feeding treatment device |
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| US4191643A (en) * | 1977-02-25 | 1980-03-04 | Gebruder Weiss K.G. | Method for the mechanical preparation of organic wastes in a biological digestion process |
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| CN206276278U (en) * | 2016-10-31 | 2017-06-27 | 四川乐根水处理设备有限公司 | One kind stirring chemicals dosing plant |
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| CN107188337A (en) * | 2017-07-07 | 2017-09-22 | 冷冰 | A kind of sewage is intelligently classified processing equipment |
| CN107827272A (en) * | 2017-11-03 | 2018-03-23 | 邱杨舒 | A kind of full-automatic sewage processing system |
| CN207238198U (en) * | 2017-07-31 | 2018-04-17 | 新昌县甄派农业发展有限公司 | A kind of construction waste bricks breaker |
| CN108057480A (en) * | 2018-01-19 | 2018-05-22 | 余成鹏 | A kind of construction material crushing and processing device of Multistage damping |
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2018
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4191643A (en) * | 1977-02-25 | 1980-03-04 | Gebruder Weiss K.G. | Method for the mechanical preparation of organic wastes in a biological digestion process |
| CN106630108A (en) * | 2016-10-31 | 2017-05-10 | 浙江大学苏州工业技术研究院 | Wastewater decolorizing device with rotating releaser and decolorizing method |
| CN206276278U (en) * | 2016-10-31 | 2017-06-27 | 四川乐根水处理设备有限公司 | One kind stirring chemicals dosing plant |
| CN107162327A (en) * | 2017-06-05 | 2017-09-15 | 浙江水利水电学院 | A kind of method of use microorganism treating sewage |
| CN107188337A (en) * | 2017-07-07 | 2017-09-22 | 冷冰 | A kind of sewage is intelligently classified processing equipment |
| CN207238198U (en) * | 2017-07-31 | 2018-04-17 | 新昌县甄派农业发展有限公司 | A kind of construction waste bricks breaker |
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Application publication date: 20181130 |