CN206359431U - A kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution - Google Patents
A kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution Download PDFInfo
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- CN206359431U CN206359431U CN201621395569.3U CN201621395569U CN206359431U CN 206359431 U CN206359431 U CN 206359431U CN 201621395569 U CN201621395569 U CN 201621395569U CN 206359431 U CN206359431 U CN 206359431U
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- slag
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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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
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Abstract
A kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution disclosed in the utility model, including：Animal fecal pollution tank, centrifugate collecting tank, centrifugation slag collecting tank, cooling condensate-water polishing groove, hydrolytic decomposition pot, grinder, centrifuge, filter, evaporation and concentration unit, liquid fertilizer metering packaging machine and solid fertile metering packaging machine.The utility model overcomes producing methane through anaerobic fermentation and the secondary pollution of biogas residue and process unit complexity, investment height, biogas slurry recycling are difficult, the problems such as high-concentration sewage processing need to being carried out, the secondary pollutions such as stench and mosquitos and flies are not produced in processing procedure of the present utility model, recycling product is water-soluble liquid and water-soluble solid fertilizer, it is good with fertilizer efficiency, added value is high, and water-fertilizer integral can be achieved.The utility model has processing time short (6 hours), and small volume, floor space is few, the advantage of low cost.In production process, the closed circulation processing of separation slag is not discharged, and is cooled down condensate recoverable, is realized zero-emission.
Description
Technical field
The utility model is related to the fertile technical field of environment protection equipment of system of reclaiming organic waste processing, more particularly to a kind of
Utilize the complexes of the aquatic production organic water-soluble fertilizer of Animal fecal pollution.
Background technology
The livestock liquid dung of traditional Large-scale pig farm and cowboying factory includes pig (ox) excrement, urine and flushing water etc., the excrement of mixing,
Urinate water water content it is very big, its be up to 90% and more than.Processing method traditional at present is direct anaerobic fermentation, and its product is natural pond
Gas, biogas residue and biogas slurry, it is therefore desirable to first handled through separation of solid and liquid, solids animal dung are fermented to compost, and liquid dung is through anaerobism
Fermentation produces biogas, biogas slurry and a small amount of biogas residue, wherein, biogas is purified to do the energy, and biogas slurry is handled by high concentrated organic wastewater,
Qualified discharge, also there is what is directly applied, and amount of application control is bad to cause crop excessive growth trophic disturbance.This processing method is present
The problem of be that processing time is long, device volume is huge, and floor space is big, and cost is high.Stench mosquitos and flies can be produced in processing procedure to post
Raw secondary pollution.Biogas does the energy, and the fertilizer efficiency of biogas residue compost is poor, and economic benefit is also poor.Biogas slurry is using at high-concentration sewage
Long flow path is managed, complex process, processing cost is high.Biogas slurry amount is big as directly applied, and causes corps nutrient body excessive growth etc. is many to ask
Topic.
Utility model content
Technical problem to be solved in the utility model：There is processing time to Animal fecal pollution method for treating water for tradition
It is long, device volume is huge, floor space is big, cost is high, produce the parasitic secondary pollution problems of stench mosquitos and flies in processing procedure,
And provide that a kind of processing time is short, device volume is small, floor space is small, cost is low, avoid producing stench in processing procedure
The complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution of the parasitic secondary pollution of mosquitos and flies.
The technical problem that the utility model is solved can be realized using following technical scheme：
A kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution, including：
There is the one Animal fecal pollution tank for collecting Animal fecal pollution water, the Animal fecal pollution tank Animal fecal pollution water to go out
Material mouth and an Animal fecal pollution water discharging opening；
One hydrolytic decomposition pot, the hydrolytic decomposition pot has a first material import, a second material import and a Discharge outlet, described
The first material import of hydrolytic decomposition pot is connected by delivery pump with the Animal fecal pollution water discharging opening of the Animal fecal pollution tank, for making
Obtain the biochemical hydrolysis of Animal fecal pollution aquatic products；
There is one grinder, the grinder material inlet and a grinding material to export, and the material of the grinder enters
Mouth is connected with the Discharge outlet of the hydrolytic decomposition pot；
One centrifuge, the centrifuge has a material inlet, a centrifugate leakage fluid dram and a centrifugation slag slag-drip opening, described
The material inlet of centrifuge is connected with the grinding material outlet of the grinder；
There is one centrifugate collecting tank, the centrifugate collecting tank centrifugate import and a centrifugate to export, it is described from
The centrifugate import of heart liquid collecting tank is connected with the centrifugate leakage fluid dram of the centrifuge；
There is one filter, the filter liquor inlet, a filtrate outlet and one to cross sludge outlet, the filtering
The liquor inlet of machine is connected with the centrifugate outlet of the centrifugate collecting tank；
One centrifugation slag collecting tank, the centrifugation slag collecting tank has one first centrifugation slag import, one second centrifugation slag import
With a centrifugation slag outlet, the first centrifugation slag import of the centrifugation slag collecting tank and the centrifugation slag slag-drip opening of the centrifuge connect
Connect, its second centrifugation slag import is connected by the first slag charge pump with the sludge outlet of crossing of the filter, and it is logical that it centrifuges slag outlet
The second slag charge pump is crossed to be connected with the second material import of the hydrolytic decomposition pot；
One is concentrated by evaporation unit, and the evaporation and concentration unit has a liquor inlet, evaporation concentrated solution outlet and one cold
But water out is condensed, the liquor inlet of the evaporation and concentration unit is connected by the filtrate outlet of feed pump and the filter
Connect；
One liquid fertilizer metering packaging machine and/or a solid fertile metering packaging machine, the liquid feeding end of the liquid fertilizer metering packaging machine and institute
State the evaporation concentrated solution outlet connection for being concentrated by evaporation unit, the feed end of the solid fertile metering packaging machine by drying machine with it is described
It is concentrated by evaporation the evaporation concentrated solution outlet connection of unit；And
One cooling condensate-water polishing groove, the recovery import of the cooling condensate-water polishing groove and the evaporation and concentration unit
Cooling condenses water out connection.
In a preferred embodiment of the present utility model, the delivery pump is screw pump.
In a preferred embodiment of the present utility model, the drying machine is spray dryer.
As a result of technical scheme as above, the beneficial effects of the utility model are：The utility model, which overcomes, to be detested
Aerobe fermentation produces biogas and process unit complexity, investment height, the biogas slurry recycling of biogas residue are difficult, need to carry out high-concentration sewage processing
The secondary pollutions such as stench and mosquitos and flies are not produced in problem, processing procedure of the present utility model, recycling product is water-soluble liquid
With the solid fertilizer of water solubility, can only production one of which or concentrate be divided into two can be good with fertilizer efficiency while produce two kinds, add
Value is high, and water-fertilizer integral can be achieved.Meanwhile, the utility model has processing time short (6 hours), and small volume, floor space is few,
The advantage of low cost.Condensate recoverable is cooled down, waste discharge, does not realize zero-emission.Device of the present utility model is also
It is suitable for activated sludge and the industrial organic waste residues by raw material of animals and plants, such as exemplary food waste, Chinese medicine slag, waster paper slag, chaff
Aldehyde slag, Klinit dregs, alcohol slag etc..
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the accompanying drawing used required in description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, is not paying the premise of creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model.
Embodiment
In order that technological means, creation characteristic, reached purpose and effect that the utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and the utility model is expanded on further.
Referring to Fig. 1, what is provided in figure is a kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution, including raises
Brid guano urine tank 110, centrifugate collecting tank 120, centrifugation slag collecting tank 130, cooling condensate-water polishing groove 140, hydrolytic decomposition pot 200,
Grinder 300, centrifuge 400, filter 500, evaporation and concentration unit 600, liquid fertilizer metering packaging machine 700 and solid fertilizer metering bag
Installation 800.
Animal fecal pollution tank 110 is used to collect Animal fecal pollution water, and Animal fecal pollution tank 110 is fed with an Animal fecal pollution water
Mouth and an Animal fecal pollution water discharging opening 111.
Hydrolytic decomposition pot 200 has a material inlet 210, a material inlet 220 and a Discharge outlet 230, the thing of hydrolytic decomposition pot 200
Material import 210 is connected by delivery pump 10 with the Animal fecal pollution water discharging opening 111 of Animal fecal pollution tank 110, for causing livestock and poultry
Fecaluria water can form small molecule carbohydrate, peptides and organic acid after producing hydrolysis, hydrolysis.In the present embodiment,
Delivery pump 10, which is preferably selected, uses screw pump, screw pump have do not formed during pumped (conveying) medium vortex, to medium it is sticky it is insensitive, can
The advantages of transfer of highly viscous medium.
Grinder 300 has a material inlet 310 and grinding material outlet 320, the material inlet and water of grinder 300
The Discharge outlet 230 of solution tank 200 is connected.The effect of grinder 300 is can by the insoluble colloid that is partially converted into by mechanical lapping
Molten part.
Centrifuge 400 has a material inlet 410, a centrifugate leakage fluid dram 420 and a centrifugation slag slag-drip opening 430, described
The material inlet of centrifuge is connected with the grinding material outlet of the grinder.Centrifuge 400 carries out separation of solid and liquid, and centrifugation slag leads to
Cross slag charge pump and return again to hydrolytic decomposition pot and reprocessed, realize that closed circulation is handled.
Centrifugate collecting tank 120 has a centrifugate import 121 and centrifugate outlet 122, centrifugate collecting tank 120
Centrifugate import 121 is connected with the centrifugate leakage fluid dram 420 of centrifuge 400.
There is filter 500 liquor inlet 510, a filtrate outlet 520 and one to cross sludge outlet 530, filter 500
The centrifugate outlet 122 of liquor inlet 510 and centrifugate collecting tank 120 be connected.
Centrifuging slag collecting tank 130, there is a centrifugation slag import 131, one to centrifuge the centrifugation slag outlet 133 of slag import 132 and one,
The centrifugation slag import 131 of centrifugation slag collecting tank 130 is connected with the centrifugation slag slag-drip opening 430 of centrifuge 400, and it centrifuges slag import
132 are connected by slag charge pump 20 with the sludge outlet 530 of crossing of filter 500, and it centrifuges slag outlet 133 and passes through slag charge pump 30 and water
The material inlet 220 of solution tank 200 is connected.Closed circulation processing can be carried out, not waste discharge.
Being concentrated by evaporation unit 600, there is a liquor inlet 610, the cooling condensate of evaporation concentrated solution outlet 620 and one to go out
Mouth 640, the liquor inlet 610 for being concentrated by evaporation unit 600 is connected by feed pump 40 with the filtrate outlet 520 of filter 500.
The concentration that filtered fluid is concentrated to required for the water-soluble liquid fertilizer of system by unit 600 is concentrated by evaporation, or required for spray dryer
Concentration.
Evaporation concentrated solution outlet 620 of the liquid feeding end of liquid fertilizer metering packaging machine 700 with being concentrated by evaporation unit 600 is connected, liquid
Product packaged by fertile metering packaging machine 700 is water-soluble liquid fertilizer.Gu the feed end of fertile metering packaging machine 800 passes through drying machine
The 900 evaporation concentrated solution outlet 620 with being concentrated by evaporation unit 600 is connected.In the present embodiment, drying machine 900 is spray drying
Machine.Gu the product packaged by fertile metering packaging machine 800 is the solid fertilizer of water-soluble powder shape.
Cooling of the import 141 with being concentrated by evaporation unit 600 of reclaiming for cooling down condensate-water polishing groove 140 condenses water out 640
Connection, cooling condensate-water polishing groove 140 can be recycled to the cooling condensate produced by being concentrated by evaporation unit 600, real
Existing zero-emission.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry is it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the utility model spirit and scope are not departed from, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed the utility model.The utility model
Claimed scope is by appended claims and its equivalent thereof.
Claims (3)
1. a kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution, it is characterised in that including：
The one Animal fecal pollution tank for collecting Animal fecal pollution water, the Animal fecal pollution tank has an Animal fecal pollution water discharging opening
With an Animal fecal pollution water discharging opening；
One hydrolytic decomposition pot, the hydrolytic decomposition pot has a first material import, a second material import and a Discharge outlet, the hydrolysis
The first material import of tank is connected by delivery pump with the Animal fecal pollution water discharging opening of the Animal fecal pollution tank, for causing poultry
Brid guano urinates the biochemical hydrolysis of aquatic products；
There is one grinder, the grinder material inlet and a grinding material to export, the material inlet of the grinder with
The Discharge outlet connection of the hydrolytic decomposition pot；
One centrifuge, the centrifuge has a material inlet, a centrifugate leakage fluid dram and a centrifugation slag slag-drip opening, the centrifugation
The material inlet of machine is connected with the grinding material outlet of the grinder；
There is one centrifugate collecting tank, the centrifugate collecting tank centrifugate import and a centrifugate to export, the centrifugate
The centrifugate import of collecting tank is connected with the centrifugate leakage fluid dram of the centrifuge；
There is one filter, the filter liquor inlet, a filtrate outlet and one to cross sludge outlet, the filter
Liquor inlet is connected with the centrifugate outlet of the centrifugate collecting tank；
One centrifugation slag collecting tank, the centrifugation slag collecting tank has one first centrifugation slag import, one second centrifugation slag import and one
Slag outlet is centrifuged, the first centrifugation slag import of the centrifugation slag collecting tank is connected with the centrifugation slag slag-drip opening of the centrifuge, its
Second centrifugation slag import is connected by the first slag charge pump with the sludge outlet of crossing of the filter, and it centrifuges slag outlet and passes through second
Slag charge pump is connected with the second material import of the hydrolytic decomposition pot；
One is concentrated by evaporation unit, and the evaporation and concentration unit has a liquor inlet, evaporation concentrated solution outlet and a cooling solidifying
Outlet is born water, the liquor inlet for being concentrated by evaporation unit is connected by feed pump with the filtrate outlet of the filter；
One liquid fertilizer metering packaging machine and/or a solid fertile metering packaging machine, the liquid feeding end of the liquid fertilizer metering packaging machine steam with described
The evaporation concentrated solution outlet connection of hair concentration unit, the feed end of the solid fertile metering packaging machine passes through drying machine and the evaporation
Concentrate the evaporation concentrated solution outlet connection of unit；And
One cooling condensate-water polishing groove, the recovery import of the cooling condensate-water polishing groove and the cooling of the evaporation and concentration unit
Condense water out connection.
2. the complexes of the aquatic production organic water-soluble fertilizer of Animal fecal pollution are utilized as claimed in claim 1, it is characterised in that described
Delivery pump is screw pump.
3. the complexes of the aquatic production organic water-soluble fertilizer of Animal fecal pollution are utilized as claimed in claim 1, it is characterised in that described
Drying machine is spray dryer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621395569.3U CN206359431U (en) | 2016-12-19 | 2016-12-19 | A kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621395569.3U CN206359431U (en) | 2016-12-19 | 2016-12-19 | A kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution |
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| Publication Number | Publication Date |
|---|---|
| CN206359431U true CN206359431U (en) | 2017-07-28 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621395569.3U Expired - Fee Related CN206359431U (en) | 2016-12-19 | 2016-12-19 | A kind of complexes of the aquatic production organic water-soluble fertilizer of utilization Animal fecal pollution |
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| Country | Link |
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| CN (1) | CN206359431U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106588136A (en) * | 2016-12-19 | 2017-04-26 | 宁波宝力农环境技术开发有限公司 | Complete equipment producing organic water-soluble fertilizer by means of livestock excrement and urine water |
-
2016
- 2016-12-19 CN CN201621395569.3U patent/CN206359431U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106588136A (en) * | 2016-12-19 | 2017-04-26 | 宁波宝力农环境技术开发有限公司 | Complete equipment producing organic water-soluble fertilizer by means of livestock excrement and urine water |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170728 Termination date: 20211219 |