CN106583424A - Resourceful treatment process for domestic organic waste - Google Patents
Resourceful treatment process for domestic organic waste Download PDFInfo
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- CN106583424A CN106583424A CN201611246741.3A CN201611246741A CN106583424A CN 106583424 A CN106583424 A CN 106583424A CN 201611246741 A CN201611246741 A CN 201611246741A CN 106583424 A CN106583424 A CN 106583424A
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- 239000010815 organic waste Substances 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 27
- 230000008569 process Effects 0.000 title claims abstract description 23
- 239000007788 liquid Substances 0.000 claims abstract description 57
- 238000000855 fermentation Methods 0.000 claims abstract description 37
- 230000004151 fermentation Effects 0.000 claims abstract description 37
- 238000010564 aerobic fermentation Methods 0.000 claims abstract description 27
- 239000003337 fertilizer Substances 0.000 claims abstract description 21
- 239000000463 material Substances 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 15
- 239000003895 organic fertilizer Substances 0.000 claims abstract description 15
- 238000000926 separation method Methods 0.000 claims abstract description 13
- 150000002500 ions Chemical class 0.000 claims abstract description 8
- 229910052751 metal Inorganic materials 0.000 claims abstract description 7
- 239000002184 metal Substances 0.000 claims abstract description 7
- 239000007787 solid Substances 0.000 claims abstract description 6
- 150000001768 cations Chemical class 0.000 claims abstract description 4
- 239000010813 municipal solid waste Substances 0.000 claims description 67
- 239000002361 compost Substances 0.000 claims description 13
- 239000002351 wastewater Substances 0.000 claims description 13
- 230000009194 climbing Effects 0.000 claims description 12
- 238000004064 recycling Methods 0.000 claims description 12
- 238000005273 aeration Methods 0.000 claims description 9
- 239000002068 microbial inoculum Substances 0.000 claims description 9
- 238000004062 sedimentation Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 244000005700 microbiome Species 0.000 claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 238000001514 detection method Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 235000015097 nutrients Nutrition 0.000 claims description 4
- 239000000047 product Substances 0.000 claims description 4
- 239000003225 biodiesel Substances 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 230000000050 nutritive effect Effects 0.000 claims description 3
- 229910052573 porcelain Inorganic materials 0.000 claims description 3
- 238000001226 reprecipitation Methods 0.000 claims description 3
- 238000007873 sieving Methods 0.000 claims description 3
- 239000010802 sludge Substances 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 239000006228 supernatant Substances 0.000 claims description 3
- 239000002912 waste gas Substances 0.000 claims description 3
- 241000628997 Flos Species 0.000 claims description 2
- 238000004332 deodorization Methods 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims description 2
- 230000018044 dehydration Effects 0.000 abstract 3
- 238000006297 dehydration reaction Methods 0.000 abstract 3
- 238000007599 discharging Methods 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 239000002689 soil Substances 0.000 description 5
- 238000012545 processing Methods 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 210000003608 fece Anatomy 0.000 description 2
- 230000005571 horizontal transmission Effects 0.000 description 2
- 238000003973 irrigation Methods 0.000 description 2
- 230000002262 irrigation Effects 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000003900 soil pollution Methods 0.000 description 2
- 239000010421 standard material Substances 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000033558 biomineral tissue development Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000003864 humus Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 230000007269 microbial metabolism Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 150000003112 potassium compounds Chemical class 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- 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 NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a resourceful treatment process for domestic organic waste. The resourceful treatment process for the domestic organic waste comprises the steps that firstly solid-liquid separation is performed; secondly, inorganic matter is sorted out and gotten rid of; thirdly, oil stains and metal cations are removed by means of spraying washing; fourthly, smashing dehydration and squeezing dehydration are performed; fifthly, high temperature aerobic fermentation is performed; sixthly, natural secondary biological fermentation is performed; seventhly, materials are screened; eighthly, water discharged from a liquid outlet below a sorting table and a water discharging port under a squeezing dehydration machine is subjected to oil-water separation; ninthly, heavy metal ions in organic waste water are removed, and then aerobic fermentation is performed so that fermented liquid can be obtained; tenthly, the fermented liquid is subjected to high temperature concentration; eleventhly, the concentrated fermented liquid is detected; and twelfthly, the fermented liquid reaching the standard is matched. After the organic waste is treated through the resourceful treatment process for the domestic organic waste, solid organic fertilizer, organic liquid fertilizer and oil are obtained, the problem that heavy metal exceeding the standard exists in the fertilizer is solved, and the utilization rate of organic waste resources is increased to 95% or above.
Description
Technical field
The present invention relates to changing food waste handling process, more particularly to a kind of domestic organic garbage recycling treatment process.
Background technology
With the continuous improvement of exhausting level, the fast development of industrial and agricultural production level, town and country organic waste is (wherein
Organic waste, agricultural stalk garbage including people and cultivation fowl and animal excrement etc.) discharge capacity increasingly increase.According to statistics, in
The annual municipal domestic organic refuse yield of state is more than 3.1 hundred million tons；Annual agricultural stalk yield more than 6.5 hundred million tons, annual animal dung
Just more than 2,600,000,000 tons, China has become organic waste output country maximum in the world to yield.At present, domestic and international organic solid
Waste treatment mainly has 3 kinds：Landfill, burning and biological treatment.Land landfill can cause the pollution of soil and high soil
Ground contamination restoration harness expense, burns not only high cost, and the exhaust emissions of castoff burning technique can produce dirt to environment
Dye, these processing methods cause serious problem of environmental pollution while organic waste is processed.Although organic waste has
The harm of pollution, but it simultaneously again can be as important resource by recycling.Not only containing a large amount of in organic waste
The nutrient such as organic matter, N P and K, also containing amount and the trace element in other such as more calcium, agricultural fertilizer can be processed into,
And feces are used as fertilizer Chinese long-standing.Organic waste is agricultural can not only to solve pollution problem, and right after applying
Soil physics, chemistry and biological character have certain improving effect.Therefore, the agricultural also field of organic waste for China
It is the most feasible, the most suitable disposal method, reclaiming organic waste is using the development also complied with Chinese current national conditions
Trend.
Aerobic compost is to make mineralization Organic substance, humification and innoxious and become rotten by fermentation under microbial action
The process of ripe fertilizer, can generate available nitrogen, phosphorus, the potassium compound that can be absorbed and used by plants in a large number, and can also synthesize
New macromolecule organic --- humus, it is the important component of organic fertilizer, is also the important substance for constituting soil fertility.
Organic waste is processed by aerobic compost and organic fertilizer is produced, is the weight that organic waste harmless treatment and Fertilizer Transformed are utilized
Want approach.Additionally, also occurring in that on market using special microbial bacterial agent is come special fermentation process organic waste and production has
Machine fertilizer, this handling process is significantly improved in Traditional compost mode：Risen using aerobic fermentation equipment and increase rubbish
The quantity of beginning microorganism is accelerating the fermentation of material, final output fertilizer.
At present, all there is Organic substance decomposition in the processing mode that either aerobic compost still carries out aerobic fermentation using equipment
Slowly, long processing period or fermentation period is short but material process not exclusively, the low problem of product fertilizer efficiency.Meanwhile, existing rubbish
Rubbish handling process generally ignores the secondary pollution problem that by-product in garbage processing procedure (waste gas, waste water) is caused to environment.
Further, since there is the phenomenon of heavy metal severe overweight in the house refuse of each department at present, and existing garbage treating process
In ignore substantially heavy metal presence hazardness, directly results in heavy metal severe overweight in output material, final fertilizer is again
Cause the transfer of water and soil pollution, heavy metal that serious pollution is caused to environment again using in soil, more endanger our people
The health of class.
The content of the invention
For the problems referred to above, the invention provides a kind of organic waste recycling treatment process, organic waste is carried out it is solid,
Liquid separating treatment, different material difference resource, improves organic waste resource degree, during reduction handling process
Emission and the heavy metal ion in solid material and liquid is eliminated respectively realizing at utmost reducing organic garbage treatment work
Pollution problem of the skill to environment.
The technical solution used in the present invention is：
A kind of domestic organic garbage recycling treatment process, comprises the following steps：
(1), domestic organic garbage is poured on realization on the pigeonholes with solid-liquid separator through collecting, measuring hypsokinesis of weighing
Preliminary solid-liquid separation, liquid outlet of the liquid from below pigeonholes is discharged, while manually rejecting on pigeonholes macroscopic
The non-organic thing that porcelain, glass, metal etc. cannot be processed；
(2), the domestic organic garbage after pigeonholes initial gross separation sorting enters horizontal conveying belt, domestic organic garbage
Tiling is taken in horizontal transmission to scatter, can again be sorted and reject the non-organic thing being hidden in domestic organic garbage；
(3), after horizontal conveying belt, into climbing conveyer belt, the top of conveyer belt of climbing is arranged domestic organic garbage
There is spray irrigation device, by the metal cation for being sprayed the oil stain and adhesion that can reduce domestic organic garbage surface,
During domestic organic garbage is delivered up, the free water in domestic organic garbage relies on self gravitation certainly to climbing conveyer belt
Dynamic backflow, the liquid outlet from below pigeonholes is discharged；
(4), domestic organic garbage is transported in pulverizer after conveyer belt of climbing and carries out crushing/dewatering, is lived organic
Rubbish directly falls in the squeezing dewatering machine of lower section after crushing/dewatering, by unnecessary in squeezing removing domestic organic garbage
Moisture, and domestic organic garbage half-dried after squeezing is transported in high-temperature aerobic fermentation chamber, pulverizer and squeezing dewatering machine
The moisture of removing is discharged by the discharge outlet immediately below squeezing dewatering machine；
(5), in high-temperature aerobic fermentation chamber, half-dried domestic organic garbage is organic under the conditions of high-temperature aerobic after squeezing
Rubbish fermentation microbial inoculum fast decoupled ferments；
(6), by domestic organic garbage by fermentation after output object take out from high-temperature aerobic fermentation chamber, be directly stacked at
Natural secondary biofermentation is carried out in compost groove；
(7), the material that natural secondary biofermentation completes to obtain is sieved, the thick material that will be unable to sieve is returned to
Fermented again in high-temperature aerobic fermentation chamber, to sieving after thin material carry out organic fertilizer detection, by detect it is not up to standard
Material is returned to and carry out in compost groove continuation natural secondary biofermentation, and the material to reaching organic fertilizer standard is packed,
Obtain the SOLID ORGANIC fertilizer of finished product；
(8), the moisture that the discharge outlet immediately below the liquid outlet and squeezing dewatering machine below pigeonholes is discharged is admitted to oil
Oil-water separation, isolated oil and organic wastewater are carried out in water separation device, oil can be used to manufacture biodiesel or iundustrial oil；
(9), the isolated organic wastewater of oily-water seperating equipment is sent in sedimentation tank, and a huge sum of money is added in sedimentation tank
Category ion precipitation agent, the heavy metal ion in organic wastewater is deposited in pool bottom sludge, so as to remove organic wastewater in weight
Metal ion, the supernatant in reprecipitation pond is sent in Aeration tank, adds organic waste aerobic fermentation microbial inoculum to enter in Aeration tank
Act charitably aerobe fermentation, obtain fermentation liquid；
(10), fermentation liquid is sent into and carry out in concentration tower high temperature concentration, kill microorganism remaining in fermentation liquid, while steaming
The moisture for sending out unnecessary, concentrates the nutrient substance in fermentation liquid and collects；
(11) take the fermentation liquid after concentration to be detected, fermentation liquid not up to standard is sent in Aeration tank and proceeds to send out
Ferment；
(12) according to the standard of organic liquid fertilizer, proportioning is carried out to fermentation liquid up to standard so as to which nutritive proportion reaches to be had
The standard of machine liquid fertilizer, so as to obtain organic liquid fertilizer.
Preferably, being provided with foul smell floss hole on described high-temperature aerobic fermentation chamber, foul smell is collected simultaneously by blower fan
In sending into emission-control equipment, waste gas safety dumping after emission-control equipment deodorization purification is up to standard.
Preferably, in the step (5) organic refuse fermentation microbial inoculum domestic organic garbage fast decoupled is fermented when
Between be 24-48 hours so that the humidity of domestic organic garbage reduces to less than 40%.
Preferably, in the step (6) output object after natural secondary biofermentation, the humidity of output object is less than
30%, stockpile temperature is less than 40 DEG C in compost groove.
Preferably, the time that organic waste aerobic fermentation microbial inoculum carries out aerobic fermentation in the step (9) is 2-3 days.
After the present invention is processed organic waste, SOLID ORGANIC fertilizer, organic liquid fertilizer and oil are obtained, and solved
There is a problem of exceeded heavy metal in fertilizer, the utilization rate of organic waste resource brought up to into more than 95%, it is to avoid be organic
The water and soil pollution that rubbish is caused in environment, solves that organic waste is innoxious, a recycling difficult problem, while also solving
Modern garbage processing procedure material corruption is smelly, percolate and a series of problems, such as Heavy-metal Polluted Environment.
Description of the drawings
Fig. 1 is the workflow diagram of the present invention.
Specific embodiment
Below by specific embodiment and combine accompanying drawing the present invention is described in further detail.
Embodiment 1
A kind of domestic organic garbage recycling treatment process, comprises the following steps：
(1), domestic organic garbage is poured on realization on the pigeonholes with solid-liquid separator through collecting, measuring hypsokinesis of weighing
Preliminary solid-liquid separation, liquid outlet of the liquid from below pigeonholes is discharged, while manually rejecting on pigeonholes macroscopic
The non-organic thing that porcelain, glass, metal etc. cannot be processed；
(2), the domestic organic garbage after pigeonholes initial gross separation sorting enters horizontal conveying belt, domestic organic garbage
Tiling is taken in horizontal transmission to scatter, can again be sorted and reject the non-organic thing being hidden in domestic organic garbage；
(3), after horizontal conveying belt, into climbing conveyer belt, the top of conveyer belt of climbing is arranged domestic organic garbage
There is spray irrigation device, by the metal cation for being sprayed the oil stain and adhesion that can reduce domestic organic garbage surface,
During domestic organic garbage is delivered up, the free water in domestic organic garbage relies on self gravitation certainly to climbing conveyer belt
Dynamic backflow, the liquid outlet from below pigeonholes is discharged；
(4), domestic organic garbage is transported in pulverizer after conveyer belt of climbing and carries out crushing/dewatering, is lived organic
Rubbish directly falls in the squeezing dewatering machine of lower section after crushing/dewatering, by unnecessary in squeezing removing domestic organic garbage
Moisture, and domestic organic garbage half-dried after squeezing is transported in high-temperature aerobic fermentation chamber, pulverizer and squeezing dewatering machine
The moisture of removing is discharged by the discharge outlet immediately below squeezing dewatering machine；
(5), in high-temperature aerobic fermentation chamber, half-dried domestic organic garbage Jia hundred under the conditions of high-temperature aerobic after squeezing
Row organic refuse fermentation I type microbial inoculums fast decoupled fermented, by the high-temperature aerobic fermentation of 24～48 hours so that the organic rubbish of life
The humidity of rubbish reduces to less than 40%；
(6), by domestic organic garbage by fermentation after output object take out from high-temperature aerobic fermentation chamber, be directly stacked at
Natural secondary biofermentation is carried out in compost groove so that the humidity of output object is less than 30%, stockpile temperature is less than 40 in compost groove
DEG C, natural secondary biofermentation is gone out moisture evaporation unnecessary in output object using the heat that microbial metabolism is produced, while
In natural secondary biological fermentation process, microorganism makes the nutritional labeling in output object reach equilibrium state；
(7), the material that natural secondary biofermentation completes to obtain is sieved, the thick material that will be unable to sieve is returned to
Fermented again in high-temperature aerobic fermentation chamber, to sieving after thin material carry out organic fertilizer detection, by detect it is not up to standard
Material is returned to and carry out in compost groove continuation natural secondary biofermentation, and the material to reaching organic fertilizer standard is packed,
Obtain the SOLID ORGANIC fertilizer of finished product；
(8), the moisture that the discharge outlet immediately below the liquid outlet and squeezing dewatering machine below pigeonholes is discharged is admitted to oil
Oil-water separation, isolated oil and organic wastewater are carried out in water separation device, oil can be used to manufacture biodiesel or iundustrial oil；
(9), the isolated organic wastewater of oily-water seperating equipment is sent in sedimentation tank, and a huge sum of money is added in sedimentation tank
Category ion precipitation agent, the heavy metal ion in organic wastewater is deposited in pool bottom sludge, so as to remove organic wastewater in weight
Metal ion, the supernatant in reprecipitation pond is sent in Aeration tank, and Cambiel organic waste aerobic fermentation is added in Aeration tank
II type microbial inoculums, carry out aerobic fermentation 2-3 days, obtain fermentation liquid；
(10), fermentation liquid is sent into and carry out in concentration tower high temperature concentration, kill microorganism remaining in fermentation liquid, while steaming
The moisture for sending out unnecessary, concentrates the nutrient substance in fermentation liquid and collects；
(11) take the fermentation liquid after concentration to be detected, fermentation liquid not up to standard is sent in Aeration tank and proceeds to send out
Ferment；
(12) according to the standard of organic liquid fertilizer, proportioning is carried out to fermentation liquid up to standard so as to which nutritive proportion reaches to be had
The standard of machine liquid fertilizer, so as to obtain organic liquid fertilizer.
Organic waste is after the PROCESS FOR TREATMENT of the present invention, and the organic fertilizer technical specification for obtaining is as follows：
As can be seen from the above table, after the PROCESS FOR TREATMENT of the present invention, the organic fertilizer for obtaining is complied fully with organic waste
, there is no heavy metal pollution problem in NY525 indexs.
Claims (5)
1. a kind of domestic organic garbage recycling treatment process, it is characterised in that comprise the following steps：
(1), domestic organic garbage through collecting, metering weigh hypsokinesis be poured on the pigeonholes with solid-liquid separator realize it is preliminary
Solid-liquid separation, liquid outlet of the liquid from below pigeonholes is discharged, at the same manually reject on pigeonholes macroscopic porcelain,
The non-organic thing that glass, metal etc. cannot be processed；
(2), the domestic organic garbage after pigeonholes initial gross separation sorting enters horizontal conveying belt, and domestic organic garbage is in water
Flat pass to send and take tiling and scatter, can again be sorted and reject the non-organic thing being hidden in domestic organic garbage；
(3), after horizontal conveying belt, into climbing conveyer belt, the top of conveyer belt of climbing is provided with spray to domestic organic garbage
Flusher is drenched, by the metal cation for being sprayed the oil stain and adhesion that can reduce domestic organic garbage surface, climbing
During domestic organic garbage is delivered up, the free water in domestic organic garbage is returned conveyer belt automatically by self gravitation
Stream, the liquid outlet from below pigeonholes is discharged；
(4), domestic organic garbage is transported in pulverizer after conveyer belt of climbing and carries out crushing/dewatering, domestic organic garbage
During the squeezing dewatering machine of lower section is directly fallen to after crushing/dewatering, by water unnecessary in squeezing removing domestic organic garbage
Point, and domestic organic garbage half-dried after squeezing is transported in high-temperature aerobic fermentation chamber, pulverizer and squeezing dewatering machine are removed
Moisture discharged by the discharge outlet immediately below squeezing dewatering machine；
(5), in high-temperature aerobic fermentation chamber, after squeezing half-dried domestic organic garbage under the conditions of high-temperature aerobic by organic waste
Fermenting agent fast decoupled ferments；
(6), by domestic organic garbage by fermentation after output object take out from high-temperature aerobic fermentation chamber, be directly stacked at compost
Natural secondary biofermentation is carried out in groove；
(7), the material that natural secondary biofermentation completes to obtain is sieved, the thick material that will be unable to sieve returns to high temperature
Fermented again in aerobic fermentation chamber, to sieving after thin material carry out organic fertilizer detection, will detection material not up to standard
Return to and carry out in compost groove continuation natural secondary biofermentation, the material to reaching organic fertilizer standard is packed, obtained
The SOLID ORGANIC fertilizer of finished product；
(8), the moisture that the discharge outlet immediately below the liquid outlet and squeezing dewatering machine below pigeonholes is discharged is admitted to profit point
Oil-water separation, isolated oil and organic wastewater are carried out in device, oil can be used to manufacture biodiesel or iundustrial oil；
(9), the isolated organic wastewater of oily-water seperating equipment is sent in sedimentation tank, and add in sedimentation tank heavy metal from
Sub- precipitant, makes the heavy metal ion in organic wastewater be deposited in pool bottom sludge, so as to remove organic wastewater in heavy metal
Ion, the supernatant in reprecipitation pond is sent in Aeration tank, adds organic waste aerobic fermentation microbial inoculum to enter to act charitably in Aeration tank
Aerobe fermentation, obtains fermentation liquid；
(10), fermentation liquid is sent into and carry out in concentration tower high temperature concentration, kill microorganism remaining in fermentation liquid, while evaporation is more
Remaining moisture, concentrates the nutrient substance in fermentation liquid and collects；
(11) take the fermentation liquid after concentration to be detected, fermentation liquid not up to standard is sent in Aeration tank and proceeds fermentation；
(12) according to the standard of organic liquid fertilizer, proportioning is carried out to fermentation liquid up to standard so as to which nutritive proportion reaches organic liquor
The standard of state fertilizer, so as to obtain organic liquid fertilizer.
2. a kind of domestic organic garbage recycling treatment process according to claim 1, it is characterised in that described high temperature
Foul smell floss hole is provided with aerobic fermentation chamber, foul smell is collected and fed in emission-control equipment by blower fan, waste gas is passed through
Emission-control equipment deodorization purifies rear safety dumping up to standard.
3. a kind of domestic organic garbage recycling treatment process according to claim 1 and 2, it is characterised in that the step
Suddenly the time that organic refuse fermentation microbial inoculum ferments to domestic organic garbage fast decoupled in (5) is 24-48 hours so that life has
The humidity of machine rubbish reduces to less than 40%.
4. a kind of domestic organic garbage recycling treatment process according to claim 3, it is characterised in that the step
(6) after natural secondary biofermentation, the humidity of output object is less than 30% to output object, and stockpile temperature is less than 40 in compost groove in
℃。
5. a kind of domestic organic garbage recycling treatment process according to claim 4, it is characterised in that the step
(9) time that organic waste aerobic fermentation microbial inoculum carries out aerobic fermentation in is 2-3 days.
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| CN107347498A (en) * | 2017-08-15 | 2017-11-17 | 中林山水（北京）生态科技股份有限公司 | The method for repairing Nutrition Soil using organic waste and sludge manufacture mine |
| CN107903097A (en) * | 2017-12-20 | 2018-04-13 | 苏州华益洁环境能源技术有限公司 | The system that kitchen garbage makes organic fertilizer |
| CN107935653A (en) * | 2017-12-29 | 2018-04-20 | 浙江浦江加百列生态科技有限公司 | A kind of organic liquid fertilizer zymotechnique and fermentation system |
| CN108046854A (en) * | 2018-01-06 | 2018-05-18 | 天津大学 | Mushroom bran for heavy metal adsorption-bacterial manure fermentation recycles coupling device and method |
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| CN109134004A (en) * | 2018-07-25 | 2019-01-04 | 深圳全钰环保科技有限公司 | Rubbish fermentation technique |
| CN109534868A (en) * | 2018-11-14 | 2019-03-29 | 文华学院 | Device and method based on fermentation method processing various heavy |
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| CN109954747A (en) * | 2019-04-25 | 2019-07-02 | 广东春天生态科技集团有限公司 | A method of the rubbish containing iron and wood is decomposed using biological mud |
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| CN111533416A (en) * | 2020-05-18 | 2020-08-14 | 宇恒(南京)环保装备科技有限公司 | Method for solid-liquid synergistic aerobic biological fermentation of high-nutrition waste organic matters |
| CN112044926A (en) * | 2020-08-05 | 2020-12-08 | 上海扬升生态农业有限公司 | Method for preparing breeding feed by using organic garbage |
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| CN112620312A (en) * | 2020-12-21 | 2021-04-09 | 北京中科博联科技集团有限公司 | Bury good oxygen fermentation system of formula rubbish intelligence |
| CN112592213A (en) * | 2020-12-31 | 2021-04-02 | 浙江丽庭环境科技有限公司 | Comprehensive treatment method for aerobic fermentation and reduction of kitchen waste in whole process |
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