CN104230401A - Treatment method of kitchen garbage - Google Patents
Treatment method of kitchen garbage Download PDFInfo
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- CN104230401A CN104230401A CN201410464789.6A CN201410464789A CN104230401A CN 104230401 A CN104230401 A CN 104230401A CN 201410464789 A CN201410464789 A CN 201410464789A CN 104230401 A CN104230401 A CN 104230401A
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- fermentation
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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
Abstract
The invention relates to a treatment method of kitchen garbage. The method comprises the following steps: sorting the kitchen garbage, and detecting out the ingredients which are difficult to transform, such as plastics; carrying out primary crushing on the kitchen garbage; carrying out dehydration on powder and removing moisture in the powder; feeding fermentation materials to the dewatered garbage, crushing the mixture, and then evenly mixing the raw materials with the fermentation materials; carrying out aerobic fermentation on the mixture for 12-15 days; and screening after fermenting. Through use of the method, dehydration is carried out before fermentation, so that the air permeability of the powder is increased, the biochemical reaction rate and the conversion ratio of the fermentation process are greatly increased, the garbage treatment cycle is shortened by 50%, the content of the screened organic matter reaches 80-90%, eggs of flies and the like are effectively prevented from generating and breeding, in addition, a harmful gas is prevented from escaping by spraying deodorization in the fermentation process, and the method is safe and environmentally friendly. According to the method disclosed by the invention, the garbage treatment cost is saved, meanwhile, the problem of environmental pollution is solved, and the method has significant economic and social benefits.
Description
Technical field
The present invention relates to technical field of waste treatment, particularly the treatment process of rubbish from cooking.
background technology
In recent years, due to being on the rise of environmental pollution, especially domestic refuse is on the impact of environment, has caused and has paid attention to widely, particularly rubbish from cooking, water content, organism amount, grease and saltiness are high, easy corruption, with traditional burying method, causes the waste of land resources, and the pollution of serious air and water quality, the health of harm people and animals.The biochemical treatment process transferring the science of comparison to is started to the process of rubbish from cooking both at home and abroad, through process, rubbish is become available resource.But complete mechanical means also costly, drop into general 500 ~ about 8,000,000.
Application number is disclose a kind of rubbish from cooking biological treating equipment and method in the Chinese invention application of 201410089559.6, and its method comprises: sorting, pulverize, add fermentation auxiliary material pulverize again, Natural compost, fermentation, screening.The feature of the method is the direct Natural compost fermentation of mixed powder, and fermentation time 20 ~ 35 days, filters out organism 20 ~ 40%, and 60 ~ 80% is residue.The plant equipment cost utilizing the method to use is higher.
Adopt above-mentioned waste disposal method, the subject matter existed is: equipment investment is high, the rear directly compost fermentation of pulverizing, sewage content is high, produce that peculiar smell is large in fermenting process, about one month time of long processing period-, garbage conversion rate are low-screening after organic content can be utilized lower, only account for 20-40%.
summary of the invention
For solving the problem, the invention provides a kind for the treatment of process of rubbish from cooking, comprising: rubbish from cooking is sorted, detect the composition that plastics etc. are difficult to transform; Residual refuse is pulverized for the first time; Powder is carried out processed; Fermentation auxiliary material is thrown in the rubbish after processed; Again compound is pulverized, make raw material and fermentation auxiliary material Homogeneous phase mixing; Compound is carried out aerobic fermentation 12 ~ 16 days; Ferment laggard row filter, wherein the organism of 80 ~ 90%, the residue of 10 ~ 20%.
For realizing the object of the present invention, selected fermentation auxiliary material is three material, i.e. wood chip, charcoal and complex micro organism fungicide, uses three material fermenting process release of heat high and not by extraneous temperature difference influence.Preferably, powder is followed successively by with the ratio of wood chip, charcoal and complex micro organism fungicide: 100:(8 ~ 12), (1.5-2.5), (0.00003 ~ 0.00005).
As preferred version of the present invention, all carried out under sealing condition before fermentation after first pulverizing.Scattering and disappearing and pollution to environment of effectively anti-stage raw material here.
For making the present invention obtain best effect, the flow process of aerobic fermentation is: first use poromeric material shop fixtures, and will mix stockpile static thereon three days, temperature rises to more than 50 degree Celsius; Thereafter turning every day in about 7 days once, makes it fully to contact with oxygen, and to complete biochemical reaction, and utilize spray equipment deodorizing, temperature is at 60 ~ 72 degrees Celsius; Temperature; Turning every day 1 time in last about four days, reducing temperature and humidity, temperature is down to less than 50 degree Celsius.
The organism filtered out, indices is all up to state standards, and is widely used in gardens, greening and flower culture; Organic vegetable matrix fertilizer (soilless culture); Make the fermentation raw material of poultry fertilizer; Culture medium of edible fungus and making biomass fuel rod etc.Remaining residue recycles as the grate-layer material of fermentation, and existing good ventilation property, can play katalysis again, accelerate fermenting speed, shorten fermentation time.
Compared with prior art, the present invention has following beneficial effect:
Owing to have employed processed and namely sealing treatment accomplishes zero sewage outflow, effectively prevent generation and the breeding of the harmful organisms such as fly class, and the spray deodorizing of fermenting process, all serve the effect of purifying treatment environment, increase the loft of fermentation material simultaneously, expand the contact area with oxygen, in addition with the residue shop fixtures filtered out, the biochemical reaction speed of great quickening fermenting process, shortens fermentation time, improves organic transformation efficiency.Use this treatment process, mechanical means cost is about 1,000,000, and economic and social benefit is remarkable.
accompanying drawing explanation
Fig. 1 is garbage treating process schema of the present invention;
Fig. 2 is fermentation flow diagram.
Embodiment
Below in conjunction with specific embodiment, set forth the present invention further.
Embodiment 1
After the preliminary rubbish from cooking ten tons except decontaminated water collected is weighed, be delivered to off-sorting station from material charging region through travelling belt and carry out manual sorting, detect the composition that plastics etc. are difficult to transform; Transmit again and pulverize into main pulverizer; Squeezing water removing machine removing moisture is taken to by closed conveying after pulverizing; Obtain powder 6 tons, then deliver to three material by closed conveying belt and throw in districts, add the complex micro organism fungicide of 0.8 ton of wood chip, 0.15 ton of charcoal and 0.3 kilogram; Crushing auxiliary machine co-grinding is taken to again by closed conveying; Mixed powder is delivered to fermentation zone carried out aerobic fermentation by short being refuted.: first use wood chip shop fixtures, about 10 cm, then by mixed powder heap thereon, every bar fermentation head of district 30 meters, wide 2 meters, high 1.2 meters.Static four days, this section, based on middle temperature actinomycetes aerobic microorganism, rose to more than 50 degree Celsius by normal temperature.Thereafter eight days with stack turner turning every day once, oxygenation wet down, open spray equipment deodorizing, this section is based on aerobic thermophilic actinomycete, and the Mierocrystalline cellulose in intensive decomposition biology and pectic substance, discharge a large amount of heat, and temperature rises to 62 degrees centigrade simultaneously.Last four days microbial activities strength reductions, once, moisture distributes in turning every day, and temperature drops to less than 50 degrees Celsius; The mixture fermented is transported to screening area, and through screening, weigh, total amount of organic is 5.9 tons, residue 1.04 tons.
Embodiment 2
After the preliminary rubbish from cooking 100 tons except decontaminated water collected is weighed, be delivered to off-sorting station from material charging region through travelling belt and carry out manual sorting, detect the composition that plastics etc. are difficult to transform; Transmit again and pulverize into main pulverizer; Squeezing water removing machine removing moisture is taken to by closed conveying after pulverizing; Obtain powder 65 tons, then deliver to three material by closed conveying belt and throw in districts, add the complex micro organism fungicide of 10 tons of wood chips, 2 tons of charcoals and 4 kilograms; Crushing auxiliary machine co-grinding is taken to again by closed conveying; Mixed powder is delivered to fermentation zone carried out aerobic fermentation by short being refuted.: first with the residue shop fixtures that the last cycle filters out, about 12 cm, then by mixed powder heap thereon, every bar fermentation head of district 30 meters, wide 2 meters, high 1.2 meters.Static three days, this section, based on middle temperature actinomycetes aerobic microorganism, rose to more than 50 degree Celsius by normal temperature.Thereafter 7 days with stack turner turning every day once, oxygenation wet down, open spray equipment deodorizing, this section is based on aerobic thermophilic actinomycete, and the Mierocrystalline cellulose in intensive decomposition biology and pectic substance, discharge a large amount of heat, and temperature rises to 70 degrees centigrade simultaneously.Last four days microbial activities strength reductions, once, moisture distributes in turning every day, and temperature drops to less than 50 degrees Celsius; The mixture fermented is transported to screening area, and through screening, weigh, total amount of organic is 66.99 tons, residue 10.01 tons.
Embodiment 3
After the preliminary rubbish from cooking 100 tons except decontaminated water collected is weighed, be delivered to off-sorting station from material charging region through travelling belt and carry out manual sorting, detect the composition that plastics etc. are difficult to transform; Transmit again and pulverize into main pulverizer; Squeezing water removing machine removing moisture is taken to by closed conveying after pulverizing; Obtain powder 70 tons, then deliver to three material by closed conveying belt and throw in districts, add the complex micro organism fungicide of 12 tons of wood chips, 2.5 tons of charcoals and 5 kilograms; Crushing auxiliary machine co-grinding is taken to again by closed conveying; Mixed powder is delivered to fermentation zone carried out aerobic fermentation by short being refuted.: first with the residue shop fixtures that the last cycle filters out, about 12 cm, then by mixed powder heap thereon, every bar fermentation head of district 30 meters, wide 2 meters, high 1.2 meters.Static three days, this section, based on middle temperature actinomycetes aerobic microorganism, rose to more than 50 degree Celsius by normal temperature.Thereafter 6 days with stack turner turning every day once, oxygenation wet down, open spray equipment deodorizing, this section is based on aerobic thermophilic actinomycete, and the Mierocrystalline cellulose in intensive decomposition biology and pectic substance, discharge a large amount of heat, and temperature rises to 72 degrees centigrade simultaneously.Last three days microbial activities strength reductions, once, moisture distributes in turning every day, and temperature drops to less than 50 degrees Celsius; The mixture fermented is transported to screening area, and through screening, weigh, total amount of organic is 76 tons, residue 8.45 tons.
Finally need described herein: above embodiment, only for being described in more detail technical scheme of the present invention, can not be interpreted as limiting the scope of the invention; Some nonessential improvement that those skilled in the art's foregoing according to the present invention is made and adjustment all belong to protection scope of the present invention.
Claims (6)
1. a treatment process for rubbish from cooking, comprises the following steps: rubbish from cooking to sort, and detects the composition that plastics etc. are difficult to transform; Residual refuse is pulverized for the first time; Fermentation auxiliary material is thrown in the rubbish after pulverizing; Again compound is pulverized, make raw material and fermentation auxiliary material Homogeneous phase mixing; Compound is carried out fermentation 12 ~ 16 days; Ferment laggard row filter, wherein the organism of 80 ~ 90%, the residue of 10 ~ 20%; It is characterized in that: described method also comprises once pulverizes the front step of powder being carried out processed of rear input three material.
2. the treatment process of rubbish from cooking according to claim 1, is characterized in that: all carried out under sealing condition before fermentation after first pulverizing.
3. the treatment process of rubbish from cooking according to claim 2, is characterized in that: described fermentation auxiliary material is made up of wood chip, charcoal and complex micro organism fungicide.
4. the treatment process of rubbish from cooking according to claim 3, is characterized in that: refuse powder is followed successively by 100:(8 ~ 12 with the mass ratio of wood chip, charcoal and complex micro organism fungicide in fermentation auxiliary material), (1.5-2.5), (0.00003 ~ 0.00005).
5. the treatment process of the rubbish from cooking according to claim 1-4, it is characterized in that: described fermentation step is high-temperature aerobic fermentation, its flow process is: first use poromeric material shop fixtures, and will mix stockpile static thereon three days, temperature rises to more than 50 degree Celsius; Thereafter turning every day 1 time in about 7 days, oxygenation, and utilize spray equipment deodorizing, temperature is at 60 ~ 72 degrees Celsius;
Turning every day 1 time in last about four days, reducing temperature and humidity, temperature is down to less than 50 degree Celsius.
6. the treatment process of rubbish from cooking according to claim 5, is characterized in that: described shop fixtures material is the residue filtered out after fermentation.
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CN201410464789.6A CN104230401A (en) | 2014-09-15 | 2014-09-15 | Treatment method of kitchen garbage |
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CN201410464789.6A CN104230401A (en) | 2014-09-15 | 2014-09-15 | Treatment method of kitchen garbage |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104529568A (en) * | 2015-01-16 | 2015-04-22 | 南开大学 | Method for processing kitchen waste by virtue of microbial technique |
CN104987143A (en) * | 2015-07-13 | 2015-10-21 | 深圳市龙吉顺实业发展有限公司 | Method for producing organic fertilizer by using kitchen waste |
CN105237307A (en) * | 2015-11-14 | 2016-01-13 | 黄海涛 | Soil conditioner as well as production method and application thereof |
CN105330349A (en) * | 2015-12-08 | 2016-02-17 | 胡舒 | High-temperature aerobic composting method of kitchen waste |
CN107162678A (en) * | 2017-05-08 | 2017-09-15 | 湖州壤之沃生物技术有限公司 | A kind of rubbish from cooking zymotechnique |
CN112679286A (en) * | 2021-02-03 | 2021-04-20 | 河北环境工程学院 | Method for preparing bio-organic fertilizer by using kitchen garbage |
CN114904879A (en) * | 2022-03-02 | 2022-08-16 | 上海市园林科学规划研究院 | Preparation method of kitchen waste biogas residue with low phytotoxicity |
-
2014
- 2014-09-15 CN CN201410464789.6A patent/CN104230401A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104529568A (en) * | 2015-01-16 | 2015-04-22 | 南开大学 | Method for processing kitchen waste by virtue of microbial technique |
CN104987143A (en) * | 2015-07-13 | 2015-10-21 | 深圳市龙吉顺实业发展有限公司 | Method for producing organic fertilizer by using kitchen waste |
CN105237307A (en) * | 2015-11-14 | 2016-01-13 | 黄海涛 | Soil conditioner as well as production method and application thereof |
CN105330349A (en) * | 2015-12-08 | 2016-02-17 | 胡舒 | High-temperature aerobic composting method of kitchen waste |
CN107162678A (en) * | 2017-05-08 | 2017-09-15 | 湖州壤之沃生物技术有限公司 | A kind of rubbish from cooking zymotechnique |
CN112679286A (en) * | 2021-02-03 | 2021-04-20 | 河北环境工程学院 | Method for preparing bio-organic fertilizer by using kitchen garbage |
CN114904879A (en) * | 2022-03-02 | 2022-08-16 | 上海市园林科学规划研究院 | Preparation method of kitchen waste biogas residue with low phytotoxicity |
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