阅读说明：本技术 一种微生物快速启动的微压高温有机固废处理系统及方法 (Micro-pressure high-temperature organic solid waste treatment system and method with quick microbial start ) 是由 王婧瑶 阎中 王凯军 于 2020-05-08 设计创作，主要内容包括：一种微生物快速启动的微压高温有机固废处理系统,包括底物菌种预混罐,高温启动仓,微压真空仓,二次腐熟仓,烟气管道和筛分装置,有机固废在底物菌种预混罐中根据含水率进行底物调节,并与微生物菌种充分混合,调配好的有机固废物料首先在高温启动仓中进行微生物的快速增殖扩繁,促进物料中有机物大分子快速降解为小分子,再输送至微压真空仓,在其中微负压导致生物进程被抑制,使其维持在对数稳定期,对有机固废物料进行主发酵,而后输送至二次腐熟仓腐熟然后输送至筛分装置筛分后保存备用,同时负压曝气使微压真空仓产生的气体抽向烟气管道,用于高温启动仓的补给；本发明可有效缩短堆肥周期,同时对尾气处理以防影响环境。(A micro-pressure high-temperature organic solid waste treatment system with quick microbial start comprises a substrate strain premixing tank, a high-temperature start bin, a micro-pressure vacuum bin, a secondary decomposition bin, a flue gas pipeline and a screening device, wherein organic solid waste is subjected to substrate adjustment in the substrate strain premixing tank according to the water content, and is fully mixed with microbial strains, the prepared organic solid waste material is firstly rapidly proliferated and propagated in a high-temperature starting bin to promote organic macromolecules in the material to be rapidly degraded into micromolecules, and then is conveyed to a micro-pressure vacuum bin, wherein the micro-negative pressure causes the biological process to be inhibited, so that the biological process is maintained in a logarithmic stationary phase, carrying out main fermentation on organic solid waste materials, then conveying the organic solid waste materials to a secondary decomposition bin for decomposition, conveying the organic solid waste materials to a screening device for screening and then storing for later use, meanwhile, the negative pressure aeration enables the gas generated by the micro-pressure vacuum bin to be pumped to a flue gas pipeline for supplying the high-temperature starting bin; the invention can effectively shorten the composting period and treat tail gas to prevent the environment from being influenced.)

1. A micro-pressure high-temperature organic solid waste treatment system started quickly by microorganisms is characterized by comprising:

a substrate strain premixing tank (1), wherein organic solid wastes are added with microbial strains for substrate adjustment;

starting a bin (2) at a high temperature, inoculating an outlet of a substrate strain premixing tank (1), and heating the organic solid waste material after substrate adjustment;

the micro-pressure vacuum bin (3) is connected with an outlet of the high-temperature starting bin (2) and is used for carrying out main fermentation on the heated organic solid waste material;

the secondary decomposition bin (4) is connected with a material outlet of the micro-pressure vacuum bin (3) and is used for carrying out secondary decomposition on the organic solid waste material after the main fermentation;

the smoke pipeline (5) is connected with a smoke outlet of the micro-pressure vacuum bin (3) and a hot side inlet of the high-temperature starting bin (2), and outputs gas generated by main fermentation for energy supply of the high-temperature starting bin;

and the screening device (7) is connected with a material outlet of the secondary decomposition bin (4) and is used for screening the organic solid waste materials subjected to secondary decomposition.

2. The micro-pressure high-temperature organic solid waste treatment system started quickly by microorganisms according to claim 1, further comprising a deodorization device (6) connected with the flue gas pipeline (5), wherein the flue gas pipeline (5) conveys one part of gas generated by main fermentation to the high-temperature starting bin (2), and the other part of gas is discharged after being harmlessly treated by the deodorization device (6).

3. The micro-pressure high-temperature organic solid waste treatment system with the rapid microbial start function according to claim 1, wherein the high-temperature start bin (2), the micro-pressure vacuum bin (3) and the secondary decomposition bin (4) form a biological drying reactor, and the biological drying reactor is used as a sub-fermentation system and adopts a cellular structure to form three bins.

4. The treatment method of the micro-pressure high-temperature organic solid waste treatment system based on the quick microbial start of claim 1 is characterized by comprising the following steps:

step a, adjusting the substrate of the organic solid waste in a substrate strain premixing tank (1) according to the water content, and fully mixing the organic solid waste with microbial strains;

b, conveying the organic solid waste materials prepared in the step a to a sub-fermentation system consisting of a high-temperature starting bin (2), a micro-pressure vacuum bin (3) and a secondary decomposition bin (4), firstly carrying out rapid propagation and proliferation of microorganisms in the high-temperature starting bin (2) to promote organic macromolecules in the materials to be rapidly degraded into micromolecules, then conveying the micromolecules to the micro-pressure vacuum bin (3), wherein the micro-negative pressure causes the biological process to be inhibited, so that the biological process is maintained in a logarithmic stabilization phase, carrying out main fermentation on the organic solid waste materials, then conveying the organic solid waste materials to the secondary decomposition bin (4) for decomposition, and simultaneously carrying out negative pressure aeration to pump gas generated by the micro-pressure vacuum bin (3) to a flue gas pipeline (5) for supplying the high-temperature starting bin (2);

and c, conveying the materials generated in the step b to a screening device (7) for screening and then storing for later use.

5. The treatment method according to claim 4, characterized in that a conditioner is mixed into the substrate strain premixing tank (1) according to the initial water content of the organic solid waste, and then microbial strains are mixed into the substrate strain premixing tank, so that the water content of the material is adjusted to be below 80%.

6. The treatment method according to claim 4 or 5, wherein the microbial strain is a composite strain mainly comprising bacillus in the phylum firmicutes, the addition amount is 1% of the weight of the organic solid waste, and the conditioner is lignocellulose agricultural and forestry waste, and the addition amount is 10% of the weight of the organic solid waste.

7. The treatment process according to claim 6, characterized in that the main component of the complex strain is one or more of Lactobacillus (Lactobacillus), Streptococcus (Streptococcus), Microbacterium (Exiguobacterium), Citrobacter (Citrobacter), Acinetobacter (Acinetobacter), Oceanobacter (Oceanobacillus), Cladosporium (Virgibacter), Pseudomonas (Pseudomonas), Bacillus (Bacillus), Chinese Bacillus (Sinibacillus), Slow-growing Bacillus (Lentibacillus), Weissella (Weissella) and Klebsiella (Kiebsiella).

8. The treatment method according to claim 4, characterized in that the temperature of the high-temperature start-up bin (2) is controlled to be 55-60 ℃, a temperature control device is adopted to forcibly raise the temperature, an aeration device is adopted to forcibly ventilate and turn over and throw to supply oxygen; the micro-pressure vacuum chamber (3) is vacuumized by micro-negative pressure and assisted by temperature control to maintain the whole fermentation process in a high-activity state; the volume of the secondary decomposition chamber (4) is larger than the volumes of the high-temperature starting chamber (2) and the micro-pressure vacuum chamber (3), and the composting is kept under natural conditions.

9. The treatment method according to claim 4, characterized in that the screening device (7) is used for screening the fermented materials, undersize materials are used for preparing organic fertilizers, oversize materials are used as fermentation backfill materials, and the fermentation backfill materials are conveyed to the substrate strain premixing tank (1) for treatment again.

10. The treatment method according to claim 4, characterized in that the flue gas pipeline (5) is connected with a deodorizing device (6), one part of the gas generated by the micro-pressure vacuum bin (3) returns to the high-temperature starting bin (2) to be used as temperature aeration supply, and the other part of the gas is conveyed to the deodorizing device (6) to be harmless and then discharged.

Technical Field

The invention belongs to the technical field of solid waste treatment, relates to harmless treatment and resource utilization of organic solid waste resources, and particularly relates to a micro-pressure high-temperature organic solid waste treatment system and method with quick microbial starting.

Background

At present, sanitary landfill and incineration are still the main modes of harmless treatment of household garbage, and account for 62 percent and 30 percent respectively. The organic solid waste is used as an important component of the garbage, the yield of the organic solid waste is increased at a speed of 8-10% per year, and meanwhile, due to small heat value, easy decay and high organic matter content, percolation liquid, stink and landfill gas are generated in the landfill process, so that the influence on the surrounding environment is great; although the reduction and the harmlessness can be realized to the maximum extent by incineration, the incineration is not suitable for treating organic solid wastes because of overhigh initial investment and operation cost, secondary pollution of incineration tail gas and higher requirements on the calorific value and the moisture content of raw materials.

And the biological treatment can carry out resource utilization while harmlessly treating the organic solid wastes, wherein the resource utilization comprises anaerobic fermentation and aerobic composting. Anaerobic fermentation is not suitable for large-scale organic waste disposal due to slow decomposition of organic matters, long fermentation period (4-6 months) and large occupied area. The modern process mostly adopts high-temperature aerobic composting, has higher harmless degree and obvious reduction effect, can realize the resource of organic garbage treatment to the maximum extent, but also has the problems of long fermentation period, difficult control of the fermentation process, unstable discharge, odor dissipation and the like.

Disclosure of Invention

In order to overcome the defects of the prior art, the invention aims to provide a micro-pressure high-temperature organic solid waste treatment system and method with quick microbial starting, so as to effectively shorten the composting period and treat tail gas to prevent the environment from being influenced.

In order to achieve the purpose, the invention adopts the technical scheme that:

a micro-pressure high-temperature organic solid waste treatment system with quick microbial start comprises:

a substrate strain premixing tank 1, wherein organic solid waste is added with microorganism strains for substrate adjustment;

starting the bin 2 at a high temperature, inoculating the outlet of the substrate strain premixing tank 1, and heating the organic solid waste material after substrate adjustment;

the micro-pressure vacuum bin 3 is connected with an outlet of the high-temperature starting bin 2, and is used for carrying out main fermentation on the heated organic solid waste material;

the secondary decomposition bin 4 is connected with a material outlet of the micro-pressure vacuum bin 3 and is used for carrying out secondary decomposition on the organic solid waste material after the main fermentation;

the flue gas pipeline 5 is connected with a flue gas outlet of the micro-pressure vacuum bin 3 and a hot side inlet of the high-temperature starting bin 2, and outputs gas generated by main fermentation for energy supply of the high-temperature starting bin;

and the screening device 7 is connected with a material outlet of the secondary decomposition bin 4 and is used for screening the organic solid waste materials subjected to secondary decomposition.

Further, the invention also comprises a deodorization device 6 connected with the flue gas pipeline 5, wherein the flue gas pipeline 5 conveys one part of gas generated by the main fermentation to the high-temperature starting bin 2, and the other part is discharged after being harmlessly treated by the deodorization device 6.

The high-temperature starting bin 2, the micro-pressure vacuum bin 3 and the secondary decomposition bin 4 form a biological drying reactor, and the biological drying reactor is used as a sub-fermentation system and forms three bins by adopting a cellular structure.

The invention also provides a treatment method of the micro-pressure high-temperature organic solid waste treatment system based on the quick microbial start, which comprises the following steps:

step a, adjusting the substrate of the organic solid waste in a substrate strain premixing tank 1 according to the water content, and fully mixing the organic solid waste with microbial strains;

b, conveying the organic solid waste materials prepared in the step a to a sub-fermentation system consisting of a high-temperature starting bin 2, a micro-pressure vacuum bin 3 and a secondary decomposition bin 4, firstly carrying out rapid propagation and proliferation of microorganisms in the high-temperature starting bin 2 to promote organic matter macromolecules in the materials to be rapidly degraded into micromolecules, then conveying the micromolecules to the micro-pressure vacuum bin 3, wherein the biological process is inhibited due to micro negative pressure, so that the biological process is maintained in a logarithmic stabilization period, carrying out main fermentation on the organic solid waste materials, then conveying the organic solid waste materials to the secondary decomposition bin 4 for decomposition, and simultaneously pumping gas generated by the micro-pressure vacuum bin 3 to a flue gas pipeline 5 for supplying the high-temperature starting bin 2 through negative pressure aeration;

and c, conveying the materials generated in the step b to a screening device 7 for screening and then storing for later use.

Further, a conditioner is mixed into the substrate strain premixing tank 1 according to the initial water content of the organic solid waste, then microbial strains are mixed, and the water content of the material is adjusted to be below 80%.

Further, the microbial strain is a composite strain system mainly containing bacillus in the phylum of firmicutes, the adding amount of the microbial strain is 1% of the weight of the organic solid waste, the conditioner is lignocellulose agricultural and forestry waste such as straw, and the adding amount of the conditioner is 10% of the weight of the organic solid waste.

Further, the main component of the complex bacterial strain is one or more of Lactobacillus (Lactobacillus), Streptococcus (Streptococcus), microbacterium (Exiguobacterium), Citrobacter (Citrobacter), Acinetobacter (Acinetobacter), oceanobacter (oceanobacter), cladosporium (virgibbsiella), Pseudomonas (Pseudomonas), Bacillus (Bacillus), china Bacillus (Sinibacillus), chronic Bacillus (Lentibacillus), Weissella (Weissella), and klebsiella (Kiebsiella).

Further, the temperature of the high-temperature starting bin 2 is controlled to be 55-60 ℃, a temperature control device is adopted to forcibly heat, and an aeration device is adopted to forcibly ventilate and turn over the stack for supplying oxygen; the micro-pressure vacuum chamber 3 is vacuumized by micro-negative pressure and is assisted with temperature control to maintain the whole fermentation process in a high-activity state; the volume of the secondary decomposition chamber 4 is larger than that of the high-temperature starting chamber 2 and the micro-pressure vacuum chamber 3, and the composting is kept under natural conditions.

Further, the screening device 7 is used for screening the fermented materials, undersize materials are used for preparing organic fertilizers, oversize materials are used as fermentation backfill materials, and the fermentation backfill materials are conveyed to the substrate strain premixing tank 1 for treatment again.

Further, the flue gas pipeline 5 is connected with a deodorizing device 6, one part of gas generated by the micro-pressure vacuum bin 3 returns to the high-temperature starting bin 2 to be used as temperature aeration supply, and the other part of gas is conveyed to the deodorizing device 6 to be discharged after harmless treatment.

Compared with the prior art, the method has the advantages that the optimal fermentation state of the material is adjusted by controlling the composting process of the organic solid waste substrate under the action of the microorganisms, the beneficial effects of the dominant microorganisms are exerted, the organic matters in the solid waste substrate are decomposed, the energy is released, and the effect of killing harmful bacteria and viruses is achieved. The system can effectively shorten the composting period to 5-7 days, reduce the water content of the organic solid waste to below 20%, ensure that the content of active ingredients and microorganism indexes of final products meet the NY525-2002 organic fertilizer standard, realize the reduction, harmlessness and recycling of the organic solid waste, collect and treat the generated tail gas, discharge the tail gas after reaching the standard and have no influence on the surrounding environment.

Drawings

FIG. 1 is a schematic diagram of the present invention.

Detailed Description

The embodiments of the present invention will be described in detail below with reference to the drawings and examples.

The invention relates to a micro-pressure high-temperature organic solid waste treatment system with quick microbial start, which is suitable for organic solid waste treatment and mainly comprises the following components in percentage by weight with reference to a figure 1:

a substrate strain premixing tank 1, wherein organic solid waste is added with microorganism strains for substrate adjustment;

the fermentation subsystem, namely a biological drying reactor, is the core of the system, and three mutually independent bins are formed by adopting a cellular structure, namely a high-temperature starting bin 2, a micro-pressure vacuum bin 3 and a secondary decomposition bin 4. The high-temperature starting bin 2 is connected with an outlet of the substrate strain premixing tank 1, and the organic solid waste material after substrate adjustment is heated; the micro-pressure vacuum bin 3 is connected with an outlet of the high-temperature starting bin 2 and is used for carrying out main fermentation on the heated organic solid waste material; the secondary decomposition bin 4 is connected with a material outlet of the micro-pressure vacuum bin 3 and is used for carrying out secondary decomposition on the organic solid waste material after main fermentation;

the flue gas pipeline 5 is connected with a flue gas outlet of the micro-pressure vacuum bin 3 and a hot side inlet of the high-temperature starting bin 2, and outputs gas generated by main fermentation for energy supply of the high-temperature starting bin;

and the screening device 7 is connected with a material outlet of the secondary decomposition bin 4 and is used for screening the organic solid waste materials subjected to secondary decomposition.

The micro-pressure high-temperature organic solid waste treatment system based on the quick microbial start comprises the following steps:

step a, adjusting the substrate of the organic solid waste in a substrate strain premixing tank 1 according to the water content, and fully mixing the organic solid waste with the microbial strain.

Wherein, the organic solid waste can be organic wet waste, a conditioner (such as dry waste) is mixed into the substrate strain premixing tank 1 according to the initial water content of the organic solid waste, and then microbial strains are mixed, and the water content of the material is adjusted to be below 80%. The microbial strain adopted by the invention is a composite strain system mainly containing bacillus in the phylum of firmicutes, the adding amount (bacterial liquid) is 1% of the weight of the organic solid waste, the conditioner is lignocellulose agricultural and forestry waste such as straw, and the adding amount is 1/8-1/10% of the weight of the organic solid waste.

The main components of the composite bacterial system of the invention are one or more of Lactobacillus (Lactobacillus), Streptococcus (Streptococcus), microbacterium (Exiguobacterium), Citrobacter (Citrobacter), Acinetobacter (Acinetobacter), Oceanobacillus (Oceanobacillus), Cladosporium (Virgibacillus), Pseudomonas (Pseudomonas), Bacillus (Bacillus), Chinese Bacillus (Sinibacillus), Slow-growing Bacillus (Lentibacillus), Weissella (Weissella) and Klebsiella (Kiebsiella), and when the strains are multiple, the dosages of the components are arbitrary.

And b, conveying the organic solid waste materials prepared in the step a to a sub-fermentation system consisting of a high-temperature starting bin 2, a micro-pressure vacuum bin 3 and a secondary decomposition bin 4, firstly carrying out rapid propagation and proliferation of microorganisms in the high-temperature starting bin 2 to promote organic matter macromolecules in the materials to be rapidly degraded into micromolecules, then conveying the micromolecules to the micro-pressure vacuum bin 3, wherein the biological process is inhibited due to micro negative pressure, so that the biological process is maintained in a logarithmic stabilization period, carrying out main fermentation on the organic solid waste materials, then conveying the organic solid waste materials to the secondary decomposition bin 4 for decomposition, and simultaneously pumping gas generated by the micro-pressure vacuum bin 3 to a flue gas pipeline 5 for supplying the high-temperature starting bin 2 through negative pressure aeration.

Wherein the temperature of the high-temperature starting bin 2 is controlled to be 55-60 ℃, a temperature control device is adopted to forcibly heat up, an aeration device is adopted to forcibly ventilate and turn over and throw for supplying oxygen, and the high temperature and the forced ventilation can lead the added microorganisms to rapidly propagate to reach a logarithmic phase, thereby rapidly starting the fermentation system. Specifically, the aeration mode is bottom intermittent aeration and ventilation, 30min is an aeration and ventilation period, 15min is opened and closed in each period, and the ventilation rate is 1.2-1.6L/min per kilogram of materials.

The micro-pressure vacuum chamber 3 is vacuumized by micro negative pressure (-5mmAp to-10 mmAp) and is assisted with temperature control to maintain the whole fermentation process in a high activity state (active metabolism period), the pressure can reduce the new and old metabolism speed of microorganisms and control the reaction process of the microorganisms, so that the whole fermentation system is in a high-activity substrate degradation and conversion reaction stage, the micro-pressure vacuum chamber 3 can be provided with an independent control unit, and the temperature is still controlled at the temperature level of the high-temperature starting chamber 2.

The volume of the secondary decomposition chamber 4 is larger than that of the high-temperature starting chamber 2 and the micro-pressure vacuum chamber 3, and the natural condition is kept for composting. After continuous high-activity reaction, deep fermentation is carried out under natural conditions, so that some residual micromolecular organic matters in the substrate are subjected to secondary degradation and conversion, and temperature and pressure are not controlled at the moment.

And c, conveying the materials generated in the step b to a screening device 7, screening, and storing for later use, wherein the whole rapid composting time is 7 days, and the dehydration, the reduction and the resource utilization of the organic solid wastes are completed.

Wherein, screening plant 7 sieves the material that the fermentation is good, and the undersize thing is used for preparing fertilizer, and the oversize thing is as fermentation backfill, carries to the processing once more of substrate bacterial premixing jar 1.

In another embodiment of the invention, the device further comprises a deodorization device 6 connected with the flue gas pipeline 5, wherein the flue gas pipeline 5 conveys one part of gas generated by main fermentation to the high-temperature starting bin 2 to be used as temperature aeration supply, and the other part is discharged after being harmlessly treated by the deodorization device 6.

In a specific embodiment of the invention, the organic solid waste is kitchen waste, the conditioner is rice straw which is uniformly mixed according to a weight ratio of 10:1, and the bacteria liquid is mixed according to a mass volume ratio of 100:1, wherein the water content of the kitchen waste is 75%, the water content of the rice straw is 15%, the length of the rice straw is 8cm, and the materials are all from Zhejiang. The temperature of the high-temperature starting bin 2 is controlled to be 55 ℃, the aeration mode is that the bottom is subjected to intermittent aeration and ventilation, 30min is an aeration and ventilation period, 15min is opened and closed in each period, and the ventilation rate is 1.6L/min per kilogram of materials.