CN107162321A - A kind of integrated treatment for cow manure method and apparatus of the livestock and poultry farm based on dry cleaning up excrement - Google Patents
A kind of integrated treatment for cow manure method and apparatus of the livestock and poultry farm based on dry cleaning up excrement Download PDFInfo
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- 210000003608 fece Anatomy 0.000 title claims abstract description 92
- 239000010871 livestock manure Substances 0.000 title claims abstract description 73
- 238000000034 method Methods 0.000 title claims abstract description 44
- 244000144972 livestock Species 0.000 title claims abstract description 24
- 244000144977 poultry Species 0.000 title claims abstract description 24
- 238000005108 dry cleaning Methods 0.000 title claims description 10
- 238000000855 fermentation Methods 0.000 claims abstract description 55
- 230000004151 fermentation Effects 0.000 claims abstract description 33
- 239000010865 sewage Substances 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000007788 liquid Substances 0.000 claims abstract description 25
- 238000000926 separation method Methods 0.000 claims abstract description 19
- 239000007787 solid Substances 0.000 claims abstract description 16
- 239000010902 straw Substances 0.000 claims abstract description 15
- 238000007599 discharging Methods 0.000 claims abstract description 7
- 238000011010 flushing procedure Methods 0.000 claims description 11
- 239000007921 spray Substances 0.000 claims description 10
- 239000002054 inoculum Substances 0.000 claims description 4
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 3
- 210000002700 urine Anatomy 0.000 claims description 3
- 230000014759 maintenance of location Effects 0.000 claims description 2
- 239000002245 particle Substances 0.000 claims description 2
- 235000009854 Cucurbita moschata Nutrition 0.000 claims 2
- 240000001980 Cucurbita pepo Species 0.000 claims 2
- 235000009852 Cucurbita pepo Nutrition 0.000 claims 2
- 230000033228 biological regulation Effects 0.000 claims 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 2
- 235000020354 squash Nutrition 0.000 claims 2
- 239000012223 aqueous fraction Substances 0.000 claims 1
- 230000004907 flux Effects 0.000 claims 1
- 239000000843 powder Substances 0.000 claims 1
- 238000010992 reflux Methods 0.000 claims 1
- 239000002689 soil Substances 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 9
- 238000000746 purification Methods 0.000 abstract description 7
- 238000002156 mixing Methods 0.000 abstract description 5
- 230000002550 fecal effect Effects 0.000 abstract description 4
- 238000009360 aquaculture Methods 0.000 abstract description 2
- 244000144974 aquaculture Species 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000009395 breeding Methods 0.000 description 6
- 230000001488 breeding effect Effects 0.000 description 6
- 238000005507 spraying Methods 0.000 description 5
- 239000002002 slurry Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000010564 aerobic fermentation Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/286—Anaerobic digestion processes including two or more steps
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/32—Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
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- 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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Abstract
本发明公开了一种基于干清粪的畜禽养殖场一体化粪污处理方法及其设备。该方法首先对畜禽粪便进行固液分离,进而对固体粪便与粪污水分别处理,处理畜禽粪便的步骤包括:与秸秆混合、进料、厌氧干发酵、出料的顺序处理,处理粪污水的步骤包括:进水、厌氧发酵、好氧塘、人工湿地、出水的顺序处理,同时公开了实现该粪污处理方法的设备,该设备由干粪处理系统、污水处理系统和沼气净化系统组成。本发明利用连续密闭进料和出料实现畜禽粪污的连续处理,利用高效厌氧系统处理污水,可降低粪污堆场所需场地面积,提高产气效率和系统运行的稳定性,确保养殖污水处理的稳定达标排放,同时还可降低粪污处理成本。
The invention discloses an integrated manure treatment method and equipment for livestock and poultry farms based on dry manure cleaning. In this method, the solid-liquid separation of livestock and poultry manure is carried out first, and then the solid manure and fecal sewage are treated separately. The steps of processing livestock and poultry manure include: mixing with straw, feeding, anaerobic dry fermentation, and sequential treatment of discharging. The steps of the sewage include: sequential treatment of water inflow, anaerobic fermentation, aerobic pond, artificial wetland, and effluent. At the same time, the equipment for realizing the method of manure treatment is disclosed. The equipment is composed of a dry manure treatment system, a sewage treatment system and biogas purification. system composition. The invention realizes the continuous treatment of livestock and poultry manure by means of continuous airtight feeding and discharging, and uses an efficient anaerobic system to treat sewage, which can reduce the site area required for the manure dump, improve the gas production efficiency and the stability of the system operation, and ensure The stable and up-to-standard discharge of aquaculture sewage treatment can also reduce the cost of manure treatment.
Description
技术领域technical field
本发明属于畜禽养殖粪污的处理领域。它涉及一种沼气干发酵装置和高效厌氧系统,是一种基于干清粪的畜禽养殖场一体化粪污处理方法及设备,具体是以粪污为原料进行厌氧发酵处理的方法及设备,可实现粪污处理。The invention belongs to the field of treatment of livestock and poultry breeding manure. It relates to a biogas dry fermentation device and a high-efficiency anaerobic system. It is an integrated manure treatment method and equipment for livestock and poultry farms based on dry manure cleaning. Specifically, it uses manure as a raw material for anaerobic fermentation treatment. Equipment for manure treatment.
背景技术Background technique
近几年,经济的发展加快了畜禽养殖业的发展,由此产生了大量的畜禽粪便,不仅污染环境,也影响养殖业的可持续发展。目前规模化的养殖生产占主要地位,这些养殖场的粪污处理工艺显得尤为重要。In recent years, economic development has accelerated the development of livestock and poultry breeding industry, resulting in a large amount of livestock and poultry manure, which not only pollutes the environment, but also affects the sustainable development of the breeding industry. At present, large-scale aquaculture production occupies a dominant position, and the manure treatment process of these farms is particularly important.
目前,按照养殖场清粪的方式来分,主要有水冲粪和干清粪两种方式。干清粪方式主要是粪便产生后即分流,干粪由机械或人工清扫和收集,尿及冲洗水则从下水道流出,分别进行处理。干清粪方式具有收集的固态粪便含水量低,粪中营养成分损失小,肥料价值高,便于高温堆肥或进行其他方式处理利用;耗水量少,产生的污水量少,且污水中的污染物含量低,易于净化处理等优势,因此已成为我国规模化养殖场清粪的主要方式。At present, according to the way of cleaning manure in farms, there are mainly two ways of washing manure with water and dry manure. The dry manure cleaning method is mainly to divert the manure after it is produced. The dry manure is cleaned and collected mechanically or manually, while the urine and flushing water flow out from the sewer and are treated separately. The dry manure method has the advantages of low water content in the collected solid manure, small loss of nutrients in the manure, high fertilizer value, and is convenient for high-temperature composting or other methods of treatment and utilization; less water consumption, less sewage generated, and pollutants in the sewage It has the advantages of low content and easy purification treatment, so it has become the main way of cleaning manure in large-scale farms in my country.
然而,当前所公开的专利分别针对畜禽粪便和污水进行处理。申请号为201610399753.3的专利公开了一种畜禽粪便处理系统,对固液分离的畜禽粪便采用滚筒烘干机进行烘干处理。该方法采用滚筒烘干机处理能耗高,同时未涉及到固液分离后的污水处理。申请号为201510832702.0的专利公开了一种动物粪便处理系统,同样采用烘干的方法处理粪便,同时由于为采用固液分离,其能耗更高。申请号为201210593996.2的专利公开了一种粪便处理装置,涉及了一种好氧发酵罐,粪便上进料下出料,上部设置送风器,同时为提高发酵效率,添加了竖向的搅拌轴,该处理方法采用好氧发酵方法处理粪便,能耗较高,同时由于增加了搅拌轴系统的稳定性不高,另外该方法同样未涉及粪污水的处理方法。申请号为201610635238.0的专利公开了养殖污水处理方法及养殖污水处理系统,采用生化处理与高级氧化相结合的方法处理养殖污水,处理效率高,但处理成本高。However, the currently disclosed patents deal with livestock manure and sewage, respectively. The patent application number 201610399753.3 discloses a livestock and poultry manure treatment system, which uses a drum dryer to dry the solid-liquid separated livestock and poultry manure. The method uses a drum dryer to treat high energy consumption and does not involve sewage treatment after solid-liquid separation. The patent application number 201510832702.0 discloses an animal manure treatment system, which also adopts the method of drying to process manure, and at the same time, because it uses solid-liquid separation, its energy consumption is higher. The patent with the application number 201210593996.2 discloses a feces treatment device, which involves an aerobic fermentation tank. The feces are fed from the top and discharged from the bottom. The upper part is equipped with an air blower. In order to improve the fermentation efficiency, a vertical stirring shaft is added. , this treatment method uses aerobic fermentation to process feces, which has high energy consumption, and at the same time, the stability of the system is not high due to the addition of the stirring shaft, and this method also does not involve the treatment of feces and sewage. The patent with the application number 201610635238.0 discloses a breeding sewage treatment method and a breeding sewage treatment system. The method of combining biochemical treatment and advanced oxidation is used to treat the breeding sewage. The treatment efficiency is high, but the treatment cost is high.
在应用推广中,处理效率高和节约能源是关键,因此如何有效提高粪污处理效率以及如何在处理过程中减少劳动力、高效利用有限资源是亟须解决的问题。In application promotion, high treatment efficiency and energy saving are the key points. Therefore, how to effectively improve the efficiency of manure treatment, how to reduce labor force and efficiently use limited resources in the treatment process is an urgent problem to be solved.
发明内容Contents of the invention
本发明的目的是针对现有规模化养殖场粪污处理效率低、建设运行成本高等问题,提供供针对规模化养殖场干清粪方式下的粪污一体化处理方法与设备,该处理方法中将粪便和粪污联合处理,为规模化养殖场提供粪便和污水一体化处理的技术方案。The purpose of the present invention is to provide an integrated treatment method and equipment for manure and sewage under the dry-cleaning mode of large-scale farms for the problems of low fecal sewage treatment efficiency and high construction and operation costs in existing large-scale farms. The joint treatment of manure and manure provides a technical solution for the integrated treatment of manure and sewage for large-scale farms.
为实现本发明的目的,本发明一方面提供规模化养殖场干清粪方式下的粪污一体化处理方法,其中粪便处理按如下步骤顺序进行:粪便与秸秆混合、进料、厌氧干发酵、出料、堆肥;粪污冲洗水处理按如下步骤顺序进行:固液分离、进水、厌氧发酵、好氧塘、人工湿地、出水。In order to achieve the purpose of the present invention, the present invention provides an integrated treatment method for manure and sewage under the method of dry manure cleaning in large-scale farms, wherein the manure treatment is carried out in the following order: mixing manure and straw, feeding, anaerobic dry fermentation , discharge, compost; manure flushing water treatment is carried out in the following steps: solid-liquid separation, water inflow, anaerobic fermentation, aerobic pond, artificial wetland, and water outflow.
其中,粪污冲洗水固液分离后的固体部分与粪便混合处理,粪便干发酵产生的渗滤液与粪污冲洗水混合处理,粪污冲洗水厌氧发酵后出水作为喷淋液回流至粪便厌氧干发酵阶段。Among them, the solid part of the feces flushing water after solid-liquid separation is mixed with the feces, the leachate produced by the dry fermentation of the feces is mixed with the feces flushing water, and the effluent of the fecal flushing water is returned to the feces as a spray liquid after anaerobic fermentation. Oxygen dry fermentation stage.
其中,在于秸秆与粪便混合前经过粉碎,粉碎粒径在0.5~1.5cm,优选为1cm,秸秆与粪便感干质量混合比例在1:1~1:5(w/w),优选为1:3(w/w)。Wherein, the straw is crushed before being mixed with the feces, the crushed particle size is 0.5-1.5 cm, preferably 1 cm, and the mixing ratio of the dry mass of the straw and the feces is 1:1-1:5 (w/w), preferably 1: 3(w/w).
其中,粪便的厌氧干发酵工艺可以是序批式厌氧干发酵和连续厌氧干发酵,优选为连续厌氧干发酵;所述连续厌氧干发酵工艺的发酵温度为30~56℃,优选为35~42℃,固体停留时间(SRT)为15~40天,优选为20天,喷淋量为0.1~1L/kgTS/天,优选为0.2L/kgTS/天;所述连续厌氧干发酵工艺每日排出的沼渣经过固液分离后固体部分作为接种物回流与粪便和秸秆混合,接种比例为0.5~3,优选为1。Wherein, the anaerobic dry fermentation process of feces can be sequential batch anaerobic dry fermentation and continuous anaerobic dry fermentation, preferably continuous anaerobic dry fermentation; the fermentation temperature of the continuous anaerobic dry fermentation process is 30-56 ° C, It is preferably 35-42°C, the solid residence time (SRT) is 15-40 days, preferably 20 days, and the spray volume is 0.1-1L/kgTS/day, preferably 0.2L/kgTS/day; the continuous anaerobic After the solid-liquid separation of the biogas residue discharged daily in the dry fermentation process, the solid part is refluxed as an inoculum and mixed with feces and straw, and the inoculum ratio is 0.5-3, preferably 1.
其中,粪污冲洗水的厌氧发酵工艺可以是UASB、IC、EGSB等厌氧工艺,优选为UASB工艺,水力停留时间(HRT)为8~36h,优选为12h。Wherein, the anaerobic fermentation process of excrement flushing water can be UASB, IC, EGSB and other anaerobic processes, preferably UASB process, and the hydraulic retention time (HRT) is 8-36h, preferably 12h.
本发明另一方面提供一种基于干清粪的畜禽养殖场一体化粪污处理设备,主要包括:粪便处理系统(1)、污水处理系统(2)及沼气净化系统(3)。Another aspect of the present invention provides an integrated manure treatment equipment for livestock and poultry farms based on dry manure cleaning, which mainly includes a manure treatment system (1), a sewage treatment system (2) and a biogas purification system (3).
其中,粪便处理系统由粪便与秸秆混合进料系统(101)、连续厌氧干发酵系统(102)、出料系统(103)、喷淋系统(104)组成,粪便与秸秆混合进料系统(101)通过螺杆泵(101c)与连续厌氧发酵系统(102)连接,连续厌氧干发酵系统(102)内设有喷淋装置(102a),连续厌氧发酵系统(102)外部有保温罐壁(102b);连续厌氧发酵系统(102)底部设有挤压式螺旋出料机(102c),挤压式螺旋出料机(102c)固体出口连接沼渣罐(103b),沼渣罐(103b)内的沼渣回流至粪便与秸秆混合进料系统(101);喷淋装置(102a)通过泵(203e)与高效厌氧处理系统(203)连接。Among them, the feces treatment system consists of a feces and straw mixed feeding system (101), a continuous anaerobic dry fermentation system (102), a discharge system (103), and a spraying system (104). The feces and straw mixed feeding system ( 101) Connect with the continuous anaerobic fermentation system (102) through the screw pump (101c), the continuous anaerobic dry fermentation system (102) is provided with a spraying device (102a), and the continuous anaerobic fermentation system (102) has a thermal insulation tank outside wall (102b); the bottom of the continuous anaerobic fermentation system (102) is provided with an extrusion type screw discharger (102c), and the solid outlet of the extrusion type screw discharger (102c) is connected to the biogas residue tank (103b), and the biogas residue tank The biogas residue in (103b) is returned to the feces and straw mixed feeding system (101); the spraying device (102a) is connected to the high-efficiency anaerobic treatment system (203) through a pump (203e).
其中,污水处理系统(2)主要由固液分离系统(201)、进水系统(202)、高效厌氧处理系统(203)、好氧塘(204)、人工湿地系统(205)组成,连续厌氧发酵系统(102)底部挤压式螺旋出料机(102c)液体出口连接调节罐(202b),调节罐(202b)内污水通过泵(202c)连接进入高效厌氧处理系统(203)底部的布水器(203a),处理后的污水部分经过回流泵(203e)进入连续厌氧发酵系统(102)的喷淋装置(102a),其余部分分别流经好氧塘(204)和人工湿地(205)后排出。Among them, the sewage treatment system (2) is mainly composed of a solid-liquid separation system (201), a water intake system (202), an efficient anaerobic treatment system (203), an aerobic pond (204), and a constructed wetland system (205). The liquid outlet of the extruding screw discharger (102c) at the bottom of the anaerobic fermentation system (102) is connected to the regulating tank (202b), and the sewage in the regulating tank (202b) is connected to the bottom of the high-efficiency anaerobic treatment system (203) through the pump (202c) The water distributor (203a), the treated sewage enters the spraying device (102a) of the continuous anaerobic fermentation system (102) through the return pump (203e), and the rest flows through the aerobic pond (204) and the artificial wetland respectively. (205) after discharge.
具体而言,本发明与现有技术相比有以下优点:Specifically, compared with the prior art, the present invention has the following advantages:
1)本发明中的干清粪方式下畜禽养殖场的粪污处理设备,采用连续式发酵方式,利用螺杆泵输送物料进入发酵系统,避免粪污长期堆存,降低了养殖场建设成本,提高养殖场的卫生水平。1) The manure treatment equipment of livestock and poultry farms under the dry manure cleaning method in the present invention adopts a continuous fermentation method, and uses a screw pump to transport materials into the fermentation system, avoiding long-term piling of manure and reducing the construction cost of the farm. Improve the sanitation level of farms.
2)本发明采用添加秸秆、干发酵渗滤液与粪污水混合两个手段分别提高了连续厌氧干发酵和高效厌氧处理污水的C/N,提高了粪便和污水的厌氧发酵效率。2) The present invention improves the C/N of continuous anaerobic dry fermentation and high-efficiency anaerobic treatment of sewage by adding straw and mixing dry fermentation leachate with feces and sewage, respectively, and improves the anaerobic fermentation efficiency of feces and sewage.
3)本发明可实现全程自动化,减少了人工,降低了养殖场的运行成本。3) The present invention can realize full automation, reduces labor and reduces the operating cost of the farm.
附图说明Description of drawings
图1为干清粪方式下畜禽养殖场一体化粪污处理方法设备结构示意图;Fig. 1 is a schematic diagram of the equipment structure of the livestock and poultry farm integrated manure treatment method under the dry manure mode;
图2为干清粪方式下畜禽养殖场一体化粪污处理方法设备净化装置示意图;Fig. 2 is the schematic diagram of the equipment purification device of the livestock and poultry farm integrated manure treatment method under the dry manure mode;
如图中所示,1—干粪处理系统,2—污水处理系统,3—沼气净化系统,101—干粪与秸秆混合进料系统,101a—电机,101b—螺旋绞龙,101c—螺杆泵,102—连续厌氧发酵系统,102a—发喷淋装置,102b—保温罐壁,102c—挤压式螺旋出料机,103—出料系统,103a—沼液出料口,103b—沼渣罐,103c—沼渣回流泵,104—喷淋系统,201—固液分离系统,202—进水系统,202a—Y型过滤器,202b—储存罐,202c—泵,203—高效厌氧系统,203a—布水器,203b—污泥床区,203c—三相分离器,203d—集气室,203e—沼液回流泵,204—好氧塘,205—人工湿地,301—脱水罐,302—脱硫罐,303—气体流量计。As shown in the figure, 1—dry manure treatment system, 2—sewage treatment system, 3—biogas purification system, 101—dry manure and straw mixed feeding system, 101a—motor, 101b—screw auger, 101c—screw pump , 102—continuous anaerobic fermentation system, 102a—spraying device, 102b—insulation tank wall, 102c—extrusion screw discharge machine, 103—discharging system, 103a—biogas slurry outlet, 103b—biogas residue Tank, 103c—big residue return pump, 104—spray system, 201—solid-liquid separation system, 202—water inlet system, 202a—Y-type filter, 202b—storage tank, 202c—pump, 203—high-efficiency anaerobic system , 203a—water distributor, 203b—sludge bed area, 203c—three-phase separator, 203d—gas collection chamber, 203e—biogas slurry return pump, 204—aerobic pond, 205—constructed wetland, 301—dehydration tank, 302—desulfurization tank, 303—gas flow meter.
具体实施方式detailed description
以下结合附图和实施例对本发明的具体结构和工作过程进一步的描述。The specific structure and working process of the present invention will be further described below in conjunction with the accompanying drawings and embodiments.
如图1的干清粪方式下畜禽养殖场一体化粪污处理设备结构示意图所示,规模化养殖场干清粪清出的粪便首先进行固液分离,固液分离产生的固体粪便与秸秆混合后经由干粪与秸秆混合进料系统(101)送至干粪处理系统(1)进行厌氧发酵处理,固液分离产生的粪污水进入污水处理系统(2)进行处理。As shown in Figure 1, the structure diagram of integrated manure treatment equipment for livestock and poultry farms under the dry manure cleaning method, the manure from large-scale farms is firstly subjected to solid-liquid separation, and the solid manure and straw produced by solid-liquid separation After mixing, it is sent to the dry manure treatment system (1) through the dry manure and straw mixed feeding system (101) for anaerobic fermentation treatment, and the manure and sewage generated by solid-liquid separation enters the sewage treatment system (2) for treatment.
在干粪处理系统(1)内,固体粪便与秸秆的混合原料在厌氧发酵过程中由沼液回流泵(203e)进行喷淋,喷淋液为污水处理系统(2)的出水,固体粪便与秸秆在连续厌氧发酵系统(102)内厌氧发酵后由出料系统(103)排出,并由挤压式螺旋出料机(102c)进行固液分离操作,固液分离后产生的沼渣部分作为接种物回流至混合进料系统(101)与混合原料混合,剩余部分排出,固液分离产生的沼液在与粪便固液分离产生的粪污水混合后经由Y型过滤器(202a)过滤后进入储存罐(202b)中,并由泵(202c)经由布水器(203a)泵入高效厌氧系统(203)进行处理。In the dry manure treatment system (1), the mixed raw material of solid manure and straw is sprayed by the biogas slurry return pump (203e) during the anaerobic fermentation process. The spray liquid is the effluent of the sewage treatment system (2), and the solid manure After anaerobic fermentation with straw in the continuous anaerobic fermentation system (102), it is discharged from the discharge system (103), and the solid-liquid separation operation is performed by the extruding screw discharge machine (102c), and the biogas produced after solid-liquid separation The slag part is returned to the mixed feeding system (101) as an inoculum to be mixed with the mixed raw materials, and the remaining part is discharged, and the biogas slurry produced by solid-liquid separation is mixed with the fecal water produced by solid-liquid separation of feces and passed through the Y-type filter (202a) After filtering, it enters the storage tank (202b), and is pumped into the high-efficiency anaerobic system (203) by the pump (202c) through the water distributor (203a) for treatment.
连续厌氧发酵系统(102)与高效厌氧系统(203)所产生的沼气混合后进入沼气净化系统(3)进行净化处理。The biogas generated by the continuous anaerobic fermentation system (102) and the high-efficiency anaerobic system (203) is mixed and then enters the biogas purification system (3) for purification treatment.
最后应说明的是,以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,其均应涵盖在本发明的权利要求范围当中。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention without limitation. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be Modifications or equivalent replacements without departing from the spirit and scope of the technical solutions of the present invention shall be covered by the claims of the present invention.
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