CN1480265A - Non-fermentation treatment method of organic materials - Google Patents
Non-fermentation treatment method of organic materials Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 32
- 239000011368 organic material Substances 0.000 title claims abstract description 28
- 238000000855 fermentation Methods 0.000 title claims abstract description 10
- 239000003337 fertilizer Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000002253 acid Substances 0.000 claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 12
- 230000004151 fermentation Effects 0.000 claims abstract description 9
- 230000032683 aging Effects 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 6
- 229910010272 inorganic material Inorganic materials 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 42
- 239000000843 powder Substances 0.000 claims description 18
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 14
- 238000002156 mixing Methods 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 14
- 235000019738 Limestone Nutrition 0.000 claims description 10
- 239000006028 limestone Substances 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 10
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 8
- 239000010459 dolomite Substances 0.000 claims description 8
- 229910000514 dolomite Inorganic materials 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- 239000002994 raw material Substances 0.000 claims description 7
- 239000003895 organic fertilizer Substances 0.000 claims description 6
- 238000005903 acid hydrolysis reaction Methods 0.000 claims description 5
- 230000009286 beneficial effect Effects 0.000 claims description 5
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 4
- 239000000292 calcium oxide Substances 0.000 claims description 4
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 4
- KMQAPZBMEMMKSS-UHFFFAOYSA-K calcium;magnesium;phosphate Chemical compound [Mg+2].[Ca+2].[O-]P([O-])([O-])=O KMQAPZBMEMMKSS-UHFFFAOYSA-K 0.000 claims description 4
- 230000020477 pH reduction Effects 0.000 claims description 3
- 150000004649 carbonic acid derivatives Chemical class 0.000 claims description 2
- 239000004615 ingredient Substances 0.000 claims description 2
- 239000000395 magnesium oxide Substances 0.000 claims description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- 238000007873 sieving Methods 0.000 claims description 2
- 239000010871 livestock manure Substances 0.000 abstract description 9
- 210000003608 fece Anatomy 0.000 abstract description 8
- 239000010802 sludge Substances 0.000 abstract description 7
- 239000010813 municipal solid waste Substances 0.000 abstract description 6
- 244000144972 livestock Species 0.000 abstract description 5
- 244000144977 poultry Species 0.000 abstract description 5
- 241001465754 Metazoa Species 0.000 abstract description 2
- 239000010828 animal waste Substances 0.000 abstract description 2
- 230000003647 oxidation Effects 0.000 abstract description 2
- 238000007254 oxidation reaction Methods 0.000 abstract description 2
- 239000010908 plant waste Substances 0.000 abstract description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 230000000813 microbial effect Effects 0.000 description 4
- 235000019645 odor Nutrition 0.000 description 4
- 241000244203 Caenorhabditis elegans Species 0.000 description 3
- 241000588724 Escherichia coli Species 0.000 description 3
- 238000009264 composting Methods 0.000 description 3
- 238000004332 deodorization Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 235000013601 eggs Nutrition 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 235000010216 calcium carbonate Nutrition 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 235000014380 magnesium carbonate Nutrition 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 208000016261 weight loss Diseases 0.000 description 1
- 239000013585 weight reducing agent Substances 0.000 description 1
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Abstract
本发明公开了一种有机物料无发酵处理方法;本发明利用酸碱、酸水反应产生的高温氧化和强酸环境,使有机物料快速熟化和无害化,达到农业利用要求,有机物料经预处理、混化酸解、陈化干燥、粉碎和酸度调节、农肥加工等工序,快速达到减量化、无害化、资源化的要求,具有设备投资省,处理周期短,占地少,见效快等特点,可应用于畜禽粪便、生活垃圾、各种动植物废弃物和污泥等有机质物料的无害化处理,成为有机肥料或进一步加工成有机无机复混肥料等。
The invention discloses a non-fermentation treatment method for organic materials; the invention utilizes the high-temperature oxidation and strong acid environment produced by acid-base and acid-water reactions to rapidly mature and harmless the organic materials and meet the requirements of agricultural utilization. The organic materials are pretreated , mixed acidolysis, aging and drying, crushing and acidity adjustment, agricultural fertilizer processing and other processes, quickly meet the requirements of reduction, harmlessness, and resource utilization, with low equipment investment, short processing cycle, less land occupation, and quick results It can be applied to the harmless treatment of organic materials such as livestock and poultry manure, domestic garbage, various animal and plant wastes, and sludge, and can be turned into organic fertilizers or further processed into organic-inorganic compound fertilizers.
Description
技术领域
本发明涉及有机物料处理领域,具体地讲,涉及各类有机物料无发酵,快速,无公害处理的方法。The invention relates to the field of organic material processing, in particular to a method for non-fermenting, fast and pollution-free processing of various organic materials.
背景技术 Background technique
目前,城市生活垃圾、养殖场的畜禽粪便、污泥及动植物废弃物等各类有机物料正逐年增加,数量大、体积大、臭味重,并传播病虫害等,造成生态环境污染日益严重,这些有机物料既是严重的污染源,但又是丰富的有机肥料资源,因此,如何实现这些有机物料的减量化、无害化、资源化,已成为农业、环保、卫生等多部门的注视目标。现在除填埋,焚烧,堆肥等处理方法外,还有利用烘干加粉碎,实施干燥减量处理的方法,但投资较大,难以推广。目前大都仍采用自然或接种微生物菌剂进行生物发酵堆肥的方式。但此方式也存在一些缺点,如发酵起动慢,周期长,一般需3~4周以上,甚至2个多月,并需要经常翻动,才能充分发酵;发酵期间养分损失较大,尤其是敞开式堆肥,氮素一般要损失20%以上;除臭效果不稳定;近年来,由这些有机废弃物料造成的环境压力越来越大,国家对此也越来越重视,已出台相关法律,明确规定规模养殖场的畜禽粪便排放制度与标准,因此,急需开发一种易操作、成本低、快速的有机物料无害化处理方法。At present, various organic materials such as municipal solid waste, livestock and poultry manure from farms, sludge, animal and plant waste are increasing year by year, with large quantities, large volumes, heavy odors, and the spread of pests and diseases, resulting in increasingly serious environmental pollution. , these organic materials are not only a serious source of pollution, but also rich in organic fertilizer resources. Therefore, how to realize the reduction, harmlessness, and recycling of these organic materials has become the focus of many departments such as agriculture, environmental protection, and health. . In addition to landfill, incineration, composting and other treatment methods, there is also a method of drying and crushing to implement drying and weight reduction treatment, but the investment is large and it is difficult to promote. At present, most of them still use natural or inoculated microbial agents to carry out biological fermentation and composting. However, this method also has some disadvantages, such as slow start of fermentation, long cycle, usually more than 3 to 4 weeks, or even more than 2 months, and frequent stirring is required to fully ferment; nutrient loss is relatively large during fermentation, especially in open fermentation. For composting, nitrogen generally loses more than 20%; the deodorization effect is unstable; in recent years, the environmental pressure caused by these organic waste materials is increasing, and the country is paying more and more attention to this, and relevant laws have been issued to clearly stipulate Therefore, it is urgent to develop an easy-to-operate, low-cost, and fast method for the harmless treatment of organic materials.
发明内容Contents of the invention
本发明的目的在于提供一种工艺流程短,处理速度快,杀菌效果好,除臭彻底,养分损失少,物料脱水快,投资省,成本低,便于各种规模畜禽养殖场、污泥处理场、垃圾处理场应用的、对有机质物料进行处理并再生利用的方法。The purpose of the present invention is to provide a short process flow, fast processing speed, good bactericidal effect, thorough deodorization, less nutrient loss, fast material dehydration, low investment, low cost, and is convenient for livestock and poultry farms of various scales and sludge treatment. It is a method for treating and reusing organic materials applied in landfills and garbage disposal sites.
本发明利用酸碱和酸水反应产生的高温氧化和强酸环境,使有机物料得到初步降解,水分大量散发,有害微生物被杀灭,快速达到无害化的要求。具体处理工艺是,先将有机物料分捡、破碎、含水量调节等预处理后(畜禽粪便、污泥等质地细而均一的物料可不经预处理),通过下述步骤予以实现:The invention utilizes the high-temperature oxidation and strong acid environment produced by the reaction of acid-base and acid-water to degrade organic materials preliminarily, emit a large amount of water, kill harmful microorganisms, and quickly meet the requirement of harmlessness. The specific treatment process is to first sort, crush, and adjust the water content of the organic materials after pretreatment (materials with fine and uniform texture such as livestock manure and sludge can not be pretreated), and then realize it through the following steps:
1、物料混化酸解处理:1. Material mixing and acid hydrolysis treatment:
混化配料为:含水量<80%的预处理后有机物料和占物料重3~6%的粉状碱性碳酸盐和/或粉状碱性氧化物中的一种或两种或两种以上的按任意比例组配的混合物,及占物料重6~8%的浓酸;The mixing ingredients are: one or two or two of pretreated organic materials with a water content of <80% and powdery alkaline carbonates and/or powdery basic oxides accounting for 3-6% of the weight of the materials. A mixture of more than one kind assembled in any proportion, and concentrated acid accounting for 6-8% of the weight of the material;
混化时,依次将预处理后有机物料与粉状碱性碳酸盐和/或粉状碱性氧化物送入混化机,搅拌混匀后,再将酸淋入,充分搅拌,反应产生的水蒸气、CO2、臭气等通过排气管排出,自投料至酸化降解约经10分钟后,打开混化机出料口,出料;When mixing, the pretreated organic material and powdery alkaline carbonate and/or powdery alkaline oxide are sent to the mixer in sequence, after stirring and mixing, the acid is poured in, fully stirred, and the reaction produces The water vapor, CO 2 , odor, etc. are discharged through the exhaust pipe, and after about 10 minutes from feeding to acidification degradation, open the outlet of the mixer and discharge;
2、陈化干燥处理:2. Aging and drying treatment:
出混化机物料堆置陈化24小时后,含水量进一步干燥至20~25%;After the material out of the mixer is stacked and aged for 24 hours, the water content is further dried to 20-25%;
3、粉碎及酸度调节处理:3. Crushing and acidity adjustment treatment:
将上述干燥后物料经粉碎机粉碎,过筛后,再加入量为该料重量6~15%的粉状钙镁磷肥或粉状碱性碳酸盐或粉状碱性氧化物,投入拌和机内充分搅拌,使物料酸度为pH5.5~7.0;The above-mentioned dried materials are pulverized by a pulverizer, and after sieving, the powdered calcium magnesium phosphate fertilizer or powdered alkaline carbonate or powdered alkaline oxide is added in an amount of 6-15% of the material weight, and put into a mixer Stir fully in the oven to make the acidity of the material pH 5.5-7.0;
4、农肥加工处理:4. Fertilizer processing:
中和后的粉状混化料即为有机肥料,或作为原料进一步与无机化肥按需要配制加工成有机无机复混肥,或接入有益微生物菌种制成有机生物肥料等。The neutralized powdery mixed material is an organic fertilizer, or it can be used as a raw material to further mix with inorganic fertilizers to produce organic-inorganic compound fertilizers, or it can be made into organic bio-fertilizers by adding beneficial microbial strains.
上述方法所述的粉状碱性碳酸盐为石灰石粉、白云石粉,所述粉状碱性氧化物为氧化钙、氧化镁,它们的纯度要求>70%,其中石灰石粉为优选材料。The powdery basic carbonate described in the above method is limestone powder and dolomite powder, and the powdery basic oxide is calcium oxide and magnesium oxide, and their purity requirement is >70%, wherein limestone powder is the preferred material.
上述方法所述的酸为浓度>80%的硫酸。The acid described in the above method is sulfuric acid with a concentration > 80%.
上述方法所述的粉状碱性碳酸盐或粉状碱性氧化物,颗粒径要求小于0.177毫米。The particle size of the powdery basic carbonate or powdery basic oxide described in the above method is required to be less than 0.177 mm.
本发明所述方法的有益效果,一是处理速度快,一般从进料酸化到陈化仅需24小时;二是脱水效果好,含水量70~80%的有机物料经酸水反应及硫酸与石灰石粉等碱性物质强烈中和反应,混化机内温度可达100℃左右,出料陈化后物料含水量可降至40~50%,再经常温干燥即可达到20~25%;三是养分损失少,一般畜禽粪便等有机物料经发酵处理后,氮素损失达20%以上,用本方法处理损失极少,仅2~3%;四是杀菌效果好,有机物料中所携带的大肠杆菌及蛔虫卵等经强酸、高温作用后均能杀灭;五是除臭较彻底,本法处理中仅产生水蒸气,二氧化碳,无废渣、废水排放,而物料中的硫化氢、甲硫醇等臭气物质均遭破坏并去除,可以达到无害化要求;此外,由于本方法工艺流程短,处理速度快,占地面积少,设备投资省,年处理一万吨有机物料的设备投资约需8万元左右,每吨新鲜畜禽粪便处理成本只需50元左右,因此本方法能达到减量化、无害化、资源化的要求。The beneficial effect of the method of the present invention, the one, processing speed is fast, generally only needs 24 hours from feed acidification to aging; Limestone powder and other alkaline substances have a strong neutralization reaction, the temperature inside the mixer can reach about 100°C, and the moisture content of the material can be reduced to 40-50% after discharging and aging, and it can reach 20-25% after drying at normal temperature; The 3rd, nutrient loss is few, after the organic material such as general livestock and poultry excrement is fermented, nitrogen loss reaches more than 20%, with this method processing loss is very little, only 2~3%; Escherichia coli and roundworm eggs carried can be killed by strong acid and high temperature; fifth, the deodorization is more thorough, only water vapor and carbon dioxide are produced in the treatment of this method, and there is no waste residue and waste water discharge, while hydrogen sulfide, Odor substances such as methyl mercaptan are destroyed and removed, which can meet the requirements of harmlessness; in addition, due to the short process flow of this method, fast processing speed, small floor area and low equipment investment, it can process 10,000 tons of organic materials per year. The equipment investment is about 80,000 yuan, and the processing cost per ton of fresh livestock and poultry manure is only about 50 yuan. Therefore, this method can meet the requirements of reduction, harmlessness, and resource utilization.
附图说明Description of drawings
图1是有机物料应用本法处理工艺流程示意图;Fig. 1 is a schematic diagram of the process flow of organic material application of this method;
图2是物料混化机结构示意图。Figure 2 is a schematic diagram of the material mixer.
具体实施方式 Detailed ways
下面结合附图对本发明作进一步的描述。The present invention will be further described below in conjunction with the accompanying drawings.
实施例1:具体步骤按照图1流程示意图操作:Embodiment 1: The specific steps are operated according to the schematic flow chart in Figure 1:
1)备料:含水量<80%的新鲜猪粪500公斤;CaCO3含量>70%,其颗粒径小于0.177毫米的石灰石粉20公斤;浓度>80%的硫酸35公斤;CaCO3+MgCO3含量>70%,其颗粒径小于0.177毫米白云石粉20公斤。猪粪质地较均匀,一般可不需要预处理。1) Raw materials: 500 kg of fresh pig manure with a water content of <80%; 20 kg of limestone powder with a CaCO3 content of >70% and a particle size of less than 0.177 mm; 35 kg of sulfuric acid with a concentration of >80%; CaCO3 + MgCO3 content >70%, 20 kg of dolomite powder whose particle size is less than 0.177 mm. The texture of pig manure is relatively uniform, and generally no pretreatment is required.
2)物料混化酸解处理:首先打开排气管4,通过提升装置6,先将猪粪,石灰石粉送入不锈钢混化机进料口1,经搅拌器3充分搅拌,3~4分钟后通过浓酸进口2将硫酸淋入,继续搅拌4~5分钟,此时混化机内物料所含的水分、石灰石粉及硫酸相接触,产生强烈的酸碱中和反应和酸水反应,产生大量的热量,混化机内温度可达100℃左右,大量的水汽,二氧化碳等,通过排气管4排出,在此过程中,猪粪中的大肠杆菌、蛔虫卵等被杀灭,硫化氢、甲硫醇等臭气物质遭到破坏而消除;在此反应过程中既无废渣,也无废水排放,因而可达到无公害要求。每批次处理,自投料至出料口5出料,全过程仅需10分钟左右;2) Material mixing acid hydrolysis treatment: firstly open the exhaust pipe 4, through the lifting device 6, first send pig manure and limestone powder into the
3)陈化干燥处理:出混化机物料堆置陈化24小时后,此时水分含量已降至40~50%,进一步经常温干燥或日晒,直至混化料含水量降至20~25%;3) Aging and drying treatment: After the materials out of the mixer are stacked and aged for 24 hours, the moisture content has dropped to 40-50% at this time, and then they are further dried at regular temperature or exposed to the sun until the moisture content of the mixed material drops to 20-50%. 25%;
4)粉碎及酸度调节处理:将干燥后的上述物料经粉碎机粉碎,过筛,要求其颗粒径0.5mm以下者占70%以上时为标准,投入拌和机内,再加入白云石粉20公斤,充分搅拌混匀后,混化料酸度逐步中和至pH5.5~7.0;4) Grinding and acidity adjustment treatment: the above-mentioned materials after drying are pulverized through a pulverizer, sieved, and it is required that those with a particle diameter below 0.5mm account for more than 70% as a standard, put it into a mixer, and then add 20 kg of dolomite powder, After fully stirring and mixing, the acidity of the mixed material is gradually neutralized to pH 5.5-7.0;
5)农肥加工处理:中和后的粉状混化料,既可直接作为有机肥料,也可作为原料,进一步加工制成有机无机复混肥,或接入有益微生物菌种制成有机生物肥料等。上述工艺,按一年处理新鲜猪粪万吨以上设计,设备投资约8万元左右,每吨处理成本价仅50元左右,该处理品经测定,其干基全氮量为1.90%,全磷3.0%,全钾1.7%,在处理产物中无活的大肠杆菌和蛔虫卵等检出。5) Fertilizer processing: The neutralized powdery mixed material can be directly used as an organic fertilizer or as a raw material to be further processed into an organic-inorganic compound fertilizer, or incorporated into beneficial microbial strains to make an organic bio-fertilizer wait. The above-mentioned process is designed to process more than 10,000 tons of fresh pig manure a year. The equipment investment is about 80,000 yuan, and the processing cost per ton is only about 50 yuan. Phosphorus 3.0%, total potassium 1.7%, no live Escherichia coli and roundworm eggs were detected in the treated products.
实施例2:Example 2:
1)生活垃圾首先要经过分捡、破碎、水分调节等预处理,以提高下一步的混化处理效果;1) Household garbage must first undergo pretreatment such as sorting, crushing, and moisture adjustment to improve the effect of the next step of mixing treatment;
2)备料:含水量<80%的生活垃圾500公斤;CaCO3+MgCO3含量>70%,其颗粒径小于0.177毫米的白云石粉20公斤;浓度>80%的硫酸35公斤;有效磷(P2O5)≥12%的粉状钙镁磷肥30公斤。2) Raw material preparation: 500 kilograms of domestic garbage with a water content of <80%; 20 kilograms of dolomite powder with a CaCO 3 + MgCO content > 70% and a particle size of less than 0.177 mm; 35 kilograms of sulfuric acid with a concentration >80%; available phosphorus (P 2 O 5 ) ≥ 12% powdered calcium magnesium phosphate fertilizer 30 kg.
3)物料混化酸解处理:先打开排气管4,通过提升装置6,先将生活垃圾,白云石粉送入混化机进料口1,经搅拌器3充分搅拌,3~4分钟后通过浓酸进口2将硫酸淋入,继续搅拌4~5分钟后出料;3) Material mixing and acid hydrolysis treatment: firstly open the exhaust pipe 4, through the lifting device 6, first send domestic garbage and dolomite powder into the
4)陈化干燥处理:出混化机物料堆置陈化24小时后,此时水分含量已降至40~50%,进一步常温干燥或日晒,直至混化料含水量降至20~25%;4) Aging and drying treatment: After the materials out of the mixer are piled up and aged for 24 hours, the moisture content has dropped to 40-50%, and further dried at room temperature or exposed to the sun until the moisture content of the mixed material drops to 20-25%. %;
5)粉碎及酸度调节处理:将干燥后的上述物料经粉碎机粉碎,过筛,要求其颗粒径0.5mm以下占70%以上时为标准,全部投入拌和机内,加入粉状钙镁磷肥30公斤,充分搅拌混匀后,混化料酸度逐步中和至pH5.5~7.0;5) Pulverization and acidity adjustment treatment: pulverize the dried above-mentioned materials through a pulverizer, sieve, and require that the particle diameter is less than 0.5mm and account for more than 70% as the standard, put them all into the mixer, and add powdered calcium magnesium phosphate fertilizer 30 After fully stirring and mixing, the acidity of the mixed material is gradually neutralized to pH 5.5-7.0;
6)农肥加工处理:中和后的粉状混化料,既可直接作为有机肥料,也可作为原料,进一步加工制成有机无机复混肥,或接入有益微生物菌种制成有机生物肥料等。6) Fertilizer processing: The neutralized powdery mixed material can be directly used as an organic fertilizer or as a raw material to be further processed into an organic-inorganic compound fertilizer, or incorporated into beneficial microbial strains to make an organic bio-fertilizer wait.
实施例3:Example 3:
1)备料:含水量<80%的污泥500公斤;其颗粒径小于0.177毫米的石灰石粉(CaCO3含量>70%)与氧化钙按1∶1比例的混合物16公斤;浓度>80%的磷酸3 5公斤;CaCO3+MgCO3含量>70%,其颗粒径小于0.177毫米的白云石粉20公斤;1) Material preparation: 500 kg of sludge with a water content of <80%; 16 kg of a mixture of limestone powder (CaCO 3 content > 70%) and calcium oxide with a particle size of less than 0.177 mm in a ratio of 1:1; 3 to 5 kg of phosphoric acid; 20 kg of dolomite powder with a CaCO 3 +MgCO 3 content > 70% and a particle size of less than 0.177 mm;
2)物料混化酸解处理:打开排气管4,通过提升装置6,先将污泥,石灰石粉与氧化钙混合物送入混化机进料口1,经搅拌器3充分搅拌,3~4分钟后通过浓酸进口2将磷酸淋入,继续搅拌4~5分钟后出料;2) Material mixed acid hydrolysis treatment: open the exhaust pipe 4, and through the lifting device 6, firstly send the mixture of sludge, limestone powder and calcium oxide into the
3)陈化干燥处理:出混化机物料堆置陈化24小时后,此时水分含量已降至40~50%;进一步常温干燥或日晒,直至混化料含水量降至20~25%;3) Aging and drying treatment: After the materials out of the mixer are stacked and aged for 24 hours, the moisture content has dropped to 40-50% at this time; further drying at room temperature or sunlight until the moisture content of the mixed material drops to 20-25% %;
4)粉碎及酸度调节处理:将干燥后的上述物料经粉碎机粉碎,过筛,要求其颗粒径0.5mm以下占70%以上时为标准,全部投入拌和机内,加入白云石粉20公斤,充分搅拌混匀后,混化料酸度逐步中和至pH5.5~7.0;4) Grinding and acidity adjustment treatment: the above-mentioned materials after drying are pulverized through a pulverizer, sieved, and it is required that the particle diameter below 0.5 mm accounts for more than 70% as a standard, and all of them are put into the mixer, and 20 kg of dolomite powder is added, fully After stirring and mixing, the acidity of the mixed material is gradually neutralized to pH 5.5-7.0;
5)农肥加工处理:中和后的粉状混化料,既可直接作为有机肥料,也可作为原料,进一步加工制成污泥复混肥。5) Fertilizer processing: The neutralized powdery mixed material can be directly used as an organic fertilizer or as a raw material to be further processed into a sludge compound fertilizer.
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101134633B (en) * | 2007-07-27 | 2012-10-03 | 苏州金桨节能与环保科技有限公司 | Material and method for materialized sludge deweighting process |
| CN103113013A (en) * | 2013-02-01 | 2013-05-22 | 深圳市水务(集团)有限公司 | Compound type sludge dewatering conditioner and application method thereof |
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| CN101134633B (en) * | 2007-07-27 | 2012-10-03 | 苏州金桨节能与环保科技有限公司 | Material and method for materialized sludge deweighting process |
| CN103113013A (en) * | 2013-02-01 | 2013-05-22 | 深圳市水务(集团)有限公司 | Compound type sludge dewatering conditioner and application method thereof |
| CN103508760A (en) * | 2013-10-10 | 2014-01-15 | 宣城市南阳生物科技有限公司 | Method for utilizing chicken manure to produce organic fertilizer |
| CN103508760B (en) * | 2013-10-10 | 2015-01-21 | 宣城市南阳生物科技有限公司 | Method for utilizing chicken manure to produce organic fertilizer |
| CN104129897A (en) * | 2014-08-15 | 2014-11-05 | 浙江方远建材科技有限公司 | Dehydration technology of domestic sludge |
| CN104129897B (en) * | 2014-08-15 | 2016-06-29 | 浙江方远建材科技有限公司 | The dewatering process of one way of life mud |
| CN104876779A (en) * | 2015-05-19 | 2015-09-02 | 珠海农神生物科技有限公司 | Method for preparing water-retaining biological organic fertilizer by using high-water-content poultry and livestock manure |
| CN104961507A (en) * | 2015-06-04 | 2015-10-07 | 贵州汇民力生物科技有限公司 | Organic fertilizer containing wormcast and chicken manure and preparation method thereof |
| CN112778036A (en) * | 2021-01-08 | 2021-05-11 | 贵州明威环保技术有限公司 | Method for producing organic fertilizer from landscaping waste |
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