CN114455997A - A method for preparing biochar base fertilizer based on hydrothermal carbonization - Google Patents
A method for preparing biochar base fertilizer based on hydrothermal carbonization Download PDFInfo
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims abstract description 45
- 238000003763 carbonization Methods 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000000463 material Substances 0.000 claims abstract description 19
- 238000005191 phase separation Methods 0.000 claims abstract description 19
- 239000007790 solid phase Substances 0.000 claims abstract description 19
- 239000002904 solvent Substances 0.000 claims abstract description 18
- 239000000203 mixture Substances 0.000 claims abstract description 16
- 230000020477 pH reduction Effects 0.000 claims abstract description 15
- 239000011230 binding agent Substances 0.000 claims abstract description 14
- 239000010806 kitchen waste Substances 0.000 claims abstract description 13
- 238000002156 mixing Methods 0.000 claims abstract description 13
- 239000000047 product Substances 0.000 claims abstract description 13
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000292 calcium oxide Substances 0.000 claims abstract description 12
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 7
- 238000001027 hydrothermal synthesis Methods 0.000 claims abstract description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 30
- 230000002378 acidificating effect Effects 0.000 claims description 17
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 15
- 229910052757 nitrogen Inorganic materials 0.000 claims description 15
- 239000011591 potassium Substances 0.000 claims description 15
- 229910052700 potassium Inorganic materials 0.000 claims description 15
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 7
- 239000004202 carbamide Substances 0.000 claims description 7
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 7
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 7
- 235000011151 potassium sulphates Nutrition 0.000 claims description 7
- 238000007873 sieving Methods 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 claims description 6
- 229920000881 Modified starch Polymers 0.000 claims description 5
- 239000004368 Modified starch Substances 0.000 claims description 5
- 235000019426 modified starch Nutrition 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 2
- YYRMJZQKEFZXMX-UHFFFAOYSA-L calcium bis(dihydrogenphosphate) Chemical compound [Ca+2].OP(O)([O-])=O.OP(O)([O-])=O YYRMJZQKEFZXMX-UHFFFAOYSA-L 0.000 claims 2
- 229910000389 calcium phosphate Inorganic materials 0.000 claims 2
- 235000019691 monocalcium phosphate Nutrition 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 1
- 239000012071 phase Substances 0.000 claims 1
- 238000005086 pumping Methods 0.000 claims 1
- 150000003839 salts Chemical class 0.000 abstract description 11
- 239000002994 raw material Substances 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 239000002028 Biomass Substances 0.000 abstract description 5
- 239000003610 charcoal Substances 0.000 abstract description 2
- 238000002360 preparation method Methods 0.000 abstract description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 11
- 229910052799 carbon Inorganic materials 0.000 description 11
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 10
- 229910052698 phosphorus Inorganic materials 0.000 description 10
- 239000011574 phosphorus Substances 0.000 description 10
- 235000015097 nutrients Nutrition 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 6
- 239000005416 organic matter Substances 0.000 description 6
- 239000011148 porous material Substances 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 6
- YYRMJZQKEFZXMX-UHFFFAOYSA-N calcium;phosphoric acid Chemical compound [Ca+2].OP(O)(O)=O.OP(O)(O)=O YYRMJZQKEFZXMX-UHFFFAOYSA-N 0.000 description 5
- 235000021049 nutrient content Nutrition 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000002426 superphosphate Substances 0.000 description 5
- YWEUIGNSBFLMFL-UHFFFAOYSA-N diphosphonate Chemical compound O=P(=O)OP(=O)=O YWEUIGNSBFLMFL-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000004537 pulping Methods 0.000 description 4
- 239000004576 sand Substances 0.000 description 4
- 230000003139 buffering effect Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000003575 carbonaceous material Substances 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 239000010794 food waste Substances 0.000 description 2
- 239000003864 humus Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000036983 biotransformation Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B1/00—Superphosphates, i.e. fertilisers produced by reacting rock or bone phosphates with sulfuric or phosphoric acid in such amounts and concentrations as to yield solid products directly
- C05B1/02—Superphosphates
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/10—Solid or semi-solid fertilisers, e.g. powders
- C05G5/12—Granules or flakes
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Pest Control & Pesticides (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
本发明属于生物炭基肥制备技术领域,公开了一种基于水热碳化法制备生物炭基肥的方法,包括:三相分离餐厨垃圾,获得有机固相物料;将所述有机固相物料与酸性溶剂混合,并水热酸化处理;将所述水热酸化处理的产物泵送至水热反应釜内,180~250℃水热碳化90~240min,反应产物经冷却、脱水、干燥后形成生物炭基;将所述生物炭基与无机化肥、氧化钙、粘结剂、水混合,混合物经挤压造粒得到生物炭基颗粒肥料;综上,在本发明所提供的方法中,以经过三相分离餐厨垃圾后获得的有机固相物料作为水热碳化反应的原料,并且还进行热水酸化预处理,基于此有效解决了反应后产物不纯、高油高盐的缺点,进而有效提高了生物质炭的品质。The invention belongs to the technical field of biochar base fertilizer preparation, and discloses a method for preparing biochar base fertilizer based on a hydrothermal carbonization method. The solvent is mixed, and hydrothermally acidified; the product of the hydrothermal acidification is pumped into the hydrothermal reaction kettle, and hydrothermally carbonized at 180 to 250 ° C for 90 to 240 minutes, and the reaction product is cooled, dehydrated, and dried to form biochar base; mixing the biochar base with inorganic fertilizer, calcium oxide, binder, and water, and extruding the mixture to obtain biochar-based granular fertilizer; The organic solid phase material obtained after the phase separation of the kitchen waste is used as the raw material for the hydrothermal carbonization reaction, and is also pretreated by hot water acidification. Based on this, the shortcomings of impure products, high oil and high salt after the reaction are effectively solved, and the quality of biomass charcoal.
Description
技术领域technical field
本发明属于生物炭基肥制备技术领域,具体涉及一种基于水热碳化法制备生物炭基肥的方法。The invention belongs to the technical field of biochar base fertilizer preparation, and in particular relates to a method for preparing biochar base fertilizer based on a hydrothermal carbonization method.
背景技术Background technique
近年来,应用水热碳化法处理餐厨垃圾受到格外关注,相对于其他的热化学(裂解、液化)及生物转化(发酵、堆肥) 技术,水热炭化具有原料无需干燥、能耗低、设备体积小、炭固定效率高、产物易储存运输等优点,在处理含水率高、分散的有机废弃物方面具有显著的优势。In recent years, the application of hydrothermal carbonization to treat food waste has received special attention. Compared with other thermochemical (pyrolysis, liquefaction) and biotransformation (fermentation, composting) technologies, hydrothermal carbonization has the advantages of no drying of raw materials, low energy consumption, and equipment. It has the advantages of small size, high carbon fixation efficiency, and easy storage and transportation of products. It has significant advantages in treating organic wastes with high moisture content and dispersion.
水热碳化是指在一个密闭的体系中,以碳水化合物或木质纤维素为原料,以水为反应媒介,在一定的温度(180~250℃)及自产生的压力下,原料经过一系列复杂反应而转化成碳材料的过程,所形成的生物质炭材料具有发达的孔隙结构、高的比表面积、稳定的芳香族结构和丰富的表面官能团等特点,具有吸附能力强、化学性质稳定和再生能力强等优点。Hydrothermal carbonization means that in a closed system, using carbohydrates or lignocellulose as raw materials and water as the reaction medium, under a certain temperature (180-250 ° C) and self-generated pressure, the raw materials undergo a series of complex processes. The process of converting into carbon materials by reaction, the formed biomass carbon materials have the characteristics of developed pore structure, high specific surface area, stable aromatic structure and abundant surface functional groups, etc., with strong adsorption capacity, stable chemical properties and regeneration. The advantages of strong ability and so on.
目前国内外餐厨垃圾处理的主流工艺路线主要包括“预处理、资源化处理和产品资源化利用”三个阶段。餐厨垃圾经分拣、除砂、破碎、制浆以及油-水-固三相分离等预处理后形成的有机固相物料,通常采用湿/干式厌氧硝化、肥料化或蛋白饲料化等资源化处理工艺进一步进行产品资源化利用,其中肥料化技术因存在杀菌不彻底,肥料含盐量高、养分配比失调,且堆肥处理周期较长,占地面积大,卫生条件相对较差等缺点而受到限制应用,亟需发展新的提高肥料品质的工艺技术是将来的必然趋势。At present, the mainstream process route of kitchen waste treatment at home and abroad mainly includes three stages: "pretreatment, resource treatment and product resource utilization". The organic solid phase material formed by the pretreatment of food waste through sorting, sand removal, crushing, pulping and oil-water-solid three-phase separation, usually using wet/dry anaerobic nitrification, fertilizer or protein feed Other resource-based treatment processes are used to further utilize product resources. Among them, the fertilizer technology is due to incomplete sterilization, high fertilizer salt content, unbalanced nutrient distribution ratio, long compost treatment cycle, large area and relatively poor sanitation conditions. It is an inevitable trend in the future to develop new technology to improve fertilizer quality.
已有报道,餐厨垃圾水热碳化后的生物质炭产物可以扩展应用于燃料能源、生态环保、电极电容和碳复合材料等多种领域(王楠,2016,环境科学与技术,39卷第S2期)。生物炭基肥被誉为一种新型绿色环保肥料,目前生物质炭和肥料复合已成为生物炭基肥新的发展方向看,然而利用餐厨垃圾经水热碳化法所产生的生物质炭作为制备生物炭基肥的原材料研究仍未见相关报道。另外,餐厨垃圾若不经过预处理而直接进行水热碳化,会造成产物成分复杂、高油高盐、碳产出率低等问题,与肥料复合后并不利于提高肥料品质,并且作为肥料应用于田地,仍然缺乏作物所需的各种养分。It has been reported that the biomass carbon products after hydrothermal carbonization of kitchen waste can be extended to various fields such as fuel energy, ecological environment protection, electrode capacitors and carbon composite materials (Wang Nan, 2016, Environmental Science and Technology, Vol. 39, S2 Expect). Biochar-based fertilizer is known as a new type of green and environmentally friendly fertilizer. At present, the combination of biomass charcoal and fertilizer has become a new development direction of biochar-based fertilizer. There are still no relevant reports on the research on raw materials of carbon-based fertilizers. In addition, if the kitchen waste is directly hydrothermally carbonized without pretreatment, it will cause problems such as complex product composition, high oil and high salt, and low carbon yield. After compounding with fertilizer, it is not conducive to improving the quality of fertilizer, and as a fertilizer Applied to the field, it still lacks various nutrients needed by crops.
发明内容SUMMARY OF THE INVENTION
鉴于此,为解决上述背景技术中所提出的问题,本发明的目的在于提供一种基于水热碳化法制备生物炭基肥的方法。In view of this, in order to solve the problems raised in the above background technology, the purpose of the present invention is to provide a method for preparing biochar-based fertilizer based on a hydrothermal carbonization method.
为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:
一种基于水热碳化法制备生物炭基肥的方法,包括:A method for preparing biochar base fertilizer based on a hydrothermal carbonization method, comprising:
三相分离餐厨垃圾,获得有机固相物料;Three-phase separation of kitchen waste to obtain organic solid materials;
将所述有机固相物料与酸性溶剂混合,并水热酸化处理;Mixing the organic solid phase material with an acidic solvent, and performing hydrothermal acidification treatment;
将所述水热酸化处理的产物泵送至水热反应釜内,180~250℃水热碳化90~240min,反应产物经冷却、脱水、干燥后形成生物炭基;The product of the hydrothermal acidification treatment is pumped into a hydrothermal reaction kettle, and hydrothermally carbonized at 180-250° C. for 90-240 min, and the reaction product is cooled, dehydrated and dried to form a biochar base;
将所述生物炭基与无机化肥、氧化钙、粘结剂、水混合,混合物经挤压造粒得到生物炭基颗粒肥料。The biochar base is mixed with inorganic fertilizer, calcium oxide, binder and water, and the mixture is extruded and granulated to obtain biochar based granular fertilizer.
优选的,所述三相分离为油-水-固三相分离。Preferably, the three-phase separation is oil-water-solid three-phase separation.
优选的,所述酸性溶剂的PH值为2~3,且所述酸性溶剂包括水和浓度为0.01mol/L的HCL溶液。Preferably, the pH value of the acidic solvent is 2-3, and the acidic solvent includes water and HCL solution with a concentration of 0.01 mol/L.
优选的,所述有机固相物料与酸性溶剂混合后的含水率为70~85%。Preferably, the water content of the organic solid phase material after mixing with the acidic solvent is 70-85%.
优选的,在所述水热酸化处理中:处理温度为20~30℃,处理时间为10~20min。Preferably, in the hydrothermal acidification treatment: the treatment temperature is 20-30° C., and the treatment time is 10-20 min.
优选的,将所述生物炭基与无机化肥、氧化钙、粘结剂、水混合时包括:Preferably, when the biochar base is mixed with inorganic fertilizer, calcium oxide, binder, and water, it includes:
200~300Rad/min混合搅拌所述生物炭基、无机化肥与氧化钙,搅拌40min后粉碎并利用16目筛网过筛;Mix and stir the biochar, inorganic fertilizer and calcium oxide at 200-300 Rad/min, pulverize after stirring for 40 minutes, and sieve with a 16-mesh screen;
向过筛得到的粉料中添加粘结剂和水,混合均匀。Add binder and water to the powder obtained by sieving and mix well.
优选的,所述生物炭基、无机化肥与氧化钙的混合百分比为55~65%:20~40%:5~8%;所述粘结剂占混合物总量的2~5%,所述水占混合物总量的5~10%。Preferably, the mixing percentage of the biochar, inorganic fertilizer and calcium oxide is 55-65%: 20-40%: 5-8%; the binder accounts for 2-5% of the total amount of the mixture, and the Water accounts for 5 to 10% of the total mixture.
优选的,所述无机化肥包括12~20%尿素、6~10%过磷酸钙和5~10%硫酸钾。Preferably, the inorganic fertilizer includes 12-20% urea, 6-10% superphosphate and 5-10% potassium sulfate.
优选的,所述尿素中氮含量为46%;所述过磷酸钙中五氧化二磷含量为18%;所述硫酸钾中钾含量为50%。Preferably, the nitrogen content in the urea is 46%; the phosphorus pentoxide content in the superphosphate is 18%; the potassium content in the potassium sulfate is 50%.
优选的,所述粘结剂采用改性淀粉。Preferably, the binder is modified starch.
本发明与现有技术相比,具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
在本发明所提供的方法中,以经过三相分离餐厨垃圾后获得的有机固相物料作为水热碳化反应的原料,并且还进行热水酸化预处理,基于此有效解决了反应后产物不纯、高油高盐的缺点,进而有效提高了生物质炭的品质。另外,利用生物炭复合无机肥制肥技术,实现生物炭基肥各成分的精准配比,并有效提高肥料品质。In the method provided by the present invention, the organic solid phase material obtained after the three-phase separation of kitchen waste is used as the raw material for the hydrothermal carbonization reaction, and the hot water acidification pretreatment is also performed. The shortcomings of pure, high oil and high salt, thus effectively improving the quality of biomass carbon. In addition, the use of biochar compound inorganic fertilizer fertilizer technology can realize the precise ratio of each component of biochar base fertilizer, and effectively improve the quality of fertilizer.
具体实施方式Detailed ways
下面对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be described clearly and completely below. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
实施例1Example 1
一种基于水热碳化法制备生物炭基肥的方法,包括:A method for preparing biochar base fertilizer based on a hydrothermal carbonization method, comprising:
三相分离餐厨垃圾,获得有机固相物料;其中三相分离包括缓存、沥水、分选、制浆、除砂、提油等操作,实现油-水-固三相分离;Three-phase separation of kitchen waste to obtain organic solid-phase materials; the three-phase separation includes operations such as buffering, draining, sorting, pulping, sand removal, and oil extraction to achieve oil-water-solid three-phase separation;
将有机固相物料泵送至水热预反应器中,添加包括水和HCL溶液的酸性溶剂,其中酸性溶剂的PH值为2,HCL溶液的浓度为0.01mol/L,且有机固相物料与酸性溶剂混合后的含水率为85%,25℃水热酸化处理10min;The organic solid phase material is pumped into the hydrothermal pre-reactor, and an acidic solvent including water and HCL solution is added, wherein the pH value of the acidic solvent is 2, the concentration of the HCL solution is 0.01 mol/L, and the organic solid phase material is combined with the HCL solution. The water content after mixing the acidic solvent is 85%, and the hydrothermal acidification treatment is performed at 25 °C for 10 minutes;
将水热酸化处理的产物泵送至水热反应釜内,250℃水热碳化120min,反应产物经冷却、脱水、干燥后形成生物炭基;The product of hydrothermal acidification treatment is pumped into the hydrothermal reaction kettle, and hydrothermally carbonized at 250°C for 120 minutes, and the reaction product is cooled, dehydrated and dried to form a biochar base;
将60%生物炭基、20%尿素(其中氮含量为46%)、10%过磷酸钙(其中五氧化二磷含量为18%)、5%硫酸钾(其中钾含量为50%)和5%氧化钙在250Rad/min的速度下混合搅拌40min,然后粉碎并利用16目筛网过筛;60% biochar based, 20% urea (46% nitrogen), 10% superphosphate (18% phosphorus pentoxide), 5% potassium sulfate (50% potassium) and 5 % calcium oxide was mixed and stirred for 40min at a speed of 250Rad/min, then pulverized and sieved with a 16-mesh sieve;
向过筛得到的粉料中添加2%的粘结剂(改性淀粉)和10%的水,混合均匀;Add 2% binder (modified starch) and 10% water to the powder obtained by sieving, and mix well;
混合物经挤压造粒得到生物炭基颗粒肥料。The mixture is extruded and granulated to obtain biochar-based granular fertilizer.
上述,在本实施例中所制成的生物炭基具有41.4%的碳产生率,5.01m/g的比表面积,4.88nm的平均吸附孔径,且其中腐殖质含量为38%,有机质含量为62%,盐分为0.22%,包括氮磷钾的总养分为4.9%;As mentioned above, the biochar base prepared in this example has a carbon production rate of 41.4%, a specific surface area of 5.01 m/g, an average adsorption pore size of 4.88 nm, and wherein the humic substance content is 38%, and the organic matter content is 62%. , the salt content is 0.22%, and the total nutrients including nitrogen, phosphorus and potassium are 4.9%;
另外,在本实施例中所制成的生物炭基颗粒肥料中包括氮磷钾的总养分含量超过25%,生物炭含量为55%。In addition, the total nutrient content of nitrogen, phosphorus and potassium in the biochar-based granular fertilizer prepared in this example exceeds 25%, and the biochar content is 55%.
实施例2Example 2
一种基于水热碳化法制备生物炭基肥的方法,包括:A method for preparing biochar base fertilizer based on a hydrothermal carbonization method, comprising:
三相分离餐厨垃圾,获得有机固相物料;其中三相分离包括缓存、沥水、分选、制浆、除砂、提油等操作,实现油-水-固三相分离;Three-phase separation of kitchen waste to obtain organic solid-phase materials; the three-phase separation includes operations such as buffering, draining, sorting, pulping, sand removal, and oil extraction to achieve oil-water-solid three-phase separation;
将有机固相物料泵送至水热预反应器中,添加包括水和HCL溶液的酸性溶剂,其中酸性溶剂的PH值为3,HCL溶液的浓度为0.01mol/L,且有机固相物料与酸性溶剂混合后的含水率为80%,25℃水热酸化处理20min;The organic solid phase material is pumped into the hydrothermal pre-reactor, and an acidic solvent including water and HCL solution is added, wherein the pH value of the acidic solvent is 3, the concentration of the HCL solution is 0.01 mol/L, and the organic solid phase material is combined with the HCL solution. The water content after mixing with the acidic solvent is 80%, and the hydrothermal acidification treatment is carried out at 25°C for 20min;
将水热酸化处理的产物泵送至水热反应釜内,220℃水热碳化180min,反应产物经冷却、脱水、干燥后形成生物炭基;The product of hydrothermal acidification is pumped into a hydrothermal reaction kettle, and hydrothermally carbonized at 220°C for 180 minutes, and the reaction product is cooled, dehydrated and dried to form a biochar base;
将65%生物炭基、12%尿素(其中氮含量为46%)、10%过磷酸钙(其中五氧化二磷含量为18%)、5%硫酸钾(其中钾含量为50%)和8%氧化钙在200Rad/min的速度下混合搅拌40min,然后粉碎并利用16目筛网过筛;65% biochar based, 12% urea (46% nitrogen), 10% superphosphate (18% phosphorus pentoxide), 5% potassium sulfate (50% potassium) and 8 % calcium oxide was mixed and stirred for 40min at a speed of 200Rad/min, then pulverized and sieved with a 16-mesh sieve;
向过筛得到的粉料中添加2%的粘结剂(改性淀粉)和10%的水,混合均匀;Add 2% binder (modified starch) and 10% water to the powder obtained by sieving, and mix well;
混合物经挤压造粒得到生物炭基颗粒肥料。The mixture is extruded and granulated to obtain biochar-based granular fertilizer.
上述,在本实施例中所制成的生物炭基具有52.7%的碳产生率,8.45m/g的比表面积,6.23nm的平均吸附孔径,且其中腐殖质含量为40%,有机质含量为72%,盐分为0.22%,包括氮磷钾的总养分为6.7%;As mentioned above, the biochar base prepared in this example has a carbon production rate of 52.7%, a specific surface area of 8.45m/g, an average adsorption pore size of 6.23nm, and wherein the humic substance content is 40%, and the organic matter content is 72% , the salt content is 0.22%, and the total nutrients including nitrogen, phosphorus and potassium are 6.7%;
另外,在本实施例中所制成的生物炭基颗粒肥料中包括氮磷钾的总养分含量超过25%,生物炭含量为65%。In addition, the total nutrient content of nitrogen, phosphorus and potassium in the biochar-based granular fertilizer prepared in this example exceeds 25%, and the biochar content is 65%.
实施例3Example 3
一种基于水热碳化法制备生物炭基肥的方法,包括:A method for preparing biochar base fertilizer based on a hydrothermal carbonization method, comprising:
三相分离餐厨垃圾,获得有机固相物料;其中三相分离包括缓存、沥水、分选、制浆、除砂、提油等操作,实现油-水-固三相分离;Three-phase separation of kitchen waste to obtain organic solid-phase materials; the three-phase separation includes operations such as buffering, draining, sorting, pulping, sand removal, and oil extraction to achieve oil-water-solid three-phase separation;
将有机固相物料泵送至水热预反应器中,添加包括水和HCL溶液的酸性溶剂,其中酸性溶剂的PH值为3,HCL溶液的浓度为0.01mol/L,且有机固相物料与酸性溶剂混合后的含水率为80%,30℃水热酸化处理20min;The organic solid phase material is pumped into the hydrothermal pre-reactor, and an acidic solvent including water and HCL solution is added, wherein the pH value of the acidic solvent is 3, the concentration of the HCL solution is 0.01 mol/L, and the organic solid phase material is combined with the HCL solution. The water content after mixing with the acidic solvent is 80%, and the hydrothermal acidification treatment is carried out at 30°C for 20min;
将水热酸化处理的产物泵送至水热反应釜内,180℃水热碳化240min,反应产物经冷却、脱水、干燥后形成生物炭基;The product of hydrothermal acidification treatment was pumped into the hydrothermal reaction kettle, and hydrothermally carbonized at 180 °C for 240 min, and the reaction product was cooled, dehydrated and dried to form a biochar base;
将55%生物炭基、20%尿素(其中氮含量为46%)、10%过磷酸钙(其中五氧化二磷含量为18%)、10%硫酸钾(其中钾含量为50%)和8%氧化钙在300Rad/min的速度下混合搅拌40min,然后粉碎并利用16目筛网过筛;55% biochar based, 20% urea (46% nitrogen), 10% superphosphate (18% phosphorus pentoxide), 10% potassium sulfate (50% potassium) and 8 % calcium oxide was mixed and stirred for 40min at a speed of 300Rad/min, then pulverized and sieved with a 16-mesh sieve;
向过筛得到的粉料中添加4%的粘结剂(改性淀粉)和6%的水,混合均匀;Add 4% binder (modified starch) and 6% water to the powder obtained by sieving, and mix well;
混合物经挤压造粒得到生物炭基颗粒肥料。The mixture is extruded and granulated to obtain biochar-based granular fertilizer.
上述,在本实施例中所制成的生物炭基具有49.8%的碳产生率,6.34m/g的比表面积,5.28nm的平均吸附孔径,且其中腐殖质含量为39%,有机质含量为70%,盐分为0.22%,包括氮磷钾的总养分为5.8%;As mentioned above, the biochar base prepared in this example has a carbon production rate of 49.8%, a specific surface area of 6.34m/g, an average adsorption pore size of 5.28nm, and wherein the humic substance content is 39%, and the organic matter content is 70%. , the salt content is 0.22%, and the total nutrients including nitrogen, phosphorus and potassium are 5.8%;
另外,在本实施例中所制成的生物炭基颗粒肥料中包括氮磷钾的总养分含量超过25%,生物炭含量为60%。In addition, in the biochar-based granular fertilizer prepared in this embodiment, the total nutrient content of nitrogen, phosphorus and potassium is more than 25%, and the biochar content is 60%.
综上可知,在以三相分离餐厨垃圾后所获得的有机固相物料作为水热碳化反应的原料时,其生物炭基中的碳产生率为41.4~52.7%,比表面积为5.01~8.45m/g,平均吸附孔径为4.88~6.23nm,腐殖质含量为38~40%,有机质含量为62~72%,盐分为0.22%,包括氮磷钾的总养分为4.9~6.7%;另外,在本实施例中所制成的生物炭基颗粒肥料中包括氮磷钾的总养分含量超过25%,生物炭含量为55~65%,由此能有效满足生物炭基肥的国家标准。In summary, when the organic solid phase material obtained after the three-phase separation of kitchen waste is used as the raw material for the hydrothermal carbonization reaction, the carbon generation rate in the biochar base is 41.4-52.7%, and the specific surface area is 5.01-8.45 m/g, the average adsorption pore size is 4.88~6.23nm, the humus content is 38~40%, the organic matter content is 62~72%, the salt content is 0.22%, and the total nutrients including nitrogen, phosphorus and potassium are 4.9~6.7%; The biochar-based granular fertilizer prepared in this example includes a total nutrient content of nitrogen, phosphorus and potassium exceeding 25%, and a biochar content of 55-65%, which can effectively meet the national standard for biochar-based fertilizers.
对比例1Comparative Example 1
将未经处理的餐厨垃圾泵送至水热反应釜内,180~250℃水热碳化90~240min,反应产物经冷却、脱水、干燥后形成生物炭基。The untreated kitchen waste is pumped into the hydrothermal reaction kettle, and hydrothermally carbonized at 180~250℃ for 90~240min, and the reaction product is cooled, dehydrated and dried to form a biochar base.
在本对比例中,其生物炭基中的碳产生率为31.3~42.8%,比表面积为3.21~5.65m/g,平均吸附孔径为2.57~4.43nm。In this comparative example, the carbon generation rate in the biochar base is 31.3-42.8%, the specific surface area is 3.21-5.65 m/g, and the average adsorption pore size is 2.57-4.43 nm.
由上,基于上述实施例与对比例1的对比可知,本发明的方法有效提高了生物炭基的生产质量。From the above, based on the comparison between the above example and Comparative Example 1, it can be seen that the method of the present invention effectively improves the production quality of biochar-based.
对比例2Comparative Example 2
三相分离餐厨垃圾,获得有机固相物料;Three-phase separation of kitchen waste to obtain organic solid materials;
堆肥处理有机固相物料,获得生物炭基。Composting processes organic solid-phase materials to obtain biochar bases.
在本对比例中,其生物炭基中的腐殖质含量为45.6%,有机质含量为39~43%,盐分为1.38%,包括氮磷钾的总养分为1.9~5.4%。In this comparative example, the humus content in the biochar base is 45.6%, the organic matter content is 39-43%, the salt content is 1.38%, and the total nutrients including nitrogen, phosphorus and potassium are 1.9-5.4%.
由上,基于上述实施例与对比例2的对比可知,腐殖质和盐分含量均大大降低,由此有效解决了反应后产物不纯、高油高盐等问题;而有机质含及包括氮磷钾的总养分的含量大大提升,由此有效提高本发明所制备的肥料养分含量,从而提升肥料品质。From the above, based on the comparison of the above-mentioned embodiment and Comparative Example 2, it can be known that humic substances and salt content are greatly reduced, thus effectively solving the problems such as impure products, high oil and high salt after the reaction; and organic matter contains and includes nitrogen, phosphorus and potassium. The content of total nutrients is greatly increased, thereby effectively increasing the nutrient content of the fertilizer prepared by the present invention, thereby improving the quality of the fertilizer.
上述描述中,虽然将各步骤描述成顺序的处理,但是其中的许多步骤可以被择一的、并行地、并发地或者同时实施。此外,各步骤的顺序可以被重新安排。并且,当其操作完成时所述处理可以被终止,但是还可以具有未包括的附加步骤。In the above description, although the steps are described as a sequential process, many of the steps may be implemented alternatively, in parallel, concurrently, or simultaneously. Furthermore, the order of the steps can be rearranged. Also, the process may be terminated when its operation is complete, but may also have additional steps not included.
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the present invention is defined by the appended claims and their equivalents.
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