CN106732362A - A kind of kitchen garbage is the sludge base charcoal preparation method of presoma - Google Patents
A kind of kitchen garbage is the sludge base charcoal preparation method of presoma Download PDFInfo
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- 239000010802 sludge Substances 0.000 title claims abstract description 37
- 238000002360 preparation method Methods 0.000 title claims description 9
- 239000003610 charcoal Substances 0.000 title 1
- 239000000843 powder Substances 0.000 claims abstract description 30
- 239000010806 kitchen waste Substances 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000000197 pyrolysis Methods 0.000 claims abstract description 16
- 239000002243 precursor Substances 0.000 claims abstract description 12
- 239000008367 deionised water Substances 0.000 claims abstract description 11
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 6
- 239000013049 sediment Substances 0.000 claims abstract description 6
- 239000010794 food waste Substances 0.000 claims description 16
- 239000000047 product Substances 0.000 claims description 12
- 238000001914 filtration Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 5
- 238000002791 soaking Methods 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 3
- 239000000706 filtrate Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 239000006228 supernatant Substances 0.000 claims description 2
- 235000013305 food Nutrition 0.000 claims 1
- 235000021190 leftovers Nutrition 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 239000010865 sewage Substances 0.000 abstract description 9
- 239000002351 wastewater Substances 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 description 10
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 6
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 6
- 229910052740 iodine Inorganic materials 0.000 description 6
- 239000011630 iodine Substances 0.000 description 6
- 229910052698 phosphorus Inorganic materials 0.000 description 6
- 239000011574 phosphorus Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 239000000149 chemical water pollutant Substances 0.000 description 3
- 238000007517 polishing process Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4875—Sorbents characterised by the starting material used for their preparation the starting material being a waste, residue or of undefined composition
- B01J2220/4887—Residues, wastes, e.g. garbage, municipal or industrial sludges, compost, animal manure; fly-ashes
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
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- Analytical Chemistry (AREA)
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- Carbon And Carbon Compounds (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明涉及一种餐厨垃圾为前驱体的污泥基生物炭制备方法。本发明将市政污泥的底泥风干后放入烘箱烘到恒重,破碎、研磨过200目筛得底泥干粉。将餐厨垃圾绞碎后调理成含水率80%的糊状物,放入烘箱于烘到恒重,破碎、研磨过200目筛得到餐厨垃圾干粉。将底泥干粉浸泡在1‑3mol/L的KOH中,过滤后滤渣置入烘箱于105℃烘去水分,取出冷却。按1~5:1~2重量份将污泥干粉和餐厨垃圾干粉充分混合置入气氛马弗炉中热解,得到热解产物。用盐酸浸洗,去离子水浸泡20min后过滤,重复5遍,再烘干至恒重,获得利用餐厨垃圾为前驱体的污泥基生物炭。本发明利用其制成的生物炭应用于污、废水处理,并取得良好的经济和环境效益。The invention relates to a method for preparing sludge-based biochar using kitchen waste as a precursor. In the invention, the bottom sludge of the municipal sludge is air-dried, put into an oven to dry to constant weight, crushed and ground through a 200-mesh sieve to obtain dry bottom sludge powder. Grind the kitchen waste and adjust it into a paste with a moisture content of 80%, put it in an oven and bake until it reaches a constant weight, crush and grind it through a 200-mesh sieve to obtain a dry kitchen waste powder. Soak the dry sediment powder in 1‑3mol/L KOH, filter the filter residue, put it in an oven at 105°C to dry out the water, take it out and cool it. The sludge dry powder and the kitchen waste dry powder are fully mixed according to the weight ratio of 1-5:1-2 and placed in an atmosphere muffle furnace for pyrolysis to obtain a pyrolysis product. Rinse with hydrochloric acid, soak in deionized water for 20 minutes, filter, repeat 5 times, and then dry to constant weight to obtain sludge-based biochar using kitchen waste as a precursor. The biochar prepared by the invention is applied to the treatment of sewage and waste water, and obtains good economic and environmental benefits.
Description
技术领域technical field
本发明涉及一种污泥基生物炭,特别是涉及一种餐厨垃圾为前驱体的污泥基生物炭制备方法。The invention relates to a sludge-based biochar, in particular to a method for preparing sludge-based biochar using kitchen waste as a precursor.
背景技术Background technique
生物炭是指生物质在缺氧条件下经高温热解后剩下的物质。生物炭具有较大的比表面积和多孔结构,具有良好的吸附性能,可作为污水处理吸附剂,吸附水中的重金属、氨氮、磷酸盐等。Biochar refers to the material left after biomass is pyrolyzed at high temperature under anoxic conditions. Biochar has a large specific surface area and porous structure, and has good adsorption performance. It can be used as an adsorbent for sewage treatment to adsorb heavy metals, ammonia nitrogen, phosphate, etc. in water.
餐厨垃圾是食物残余,含有大量有机成分,存在很大的环境风险和危害。经济发展和生活水平提高的同时伴随着餐厨垃圾产生量逐年增长,当前我国餐厨垃圾量已超过2万t/d,迫切寻获安全“出口”。Food waste is food residue, which contains a large amount of organic components and presents great environmental risks and hazards. With economic development and improvement of living standards, the amount of kitchen waste is increasing year by year. At present, the volume of kitchen waste in my country has exceeded 20,000 t/d, and it is urgent to find a safe "export".
餐厨垃圾中含有大量的有机物,可作为制备生物炭的原材料。由于其所含成分复杂,制成的生物炭品质及性能较商业生物炭差距很大,其应用范围与价值也受限制。Food waste contains a large amount of organic matter, which can be used as raw materials for the preparation of biochar. Due to its complex composition, the quality and performance of the biochar produced are far from those of commercial biochar, and its application range and value are also limited.
水处理常使用活性炭工艺,它的高效性为行业所公认。而污水或废水处理对于所使用的活性炭要求品质不高,故利用含有有机成分废弃物制得的生物炭可应用于污(废)水处理领域。Activated carbon technology is often used in water treatment, and its high efficiency is recognized by the industry. Sewage or wastewater treatment does not require high-quality activated carbon, so biochar produced from waste containing organic components can be used in the field of sewage (waste) water treatment.
本发明从“以废治废”的理念出发,利用餐厨垃圾来制备生物炭,应用于污(废)水处理,并取得良好的成效。Starting from the idea of "treating waste with waste", the present invention utilizes kitchen waste to prepare biochar, which is applied to sewage (waste) water treatment and achieves good results.
发明内容Contents of the invention
本发明的目的在于提供一种利用餐厨垃圾为前驱体的污泥基生物炭制备方法,该方法简单,易操作,并可实现“以废治废”成效。The purpose of the present invention is to provide a method for preparing sludge-based biochar using kitchen waste as a precursor. The method is simple, easy to operate, and can achieve the effect of "treating waste with waste".
1、原料准备1. Raw material preparation
市政污泥的底泥(含水率72-80%)在自然条件下风干,然后放入烘箱于105℃烘到恒重,除去石块等杂物后破碎至4-8mm,再经研磨、过200目筛得底泥干粉。The bottom sludge of municipal sludge (moisture content 72-80%) is air-dried under natural conditions, then put into an oven and baked at 105°C to constant weight, remove stones and other sundries, and then crush to 4-8mm, and then grind, pass through A 200-mesh sieve was used to obtain dry bottom mud powder.
将餐厨垃圾沥水并除去大颗粒杂物,绞碎后调理成含水率80%的糊状物,放入烘箱于105℃烘到恒重,破碎至4-8mm、研磨,过200目筛得到餐厨垃圾干粉。Drain the kitchen waste and remove large particles of debris, grind it and adjust it into a paste with a moisture content of 80%, put it in an oven and dry it at 105°C to constant weight, crush it to 4-8mm, grind it, and pass it through a 200-mesh sieve to obtain Food waste dry powder.
2、制备步骤2. Preparation steps
⑴将过200目筛的底泥干粉浸泡在1-3mol/L的KOH中8-24h,过滤后滤渣置入烘箱于105℃烘去水分,直至恒重后取出冷却。(1) Soak the dry powder of the sediment that has passed through a 200-mesh sieve in 1-3mol/L KOH for 8-24 hours, and put the filtered residue into an oven at 105°C to dry out the water until the weight is constant, then take it out and cool it.
⑵按1~5:1~2重量份比例的将污泥干粉和餐厨垃圾干粉充分混合,将混合物料置入气氛马弗炉中热解,通入100-200mL/min的氮气15min,后以10-20℃/min的升温速度加热至400-600℃,停留2-3h后,停止加热并降温至80℃出料,放在干燥器内冷却得到热解产物。(2) Fully mix the dry sludge powder and the dry kitchen waste powder in a ratio of 1 to 5:1 to 2 parts by weight, put the mixed material into an atmosphere muffle furnace for pyrolysis, and inject 100-200mL/min nitrogen gas for 15 minutes, and then Heat to 400-600°C at a heating rate of 10-20°C/min, stay for 2-3 hours, stop heating and cool down to 80°C to discharge, and cool in a desiccator to obtain pyrolysis products.
⑶将步骤⑵得到的热解产物用1mol/L的盐酸浸洗5min。(3) Rinse the pyrolysis product obtained in step (2) with 1mol/L hydrochloric acid for 5 minutes.
⑷滤去步骤⑶的盐酸,将固形物用去离子水浸泡20min后过滤,去离子水浸泡与过滤步骤重复5遍,直至滤液pH为7-8。再把滤上物放入烘箱于105℃烘干至恒重,最终获得利用餐厨垃圾为前驱体的污泥基生物炭。(4) Filter out the hydrochloric acid in step (3), soak the solid matter in deionized water for 20 minutes and then filter, repeat the steps of soaking in deionized water and filtering for 5 times until the pH of the filtrate is 7-8. Then put the supernatant into an oven and dry at 105°C to a constant weight, and finally obtain sludge-based biochar using kitchen waste as a precursor.
本发明用的餐厨垃圾是指酒店、餐馆、食堂的所有餐厨剩余物。The kitchen waste used in the present invention refers to all kitchen residues in hotels, restaurants and canteens.
本发明的优点在于:The advantages of the present invention are:
从“废物资源化”的理念出发,赋予了餐厨垃圾一种变废为宝的新用途,利用其制成的生物炭应用于污(废)水处理,并取得良好的经济效益和环境效益。Starting from the concept of "recycling of waste", a new use of turning waste into treasure has been given to kitchen waste. The biochar made from it is used in sewage (waste) water treatment, and good economic and environmental benefits have been achieved. .
具体实施方式detailed description
实施例1Example 1
⑴将市政污泥的底泥(含水率72%)在自然条件下风干,然后放入烘箱于105℃烘到恒重,除去石块等杂物后破碎至4-8mm,再经研磨、过200目筛得底泥干粉。(1) Air-dry the bottom sludge (moisture content 72%) of municipal sludge under natural conditions, then put it in an oven and dry it at 105°C to constant weight, remove stones and other sundries, and then crush it to 4-8mm, then grind, pass A 200-mesh sieve was used to obtain dry bottom mud powder.
将餐厨垃圾沥水并除去大颗粒杂物,绞碎后调理成含水率80%的糊状物,放入烘箱于105℃烘到恒重,破碎至4-8mm、研磨,过200目筛得到餐厨垃圾干粉;将过200目筛的餐厨垃圾干粉末浸泡在1mol/L的KOH中24h,过滤后滤渣置入烘箱于105℃烘去水分,直至恒重后取出冷却。Drain the kitchen waste and remove large particles of debris, grind it and adjust it into a paste with a moisture content of 80%, put it in an oven and dry it at 105°C to constant weight, crush it to 4-8mm, grind it, and pass it through a 200-mesh sieve to obtain Dry food waste powder: Soak the dry food waste powder passed through a 200-mesh sieve in 1mol/L KOH for 24 hours. After filtering, put the filter residue into an oven at 105°C to dry out the water until it reaches a constant weight, then take it out and cool it.
⑵按1:1重量份比例的分别取50g污泥干粉和餐厨垃圾干粉充分混合,将混合物料放入气氛马弗炉高温热解处理。先以200mL/min速率通入氮气15min,然后开始升温加热,以10℃/min升温速度至400℃并保持该温度3h,关闭加热系统使之自然降温到80℃,取出物料放在干燥器内冷却得到热解产物。(2) Take 50g of sludge dry powder and kitchen waste dry powder in a ratio of 1:1 by weight and mix them thoroughly, and put the mixed materials into an atmosphere muffle furnace for high-temperature pyrolysis treatment. First pass nitrogen gas at a rate of 200mL/min for 15 minutes, then start heating, increase the temperature at a rate of 10°C/min to 400°C and maintain the temperature for 3 hours, turn off the heating system and let it cool down to 80°C naturally, take out the material and put it in the dryer Cool to get pyrolysis products.
⑶待热解产物冷却至室温后,用1mol/L的盐酸浸洗5min。(3) After the pyrolysis product is cooled to room temperature, soak it with 1mol/L hydrochloric acid for 5 minutes.
⑷滤去盐酸,将滤渣用去离子水浸泡,搅拌清洗15min后过滤,重复5次的去离子水浸洗和过滤步骤。最后将滤上物放入烘箱于105℃烘干至恒重,取出干燥冷却后即得到本实施例的所述的餐厨垃圾为前驱体的污泥基生物炭成品。(4) Filter out the hydrochloric acid, soak the filter residue with deionized water, stir and wash for 15 minutes and then filter, repeat the steps of immersing with deionized water and filtering for 5 times. Finally, put the filtered matter into an oven and dry it at 105° C. to a constant weight, take it out, dry it and cool it, and then obtain the finished sludge-based biochar product described in this embodiment with kitchen waste as a precursor.
碘值测定:采用本实施例步骤所制备的底泥基生物炭的碘值与比表面积分别是489.9mg/g、463.7m2/g。Determination of iodine value: the iodine value and specific surface area of the sediment-based biochar prepared by the steps in this example are 489.9 mg/g and 463.7 m 2 /g, respectively.
用于含磷废水处理:当投加量为1g/L时,本实施例制得的生物炭对TP浓度186mg/L的机电抛光工序含磷废水处理,出水TP浓度6.51mg/L,TP去除率分别96.5%。For the treatment of phosphorus-containing wastewater: when the dosage is 1g/L, the biochar prepared in this example can treat phosphorus-containing wastewater in the electromechanical polishing process with a TP concentration of 186mg/L, and the TP concentration in the effluent is 6.51mg/L, and the TP removal The rates were 96.5%.
用于渗滤液预处理:当投加量为800mg/L时,本实施例制得的生物炭对主要水质指标:CODCr浓度3546mg/L、NH4 +-N浓度867mg/L、TP浓度16.7mg/L的垃圾渗滤液预处理,上述三项指标的去除率分别79.3%、33.2%和96.7%。For leachate pretreatment: When the dosage is 800mg/L, the biochar prepared in this example has the main water quality indicators: COD Cr concentration 3546mg/L, NH 4 + -N concentration 867mg/L, TP concentration 16.7 mg/L landfill leachate pretreatment, the removal rates of the above three indicators were 79.3%, 33.2% and 96.7%, respectively.
本实施例所述的市政污泥取自福州市城区某污水处理厂。The municipal sludge described in this example was taken from a sewage treatment plant in the urban area of Fuzhou City.
实施例2Example 2
⑴将市政污泥的底泥(含水率78%)在自然条件下风干,然后放入烘箱于105℃烘到恒重,除去石块等杂物后破碎至4-8mm,再经研磨、过200目筛得底泥干粉。⑴ Air-dry the bottom sludge (moisture content 78%) of municipal sludge under natural conditions, then put it into an oven and bake it at 105°C until it reaches a constant weight, remove stones and other sundries, and then crush it to 4-8mm, then grind, pass A 200-mesh sieve was used to obtain dry bottom mud powder.
将餐厨垃圾沥水并除去大颗粒杂物,绞碎后调理成含水率80%的糊状物,放入烘箱于105℃烘到恒重,破碎至4-8mm、研磨,过200目筛得到餐厨垃圾干粉;Drain the kitchen waste and remove large particles of debris, grind it and adjust it into a paste with a moisture content of 80%, put it in an oven and dry it at 105°C to constant weight, crush it to 4-8mm, grind it, and pass it through a 200-mesh sieve to obtain Food waste dry powder;
将过200目筛的餐厨垃圾干粉浸泡在2mol/L的KOH中16h,过滤后滤渣置入烘箱于105℃烘去水分,直至恒重后取出冷却。Soak the dry food waste powder passed through a 200-mesh sieve in 2mol/L KOH for 16 hours. After filtering, put the filter residue into an oven at 105°C to dry out the water until it reaches a constant weight, then take it out and cool it.
⑵按3:1重量份比例的分别取90g污泥干粉和30g餐厨垃圾干粉充分混合,将混合物料放入气氛马弗炉高温热解处理。先以200mL/min速率通入氮气15min,然后开始升温加热,以10℃/min升温速度至500℃并保持该温度2.5h,关闭加热系统使之自然降温到80℃,取出物料放在干燥器内冷却得到高温热解产物。(2) Take 90g of sludge dry powder and 30g of food waste dry powder in a ratio of 3:1 parts by weight and mix them thoroughly, and put the mixed materials into an atmosphere muffle furnace for high-temperature pyrolysis treatment. First pass nitrogen gas at a rate of 200mL/min for 15 minutes, then start to heat up and heat up to 500°C at a rate of 10°C/min and maintain the temperature for 2.5 hours, turn off the heating system and let it cool down to 80°C naturally, take out the material and put it in the dryer Internal cooling produces high temperature pyrolysis products.
⑶将高温热解产物冷却至室温后,用1mol/L的盐酸浸洗5min。。(3) After cooling the high-temperature pyrolysis product to room temperature, soak it with 1mol/L hydrochloric acid for 5 minutes. .
⑷滤去盐酸,将滤渣用去离子水浸泡,搅拌清洗15min后过滤,重复5次的去离子水浸洗和过滤步骤。最后将滤上物放入烘箱于105℃烘干至恒重,取出干燥冷却后即得到本实施例所述的餐厨垃圾为前驱体的污泥基生物炭成品。(4) Filter out the hydrochloric acid, soak the filter residue with deionized water, stir and wash for 15 minutes and then filter, repeat the steps of immersing with deionized water and filtering for 5 times. Finally, put the filtered matter into an oven and dry it at 105° C. to a constant weight, take it out, dry it and cool it, and then obtain the finished sludge-based biochar product described in this example with kitchen waste as a precursor.
碘值测定:采用本实施例步骤所制备的底泥基生物炭的碘值与比表面积分别是526.2mg/g、503.5m2/g。Determination of iodine value: the iodine value and specific surface area of the sediment-based biochar prepared by the steps in this example are 526.2 mg/g and 503.5 m 2 /g, respectively.
用于含磷废水处理:当投加量为1g/L时,本实施例制得的生物炭对TP浓度186mg/L的机电抛光工序含磷废水处理,出水TP浓度5.20mg/L,TP去除率分别97.2%。For phosphorus-containing wastewater treatment: when the dosage is 1g/L, the biochar prepared in this example can treat phosphorus-containing wastewater in the electromechanical polishing process with a TP concentration of 186mg/L. The TP concentration in the effluent is 5.20mg/L, and the TP removal The rates were 97.2%.
用于渗滤液预处理:当投加量为800mg/L时,本实施例制得的生物炭对主要水质指标:CODCr浓度3546mg/L、NH4 +-N浓度867mg/L、TP浓度16.7mg/L的垃圾渗滤液预处理,上述三项指标的去除率分别80.2%、33.4%和97.1%。For leachate pretreatment: When the dosage is 800mg/L, the biochar prepared in this example has the main water quality indicators: COD Cr concentration 3546mg/L, NH 4 + -N concentration 867mg/L, TP concentration 16.7 mg/L landfill leachate pretreatment, the removal rates of the above three indicators were 80.2%, 33.4% and 97.1%, respectively.
本实施例所述的市政污泥取自福州市城区某污水处理厂。The municipal sludge described in this example is taken from a sewage treatment plant in the urban area of Fuzhou City.
实施例3Example 3
⑴将市政污泥的底泥(含水率78%)在自然条件下风干,然后放入烘箱于105℃烘到恒重,除去石块等杂物后破碎至4-8mm,再经研磨、过200目筛得底泥干粉。⑴ Air-dry the bottom sludge (moisture content 78%) of municipal sludge under natural conditions, then put it into an oven and bake it at 105°C until it reaches a constant weight, remove stones and other sundries, and then crush it to 4-8mm, then grind, pass A 200-mesh sieve was used to obtain dry bottom mud powder.
将餐厨垃圾沥水并除去大颗粒杂物,绞碎后调理成含水率80%的糊状物,放入烘箱于105℃烘到恒重,破碎至4-8mm、研磨,过200目筛得到餐厨垃圾干粉。Drain the kitchen waste and remove large particles of debris, grind it and adjust it into a paste with a moisture content of 80%, put it in an oven and dry it at 105°C to constant weight, crush it to 4-8mm, grind it, and pass it through a 200-mesh sieve to obtain Food waste dry powder.
将过200目筛的餐厨垃圾干粉浸泡在3mol/L的KOH中8h,过滤后滤渣置入烘箱于105℃烘去水分,直至恒重后取出冷却。Soak the dry food waste powder passed through a 200-mesh sieve in 3mol/L KOH for 8 hours. After filtering, put the filter residue into an oven at 105°C to dry out the water until it reaches a constant weight, then take it out and cool it down.
⑵按5:2重量份比例的分别取100g污泥干粉和40g餐厨垃圾干粉充分混合,将混合物料放入气氛马弗炉高温热解处理。先以200mL/min速率通入氮气15min,然后开始升温加热,以10℃/min升温速度至600℃并保持该温度2h,关闭加热系统使之自然降温到80℃,取出物料放在干燥器内冷却。(2) Fully mix 100g of sludge dry powder and 40g of kitchen waste dry powder in a ratio of 5:2 parts by weight, and put the mixed materials into an atmosphere muffle furnace for high-temperature pyrolysis treatment. First pass nitrogen gas at a rate of 200mL/min for 15 minutes, then start heating, increase the temperature at a rate of 10°C/min to 600°C and maintain the temperature for 2 hours, turn off the heating system and let it cool down to 80°C naturally, take out the material and put it in the dryer cool down.
⑶待热解后的产品降冷却至室温后,用1M的盐酸浸洗5min。。(3) After the pyrolyzed product is cooled to room temperature, soak it with 1M hydrochloric acid for 5 minutes. .
⑷滤去盐酸,将滤渣用去离子水浸泡,搅拌清洗15min后过滤,重复5次的去离子水浸洗和过滤步骤。最后将滤上物放入烘箱于105℃烘干至恒重,取出干燥冷却后即得到本实施例的成品。(4) Filter out the hydrochloric acid, soak the filter residue with deionized water, stir and wash for 15 minutes and then filter, repeat the steps of immersing with deionized water and filtering for 5 times. Finally, put the filtered matter into an oven and dry it at 105° C. to a constant weight, take it out, dry it and cool it down to obtain the finished product of this embodiment.
碘值测定:采用本实施例步骤所制备的底泥基生物炭的碘值与比表面积分别是349.9mg/g、362.8m2/g。Determination of iodine value: the iodine value and specific surface area of the sediment-based biochar prepared by the steps in this example are 349.9 mg/g and 362.8 m 2 /g, respectively.
用于含磷废水处理:当投加量为1g/L时,本实施例制得的生物炭对TP浓度186mg/L的机电抛光工序含磷废水处理,出水TP浓度11.90mg/L,TP去除率分别93.6%。For phosphorus-containing wastewater treatment: when the dosage is 1g/L, the biochar prepared in this example can treat phosphorus-containing wastewater in the electromechanical polishing process with a TP concentration of 186mg/L, and the effluent TP concentration is 11.90mg/L, and the TP removal The rates were 93.6%.
用于渗滤液预处理:当投加量为800mg/L时,本实施例制得的生物炭对主要水质指标:CODCr浓度3546mg/L、NH4 +-N浓度867mg/L、TP浓度16.7mg/L的垃圾渗滤液预处理,上述三项指标的去除率分别73.4%、30.8%和90.3%。For leachate pretreatment: When the dosage is 800mg/L, the biochar prepared in this example has the main water quality indicators: COD Cr concentration 3546mg/L, NH 4 + -N concentration 867mg/L, TP concentration 16.7 mg/L landfill leachate pretreatment, the removal rates of the above three indicators were 73.4%, 30.8% and 90.3% respectively.
本实施例所述的市政污泥取自福州市城区某污水处理厂。The municipal sludge described in this example is taken from a sewage treatment plant in the urban area of Fuzhou City.
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CN111266086A (en) * | 2020-01-22 | 2020-06-12 | 青岛农业大学 | A method for producing magnetic biochar from kitchen waste |
CN118719003A (en) * | 2024-09-04 | 2024-10-01 | 江西省科学院微生物研究所(江西省流域生态研究所) | A kind of sludge-based magnetic biochar, preparation method and application |
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CN104084128A (en) * | 2014-07-22 | 2014-10-08 | 天津城建大学 | Kitchen waste residue modified sludge activated carbon for sweater treatment |
CN104557160A (en) * | 2015-01-19 | 2015-04-29 | 青岛农业大学 | A method for preparing biochar from kitchen waste |
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CN102120575A (en) * | 2011-03-04 | 2011-07-13 | 南京工业大学 | A process for preparing activated carbon from chemical sludge |
CN104084128A (en) * | 2014-07-22 | 2014-10-08 | 天津城建大学 | Kitchen waste residue modified sludge activated carbon for sweater treatment |
CN104557160A (en) * | 2015-01-19 | 2015-04-29 | 青岛农业大学 | A method for preparing biochar from kitchen waste |
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CN107720977A (en) * | 2017-09-27 | 2018-02-23 | 浙江海洋大学 | A kind of ecological soil system nitrogen phosphorus pollution of area source cutting method based on compound bio charcoal |
CN111266086A (en) * | 2020-01-22 | 2020-06-12 | 青岛农业大学 | A method for producing magnetic biochar from kitchen waste |
CN118719003A (en) * | 2024-09-04 | 2024-10-01 | 江西省科学院微生物研究所(江西省流域生态研究所) | A kind of sludge-based magnetic biochar, preparation method and application |
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