CN111266086A - A method for producing magnetic biochar from kitchen waste - Google Patents
A method for producing magnetic biochar from kitchen waste Download PDFInfo
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- 239000010806 kitchen waste Substances 0.000 title claims abstract description 48
- 238000004519 manufacturing process Methods 0.000 title description 2
- 238000000034 method Methods 0.000 claims abstract description 24
- 150000003839 salts Chemical class 0.000 claims abstract description 18
- 238000005336 cracking Methods 0.000 claims abstract description 17
- 239000000243 solution Substances 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000001035 drying Methods 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims abstract 3
- 238000007873 sieving Methods 0.000 claims abstract 3
- 238000003828 vacuum filtration Methods 0.000 claims abstract 3
- 239000012670 alkaline solution Substances 0.000 claims abstract 2
- 238000010407 vacuum cleaning Methods 0.000 claims abstract 2
- 238000001291 vacuum drying Methods 0.000 claims abstract 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 18
- 239000008367 deionised water Substances 0.000 claims description 13
- 229910021641 deionized water Inorganic materials 0.000 claims description 13
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 12
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 229910017604 nitric acid Inorganic materials 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 8
- 238000001027 hydrothermal synthesis Methods 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 239000004570 mortar (masonry) Substances 0.000 claims description 5
- 239000010813 municipal solid waste Substances 0.000 claims description 5
- 238000005406 washing Methods 0.000 claims description 4
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 3
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical group Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 claims description 3
- JZCCFEFSEZPSOG-UHFFFAOYSA-L copper(II) sulfate pentahydrate Chemical compound O.O.O.O.O.[Cu+2].[O-]S([O-])(=O)=O JZCCFEFSEZPSOG-UHFFFAOYSA-L 0.000 claims description 3
- VEPSWGHMGZQCIN-UHFFFAOYSA-H ferric oxalate Chemical compound [Fe+3].[Fe+3].[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O VEPSWGHMGZQCIN-UHFFFAOYSA-H 0.000 claims description 3
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical group Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 3
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 claims description 3
- 229910000360 iron(III) sulfate Inorganic materials 0.000 claims description 3
- SXTLQDJHRPXDSB-UHFFFAOYSA-N copper;dinitrate;trihydrate Chemical compound O.O.O.[Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O SXTLQDJHRPXDSB-UHFFFAOYSA-N 0.000 claims description 2
- 235000013305 food Nutrition 0.000 claims description 2
- SZQUEWJRBJDHSM-UHFFFAOYSA-N iron(3+);trinitrate;nonahydrate Chemical compound O.O.O.O.O.O.O.O.O.[Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O SZQUEWJRBJDHSM-UHFFFAOYSA-N 0.000 claims description 2
- 230000007935 neutral effect Effects 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 238000000227 grinding Methods 0.000 claims 2
- 238000000643 oven drying Methods 0.000 claims 2
- 238000007605 air drying Methods 0.000 claims 1
- 238000012216 screening Methods 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 8
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 229910052573 porcelain Inorganic materials 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 238000010335 hydrothermal treatment Methods 0.000 abstract description 4
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 4
- 239000003610 charcoal Substances 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 24
- 239000010794 food waste Substances 0.000 description 19
- 239000010949 copper Substances 0.000 description 16
- 238000005516 engineering process Methods 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 6
- 230000008929 regeneration Effects 0.000 description 6
- 238000011069 regeneration method Methods 0.000 description 6
- 238000004064 recycling Methods 0.000 description 5
- 238000005119 centrifugation Methods 0.000 description 4
- 230000001699 photocatalysis Effects 0.000 description 4
- 241000209094 Oryza Species 0.000 description 3
- 235000007164 Oryza sativa Nutrition 0.000 description 3
- 235000008429 bread Nutrition 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 3
- 235000013980 iron oxide Nutrition 0.000 description 3
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 3
- 235000013372 meat Nutrition 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 235000009566 rice Nutrition 0.000 description 3
- 239000012266 salt solution Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 235000013311 vegetables Nutrition 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 229960000935 dehydrated alcohol Drugs 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 235000012054 meals Nutrition 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 240000002234 Allium sativum Species 0.000 description 1
- 208000035473 Communicable disease Diseases 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910002554 Fe(NO3)3·9H2O Inorganic materials 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- BSLPSRLINXAITB-UHFFFAOYSA-L O.O.O.O.O.C(C(=O)[O-])(=O)[O-].[Fe+2] Chemical compound O.O.O.O.O.C(C(=O)[O-])(=O)[O-].[Fe+2] BSLPSRLINXAITB-UHFFFAOYSA-L 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000149 chemical water pollutant Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 235000004611 garlic Nutrition 0.000 description 1
- 230000001146 hypoxic effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- CXKWCBBOMKCUKX-UHFFFAOYSA-M methylene blue Chemical compound [Cl-].C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 CXKWCBBOMKCUKX-UHFFFAOYSA-M 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 235000021404 traditional food Nutrition 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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- 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
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
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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
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28009—Magnetic properties
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- 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
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3416—Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
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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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- 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
- 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
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Processing Of Solid Wastes (AREA)
Abstract
Description
技术领域technical field
本发明属于生物炭材料技术领域,具体地说涉及一种利用餐厨垃圾制取磁性生物炭的方法。The invention belongs to the technical field of biochar materials, in particular to a method for preparing magnetic biochar from kitchen waste.
背景技术Background technique
2019年6月,中央农办,住建部、生态环境部和科技部等九部门联合印发《住房和城乡建设部等部门关于在全国地级及以上城市全面开展生活垃圾分类工作的通知》,提出自2019年起在全国地级及以上城市全面启动生活垃圾分类工作。随着垃圾分类政策的全面推行,加强餐厨垃圾的收集运输处理成为关注的热点问题。餐厨垃圾是指公共食堂、家庭、餐饮行业在日常生活消费过程中产生的食品废弃物,主要包括餐前食品加工时的食物废料和餐后的食物残余。传统的餐厨垃圾处置方法主要有填埋和焚烧。填埋过程产生的垃圾渗滤液和焚烧过程产生的二噁英等有毒气体对环境存在潜在危害,并且极易造成传染病的爆发,严重影响人类健康。因此,对于餐厨垃圾的资源化利用具有十分重要的意义。通过对餐厨垃圾在低氧或无氧条件下进行热解,垃圾中的大部分含碳有机物无法变为有害的CO2,而是转化为生物炭,防止CO2进入大气,可减少21%的碳排量[环境科学与技术,2016,39(S2):245-250]。鉴于此,近年来对于餐厨垃圾通过裂解制备生物炭技术日益活跃。在我们之前的研究中发现以餐厨垃圾为原料通过裂解制备的生物炭可以用于改良土壤的性质、提高土壤肥力(专利授权公号:CN104557160A),还可以有效的吸附水中亚甲基蓝(农业资源与环境学报,2019,36(1):115-120)。然而,单纯的生物炭粉末在使用过程中,回收分离较困难易造成资源浪费。研究者将磁性材料与生物炭结合制备磁性生物炭的方法可有效解决生物炭难回收的问题。In June 2019, nine departments including the Central Agriculture Office, the Ministry of Housing and Urban-Rural Development, the Ministry of Ecology and Environment, and the Ministry of Science and Technology jointly issued the "Notice of the Ministry of Housing and Urban-Rural Development and Other Departments on Comprehensively Carrying out Domestic Waste Classification in Cities at and Above the National Prefectural Level". Since 2019, domestic waste classification has been fully launched in cities at the prefecture level and above across the country. With the full implementation of the waste classification policy, strengthening the collection, transportation and disposal of kitchen waste has become a hot issue of concern. Food waste refers to the food waste generated in the daily consumption process of public canteens, households, and catering industries, mainly including food waste during pre-meal food processing and food residue after meals. Traditional food waste disposal methods mainly include landfill and incineration. The landfill leachate and dioxins and other toxic gases produced in the incineration process are potentially harmful to the environment, and can easily lead to the outbreak of infectious diseases, which seriously affects human health. Therefore, the resource utilization of kitchen waste is of great significance. By pyrolysis of kitchen waste under hypoxic or anaerobic conditions, most of the carbon-containing organic matter in the waste cannot be converted into harmful CO 2 , but converted into biochar, preventing CO 2 from entering the atmosphere, which can be reduced by 21% of carbon emissions [Environmental Science and Technology, 2016, 39(S2):245-250]. In view of this, in recent years, the technology of preparing biochar by pyrolysis of kitchen waste has become increasingly active. In our previous research, it was found that biochar prepared by cracking kitchen waste as raw material can be used to improve soil properties and improve soil fertility (patent authorization number: CN104557160A), and can also effectively adsorb methylene blue in water (agricultural resources and Journal of the Environment, 2019, 36(1):115-120). However, in the process of using pure biochar powder, it is difficult to recover and separate, which may lead to waste of resources. The method of combining magnetic materials with biochar to prepare magnetic biochar can effectively solve the problem of difficult recovery of biochar.
此外,吸附饱和生物炭的再生不仅可以提高生物炭的利用率,还可以减少其对环境的二次污染。光催化再生技术在太阳光照射下,利用产生的具有强氧化性自由基降解吸附在吸附剂表面上的有机物,达到吸附剂再生的目的。因此,通过某种手段为餐厨垃圾裂解制备的生物炭赋予磁性,同时通过光催化技术实现生物炭的再生,这不仅可以实现对通过垃圾分类回收后的餐厨垃圾资源化利用、减少餐厨垃圾对环境的危害,还可以为其制备的生物炭在回收和循环再生方面提高重要的指导意义。In addition, the regeneration of adsorbed saturated biochar can not only improve the utilization rate of biochar, but also reduce its secondary pollution to the environment. The photocatalytic regeneration technology uses the generated strong oxidizing free radicals to degrade the organic matter adsorbed on the surface of the adsorbent under the irradiation of sunlight, so as to achieve the purpose of regeneration of the adsorbent. Therefore, by some means, the biochar produced by the cracking of kitchen waste is given magnetic properties, and at the same time, the regeneration of the biochar is realized by photocatalytic technology, which can not only realize the resource utilization of the kitchen waste recovered through garbage classification, reduce the number of kitchen waste The harm of garbage to the environment can also improve the important guiding significance of the biochar prepared for it in recycling and recycling.
发明内容SUMMARY OF THE INVENTION
本发明提供一种利用餐厨垃圾制取磁性生物炭的方法,实现对通过垃圾分类回收后的餐厨垃圾资源化利用、减少餐厨垃圾对环境的危害,同时实现其制备的生物炭在使用过程中的回收和循环再生。该方法采用裂解技术制备餐厨垃圾生物炭,使其与一定量的Fe3+盐和Cu2+盐混合,在碱性条件下,通过水热技术,制备含有铁氧化物(Fe3O4和Fe2O3)和铜铁矿型CuFeO2的餐厨垃圾磁性生物炭,其中Fe3O4和Fe2O3可以为餐厨垃圾生物炭提供磁性便于生物炭的回收,利用铜铁矿型CuFeO2的光催化特性实现对吸附饱和后生物炭的循环再生。The invention provides a method for preparing magnetic biochar from kitchen waste, which realizes the resource utilization of the kitchen waste recovered through garbage classification, reduces the harm of the kitchen waste to the environment, and at the same time realizes that the prepared biochar can be used Recycling and recycling in the process. The method adopts pyrolysis technology to prepare kitchen waste biochar, mixes it with a certain amount of Fe 3+ salts and Cu 2+ salts, and prepares iron oxides (Fe 3 O 4 ) through hydrothermal technology under alkaline conditions. and Fe 2 O 3 ) and delafossite-type CuFeO 2 food waste magnetic biochar, of which Fe 3 O 4 and Fe 2 O 3 can provide magnetic properties for the food waste biochar to facilitate the recovery of biochar, using delafossite The photocatalytic properties of CuFeO 2 realize the cyclic regeneration of biochar after adsorption saturation.
为解决上述技术问题,本发明采用的技术方案如下:In order to solve the above-mentioned technical problems, the technical scheme adopted in the present invention is as follows:
一种利用餐厨垃圾制取磁性生物炭的方法,包括以下步骤:A method for preparing magnetic biochar from kitchen waste, comprising the following steps:
S1:收集餐厨垃圾,风干至水分低于10%,粉碎过筛得到粉碎物;S1: Collect kitchen waste, air-dry to a moisture content of less than 10%, crush and sieve to obtain crushed products;
S2:将粉碎物通过裂解制备餐厨垃圾生物炭,将制备的餐厨垃圾生物炭经洗涤、烘干、研磨并筛分备用;S2: the pulverized material is cracked to prepare food waste biochar, and the prepared food waste biochar is washed, dried, ground and screened for use;
S3:将餐厨垃圾生物炭与Fe3+盐和Cu2+盐在水中超声混合,不断搅拌条件下持续加入强碱溶液;S3: ultrasonically mix food waste biochar with Fe 3+ salt and Cu 2+ salt in water, and continuously add strong alkali solution under constant stirring;
S4:将上述溶液转移至水热反应釜中,进行水热裂解反应;S4: the above-mentioned solution is transferred to the hydrothermal reactor, and the hydrothermal cracking reaction is carried out;
S5:将水热裂解后的产物经真空抽滤、清洗、干燥处理,即可。S5: The product after hydrothermal cracking is vacuum filtered, washed and dried.
优选地,餐厨垃圾生物炭在惰性氛围下进行裂解制备,升温速率为5~10℃min-1,裂解温度为250~600℃,裂解时间为2~4小时。Preferably, the kitchen waste biochar is prepared by cracking in an inert atmosphere, the heating rate is 5-10°C min -1 , the cracking temperature is 250-600°C, and the cracking time is 2-4 hours.
优选地,步骤S2中依次用去无水乙醇,浓度为0.5~1.0molL-1盐酸、硝酸或硫酸、去离子水进行洗涤,烘干温度为60~80℃,烘干5~10小时,采用研钵进行研磨,采用300-500目筛子进行筛分。Preferably, in step S2, dehydrated ethanol is used successively, and the concentration is 0.5-1.0 molL -1 hydrochloric acid, nitric acid or sulfuric acid, and deionized water for washing, and the drying temperature is 60-80 ° C, drying for 5-10 hours, using Grind in a mortar and sieve with a 300-500 mesh sieve.
优选地,所述餐厨垃圾生物炭含量40gL-1~100gL-1。Preferably, the food waste biochar content is 40 gL -1 to 100 gL -1 .
优选地,Fe3+盐为氯化铁、九水合硝酸铁、硫酸铁或五水合草酸铁。Preferably, the Fe 3+ salt is ferric chloride, ferric nitrate nonahydrate, ferric sulfate or ferric oxalate pentahydrate.
优选地,Cu2+盐为氯化铜、三水合硝酸铜或五水合硫酸铜。Preferably, the Cu 2+ salt is copper chloride, copper nitrate trihydrate or copper sulfate pentahydrate.
优选地,Fe3+盐和Cu2+盐浓度为10mmolL-1~30mmolL-1。Preferably, the concentration of Fe 3+ salt and Cu 2+ salt is 10 mmolL -1 to 30 mmolL -1 .
优选地,所述强碱溶液为氢氧化钠或氢氧化钾,浓度为50gL-1~80gL-1。Preferably, the strong alkali solution is sodium hydroxide or potassium hydroxide, and the concentration is 50 gL -1 to 80 gL -1 .
优选地,水热反应温度为100~200℃,水热反应时间为6-48小时,水热后的产物依次选用无水乙醇,盐酸、硝酸或硫酸的稀溶液和去离子水冲洗,经真空抽滤清洗至中性后置于烘箱中,烘干温度为70~80℃,烘干8~12小时。Preferably, the hydrothermal reaction temperature is 100-200 °C, the hydrothermal reaction time is 6-48 hours, and the product after the hydrothermal selects dehydrated ethanol, a dilute solution of hydrochloric acid, nitric acid or sulfuric acid and deionized water to rinse in turn, and the vacuum After being cleaned by suction filtration to neutrality, it is placed in an oven, and the drying temperature is 70-80°C, and drying is performed for 8-12 hours.
优选地,盐酸、硝酸或硫酸的稀溶液的浓度为0.5~1.0molL-1。Preferably, the concentration of the dilute solution of hydrochloric acid, nitric acid or sulfuric acid is 0.5˜1.0 mol L −1 .
本发明的有益效果是:The beneficial effects of the present invention are:
1、本发明的餐厨垃圾磁性生物炭,比表面积增加,实现对通过垃圾分类回收后的餐厨垃圾资源化利用、减少餐厨垃圾对环境的危害具有良好的社会效益和环境效益。1. The kitchen waste magnetic biochar of the present invention has an increased specific surface area, which realizes the resource utilization of the kitchen waste after garbage classification and recycling, and reduces the harm of the kitchen waste to the environment, which has good social and environmental benefits.
2、本发明的餐厨垃圾磁性生物炭,通过裂解制备的餐厨垃圾生物炭与Fe3+盐和Cu2 +盐混合,在碱性条件下,经水热制备了含有一系列铁氧化物(Fe3O4和Fe2O3)和铜铁矿型CuFeO2的磁性大蒜秸秆生物炭,其中Fe3O4和Fe2O3可以为生物炭提供磁性便于生物炭的回收,利用铜铁矿型CuFeO2的光催化特性实现对吸附饱和后生物炭的循环再生。2. The kitchen waste magnetic biochar of the present invention, the kitchen waste biochar prepared by cracking is mixed with Fe 3+ salt and Cu 2 + salt, and a series of iron oxides containing a series of iron oxides are prepared by hydrothermal under alkaline conditions. (Fe 3 O 4 and Fe 2 O 3 ) and delafossite-type CuFeO 2 magnetic garlic straw biochar, of which Fe 3 O 4 and Fe 2 O 3 can provide magnetic properties for biochar to facilitate the recovery of biochar, using copper and iron The photocatalytic properties of ore-type CuFeO 2 realize the cyclic regeneration of biochar after adsorption saturation.
具体实施方式Detailed ways
下面将结合本发明实施例,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 clearly and completely described below with reference to the embodiments of the present invention. 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.
实施例一:Example 1:
一种利用餐厨垃圾制取磁性生物炭的方法,具体步骤如下:A method for preparing magnetic biochar from kitchen waste, the specific steps are as follows:
(1)餐厨垃圾生物炭的制备(1) Preparation of food waste biochar
收集餐厨垃圾,所述餐厨垃圾包括米饭、馒头碎屑、蔬菜和肉类,自然风干至含水率低于10%,随后粉碎过筛得到粉碎物。将粉碎物放入瓷方舟置于管式炉中,通入氮气提供缺氧条件,以5℃min-1的升温速率升温至250℃,裂解时间为2小时,将裂解产物依次选用无水乙醇,0.5molL-1的盐酸和去离子水进行洗涤,置于烘箱中在60℃下干燥5小时,将干燥后的产物经研钵研磨,过300目筛子,得到餐厨垃圾生物炭。Collecting kitchen waste, which includes rice, steamed bread scraps, vegetables and meat, naturally air-dried to a moisture content of less than 10%, and then crushed and sieved to obtain crushed products. Put the pulverized product into a porcelain ark and place it in a tube furnace, feed nitrogen to provide anoxic conditions, heat up to 250 °C at a heating rate of 5 °C min -1 , and the cracking time is 2 hours. , washed with 0.5molL -1 hydrochloric acid and deionized water, dried in an oven at 60°C for 5 hours, ground the dried product with a mortar, and passed through a 300-mesh sieve to obtain food waste biochar.
(2)餐厨垃圾磁性生物炭的制备(2) Preparation of kitchen waste magnetic biochar
在室温下按Fe:Cu摩尔比1:1称取氯化铜(99.99%)和氯化铁(99.99%)溶于60ml去离子水中,持续搅拌待固体完全溶解后,制得Fe:Cu摩尔比1:1且浓度为10mmolL-1的Fe3+盐和Cu2+盐溶液。将2.5g餐厨垃圾生物炭加入到上述溶液中,再加入50gL-1的NaOH溶液提供碱性条件,继续搅拌10分钟左右至完全溶解。将上述混合液转移至水热反应釜,置于均相反应器进行水热反应,在温度为100℃下反应6小时。反应结束,将水热后的产物依次经无水乙醇、0.5molL-1的稀硝酸和去离子水进行离心洗涤至中性,将离心后的产物至于烘箱中在70℃下烘干12小时,即可。Weigh copper chloride (99.99%) and ferric chloride (99.99%) in 60 ml of deionized water at room temperature according to the Fe:Cu molar ratio of 1:1, and continue stirring until the solid is completely dissolved to obtain Fe:Cu moles Fe 3+ salt and Cu 2+ salt solution at a ratio of 1:1 and a concentration of 10 mmol L -1 . 2.5g of food waste biochar was added to the above solution, and then 50gL -1 of NaOH solution was added to provide alkaline conditions, and the stirring was continued for about 10 minutes until it was completely dissolved. The above mixed solution was transferred to a hydrothermal reactor, placed in a homogeneous reactor for hydrothermal reaction, and reacted at a temperature of 100° C. for 6 hours. After the reaction, the product after the hydrothermal treatment was successively washed with dehydrated alcohol, 0.5 molL of dilute nitric acid and deionized water until neutral, and the product after the centrifugation was dried in an oven at 70° C. for 12 hours. That's it.
实施例二Embodiment 2
一种利用餐厨垃圾制取磁性生物炭的方法,本是实例中,餐厨垃圾生物炭量为3.5g,其他步骤与实例一相同,具体如下:A method for producing magnetic biochar from kitchen waste, in this example, the amount of kitchen waste biochar is 3.5g, and other steps are the same as in Example 1, as follows:
(1)餐厨垃圾生物炭的制备(1) Preparation of food waste biochar
收集餐厨垃圾,包括米饭、馒头碎屑、蔬菜和肉类等,自然风干至含水率低于10%,随后粉碎过筛得到粉碎物。将粉碎物放入瓷方舟置于管式炉中,通入氮气提供缺氧条件,以8℃min-1的升温速率升温至600℃,裂解时间为4小时,将裂解产物依次选用无水乙醇、1molL-1的盐酸和去离子水进行洗涤,置于烘箱中在80℃下干燥10小时,将干燥后的产物经研钵研磨,过500目筛子,得到餐厨垃圾生物炭。The kitchen waste is collected, including rice, steamed bread scraps, vegetables and meat, etc., naturally air-dried to a moisture content of less than 10%, and then pulverized and sieved to obtain pulverized products. Put the pulverized product into a porcelain ark and place it in a tube furnace, feed nitrogen to provide anoxic conditions, and heat up to 600 °C at a heating rate of 8 °C min -1 , the cracking time is 4 hours, and the cracked products are sequentially selected from anhydrous ethanol , 1molL -1 hydrochloric acid and deionized water were washed, placed in an oven to dry at 80°C for 10 hours, the dried product was ground in a mortar and passed through a 500-mesh sieve to obtain food waste biochar.
(2)餐厨垃圾磁性生物炭的制备(2) Preparation of kitchen waste magnetic biochar
在室温下按Fe:Cu摩尔比1:1称取Cu(NO3)2·3H2O(99.99%)和Fe(NO3)3·9H2O(99.99%)溶于60ml去离子水中,持续搅拌待固体完全溶解后,制得Fe:Cu摩尔比1:1且浓度为30mmolL-1的Fe3+盐和Cu2+盐溶液。将3.5g餐厨垃圾生物炭加入到上述溶液中,再加入80gL-1的氢氧化钾溶液,提供碱性条件,继续搅拌10分钟至完全溶解。将上述混合液转移至水热反应釜,置于均相反应器进行水热反应,在温度为200℃下反应48小时。反应结束,将水热后的产物依次经无水乙醇、1molL-1的稀硝酸和去离子水进行离心洗涤至中性,将离心后的产物至于烘箱中在80℃下烘干12小时,即可。Weigh Cu(NO 3 ) 2 ·3H 2 O (99.99%) and Fe(NO 3 ) 3 ·9H 2 O (99.99%) at room temperature according to Fe:Cu molar ratio of 1:1 and dissolve them in 60 ml of deionized water, After continuous stirring until the solid was completely dissolved, Fe 3+ salt and Cu 2+ salt solutions with Fe:Cu molar ratio of 1:1 and a concentration of 30 mmolL −1 were prepared. Add 3.5g of food waste biochar to the above solution, and then add 80gL -1 of potassium hydroxide solution to provide alkaline conditions, and continue to stir for 10 minutes until it is completely dissolved. The above mixed solution was transferred to a hydrothermal reactor, placed in a homogeneous reactor for hydrothermal reaction, and reacted at a temperature of 200° C. for 48 hours. After the reaction, the product after the hydrothermal treatment was successively subjected to centrifugation and washing to neutrality through absolute ethanol, 1 molL of dilute nitric acid and deionized water, and the product after the centrifugation was dried in an oven at 80° C. for 12 hours, that is, Can.
实施例三Embodiment 3
一种利用餐厨垃圾制取磁性生物炭的方法,本实施例中,餐厨垃圾生物炭量为5.0g,其他步骤与实例一相同,具体如下:A method for preparing magnetic biochar from kitchen waste, in this embodiment, the amount of kitchen waste biochar is 5.0g, and other steps are the same as in Example 1, and the details are as follows:
(1)餐厨垃圾生物炭的制备(1) Preparation of food waste biochar
收集餐厨垃圾,所述餐厨垃圾包括米饭、馒头碎屑、蔬菜和肉类等,自然风干至含水率低于10%,随后粉碎过筛得到粉碎物。将粉碎物放入瓷方舟置于管式炉中,通入氮气提供缺氧条件,以8℃min-1的升温速率升温至400℃,裂解时间为3小时,将裂解产物依次选用无水乙醇、0.5molL-1的盐酸和去离子水进行洗涤,置于烘箱中在70℃下干燥8小时,将干燥后的产物经研钵研磨,过400目筛子,得到餐厨垃圾生物炭。The kitchen waste is collected, including rice, steamed bread scraps, vegetables and meat, etc., and is naturally air-dried to a moisture content of less than 10%, and then crushed and sieved to obtain crushed products. Put the pulverized product into a porcelain ark and place it in a tube furnace, feed nitrogen to provide anoxic conditions, heat up to 400 °C at a heating rate of 8 °C min -1 , and the cracking time is 3 hours. , 0.5molL -1 hydrochloric acid and deionized water were washed, placed in an oven and dried at 70°C for 8 hours, the dried product was ground in a mortar and passed through a 400-mesh sieve to obtain food waste biochar.
(2)餐厨垃圾磁性生物炭的制备(2) Preparation of kitchen waste magnetic biochar
在室温下按Fe:Cu摩尔比1:1称取五水合硫酸铜(99.99%)和五水合草酸铁(99.99%)溶于60ml去离子水中,持续搅拌待固体完全溶解后,制得Fe:Cu摩尔比1:1且浓度为20mmolL-1的Fe3+盐和Cu2+盐溶液。将5.0g餐厨垃圾生物炭加入到上述溶液中,再加入60gL-1的氢氧化钾溶液中,继续搅拌10分钟至完全溶解。将上述混合液转移至水热反应釜,置于均相反应器进行水热反应,在温度为160℃下反应24小时。反应结束,将水热后的产物依次经无水乙醇、0.5mol L-1的稀硝酸和去离子水进行离心洗涤至中性,将离心后的产物置于烘箱中在80℃下烘干10小时,即可。在其他实施例中五水合草酸铁还可以用硫酸铁取代。Weigh copper sulfate pentahydrate (99.99%) and iron oxalate pentahydrate (99.99%) at room temperature according to Fe:Cu molar ratio of 1:1, dissolve in 60 ml of deionized water, and continue stirring until the solid is completely dissolved to obtain Fe: Fe 3+ salt and Cu 2+ salt solution with Cu molar ratio 1:1 and concentration of 20 mmolL -1 . 5.0g of kitchen waste biochar was added to the above solution, then added to 60gL -1 of potassium hydroxide solution, and continued to stir for 10 minutes until it was completely dissolved. The above mixed solution was transferred to a hydrothermal reactor, placed in a homogeneous reactor for hydrothermal reaction, and reacted at a temperature of 160° C. for 24 hours. After the reaction, the product after the hydrothermal treatment was sequentially washed by dehydrated alcohol, 0.5 mol L of dilute nitric acid and deionized water to neutrality, and the product after the centrifugation was placed in an oven and dried at 80 ° C for 10 ℃. hours, you can. In other embodiments, ferric oxalate pentahydrate can also be replaced with ferric sulfate.
此外,应当理解,虽然本说明书按照实施方式加以描述,但并非每个实施方式仅包含一个独立的技术方案,说明书的这种叙述方式仅仅是为清楚起见,本领域技术人员应当将说明书作为一个整体,各实施例中的技术方案也可以经适当组合,形成本领域技术人员可以理解的其他实施方式。In addition, it should be understood that although this specification is described in terms of embodiments, not each embodiment only includes an independent technical solution, and this description in the specification is only for the sake of clarity, and those skilled in the art should take the specification as a whole , the technical solutions in each embodiment can also be appropriately combined to form other implementations that can be understood by those skilled in the art.
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CN113578300A (en) * | 2021-07-15 | 2021-11-02 | 华南理工大学 | Ag-g-C3N4Biological carbon composite material and preparation method and application thereof |
CN114259985A (en) * | 2021-12-21 | 2022-04-01 | 中州水务控股有限公司 | Method for preparing biochar by using kitchen waste as biomass |
CN114768807A (en) * | 2022-04-29 | 2022-07-22 | 西北工业大学深圳研究院 | Iron-carbon composite Fenton catalyst and preparation method and application thereof |
CN115445573A (en) * | 2022-09-22 | 2022-12-09 | 山东大学 | A method for modifying iron and aluminum of kitchen waste biochar |
CN115744999A (en) * | 2022-09-27 | 2023-03-07 | 青岛农业大学 | CuFeO with delafossite type structure 2 Biological carbon composite material and preparation method thereof |
CN116040752A (en) * | 2022-10-18 | 2023-05-02 | 青岛农业大学 | Preparation method and application of biochar electrode |
CN116040752B (en) * | 2022-10-18 | 2024-05-14 | 青岛农业大学 | Preparation method and application of biochar electrode |
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