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CN111514866A - Solvent recovery efficient wood activated carbon and preparation method thereof - Google Patents

Solvent recovery efficient wood activated carbon and preparation method thereof Download PDF

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Publication number
CN111514866A
CN111514866A CN202010413561.XA CN202010413561A CN111514866A CN 111514866 A CN111514866 A CN 111514866A CN 202010413561 A CN202010413561 A CN 202010413561A CN 111514866 A CN111514866 A CN 111514866A
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activated carbon
solvent recovery
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单由剑
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Hunan Yujie Activated Carbon Environmental Protection Technology Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/261Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid 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 form
    • B01J20/28016Particle form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3007Moulding, shaping or extruding
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds

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  • Engineering & Computer Science (AREA)
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  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Inorganic Chemistry (AREA)
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  • Processing Of Solid Wastes (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

本发明公开了一种溶剂回收高效木质活性炭及其制备方法,其原料重量配比为:木质粉炭95‑105份、聚乙烯醇15‑22份、表面活性剂0.5‑5份、交联剂0.5‑5份和水95‑105份,以木质粉炭作为原炭,聚乙烯醇、表面活性剂、交联剂和水经混合配制成为胶黏剂,将胶黏剂与木质粉炭混合粘结成型后,活性炭被堵塞的孔隙结构较少,制备成型活性炭有更发达的孔隙结构和更好的粘结强度,提高了耐酸碱作用,使用时不掉灰,本申请解决交联剂堵塞炭孔及耐酸碱问题,吸附总量提高5‑10倍,进一步提高活性炭的使用寿命,能很好地适用于溶剂回收,降低企业成本、提高效率。The invention discloses a solvent recovery high-efficiency wood activated carbon and a preparation method thereof. The raw material weight ratio is: 95-105 parts of wood powder carbon, 15-22 parts of polyvinyl alcohol, 0.5-5 parts of surfactant, and 0.5 parts of cross-linking agent. ‑5 parts and 95‑105 parts of water, using wood powder charcoal as raw charcoal, polyvinyl alcohol, surfactant, cross-linking agent and water are mixed to form an adhesive, and the adhesive and wood powder charcoal are mixed and bonded to form , the activated carbon has less pore structure blocked, and the prepared activated carbon has a more developed pore structure and better bonding strength, which improves the acid and alkali resistance, and does not lose ash when used. Acid and alkali resistance problem, the total amount of adsorption is increased by 5-10 times, and the service life of activated carbon is further improved. It can be well applied to solvent recovery, reducing enterprise costs and improving efficiency.

Description

一种溶剂回收高效木质活性炭及其制备方法A kind of solvent recovery high-efficiency wood activated carbon and preparation method thereof

【技术领域】【Technical field】

本发明涉及活性炭技术领域,具体为一种溶剂回收高效木质活性炭及其制备方法。The invention relates to the technical field of activated carbon, in particular to a solvent recovery high-efficiency wood activated carbon and a preparation method thereof.

【背景技术】【Background technique】

随着工业化程度不断深入,人类赖以生存的水、土、空气受污染越来越严重,企业排放的废水、废渣、废气越来越多,三废严重影响人民的生活质量,环境治理变得非常重要,国家也大力推进。企业的生产的三废必须经过处理并达排放标准方可进行排放,去除这些有害物最理想、最有效、最环保的方法就是使用活性炭。With the deepening of industrialization, the water, soil and air that human beings depend on are becoming more and more polluted, and more and more waste water, waste residue and waste gas are discharged by enterprises. The three wastes seriously affect people's quality of life, and environmental governance has become very Important, the country is also vigorously promoting. The three wastes produced by the enterprise must be treated and meet the emission standards before they can be discharged. The most ideal, most effective and most environmentally friendly way to remove these harmful substances is to use activated carbon.

活性炭是一种孔隙发达、化学性质稳定的物质,分为煤质活性炭、木质活性炭和果壳活性炭,其中木质活性炭孔隙更发达。目前大多企业采用的是煤质活性炭进行处理,但存在成本比较高、处理效果不理想、使用寿命短的缺点,不仅增加了企业成本,更重要的是还要处理使用过的活性炭(危废物)。Activated carbon is a substance with developed pores and stable chemical properties. At present, most enterprises use coal-based activated carbon for treatment, but there are disadvantages such as relatively high cost, unsatisfactory treatment effect, and short service life, which not only increases the cost of the enterprise, but also disposes of used activated carbon (hazardous waste). .

木质活性炭用于溶剂回收发展很晚,在此领域占有率不高,其根本原因有:1、耐酸碱性能一般,遇到酸液或碱液时,胶黏剂很快会失去粘性,导致木质活性炭断裂或掉屑造成损失;2、胶黏剂堵塞炭孔,现有木质活性炭中胶黏剂容易渗入到活性炭孔隙内部,对成型活性炭的孔隙产生一定的影响,造成木质活性炭使用寿命相对偏短。因此,必须解决胶黏剂堵塞炭孔及耐酸碱问题,否则木质活性炭很难被适用于溶剂回收。The development of wood activated carbon for solvent recovery is very late, and its share in this field is not high. The fundamental reasons are: 1. The acid and alkali resistance is average. When encountering acid or alkali, the adhesive will quickly lose its viscosity, resulting in The wood activated carbon is broken or chipped, causing losses; 2. The adhesive blocks the carbon pores, and the adhesive in the existing wood activated carbon easily penetrates into the activated carbon pores, which has a certain impact on the pores of the formed activated carbon, resulting in a relatively long service life of the wood activated carbon. short. Therefore, it is necessary to solve the problems of clogging carbon pores and acid and alkali resistance by adhesives, otherwise it is difficult for wood activated carbon to be suitable for solvent recovery.

【发明内容】[Content of the invention]

本发明的目的在于解决现有活性炭使用寿命相对偏短问题,提供开一种能吸附多种VOC气体且吸附量提升的高效改性活性炭,可提高活性炭使用寿命以及降低企业生产大本。The purpose of the present invention is to solve the problem that the service life of the existing activated carbon is relatively short, and to provide a high-efficiency modified activated carbon that can adsorb various VOC gases and increase the adsorption capacity, which can improve the service life of the activated carbon and reduce the production cost of the enterprise.

本发明的另一个目的是提供一种溶剂回收高效木质活性炭的制备方法。Another object of the present invention is to provide a method for preparing high-efficiency wood-based activated carbon for solvent recovery.

本发明提供技术方案如下:一种溶剂回收高效木质活性炭,原料重量配比为:木质粉炭95-105份、聚乙烯醇15-22份、表面活性剂 0.5-5份、交联剂0.5-5份和水95-105份。The present invention provides the following technical solutions: a solvent recovery high-efficiency wood activated carbon, the raw material weight ratio is: 95-105 parts of wood powder carbon, 15-22 parts of polyvinyl alcohol, 0.5-5 parts of surfactant, and 0.5-5 parts of cross-linking agent parts and 95-105 parts of water.

本申请的一种溶剂回收高效木质活性炭,以木质粉炭作为原炭,聚乙烯醇、表面活性剂、交联剂和水经混合配制成为胶黏剂,按一定比例经配胶、混合、挤压成型、破碎、过筛制备而成,胶黏剂配制过程中,聚乙烯醇作为粘合剂与交联剂混合时发生交联反应,由原来的线状结构交叉连接起来变成空间网状结构,形成分子量较大的高聚交联物很难进入活性炭的孔隙内部,同时具有空间网状结构的高聚交联物不仅增加了粘度同时提高了耐酸碱性能,使得粘结性能更好,而表面活性剂的加入提高了高聚交联物的分散程度,同时起到增稠作用,解决了结块问题,在表面活性剂的催化改性作用下进一步提高了胶黏剂的柔韧性和粘结性能,将胶黏剂与木质粉炭混合粘结成型后制得的木质活性炭具有更大的比表面积,活性炭被堵塞的孔隙结构较少,制备成型活性炭有更发达的孔隙结构和更好的粘结强度,微孔结构越发达使得成型的木质活性炭吸附性能更强,粘结强度的增加使得成型产品不再与酸或碱反应,继而提高了耐酸碱作用,使用时不掉灰,本申请解决交联剂堵塞炭孔及耐酸碱问题,能很好地适用于溶剂回收,可大地降低企业成本、提高效率。A kind of solvent recovery high-efficiency wood activated carbon of the present application, using wood powder carbon as raw carbon, polyvinyl alcohol, surfactant, cross-linking agent and water are mixed and prepared into an adhesive, which is compounded, mixed and extruded according to a certain proportion. It is prepared by molding, crushing and sieving. During the preparation process of the adhesive, polyvinyl alcohol as a binder and a cross-linking agent are mixed with a cross-linking reaction, and the original linear structure is cross-connected and becomes a spatial network structure. , it is difficult to form a polymer cross-linked product with a large molecular weight into the pores of the activated carbon. At the same time, the polymer cross-linked product with a spatial network structure not only increases the viscosity but also improves the acid and alkali resistance, making the bonding performance better. The addition of surfactant improves the dispersion degree of the polymer cross-linked product, and at the same time plays a thickening effect, solves the problem of agglomeration, and further improves the flexibility and viscosity of the adhesive under the catalytic modification of the surfactant. The wood activated carbon obtained by mixing the adhesive and wood powder carbon has a larger specific surface area, and the pore structure of the activated carbon is less blocked, and the prepared activated carbon has a more developed pore structure and better adhesion. Bond strength, the more developed the microporous structure, the stronger the adsorption performance of the formed wood activated carbon, the increase of the bonding strength makes the formed product no longer react with acid or alkali, and then improves the acid and alkali resistance, and does not lose ash during use, this application It solves the problem of cross-linking agent blocking carbon pores and acid and alkali resistance, and can be well applied to solvent recovery, which can greatly reduce enterprise costs and improve efficiency.

优选的,所述木质粉炭为采用磷酸法生产的目数≥200目、碘值≥1100mg/g、PH值≥5.6的木质粉状活性炭。所述木质粉炭为污水专用粉状活性炭,具有发达的中孔结构,吸附容量大、快速过滤等特性,可提高溶剂的回收率。Preferably, the wood powdered carbon is wood powder activated carbon with mesh number ≥ 200 mesh, iodine value ≥ 1100 mg/g, and pH value ≥ 5.6 produced by phosphoric acid method. The wood powdered carbon is a special powdered activated carbon for sewage, has developed mesoporous structure, large adsorption capacity, fast filtration and other characteristics, which can improve the recovery rate of the solvent.

优选的,所述聚乙烯醇为PVA1792、PVA1799、PVA2099、PVA2092、 PVA2499、PVA2492中一种或几种组合。其作用是作为粘合剂,能与胶黏剂中其他组分发生交联反应形成网状交联物,将PVA线型结构交联而成网状结构,提高耐酸碱性能,使得活性炭孔隙分布和大小均匀。Preferably, the polyvinyl alcohol is one or a combination of PVA1792, PVA1799, PVA2099, PVA2092, PVA2499 and PVA2492. Its function is as an adhesive, which can cross-link with other components in the adhesive to form a network cross-linked product, cross-link the PVA linear structure to form a network structure, improve acid and alkali resistance, and make activated carbon pores. Evenly distributed and sized.

优选的,所述表面活性剂为椰子油、十二烷基磺酸钠中一种或组合。所述表面活性剂作用是提高活性炭的吸附能力。十二烷基磺酸钠为阴离子表面活性剂起到增稠作用,改变聚乙烯醇的流变性能,提高了聚乙烯醇的分散性和相容性。Preferably, the surfactant is one or a combination of coconut oil and sodium lauryl sulfonate. The function of the surfactant is to improve the adsorption capacity of the activated carbon. Sodium dodecyl sulfonate acts as an anionic surfactant to thicken, change the rheological properties of polyvinyl alcohol, and improve the dispersibility and compatibility of polyvinyl alcohol.

优选的,所述交联剂为硼砂、淀粉中一种或组合。其作用是与聚乙烯醇交联后,将炭分子之间联合固化起来,使得固化后的孔隙结构适合对有害物的吸附。硼砂能与聚乙烯醇的顺式羟基发生交联,使原来的线状结构变成网状结构,形成的具有空间网状结构的高聚物交联物具有抗剪切性能及耐酸碱性等性质,因此粘度增加,粘结性能变好。Preferably, the crosslinking agent is one or a combination of borax and starch. Its function is to combine and solidify the carbon molecules after cross-linking with polyvinyl alcohol, so that the solidified pore structure is suitable for the adsorption of harmful substances. Borax can be cross-linked with the cis-hydroxyl group of polyvinyl alcohol, so that the original linear structure becomes a network structure, and the formed polymer cross-linked product with a spatial network structure has shear resistance and acid and alkali resistance. and other properties, so the viscosity increases and the bonding performance becomes better.

一种溶剂回收高效木质活性炭的制备方法,包括以下步骤:A preparation method of solvent recovery high-efficiency wood activated carbon, comprising the following steps:

S1、备料:按重量配比准备原料,备用;S1. Material preparation: prepare the raw materials according to the weight ratio, spare;

S2、胶黏剂的配制:将聚乙烯醇加入水中搅拌均匀,静置4-6小时后再高速搅拌10-20分钟,加入表面活性剂中速搅拌4-6分钟,再加入交联剂中速搅拌4-6分钟;S2. Preparation of adhesive: Add polyvinyl alcohol into water and stir evenly, let stand for 4-6 hours, then stir at high speed for 10-20 minutes, add surfactant and stir at medium speed for 4-6 minutes, and then add in cross-linking agent Stir at high speed for 4-6 minutes;

S3、混料:将木质粉炭和胶黏剂加入反应釜中,边加入边搅拌,待加入完全后,再继续搅拌0.5-2小时;S3. Mixing: Add the wood powder charcoal and the adhesive to the reaction kettle, stir while adding, and continue stirring for 0.5-2 hours after the addition is complete;

S4、造粒成型:混料后送入造粒设备中,挤压成颗粒炭;S4, granulation and molding: after mixing, it is sent to the granulation equipment and extruded into granular carbon;

S5、烘烤:将颗粒炭烘烤至水分含量≤5%;S5. Baking: Bake the granular charcoal to a moisture content of ≤5%;

S6、破碎过筛:将烘烤好的颗粒炭送入破碎设备中破碎,破碎后过筛,即得。S6, crushing and sieving: the baked granular carbon is sent to crushing equipment to be crushed, and then sieved after crushing.

优选的,步骤S4中挤压成粒径为2-5mm的颗粒炭。Preferably, in step S4, it is extruded into granular carbon with a particle size of 2-5 mm.

优选的,步骤S5中在80-150℃温度下烘烤2-8小时。Preferably, in step S5, baking is performed at a temperature of 80-150° C. for 2-8 hours.

优选的,步骤S6具体包括:将烘烤好的颗粒炭送入破碎设备中破碎成规格为0.9mm-9mm的颗粒状,破碎后进行过筛,选出符合粒径和长度要求的颗粒状真空包装。Preferably, step S6 specifically includes: sending the baked granular carbon into a crushing device to be crushed into granular shapes with a size of 0.9mm-9mm, sieving after crushing, and selecting a granular vacuum that meets the requirements of particle size and length. Package.

优选的,所述中速搅拌为以300-500r/min的转速搅拌,所述高速搅拌为以800-1000r/min的转速搅拌。Preferably, the medium-speed stirring is stirring at a rotational speed of 300-500 r/min, and the high-speed stirring is stirring at a rotational speed of 800-1000 r/min.

本发明相对于现有技术,有以下优点:Compared with the prior art, the present invention has the following advantages:

本发明一种溶剂回收高效木质活性炭,其原料重量配比为:木质粉炭95-105份、聚乙烯醇15-22份、表面活性剂0.5-5份、交联剂 0.5-5份和水95-105份,以木质粉炭作为原炭,聚乙烯醇、表面活性剂、交联剂和水经混合配制成为胶黏剂,按一定比例经配胶、混合、挤压成型、破碎、过筛制备而成,胶黏剂配制过程中,聚乙烯醇作为粘合剂与交联剂混合时发生交联反应,由原来的线状结构交叉连接起来变成空间网状结构,形成分子量较大的高聚交联物很难进入活性炭的孔隙内部,同时具有空间网状结构的高聚交联物不仅增加了粘度同时提高了耐酸碱性能,使得粘结性能更好,而表面活性剂的加入提高了高聚交联物的分散程度,同时起到增稠作用,解决了结块问题,在表面活性剂的催化改性作用下进一步提高了胶黏剂的柔韧性和粘结性能,将胶黏剂与木质粉炭混合粘结成型后,活性炭被堵塞的孔隙结构较少,制备成型活性炭有更发达的孔隙结构和更好的粘结强度,微孔结构越发达使得成型的木质活性炭吸附性能更强,粘结强度的增加使得成型产品不再与酸或碱反应,继而提高了耐酸碱作用,使用时不掉灰,本申请解决交联剂堵塞炭孔及耐酸碱问题,吸附总量提高5-10 倍,进一步提高活性炭的使用寿命,能很好地适用于溶剂回收,降低企业成本、提高效率。The present invention is a solvent recovery high-efficiency wood activated carbon, and the raw material weight ratio is: 95-105 parts of wood powder carbon, 15-22 parts of polyvinyl alcohol, 0.5-5 parts of surfactant, 0.5-5 parts of cross-linking agent and 95 parts of water -105 parts, using wood powder charcoal as raw charcoal, polyvinyl alcohol, surfactant, cross-linking agent and water are mixed to prepare an adhesive, which is prepared by compounding, mixing, extrusion molding, crushing and sieving according to a certain proportion During the preparation of the adhesive, the cross-linking reaction occurs when the polyvinyl alcohol is used as the adhesive and the cross-linking agent is mixed, and the original linear structure is cross-connected into a spatial network structure, forming a high molecular weight high molecular weight. It is difficult for the polymer cross-links to enter the pores of the activated carbon, and the high-polymer cross-links with a spatial network structure not only increase the viscosity but also improve the acid and alkali resistance, making the bonding performance better, and the addition of surfactants improves The dispersion degree of the polymer cross-linked product is improved, and at the same time, it has a thickening effect and solves the problem of agglomeration. Under the catalytic modification of the surfactant, the flexibility and bonding performance of the adhesive are further improved. After mixing and bonding with wood powder carbon, the activated carbon has less pore structure blocked. The prepared activated carbon has a more developed pore structure and better bonding strength. The more developed the microporous structure, the stronger the adsorption performance of the formed wood activated carbon. The increase in bonding strength makes the molded product no longer react with acid or alkali, thereby improving the acid and alkali resistance, and no ash will be lost when used. -10 times, further improve the service life of activated carbon, can be well applied to solvent recovery, reduce enterprise cost and improve efficiency.

本发明的一种溶剂回收高效木质活性炭的制备方法,制备技术简单,木质粉炭原料经过特殊工艺生产,制得的溶剂回收高效木质活性炭使用寿命可提高50%以上,企业使用成本可降低30%以上,适合大批量连续生产。The preparation method of the solvent recovery high-efficiency wood activated carbon of the invention has the advantages of simple preparation technology, and the wood powder carbon raw material is produced by a special process, the service life of the solvent recovery high-efficiency wood activated carbon can be increased by more than 50%, and the enterprise use cost can be reduced by more than 30%. , suitable for mass continuous production.

【具体实施方式】【Detailed ways】

下面结合具体实施例1~4说明本发明的具体技术方案:The specific technical solutions of the present invention are described below in conjunction with specific embodiments 1 to 4:

实施例1:Example 1:

一种的溶剂回收高效木质活性炭的制备方法,包括以下步骤:A kind of preparation method of solvent recovery high-efficiency wood activated carbon, comprises the following steps:

S1、备料:按表1重量配比准备原料,备用;S1. Material preparation: prepare the raw materials according to the weight ratio in Table 1, for use;

S2、胶黏剂的配制:将聚乙烯醇加入水中搅拌均匀,静置6小时后再高速搅拌10分钟,加入表面活性剂中速搅拌4分钟,再加入交联剂中速搅拌4分钟,备用;S2. Preparation of adhesive: add polyvinyl alcohol into water and stir evenly, let stand for 6 hours, then stir at high speed for 10 minutes, add surfactant and stir at medium speed for 4 minutes, and then add crosslinking agent and stir at medium speed for 4 minutes. ;

S3、混料:将木质粉炭和胶黏剂按重量比100:22加入反应釜中,边加入边搅拌,待加入完全后,再继续搅拌1小时;S3. Mixing: add the wood powder charcoal and the adhesive to the reaction kettle at a weight ratio of 100:22, and stir while adding, and continue stirring for 1 hour after the addition is complete;

S4、造粒成型:混料后送入造粒设备中,挤压成粒径为2-5mm的颗粒炭;S4, granulation and molding: after mixing, it is sent to the granulation equipment, and extruded into granular carbon with a particle size of 2-5mm;

S5、烘烤:将颗粒炭在120℃温度下烘烤4小时,检测水分含量≤5%;S5. Baking: Bake the granular carbon at a temperature of 120 °C for 4 hours, and the detected moisture content is less than or equal to 5%;

S6、破碎过筛:将烘烤好的颗粒炭送入破碎设备中破碎成规格为 0.9mm-9mm的颗粒状,破碎后进行过筛,选出符合粒径和长度要求的颗粒状真空包装,即得(上述高速搅拌为1000r/min,中速搅拌为 500r/min)。S6. Crushing and sieving: The baked granular carbon is sent to the crushing equipment to be crushed into granules with a size of 0.9mm-9mm, and then sieved after crushing, and the granular vacuum packaging that meets the requirements of particle size and length is selected. That is (the above-mentioned high-speed stirring is 1000 r/min, and the medium-speed stirring is 500 r/min).

实施例2:Example 2:

一种的溶剂回收高效木质活性炭的制备方法,包括以下步骤:A kind of preparation method of solvent recovery high-efficiency wood activated carbon, comprises the following steps:

S1、备料:按表1重量配比准备原料,备用;S1. Material preparation: prepare the raw materials according to the weight ratio in Table 1, for use;

S2、胶黏剂的配制:将聚乙烯醇加入水中搅拌均匀,静置5小时后再高速搅拌20分钟,加入表面活性剂中速搅拌5分钟,再加入交联剂中速搅拌5分钟,备用;S2. Preparation of adhesive: Add polyvinyl alcohol into water and stir evenly, let stand for 5 hours, then stir at high speed for 20 minutes, add surfactant and stir at medium speed for 5 minutes, and then add crosslinking agent and stir at medium speed for 5 minutes. ;

S3、混料:将木质粉炭和胶黏剂按重量比100:30加入反应釜中,边加入边搅拌,待加入完全后,再继续搅拌1.5小时;S3. Mixing: add the wood powder charcoal and the adhesive to the reaction kettle at a weight ratio of 100:30, stir while adding, and continue stirring for 1.5 hours after the addition is complete;

S4、造粒成型:混料后送入造粒设备中,挤压成粒径为2-5mm的颗粒炭;S4, granulation and molding: after mixing, it is sent to the granulation equipment, and extruded into granular carbon with a particle size of 2-5mm;

S5、烘烤:将颗粒炭在150℃温度下烘烤2小时,检测水分含量≤5%;S5. Baking: Bake the granular carbon at a temperature of 150 °C for 2 hours, and the moisture content is less than or equal to 5%;

S6、破碎过筛:将烘烤好的颗粒炭送入破碎设备中破碎成规格为 0.9mm-9mm的颗粒状,破碎后进行过筛,选出符合粒径和长度要求的颗粒状真空包装,即得(上述高速搅拌为800r/min,中速搅拌为 300r/min)。S6. Crushing and sieving: The baked granular carbon is sent to the crushing equipment to be crushed into granules with a size of 0.9mm-9mm, and then sieved after crushing, and the granular vacuum packaging that meets the requirements of particle size and length is selected. That is (the above-mentioned high-speed stirring is 800 r/min, and the medium-speed stirring is 300 r/min).

实施例3:Example 3:

S1、备料:按表1重量配比准备原料,备用;S1. Material preparation: prepare the raw materials according to the weight ratio in Table 1, for use;

S2、胶黏剂的配制:将聚乙烯醇加入水中搅拌均匀,静置4小时后再高速搅拌15分钟,加入表面活性剂中速搅拌5分钟,再加入交联剂中速搅拌5分钟,备用;S2. Preparation of adhesive: Add polyvinyl alcohol into water and stir evenly, let stand for 4 hours, then stir at high speed for 15 minutes, add surfactant and stir at medium speed for 5 minutes, and then add crosslinking agent and stir at medium speed for 5 minutes. ;

S3、混料:将木质粉炭和胶黏剂按重量比100:1加入反应釜中,边加入边搅拌,待加入完全后,再继续搅拌0.5小时;S3. Mixing: Add the wood powder charcoal and the adhesive to the reaction kettle in a weight ratio of 100:1, and stir while adding, and continue stirring for 0.5 hours after the addition is complete;

S4、造粒成型:混料后送入造粒设备中,挤压成粒径为2-5mm的颗粒炭;S4, granulation and molding: after mixing, it is sent to the granulation equipment, and extruded into granular carbon with a particle size of 2-5mm;

S5、烘烤:将颗粒炭在80℃温度下烘烤8小时,检测水分含量≤5%;S5. Baking: Bake the granular carbon at a temperature of 80 °C for 8 hours, and the detected moisture content is less than or equal to 5%;

S6、破碎过筛:将烘烤好的颗粒炭送入破碎设备中破碎成规格为0.9mm-9mm的颗粒状,破碎后进行过筛,选出符合粒径和长度要求的颗粒状真空包装,即得(上述高速搅拌为900r/min,中速搅拌为 400r/min)。S6. Crushing and sieving: The baked granular carbon is sent to the crushing equipment to be crushed into granules with a size of 0.9mm-9mm, and then sieved after crushing, and the granular vacuum packaging that meets the requirements of particle size and length is selected. That is (the above high-speed stirring is 900 r/min, and the medium-speed stirring is 400 r/min).

实施例4:Example 4:

S1、备料:按表1重量配比准备原料,备用;S1. Material preparation: prepare the raw materials according to the weight ratio in Table 1, for use;

S2、胶黏剂的配制:将聚乙烯醇加入水中搅拌均匀,静置4.5小时后再高速搅拌12分钟,加入表面活性剂中速搅拌5.5分钟,再加入交联剂中速搅拌5.5分钟,备用;S2. Preparation of adhesive: add polyvinyl alcohol into water and stir evenly, let stand for 4.5 hours, then stir at high speed for 12 minutes, add surfactant and stir at medium speed for 5.5 minutes, and then add crosslinking agent and stir at medium speed for 5.5 minutes. ;

S3、混料:将木质粉炭和胶黏剂按重量比100:14加入反应釜中,边加入边搅拌,待加入完全后,再继续搅拌1小时;S3. Mixing: add the wood powder charcoal and the adhesive to the reaction kettle in a weight ratio of 100:14, stir while adding, and continue stirring for 1 hour after the addition is complete;

S4、造粒成型:混料后送入造粒设备中,挤压成粒径为2-5mm的颗粒炭;S4, granulation and molding: after mixing, it is sent to the granulation equipment, and extruded into granular carbon with a particle size of 2-5mm;

S5、烘烤:将颗粒炭在130℃温度下烘烤3小时,检测水分含量≤5%;S5. Baking: Bake the granular carbon at a temperature of 130 °C for 3 hours, and the detected moisture content is less than or equal to 5%;

S6、破碎过筛:将烘烤好的颗粒炭送入破碎设备中破碎成规格为 0.9mm-9mm的颗粒状,破碎后进行过筛,选出符合粒径和长度要求的颗粒状真空包装,即得(上述高速搅拌为1000r/min,中速搅拌为500r/min)。S6. Crushing and sieving: The baked granular carbon is sent to the crushing equipment to be crushed into granules with a size of 0.9mm-9mm, and then sieved after crushing, and the granular vacuum packaging that meets the requirements of particle size and length is selected. That is (the above-mentioned high-speed stirring is 1000 r/min, and the medium-speed stirring is 500 r/min).

表1:实施例1~4溶剂回收高效木质活性炭的组分配比:Table 1: The component allocation ratio of embodiment 1~4 solvent recovery high-efficiency wood activated carbon:

Figure BDA0002494204530000091
Figure BDA0002494204530000091

测试实验:Test experiment:

1、吸附总量:分别取相同量的实施例1~4所制得的溶剂回收高效木质活性炭和市售某品牌木质活性炭(对比例)在相同条件下处理污水,进行活性炭吸附总量测试,测试结果如表2所示。其中活性炭吸附总量q的计算公式为:q=V(C0-Ci)/W;其中V污水体积,单位L;C0为吸附前原污水有机物初始浓度,单位mg/L;Ci为吸附后处理水有机物平衡浓度,单位mg/L;W为木质活性炭的用量,单位g。1. Total amount of adsorption: Take the same amount of solvent recovery high-efficiency wood activated carbon prepared in Examples 1 to 4 and commercially available wood activated carbon of a certain brand (comparative example) to treat sewage under the same conditions, and carry out the total adsorption test of activated carbon, The test results are shown in Table 2. The formula for calculating the total amount q adsorbed by activated carbon is: q=V(C 0 -C i )/W; where V is the volume of sewage, in L; C 0 is the initial concentration of organic matter in the raw sewage before adsorption, in mg/L; C i is Equilibrium concentration of organic matter in water after adsorption, unit mg/L; W is the amount of wood activated carbon, unit g.

2、耐酸性:将实施例1~4所制得的溶剂回收高效木质活性炭和市售某品牌木质活性炭(对比例)浸泡在盐酸溶液中,观察实验样品变化,测试结果如表2所示。2. Acid resistance: The solvent recovery high-efficiency wood activated carbon prepared in Examples 1 to 4 and the commercially available wood activated carbon of a certain brand (comparative example) were soaked in hydrochloric acid solution, and the changes of the experimental samples were observed. The test results are shown in Table 2.

3、耐碱性:将实施例1~4所制得的溶剂回收高效木质活性炭和市售某品牌木质活性炭(对比例)浸泡在碳酸钠溶液中,观察实验样品变化,测试结果如表2所示。3. Alkali resistance: the solvent recovery high-efficiency wood activated carbon prepared in Examples 1 to 4 and the commercially available wood activated carbon of a certain brand (comparative example) were soaked in sodium carbonate solution, and the changes of the experimental samples were observed, and the test results were shown in Table 2. Show.

4、净化能力测试,分别测试实施例1~4所制得的溶剂回收高效木质活性炭和市售某品牌木质活性炭(对比例)的CADR值,测试仪器:激光粒子计数器,测试环境:温度为:25±1.5℃,湿度为:40 ±5%,测试结果如表2所示。4. Purification ability test, test the CADR value of the solvent recovery high-efficiency wood activated carbon prepared in Examples 1 to 4 and the commercially available wood activated carbon of a certain brand (comparative example), test instrument: laser particle counter, test environment: temperature is: 25±1.5℃, humidity: 40±5%, the test results are shown in Table 2.

表2测试结果:Table 2 Test results:

Figure BDA0002494204530000101
Figure BDA0002494204530000101

从表2测试数据可知,本申请实施例相较对比例,其吸附总量可提高5-10倍,本申请胶黏剂固化后可以使得活性炭孔隙大小和分布均匀,避免堵塞活性炭空隙,提高孔隙密度,孔隙结构适合对有害物的吸附,而对比例由于炭分子间的空隙堵塞,损失了很多有效吸附的孔,导致吸附到一定量后会中毒不再吸附。且本申请具有很好的耐酸碱性,胶黏剂在生产过程中发生交联反应,使得产品不再与酸或碱反应,继而提高了耐酸碱作用,使用时不掉灰,而对比例遇酸或碱会破坏里面的胶,使胶很快失去粘性,继而炭失去连接作用而脱落,从而炭颗粒分散变成泥样,失去作用;相较对比例本申请还具有很好的净化能力;本申请解决交联剂堵塞炭孔及耐酸碱问题,能很好地适用于溶剂回收,可大地降低企业成本、提高效率。From the test data in Table 2, it can be seen that the total amount of adsorption in the examples of the present application can be increased by 5-10 times compared with the comparative examples. After the adhesive of the present application is cured, the size and distribution of the activated carbon pores can be made uniform, so as to avoid blocking the activated carbon pores and improve the pore size. The density and pore structure are suitable for the adsorption of harmful substances, while the comparative example loses a lot of effective adsorption pores due to the blockage of the gaps between the carbon molecules, resulting in poisoning and no longer adsorption after a certain amount of adsorption. In addition, the present application has good acid and alkali resistance, and the adhesive undergoes a cross-linking reaction during the production process, so that the product no longer reacts with acid or alkali, thereby improving acid and alkali resistance, and does not lose ash during use, and The proportion of acid or alkali will destroy the glue inside, so that the glue quickly loses its viscosity, and then the carbon loses its connection and falls off, so that the carbon particles are dispersed and become mud-like and lose their effect; compared with the comparative example, the present application also has a good purification effect. Ability; the application solves the problem of crosslinking agent blocking carbon pores and acid and alkali resistance, can be well applied to solvent recovery, can greatly reduce enterprise costs and improve efficiency.

Claims (10)

1.一种溶剂回收高效木质活性炭,其特征在于,其原料重量配比为:木质粉炭95-105份、聚乙烯醇15-22份、表面活性剂0.5-5份、交联剂0.5-5份和水95-105份。1. a solvent recovery high-efficiency wood activated carbon is characterized in that, its raw material weight proportioning is: 95-105 parts of wood powder carbon, 15-22 parts of polyvinyl alcohol, 0.5-5 part of surfactant, 0.5-5 part of crosslinking agent parts and 95-105 parts of water. 2.根据权利要求1所述的一种溶剂回收高效木质活性炭,其特征在于:所述木质粉炭为采用磷酸法生产的目数≥200目、碘值≥1100mg/g、PH值≥5.6的木质粉状活性炭。2. a kind of solvent recovery high-efficiency wood activated carbon according to claim 1, is characterized in that: described wood powder charcoal is the wood that adopts phosphoric acid method to produce order number ≥ 200 orders, iodine value ≥ 1100mg/g, pH value ≥ 5.6 Powdered activated carbon. 3.根据权利要求1所述的一种溶剂回收高效木质活性炭,其特征在于:所述聚乙烯醇为PVA1792、PVA1799、PVA2099、PVA2092、PVA2499、PVA2492中一种或几种组合。3. a kind of solvent recovery high-efficiency wood activated carbon according to claim 1 is characterized in that: described polyvinyl alcohol is one or more combinations in PVA1792, PVA1799, PVA2099, PVA2092, PVA2499, PVA2492. 4.根据权利要求1所述的一种溶剂回收高效木质活性炭,其特征在于:所述表面活性剂为椰子油、十二烷基磺酸钠中一种或组合。4. a kind of solvent recovery high-efficiency wood activated carbon according to claim 1 is characterized in that: described tensio-active agent is one or a combination in coconut oil, sodium dodecyl sulfonate. 5.根据权利要求1所述的一种溶剂回收高效木质活性炭,其特征在于:所述交联剂为硼砂、淀粉中一种或组合。5. a kind of solvent recovery high-efficiency wood activated carbon according to claim 1 is characterized in that: described cross-linking agent is one or a combination of borax and starch. 6.一种根据权利要求1-5任一项所述的溶剂回收高效木质活性炭的制备方法,其特征在于包括以下步骤:6. a preparation method of solvent recovery high-efficiency wood activated carbon according to any one of claims 1-5, is characterized in that comprising the following steps: S1、备料:按重量配比准备原料,备用;S1. Material preparation: prepare the raw materials according to the weight ratio, spare; S2、胶黏剂的配制:将聚乙烯醇加入水中搅拌均匀,静置4-6小时后再高速搅拌10-20分钟,而后加入表面活性剂中速搅拌4-6分钟,再加入交联剂中速搅拌4-6分钟;S2. Preparation of adhesive: add polyvinyl alcohol into water and stir evenly, let stand for 4-6 hours, then stir at high speed for 10-20 minutes, then add surfactant and stir at medium speed for 4-6 minutes, and then add cross-linking agent Mix at medium speed for 4-6 minutes; S3、混料:将木质粉炭和胶黏剂加入反应釜中,边加入边搅拌,待加入完全后,再继续搅拌0.5-2小时;S3. Mixing: Add the wood powder charcoal and the adhesive to the reaction kettle, stir while adding, and continue stirring for 0.5-2 hours after the addition is complete; S4、造粒成型:混料后送入造粒设备中,挤压成颗粒炭;S4, granulation and molding: after mixing, it is sent to the granulation equipment and extruded into granular carbon; S5、烘烤:将颗粒炭烘烤至水分含量≤5%;S5. Baking: Bake the granular charcoal to a moisture content of ≤5%; S6、破碎过筛:将烘烤好的颗粒炭送入破碎设备中破碎,破碎后过筛,即得。S6, crushing and sieving: the baked granular carbon is sent to crushing equipment to be crushed, and then sieved after crushing. 7.根据权利要求6所述的溶剂回收高效木质活性炭的制备方法,其特征在于:步骤S5中在80-150℃温度下烘烤2-8小时。7. The preparation method of solvent recovery high-efficiency wood activated carbon according to claim 6, characterized in that: in step S5, baking is performed at a temperature of 80-150° C. for 2-8 hours. 8.根据权利要求6所述的溶剂回收高效木质活性炭的制备方法,其特征在于:步骤S6具体包括:将烘烤好的颗粒炭送入破碎设备中破碎成规格为0.9mm-9mm的颗粒状,破碎后进行过筛,选出符合粒径和长度要求的颗粒状真空包装。8. The preparation method of solvent recovery high-efficiency wood-based activated carbon according to claim 6, characterized in that: step S6 specifically comprises: sending the baked granular carbon into a crushing device to be crushed into granular particles with a specification of 0.9mm-9mm , sieve after crushing, and select granular vacuum packaging that meets the requirements of particle size and length. 9.根据权利要求6所述的溶剂回收高效木质活性炭的制备方法,其特征在于:所述中速搅拌为以300-500r/min的转速搅拌,所述高速搅拌为以800-1000r/min的转速搅拌。9. the preparation method of solvent recovery high-efficiency wood-based activated carbon according to claim 6, is characterized in that: described medium-speed stirring is stirring with the rotating speed of 300-500r/min, and described high-speed stirring is with 800-1000r/min Stir at speed. 10.根据权利要求6所述的溶剂回收高效木质活性炭的制备方法,其特征在于:步骤S4中挤压成粒径为2-5mm的颗粒炭。10. The method for preparing high-efficiency wood-based activated carbon for solvent recovery according to claim 6, characterized in that: in step S4, it is extruded into granular carbon with a particle size of 2-5 mm.
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