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CN104941663A - Preparation method of high acid content solid acid catalyst - Google Patents

Preparation method of high acid content solid acid catalyst Download PDF

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Publication number
CN104941663A
CN104941663A CN201510286135.3A CN201510286135A CN104941663A CN 104941663 A CN104941663 A CN 104941663A CN 201510286135 A CN201510286135 A CN 201510286135A CN 104941663 A CN104941663 A CN 104941663A
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acid catalyst
solid acid
mixture
preparation
solid
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郭万平
郭锐
刘娟
顾岩
余林
王洛生
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Guangzhou Aoyin Biological Science & Technology Co Ltd
Guangdong University of Technology
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Guangzhou Aoyin Biological Science & Technology Co Ltd
Guangdong University of Technology
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Priority to CN201510286135.3A priority Critical patent/CN104941663A/en
Priority to PCT/CN2015/083776 priority patent/WO2016192175A1/en
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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
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/02Sulfur, selenium or tellurium; Compounds thereof
    • B01J27/053Sulfates
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/05Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30

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  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
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Abstract

本发明公开了一种高酸量固体酸催化剂的制备方法,该方法以植物废料为原料,首先将植物废料干燥后粉碎过筛,在搅拌下加入到浓硫酸中并混合均匀,然后在室温下脱水碳化10~24h,100~200℃下进一步磺化15~30h,得到固体混合物;将该混合物用热水洗涤,除净固体混合物中残留的液体酸,洗净后的固体物经过滤、烘干、粉碎,即制得固体酸催化剂;所得固体酸酸度为3.5~5.0mmol/g,该固体酸催化剂称作GDUT-1;本发明制备方法简易可行,利用该方法制得的GDUT-1固体酸催化剂具有酸量高、催化活性好、可循环利用、绿色环保等特点,并且制备成本低廉,适合工业化生产。The invention discloses a preparation method of a high-acid solid acid catalyst. The method uses plant waste as raw material. Firstly, the plant waste is dried, crushed and sieved, added to concentrated sulfuric acid under stirring and mixed uniformly, and then heated at room temperature Dehydration and carbonization for 10-24 hours, further sulfonation at 100-200°C for 15-30 hours to obtain a solid mixture; wash the mixture with hot water to remove the residual liquid acid in the solid mixture, and filter and dry the washed solid Dry and pulverize to obtain a solid acid catalyst; the acidity of the obtained solid acid is 3.5 to 5.0 mmol/g, and the solid acid catalyst is called GDUT-1; the preparation method of the present invention is simple and feasible, and the GDUT-1 solid prepared by this method is The acid catalyst has the characteristics of high acid content, good catalytic activity, recyclable utilization, green environmental protection, etc., and has low preparation cost, and is suitable for industrial production.

Description

一种高酸量固体酸催化剂的制备方法A kind of preparation method of high acid content solid acid catalyst

技术领域 technical field

   本发明属于固体酸催化剂技术领域,具体涉及一种高酸量固体酸催化剂的制备方法。 The invention belongs to the technical field of solid acid catalysts, and in particular relates to a preparation method of a high acid content solid acid catalyst.

背景技术 Background technique

    在现代化学工业生产中,酸催化剂占据十分重要的地位,液体酸催化剂如硫酸、盐酸、磷酸、氢氟酸、对甲苯磺酸等因具有催化性能良好、价格低廉等特点大量应用于化工生产中,但存在对设备腐蚀严重,难以重复再生利用,与反应物及产物难分离,三废排放量大等缺点,给人类的健康、工作和生存环境造成了严重的负面影响。 In the production of modern chemical industry, acid catalyst occupies a very important position. Liquid acid catalysts such as sulfuric acid, hydrochloric acid, phosphoric acid, hydrofluoric acid, p-toluenesulfonic acid, etc. are widely used in chemical production because of their good catalytic performance and low price. , but there are shortcomings such as serious corrosion to equipment, difficulty in repeated recycling, difficulty in separation from reactants and products, and large discharge of three wastes, which have caused serious negative effects on human health, work and living environment.

    随着人们环保意识的增强以及绿色化学概念的提出,开发效益兼顾环境、实现化学工业品清洁化生产的固体酸催化剂已成为促使化学工业可持续发展的内在需求。相比于液体酸催化剂,固体酸催化剂具有催化剂与原料和产物易分离,可回收重复利用,不腐蚀反应设备以及不污染环境等优点。其中,生物质固体酸催化剂因具有催化反应性能良好、成本低廉、资源化有效利用等优点成为催化剂制备领域的研究热点,但目前这类催化剂主要是通过高温碳化磺化法制得,即将原料在高温(>350℃)下在惰性气氛保护下进行不完全碳化,再用浓硫酸或者发烟硫酸对其进行磺酸化处理。这种方法操作比较复杂,需要高温、惰性气氛等制备条件,并且制得的固体酸催化剂比表面积小,原有结构破坏严重,同时表面酸量低且易于流失。例如中国发明专利申请CN104475127A报道用菠萝渣制成活性炭,再用制得的活性炭制备固体酸催化剂,需要在450~500℃下高温活化。可以看出,现有的生物质固体酸制备工艺很难用于大规模工业化生产,因此急需改进制备工艺,用简易的方法合成一种高酸量、结构稳定、并且适合工业化生产的固体酸催化剂,从而实现将此类催化剂真正用于化学工业品清洁化生产的目的。 With the enhancement of people's awareness of environmental protection and the introduction of the concept of green chemistry, the development of solid acid catalysts that take into account the environment and realize the clean production of chemical industrial products has become an internal demand for the sustainable development of the chemical industry. Compared with liquid acid catalysts, solid acid catalysts have the advantages of easy separation of catalysts, raw materials and products, recyclable reuse, no corrosion of reaction equipment, and no pollution to the environment. Among them, biomass solid acid catalyst has become a research hotspot in the field of catalyst preparation due to its good catalytic performance, low cost, and effective utilization of resources. (>350°C) under the protection of an inert atmosphere for incomplete carbonization, and then sulfonate it with concentrated sulfuric acid or fuming sulfuric acid. This method is relatively complicated to operate, requires high temperature, inert atmosphere and other preparation conditions, and the prepared solid acid catalyst has a small specific surface area, serious damage to the original structure, and low surface acid content and is easy to lose. For example, Chinese invention patent application CN104475127A reports that pineapple pomace is used to make activated carbon, and then the prepared activated carbon is used to prepare a solid acid catalyst, which needs to be activated at a high temperature of 450-500°C. It can be seen that the existing biomass solid acid preparation process is difficult to be used in large-scale industrial production, so there is an urgent need to improve the preparation process and use a simple method to synthesize a solid acid catalyst with high acid content, stable structure, and suitable for industrial production , so as to realize the purpose of using this kind of catalyst in the clean production of chemical industrial products.

发明内容 Contents of the invention

    本发明解决的技术问题在于提供一种高酸量固体酸催化剂的制备方法,利用该方法制得的固体酸表面酸度为3.5~5.0mmol/g,该固体酸催化剂称作GDUT-1,具有低成本、高酸量、简易高效、适合工业化生产的特点。 The technical problem that the present invention solves is to provide a kind of preparation method of solid acid catalyst with high acid content, the solid acid surface acidity that utilizes this method to make is 3.5~5.0mmol/g, and this solid acid catalyst is called GDUT-1, has low Low cost, high acid content, simple and efficient, suitable for industrial production.

为实现上述技术目标,本发明采用的技术方案是: For realizing above-mentioned technical goal, the technical scheme that the present invention adopts is:

一种高酸量固体酸催化剂的制备方法,该方法以植物废料为原料,先加入浓硫酸脱水碳化,后进行磺化,包括以下步骤: A preparation method of a high-acid solid acid catalyst, the method uses plant waste as raw material, first adds concentrated sulfuric acid for dehydration and carbonization, and then performs sulfonation, comprising the following steps:

 (1)将干燥的植物废料粉碎并20~80目过筛; (1) Crush the dried plant waste and sieve it with 20-80 mesh;

 (2)过筛后加入到浓硫酸中并机械搅拌,在室温下脱水碳化10~24h,然后在烘箱中100~200℃下磺化15~30h,得到固体混合物; (2) After sieving, add to concentrated sulfuric acid and mechanically stir, dehydrate and carbonize at room temperature for 10-24 hours, and then sulfonate in an oven at 100-200°C for 15-30 hours to obtain a solid mixture;

 (3)将该混合物水洗至滤液中pH不再变化,然后过滤、烘干,粉碎并20~80目过筛即制得固体酸催化剂。 (3) Wash the mixture with water until the pH of the filtrate does not change, then filter, dry, pulverize and sieve with 20-80 meshes to obtain a solid acid catalyst.

所述步骤(1)中植物废料为黄姜废渣、椰糠、米糠、麦壳、花生壳、竹屑、木屑、秸秆的任意一种或几种。 The plant waste in the step (1) is any one or more of turmeric waste residue, coconut bran, rice bran, wheat husk, peanut shell, bamboo chips, wood chips, and straw.

所述步骤(2)中按植物废料与浓硫酸的质量比1:1~10的比例将植物废料加入到浓硫酸中。 In the step (2), the plant waste is added to the concentrated sulfuric acid at a mass ratio of plant waste to concentrated sulfuric acid of 1:1-10.

所述步骤(3)中水洗方法为按混合物与水的质量/体积比1:3~5的比例向混合物中加水,置于60~80℃的水浴锅中磁力搅拌,搅拌时间为30~60min,水洗4~6次。 The water washing method in the step (3) is to add water to the mixture according to the mass/volume ratio of the mixture and water in the ratio of 1:3-5, and place it in a water bath at 60-80°C for magnetic stirring, and the stirring time is 30-60 minutes , washed 4 to 6 times with water.

   本发明制得的GDUT-1固体酸催化剂以廉价易得的植物废料为原料,利用浓硫酸的脱水性以及强酸性将原料在室温下脱水碳化,得到具有稳定结构的固体炭材料,再进一步在100~200℃下加热磺化,因而能够保持生物质原有的结构特性,形成结构稳定、比表面积大、酸量高的固体酸催化剂。 The GDUT-1 solid acid catalyst prepared by the present invention uses cheap and easy-to-obtain plant waste as raw material, and utilizes the dehydration and strong acidity of concentrated sulfuric acid to dehydrate and carbonize the raw material at room temperature to obtain a solid carbon material with a stable structure. Heating sulfonation at 100-200°C, so that the original structural characteristics of biomass can be maintained, and a solid acid catalyst with stable structure, large specific surface area and high acid content can be formed.

本发明与现有的生物质固体酸催化剂制备技术相比,具有以下有益效果: Compared with the existing biomass solid acid catalyst preparation technology, the present invention has the following beneficial effects:

   (1)制备工艺简单,生物质原有结构没有破坏。先在室温下脱水碳化,然后在100~200℃下磺化即可,无需高温和惰性气氛,植物废料成本低廉,适合工业化生产; (1) The preparation process is simple, and the original structure of the biomass is not damaged. Dehydration and carbonization at room temperature first, and then sulfonation at 100-200 ° C, without high temperature and inert atmosphere, low cost of plant waste, suitable for industrial production;

   (2)制得的GDUT-1固体酸催化剂酸量高,为3.5~5.0mmol/g。热稳定性高,热分解温度在200℃以上,并且具有较高的催化活性,且可多次循环利用,是一种具有广泛应用前景的高效、稳定、清洁催化剂。 (2) The prepared GDUT-1 solid acid catalyst has a high acid content of 3.5-5.0 mmol/g. It has high thermal stability, thermal decomposition temperature above 200°C, high catalytic activity, and can be recycled many times. It is an efficient, stable and clean catalyst with wide application prospects.

具体实施方式 Detailed ways

   下面结合具体实施例对本发明的技术方案作详细的说明,以下实施例是为了本领域的技术人员更好地理解本发明,而非限制本发明的技术方案。 The technical solution of the present invention will be described in detail below in conjunction with specific examples. The following examples are for those skilled in the art to better understand the present invention, rather than limiting the technical solution of the present invention.

实施例1 Example 1

将干燥的黄姜废渣粉碎并80目过筛;称取350g姜渣粉加入到350g浓硫酸中,机械搅拌,搅拌时间为18h,然后置于烘箱中,150℃6h,190℃12h得到混合物,按混合物质量与水体积比1:3比例向混合物中加水,置于70℃水浴锅中磁力搅拌,搅拌时间为60min,水洗4次,水洗后过滤烘干,粉碎并80目过筛即制得GDUT-1固体酸催化剂,酸度为4.28mmol/g。 Grind the dried turmeric waste residue and sieve it through 80 meshes; weigh 350g ginger residue powder and add it to 350g concentrated sulfuric acid, stir it mechanically for 18 hours, then place it in an oven at 150°C for 6h and 190°C for 12h to obtain the mixture, press Add water to the mixture at a ratio of 1:3 between the mass of the mixture and the volume of water, place it in a water bath at 70°C for magnetic stirring, stir for 60 minutes, wash with water 4 times, filter and dry after washing, crush and sieve through an 80-mesh sieve to obtain GDUT -1 solid acid catalyst, acidity is 4.28mmol/g.

实施例2 Example 2

将干燥的椰糠粉碎并60目过筛;称取150g椰糠粉加入到450g浓硫酸中,机械搅拌,搅拌时间为12h,然后置于烘箱中,140℃6h,200℃10h得到混合物,按混合物质量与水体积比1:5比例向混合物中加水,置于60℃水浴锅中磁力搅拌,搅拌时间为50min,水洗5次,水洗后过滤烘干,粉碎并60目过筛即制得GDUT-1固体酸催化剂,酸度为4.84mmol/g。 Grind the dried coconut peat and sieve it through a 60-mesh sieve; weigh 150g of coconut peat powder and add it to 450g of concentrated sulfuric acid, stir it mechanically for 12 hours, then place it in an oven, heat it at 140°C for 6h, and at 200°C for 10h to obtain the mixture, press Add water to the mixture at a ratio of 1:5 between the mass of the mixture and the volume of water, place it in a water bath at 60°C for magnetic stirring, stir for 50 minutes, wash with water 5 times, filter and dry after washing, crush and sieve through a 60-mesh sieve to obtain GDUT -1 solid acid catalyst, acidity is 4.84mmol/g.

实施例3 Example 3

将干燥的米糠粉碎并20目过筛;称取300g米糠粉加入到1500g浓硫酸中,机械搅拌,搅拌时间为20h,然后置于烘箱中,130℃8h,180℃16h得到混合物,按混合物质量与水体积比1:4比例向混合物中加水,置于80℃水浴锅中磁力搅拌,搅拌时间为40min,水洗6次,水洗后过滤烘干,粉碎并20目过筛即制得GDUT-1固体酸催化剂,酸度为4.25mmol/g。 Grind the dried rice bran and sieve it with 20 meshes; weigh 300g of rice bran powder and add it to 1500g of concentrated sulfuric acid, stir it mechanically for 20 hours, then place it in an oven at 130°C for 8h and 180°C for 16h to obtain the mixture. Add water to the mixture at a volume ratio of 1:4, place it in a water bath at 80°C for magnetic stirring, stir for 40 minutes, wash with water 6 times, filter and dry after washing, crush and sieve through a 20-mesh sieve to obtain GDUT-1 Solid acid catalyst, acidity is 4.25mmol/g.

实施例4 Example 4

将干燥的麦壳粉碎并40目过筛;称取200g麦壳粉加入到1900g浓硫酸中,机械搅拌,搅拌时间为24h,然后置于烘箱中,140℃12h,180℃14h得到混合物,按混合物质量与水体积比1:4比例向混合物中加水,置于70℃水浴锅中磁力搅拌,搅拌时间为60min,水洗4次,水洗后过滤烘干,粉碎并40目过筛即制得GDUT-1固体酸催化剂,酸度为4.90mmol/g。 Crush the dried wheat husks and sieve them through a 40-mesh sieve; weigh 200g of wheat husk powders and add them to 1900g of concentrated sulfuric acid, stir them mechanically for 24 hours, then place them in an oven at 140°C for 12h and 180°C for 14h to obtain the mixture, press Add water to the mixture at a ratio of 1:4 between the mass of the mixture and the volume of water, place it in a water bath at 70°C for magnetic stirring, stir for 60 minutes, wash with water 4 times, filter and dry after washing, crush and sieve through a 40-mesh sieve to obtain GDUT -1 solid acid catalyst, acidity is 4.90mmol/g.

实施例5 Example 5

将干燥的花生壳粉碎并20目过筛;称取750g花生壳粉加入到1500g浓硫酸中,机械搅拌,搅拌时间为14h,然后置于烘箱中,120℃11h, 200℃9h得到混合物,按混合物质量与水体积比1:3比例向混合物中加水,置于60℃水浴锅中磁力搅拌,搅拌时间为50min,水洗5次,水洗后过滤烘干,粉碎并20目过筛即制得GDUT-1固体酸催化剂,酸度为4.13mmol/g。 Crush the dried peanut shells and sieve them through a 20-mesh sieve; weigh 750g of peanut shell powder and add them to 1500g of concentrated sulfuric acid, stir them mechanically for 14 hours, then place them in an oven at 120°C for 11h and 200°C for 9h to obtain the mixture, press Add water to the mixture at a ratio of 1:3 between the mass of the mixture and the volume of water, place it in a water bath at 60°C for magnetic stirring, stir for 50 minutes, wash with water 5 times, filter and dry after washing, crush and sieve through a 20-mesh sieve to obtain GDUT -1 solid acid catalyst, acidity is 4.13mmol/g.

实施例6 Example 6

将干燥的竹屑粉碎并60目过筛;称取200g竹粉加入到1200g浓硫酸中,机械搅拌,搅拌时间为20h,然后置于烘箱中,100℃14h,200℃10h得到混合物,按混合物质量与水体积比1:4比例向混合物中加水,置于80℃水浴锅中磁力搅拌,搅拌时间为40min,水洗6次,水洗后过滤烘干,粉碎并60目过筛即制得GDUT-1固体酸催化剂,酸度为3.89mmol/g。 Grind the dried bamboo chips and sieve them through a 60-mesh sieve; weigh 200g of bamboo powder and add it to 1200g of concentrated sulfuric acid, stir it mechanically for 20 hours, then place it in an oven, keep it at 100°C for 14h, then at 200°C for 10h to get the mixture, press the mixture Add water to the mixture at a mass to water volume ratio of 1:4, place it in a water bath at 80°C for magnetic stirring, stir for 40 minutes, wash with water 6 times, filter and dry after washing, crush and sieve through a 60-mesh sieve to obtain GDUT- 1 solid acid catalyst, the acidity is 3.89mmol/g.

实施例7 Example 7

将干燥的木屑粉碎并40目过筛;称取400g木粉加入到1600g浓硫酸中,机械搅拌,搅拌时间为18h,然后置于烘箱中,130℃8h,180℃16h得到混合物,按混合物质量与水体积比1:4比例向混合物中加水,置于70℃水浴锅中磁力搅拌,搅拌时间为50min,水洗5次,水洗后过滤烘干,粉碎并40目过筛即制得GDUT-1固体酸催化剂,酸度为4.77mmol/g。 Crush the dried sawdust and sieve it through a 40-mesh sieve; weigh 400g of wood powder and add it to 1600g of concentrated sulfuric acid, stir it mechanically for 18 hours, then place it in an oven, keep it at 130°C for 8 hours, and then at 180°C for 16 hours to obtain the mixture. Add water to the mixture at a volume ratio of 1:4, place it in a water bath at 70°C for magnetic stirring, stir for 50 minutes, wash with water 5 times, filter and dry after washing, crush and sieve through a 40-mesh sieve to obtain GDUT-1 Solid acid catalyst, acidity is 4.77mmol/g.

实施例8 Example 8

将干燥的秸秆粉碎并20目过筛;称取500g秸秆粉加入到3500g浓硫酸中,机械搅拌,搅拌时间为16h,然后置于烘箱中,150℃6h,190℃13h得到混合物,按混合物质量与水体积比1:5比例向混合物中加水,置于80℃水浴锅中磁力搅拌,搅拌时间为40min,水洗6次,水洗后过滤烘干,粉碎并20目过筛即制得GDUT-1固体酸催化剂,酸度为4.19mmol/g。 Crush the dried straw and sieve it through 20 meshes; weigh 500g of straw powder and add it to 3500g of concentrated sulfuric acid, stir it mechanically for 16 hours, then put it in an oven, keep it at 150°C for 6 hours, and then at 190°C for 13 hours to get the mixture. Add water to the mixture at a volume ratio of 1:5, place it in a water bath at 80°C for magnetic stirring, stir for 40 minutes, wash with water 6 times, filter and dry after washing, crush and sieve through a 20-mesh sieve to obtain GDUT-1 Solid acid catalyst, acidity is 4.19mmol/g.

实施例9 Example 9

将干燥的竹屑和木屑粉碎并60目过筛;分别称取300g竹粉和 300g木粉,依次加入到3600g浓硫酸中,机械搅拌,搅拌时间为12h,然后置于烘箱中,130℃10h,180℃15h得到混合物,按混合物质量与水体积比1:4比例向混合物中加水,置于70℃水浴锅中磁力搅拌,搅拌时间为50min,水洗5次,水洗后过滤烘干,粉碎并60目过筛即制得GDUT-1固体酸催化剂,酸度为4.62mmol/g。 Crush the dried bamboo and wood chips and sieve them through a 60-mesh sieve; weigh 300g of bamboo powder and 300g of wood powder respectively, add them to 3600g of concentrated sulfuric acid in turn, stir them mechanically for 12 hours, then place them in an oven at 130°C for 10 hours , 180°C for 15h to obtain the mixture, add water to the mixture according to the ratio of the mass of the mixture to the volume of water 1:4, place it in a water bath at 70°C for magnetic stirring, stir for 50 minutes, wash with water 5 times, filter and dry after washing, crush and GDUT-1 solid acid catalyst was obtained by sieving with 60 mesh, and the acidity was 4.62mmol/g.

最后所应说明的是:以上实施例仅用以说明,而非限制本发明的技术方案,尽管参照上述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:依然可以对本发明进行修改或者等同交换,而不脱离本发明的精神和范围的任何修改或局部替换,其均应涵盖在本发明的权利要求范围之中。 Finally, it should be noted that: the above embodiments are only used to illustrate, rather than limit the technical solution of the present invention, although the present invention has been described in detail with reference to the above embodiments, those of ordinary skill in the art should understand that: the present invention can still be Any modification or partial replacement without departing from the spirit and scope of the present invention shall be covered by the claims of the present invention.

Claims (5)

1. a preparation method for peracid amount solid acid catalyst, described method take plant waste as raw material, first add the concentrated sulfuric acid dehydration carbonization, after carry out sulfonation, it is characterized in that comprising the steps:
(1) plant waste of drying is pulverized also 20 ~ 80 orders to sieve;
(2) to join after sieving in the concentrated sulfuric acid and mechanical agitation, at room temperature dewater carbonization 10 ~ 24h, then sulfonation 15 ~ 30h at 100 ~ 200 DEG C in an oven, obtains solid mixture;
(3) this mixture is washed to pH in solution no longer to change, then filters, dry, pulverize the i.e. obtained solid acid catalyst and 20 ~ 80 orders sieve.
2. the preparation method of peracid amount solid acid catalyst according to claim 1, is characterized in that: in described step (1) plant waste be peltate yam waste slag, coconut palm chaff, rice bran, wheat husk, peanut shell, bamboo bits, wood chip, stalk any one or a few.
3. the preparation method of peracid amount solid acid catalyst according to claim 1, is characterized in that: plant waste joins in the concentrated sulfuric acid by the ratio of mass ratio 1:1 ~ 10 in plant waste and the concentrated sulfuric acid in described step (2).
4. the preparation method of peracid amount solid acid catalyst according to claim 1, it is characterized in that: in described step (3), method for washing is add water in mixture than the ratio of 1:3 ~ 5 in the mass/volume of mixture with water, be placed in the water-bath magnetic agitation of 60 ~ 80 DEG C, mixing time is 30 ~ 60min, washes 4 ~ 6 times.
5. the preparation method of peracid amount solid acid catalyst according to claim 1, is characterized in that: gained solid acid surface acidity is 3.5 ~ 5.0mmol/g, and this solid acid catalyst is called GDUT-1.
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