WO2021115264A1 - 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法 - Google Patents

基于熔盐水合物的纤维素水解制备乙酰丙酸的方法 Download PDF

Info

Publication number
WO2021115264A1
WO2021115264A1 PCT/CN2020/134566 CN2020134566W WO2021115264A1 WO 2021115264 A1 WO2021115264 A1 WO 2021115264A1 CN 2020134566 W CN2020134566 W CN 2020134566W WO 2021115264 A1 WO2021115264 A1 WO 2021115264A1
Authority
WO
WIPO (PCT)
Prior art keywords
molten salt
salt hydrate
levulinic acid
cellulose
reaction
Prior art date
Application number
PCT/CN2020/134566
Other languages
English (en)
French (fr)
Inventor
崔洪友
王景华
王鸣
易维明
夏恒
张远
王勇
李春晓
王帅
王永帅
孟祥浩
Original Assignee
山东理工大学
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 山东理工大学 filed Critical 山东理工大学
Priority to US17/611,811 priority Critical patent/US20220306562A1/en
Publication of WO2021115264A1 publication Critical patent/WO2021115264A1/zh

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C07C51/48—Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/584—Recycling of catalysts

Definitions

  • the invention belongs to the technical field of biomass resource utilization, and specifically relates to a method for preparing levulinic acid based on cellulose hydrolysis of molten salt hydrate.
  • Biomass is one of the alternatives to fossil energy on the earth, and biomass is renewable.
  • the main components of biomass are lignin, cellulose and hemicellulose.
  • the content of cellulose is about 40-50%.
  • the conversion of cellulose into chemicals is one of the main ways to utilize biomass.
  • Levulinic acid is widely used in food, medicine, pesticide, chemical and other fields, and is one of the important platform compounds for biomass conversion. In recent years, researchers from all over the world have done a lot of research work in the field of cellulose preparation of levulinic acid.
  • Zuo et al. studied the use of sulfonated chloromethyl polystyrene solid acid to catalyze the conversion of cellulose to LA, 90% (w/w) ⁇ -valerolactone and 10% (w/w) water as solvents, and reacted for 10 hours to obtain The best LA yield is 65.5%.
  • Yang et al. reported the selective conversion of microcrystalline cellulose, adding 5% (w/w) sodium chloride solution under hydrothermal conditions, using resin-treated iron solid catalyst to treat microcrystalline cellulose, at 200°C, 5h Under the conditions, 90.9% of the microcrystalline cellulose was completely converted and the LA conversion rate was 33.3%.
  • Khan et al. used indium chloride dinuclear ionic liquid as the reaction system and catalyst to catalyze the hydrolysis of cellulose to prepare levulinic acid in one step. Under highly acidic conditions, at 100°C for 3.0 hours, the yield of levulinic acid was 55%.
  • Chinese patent CN 107268313A discloses a microwave-accelerated carbon-based solid acid catalyst hydrolysis method for lignocellulose.
  • the patent first uses 40% ZnCl 2 solution to soak lignocellulose.
  • the coupling of ZnCl 2 and microwave radiation promotes the synthesis of lignin and cellulose.
  • Hydrolysis promotes the breaking of the hydrogen bond of cellulose and increases the degradation rate of cellulose.
  • the specific degradation yield is not mentioned.
  • a 40% ZnCl 2 solution cannot dissolve cellulose, and the hydrolysis reaction of cellulose is still the reaction of solid cellulose under the action of a solid acid catalyst, so the reaction rate is slow.
  • Chinese Patent CN 103435577A discloses a method for preparing levulinic acid from biomass or co-producing ⁇ -valerolactone at the same time.
  • the method uses an aqueous solution of ⁇ -valerolactone as a solvent to dissolve cellulose and hemicellulose, and uses a solid acid catalyst as A catalyst is used to prepare levulinic acid or a hydrogenation catalyst is further added to prepare ⁇ -valerolactone.
  • the method solves the problem of cellulose dissolution, the maximum yield of the prepared levulinic acid is only 60%.
  • Cionic liquid-water medium Chinese Patent CN 104529752A discloses a process for preparing levulinic acid by continuous degradation of cellulose in an ionic liquid-water medium.
  • the process uses ionic liquid as a solvent and another ionic liquid as a catalyst, although it also realizes the dissolution and dissolution of cellulose. Homogeneous reaction, but ionic liquids are more expensive and difficult to separate.
  • the preheating temperature of the reaction is 290°C to 310°C
  • the reaction temperature is 200°C to 220°C
  • the reaction pressure is 4MPa to 5MPa
  • the yield of levulinic acid is 72.1%.
  • the purpose of the present invention is to provide a method for preparing levulinic acid by cellulose hydrolysis based on molten salt hydrate, which greatly improves the rate and yield of cellulose hydrolysis to prepare levulinic acid, the product is easy to separate, and the reaction solvent and catalyst can be recycled use.
  • the method for preparing levulinic acid by hydrolyzing cellulose based on molten salt hydrate according to the present invention is to first prepare inorganic salt and water into an inorganic molten salt hydrate, then add cellulose to stir and dissolve, and finally add a solid catalyst to increase the temperature and reduce the temperature.
  • Levulinic acid is separated, and the separated inorganic molten salt hydrate and solid catalyst are returned for recycling; the inorganic salt is one or more of LiCl, LiBr, CaBr 2 , Ca(NO 3 ) 2 , LiNO 3 or KNO 3 .
  • the molar ratio of water to inorganic salt is 1-6:1.
  • the solid catalyst is one or two of Nb-Ce/SBA-15 or Nb-CeP/SBA-15.
  • the mass ratio of solid catalyst to cellulose is 1:1-5.
  • the method for preparing levulinic acid by hydrolyzing cellulose based on molten salt hydrate of the present invention can also add a solid catalyst and an extractant for temperature-rising reaction.
  • the extractant is one or more of MIBK, n-butanol, ethyl acetate or octanol.
  • the volume ratio of extractant to molten salt hydrate is 0.1-3:1.
  • the reaction temperature is 150-200°C.
  • the reaction time is 30-120min.
  • the invention provides a method for preparing levulinic acid by hydrolyzing cellulose in one step with high efficiency and speed.
  • the one-pot method of the present invention is based on the cellulose hydrolysis of molten salt hydrate to prepare levulinic acid.
  • the method specifically includes pre-preparing inorganic salt and water in a certain proportion into inorganic molten salt hydrate, and then adding cellulose to raise temperature and stir to dissolve. After the cellulose is dissolved, a catalyst and an extractant are added, and the reaction is carried out at a certain temperature for a certain time, the temperature is lowered, and the solid-liquid and the organic phase are separated to obtain the levulinic acid organic phase.
  • the solvent inorganic molten salt hydrate and the solid catalyst are returned for recycling.
  • the reaction of the present invention can be carried out under normal pressure or low pressure.
  • the present invention uses inorganic molten salt hydrate as a solvent. On the one hand, it can be used as a solvent to dissolve cellulose. On the other hand, the inorganic molten salt hydrate has a temperature-rising effect, which can realize the reaction under normal pressure or low pressure, and the reaction conditions are mild. Both the cations and anions in the inorganic molten salt hydrate can catalyze the hydrolysis of cellulose and the hydrolysis and conversion of intermediate products;
  • the heterogeneous catalyst is used, which is easy to separate and reusable.
  • the carrier and active components of the heterogeneous catalyst have a catalytic effect;
  • the hydrolysis reaction is a coupled catalytic reaction of a homogeneous catalyst and a heterogeneous catalyst.
  • the anion and cations in the inorganic molten salt hydrate have a catalytic effect on cellulose and intermediate products, and the synergy with the solid catalyst greatly improves the reaction.
  • extractant can extract the product into the organic phase in time, reducing the occurrence of side reactions
  • the inorganic molten salt hydrate and the solid catalyst can be separated by cooling, and they can be recycled and reused;
  • the yield of cellulose one-step hydrolysis to prepare levulinic acid can reach more than 90%.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

属于生物质资源化利用技术领域，具体涉及一种基于熔盐水合物的纤维素水解制备乙酰丙酸的方法。先将无机盐和水配制成无机熔盐水合物，然后加入纤维素搅拌溶解，最后加入固体催化剂升温反应，降温分离得到乙酰丙酸，分离后的无机熔盐水合物和固体催化剂返回循环使用；无机盐为LiCl、LiBr、CaBr 2、Ca(NO 3) 2、LiNO 3或KNO 3中的一种或多种。所述方法以无机熔盐水合物为溶剂，一方面可以作为溶剂溶解纤维素，另一方面无机熔盐水合物具有温升效应，可以实现常压或低压状态下反应，反应条件温和，无机熔盐水合物中的阳离子、阴离子均具有催化纤维素水解及中间产物的水解转化作用。

Description

基于熔盐水合物的纤维素水解制备乙酰丙酸的方法 技术领域
本发明属于生物质资源化利用技术领域，具体涉及一种基于熔盐水合物的纤维素水解制备乙酰丙酸的方法。
背景技术
化石能源日益枯竭，寻找可替代资源迫在眉睫，生物质是地球上化石能源替代品之一，并且生物质具有可再生性。生物质的主要成分是木质素、纤维素和半纤维素，其中纤维素的含量约为40-50％，将纤维素转化为化学品是生物质利用的主要途径之一。乙酰丙酸广泛应用于食品、医药、农药、化工等领域，是生物质转化的重要平台化合物之一，近年来，世界各国的研究者在纤维素制备乙酰丙酸领域进行了大量的研究工作。
Zuo等研究了用磺化氯甲基聚苯乙烯固体酸催化纤维素转化为LA，90％(w/w)γ-戊内酯和10％(w/w)水作为溶剂，反应10h，得到LA最佳产率为65.5％。
Yang等报道了微晶纤维素的选择性转化，在水热条件下添加5％(w/w)氯化钠溶液，使用树脂处理过的铁固体催化剂处理微晶纤维素，在200℃，5h的条件下，90.9％的微晶纤维素完全转化且LA转化率为33.3％。
王攀等通过固体酸SO 4 2-/TiO 2和三氯化铁催化纤维素制备LA，并探讨了反应温度、反应时间、催化剂投加量、固液比诸因素对产率的影响。实验表明反应温度220℃、时间15min、催化剂投加量为m(纤维素)∶m(催化剂)＝2∶1、固液比为1∶15时为较优的工艺条件，LA的产率为25.52％。
Han等以γ-戊内酯为溶剂，木质素基固体催化剂催化纤维素制备乙酰丙酸，180℃反应120min，乙酰丙酸的产率为35.64％。
Khan等以氯化铟双核离子液体为反应体系和催化剂一步法催化纤维素水解制备乙酰丙酸，在高酸性条件下，100℃，反应3.0h，乙酰丙酸的产率为55％。
中国专利CN 107268313A公开一种微波促进碳基固体酸催化剂水解木质纤维素的方法，该专利首先采用40％的ZnCl 2溶液浸泡木质纤维素，ZnCl 2和微波辐射耦合促进了木质素和纤维素的水解，同时促进纤维素的氢键断裂，提高纤维素的降解速率，具体的降解产率未涉及。该方法中40％的ZnCl 2溶液并不能溶解纤维素，纤维素的水解反应仍是固体纤维素在固体酸催化剂作用下的反应，因而反应速率慢。
中国专利CN 103435577A公开一种生物质制备乙酰丙酸或同时联产γ-戊内酯的方法， 该方法采用γ-戊内酯的水溶液作为溶剂溶解纤维素和半纤维素，以固体酸催化剂为催化剂制备乙酰丙酸或进一步加入加氢催化剂制备γ-戊内酯，该方法虽然解决了纤维素的溶解问题但制备的乙酰丙酸的产率最高仅为60％。
中国专利CN 104529752A公开一种纤维素在离子液体-水介质中连续降解制备乙酰丙酸的工艺，该工艺以离子液体为溶剂，另一种离子液体为催化剂，虽然也实现了纤维素的溶解及均相反应，但是离子液体比较昂贵，分离困难。本反应预热温度为290℃～310℃，反应的温度为200℃～220℃，反应的压力为4MPa～5MPa，乙酰丙酸的产率为72.1％。
纤维素既不溶于水也不溶于一般的有机溶剂，因此纤维素的水解速率慢、反应温度高、反应时间长，目标产物产率低，无机酸催化剂可以明显加快反应的速率，但是无机酸的使用不但分离困难，而且难以回收重复使用，后续的处理困难，造成资源的浪费和环境的危害。发明内容
本发明的目的是提供一种基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，大大提高了纤维素水解制备乙酰丙酸的速率和产率，产物易分离，反应溶剂和催化剂能够循环使用。
本发明所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法是先将无机盐和水配制成无机熔盐水合物，然后加入纤维素搅拌溶解，最后加入固体催化剂升温反应，降温分离得到乙酰丙酸，分离后的无机熔盐水合物和固体催化剂返回循环使用；无机盐为LiCl、LiBr、CaBr 2、Ca(NO 3) 2、LiNO 3或KNO 3中的一种或多种。
水与无机盐的摩尔比为1-6：1。
每1L的无机熔盐水合物中加入10-50g纤维素。
固体催化剂为Nb-Ce/SBA-15或Nb-CeP/SBA-15中的一种或两种。
固体催化剂与纤维素的质量比为1:1-5。
本发明所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法还可以最后加入固体催化剂和萃取剂升温反应。
萃取剂为MIBK、正丁醇、乙酸乙酯或辛醇中的一种或多种。
萃取剂与无机熔盐水合物的体积比为0.1-3:1。
反应温度为150-200℃。
反应时间为30-120min。
本发明提供一种高效、快速一步法水解纤维素制备乙酰丙酸的方法。
本发明所述的一锅法基于熔盐水合物的纤维素水解制备乙酰丙酸的方法具体是预先将无机盐和水按一定比例配制成无机熔盐水合物，然后加入纤维素升温搅拌溶解，待纤维素溶解 完毕，加入催化剂和萃取剂，在一定温度下反应一定时间，降温固液、有机相分离得到乙酰丙酸有机相，溶剂无机熔盐水合物和固体催化剂返回循环使用。
本发明的反应可以在常压或低压状态下进行。
本发明的有益效果如下：
(1)本发明以无机熔盐水合物为溶剂，一方面可以作为溶剂溶解纤维素，另一方面无机熔盐水合物具有温升效应，可以实现常压或低压状态下反应，反应条件温和，无机熔盐水合物中的阳离子、阴离子均具有催化纤维素水解及中间产物的水解转化作用；
(2)采用非均相催化剂，易分离，可重复使用，非均相催化剂的载体、活性组分均具有催化作用；
(3)本发明中水解反应是均相催化剂与非均相催化剂的耦合催化反应，无机熔盐水合物中阴阳离子对纤维素及中间产物的催化作用，与固体催化剂的协同作用大大提高了反应的速率、选择性和产率；
(4)萃取剂的使用可将产物及时提取到有机相，减少了副反应的发生；
(5)反应完毕无机熔盐水合物和固体催化剂通过降温的方式可实现分离，循环重复使用；
(6)在此反应体系中纤维素一步法水解制备乙酰丙酸的产率可达90％以上。
具体实施方式
以下结合实施例对本发明做进一步描述。
实施例1
(1)先称取LiBr，然后按水与LiBr的摩尔比3:1称取水，搅拌溶解后，得到LiBr·3H 2O；
(2)取5mL LiBr·3H 2O，加入0.1g纤维素，搅拌溶解，加入0.1gNb-Ce/SBA-15，5mL MIBK；
(3)加热升温至150℃，在150℃反应120min；
(4)反应完毕降温，离心分离进行检测。分离后的LiBr·3H 2O和Nb-Ce/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为91.3％。
实施例2
(1)先称取LiCl，然后按水与LiCl的摩尔比2:1称取水，搅拌溶解后，得到LiCl·2H 2O；
(2)取5mL LiCl·2H 2O，加入0.2g纤维素，搅拌溶解，加入0.1gNb-Ce/SBA-15，10mL MIBK；
(3)加热升温至175℃，在175℃反应90min；
(4)反应完毕降温，离心分离进行检测。分离后的LiCl·2H 2O和Nb-Ce/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为92.7％。
实施例3
(1)先称取LiCl，然后按水与LiCl的摩尔比3:1称取水，搅拌溶解后，得到LiCl·3H 2O；
(2)取5mL LiCl·3H 2O，加入0.1g纤维素，搅拌溶解，加入0.1gNb-Ce/SBA-15，5mL MIBK；
(3)加热升温至160℃，在160℃反应120min；
(4)反应完毕降温，离心分离进行检测。分离后的LiCl·3H 2O和Nb-Ce/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为91.2％。
实施例4
(1)先称取LiBr，然后按水与LiBr的摩尔比4:1称取水，搅拌溶解后，得到LiBr·4H 2O；
(2)取5mL LiBr·4H 2O，加入0.1g纤维素，搅拌溶解，加入0.1gNb-CeP/SBA-15，5mL辛醇；
(3)加热升温至175℃，在175℃反应60min；
(4)反应完毕降温，离心分离进行检测。分离后的LiBr·4H 2O和Nb-CeP/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为93.1％。
实施例5
(1)先称取LiBr，然后按水与LiBr的摩尔比2:1称取水，搅拌溶解后，得到LiBr·2H 2O；先称取Ca(NO 3) 2，然后按水与Ca(NO 3) 2的摩尔比2:1称取水，搅拌溶解后，得到Ca(NO 3) 2·2H 2O；
(2)取5mL LiBr·2H 2O+Ca(NO 3) 2·2H 2O(LiBr·2H 2O和Ca(NO 3) 2·2H 2O的体积比为1:1)，加入0.1g纤维素，搅拌溶解，加入0.1gNb-CeP/SBA-15，5mL MIBK；
(3)加热升温至160℃，在160℃反应50min；
(4)反应完毕降温，离心分离进行检测。分离后的LiBr·2H 2O+Ca(NO 3) 2·2H 2O和Nb-CeP/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为92.2％。
实施例6
(1)先称取LiCl，然后按水与LiCl的摩尔比2:1称取水，搅拌溶解后，得到LiCl·2H 2O；先称取LiNO 3，然后按水与LiNO 3的摩尔比2:1称取水，搅拌溶解后，得到LiNO 3·2H 2O；
(2)取5mL LiCl·2H 2O+LiNO 3·2H 2O(LiCl·2H 2O和LiNO 3·2H 2O的体积比为1:1)，加入0.2g纤维素，搅拌溶解，加入0.1gNb-CeP/SBA-15；
(3)加热升温至175℃，在175℃反应30min；
(4)反应完毕降温，离心分离进行检测。分离后的LiCl·2H 2O+LiNO 3·2H 2O和Nb-CeP/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为91.3％。
实施例7
(1)先称取LiCl，然后按水与LiCl的摩尔比2:1称取水，搅拌溶解后，得到LiCl·2H 2O；先称取KNO 3，然后按水与KNO 3的摩尔比1:1称取水，搅拌溶解后，得到KNO 3·H 2O；
(2)取5mL LiCl·2H 2O+KNO 3·H 2O(LiCl·2H 2O和KNO 3·H 2O的体积比为1:1)，加入0.2g纤维素，搅拌溶解，加入0.1gNb-CeP/SBA-15，MIBK10mL；
(3)加热升温至175℃，在175℃反应30min；
(4)反应完毕降温，离心分离进行检测。分离后的LiCl·2H 2O+KNO 3·H 2O和Nb-CeP/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为93.6％。
实施例8
(1)先称取CaBr 2，然后按水与CaBr 2的摩尔比2:1称取水，搅拌溶解后，得到CaBr 2·2H 2O；
(2)取5mL CaBr 2·2H 2O，加入0.2g纤维素，搅拌溶解，加入0.1gNb-CeP/SBA-15；
(3)加热升温至175℃，在175℃反应30min；
(4)反应完毕降温，离心分离进行检测。分离后的CaBr 2·2H 2O和Nb-CeP/SBA-15返回循环使用。
经检测，乙酰丙酸的产率为90.4％。
对比例1
(1)取5mLH 2O，加入0.1g纤维素，搅拌溶解，加入0.1gNb-CeP/SBA-15；
(2)加热升温至175℃，在175℃反应30min；
(3)反应完毕降温，离心分离进行检测。
经检测，乙酰丙酸的产率为33.8％。
对比例2
(1)取5mLH 2O，加入0.1g纤维素，搅拌溶解，加入0.1gNb-Ce/SBA-15，10mLMIBK；
(2)加热升温至175℃，在175℃反应30min；
(3)反应完毕降温，离心分离进行检测。
经检测，乙酰丙酸的产率为30.2％。
实施例1-8与对比例1-2的检测结果见表1。
表1 实施例1-8与对比例1-2的检测结果
Figure PCTCN2020134566-appb-000001
通过表1可以看出，本发明在无机熔盐水合物、萃取剂和固体催化剂的共同作用下，乙酰丙酸的产率达到了90％以上。

Claims (10)

  1. 一种基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于先将无机盐和水配制成无机熔盐水合物，然后加入纤维素搅拌溶解，最后加入固体催化剂升温反应，降温分离得到乙酰丙酸，分离后的无机熔盐水合物和固体催化剂返回循环使用；无机盐为LiCl、LiBr、CaBr 2、Ca(NO 3) 2、LiNO 3或KNO 3中的一种或多种。
  2. 根据权利要求1所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于水与无机盐的摩尔比为1-6：1。
  3. 根据权利要求1所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于每1L的无机熔盐水合物中加入10-50g纤维素。
  4. 根据权利要求1所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于固体催化剂为Nb-Ce/SBA-15或Nb-CeP/SBA-15中的一种或两种。
  5. 根据权利要求1所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于固体催化剂与纤维素的质量比为1:1-5。
  6. 根据权利要求1所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于最后加入固体催化剂和萃取剂升温反应。
  7. 根据权利要求6所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于萃取剂为MIBK、正丁醇、乙酸乙酯或辛醇中的一种或多种。
  8. 根据权利要求7所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于萃取剂与无机熔盐水合物的体积比为0.1-3:1。
  9. 根据权利要求1所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于反应温度为150-200℃。
  10. 根据权利要求1所述的基于熔盐水合物的纤维素水解制备乙酰丙酸的方法，其特征在于反应时间为30-120min。
PCT/CN2020/134566 2019-12-12 2020-12-08 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法 WO2021115264A1 (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US17/611,811 US20220306562A1 (en) 2019-12-12 2020-12-08 Method for producing levulinic acid in molten salt hydrate from cellulose hydrolysis

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201911292505.9A CN110963908B (zh) 2019-12-12 2019-12-12 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法
CN201911292505.9 2019-12-12

Publications (1)

Publication Number Publication Date
WO2021115264A1 true WO2021115264A1 (zh) 2021-06-17

Family

ID=70034383

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2020/134566 WO2021115264A1 (zh) 2019-12-12 2020-12-08 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法

Country Status (3)

Country Link
US (1) US20220306562A1 (zh)
CN (1) CN110963908B (zh)
WO (1) WO2021115264A1 (zh)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110963908B (zh) * 2019-12-12 2021-03-09 山东理工大学 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009047023A1 (en) * 2007-10-09 2009-04-16 Bioecon International Holding N.V. Process for the conversion of cellulose in hydrated molten salts
CN110950750A (zh) * 2019-12-12 2020-04-03 山东理工大学 熔盐水合物中纤维素水解制备乙酰丙酸的方法
CN110963908A (zh) * 2019-12-12 2020-04-07 山东理工大学 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3008412B1 (fr) * 2013-07-12 2015-08-21 IFP Energies Nouvelles Procede de transformation de biomasses lignocellulosiques en molecules mono ou poly-oxygenees

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009047023A1 (en) * 2007-10-09 2009-04-16 Bioecon International Holding N.V. Process for the conversion of cellulose in hydrated molten salts
CN110950750A (zh) * 2019-12-12 2020-04-03 山东理工大学 熔盐水合物中纤维素水解制备乙酰丙酸的方法
CN110963908A (zh) * 2019-12-12 2020-04-07 山东理工大学 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法

Non-Patent Citations (9)

* Cited by examiner, † Cited by third party
Title
DENG WEIHUA, KENNEDY JAMES R., TSILOMELEKIS GEORGE, ZHENG WEIQING, NIKOLAKIS VLADIMIROS: "Cellulose Hydrolysis in Acidified LiBr Molten Salt Hydrate Media", INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, AMERICAN CHEMICAL SOCIETY, vol. 54, no. 19, 20 May 2015 (2015-05-20), pages 5226 - 5236, XP055820919, ISSN: 0888-5885, DOI: 10.1021/acs.iecr.5b00757 *
JOSHUA POTVIN; ERIN SORLIEN; JESSICA HEGNER; BRENTON DEBOEF; BRETT L. LUCHT;: "Effect of NaCl on the conversion of cellulose to glucose and levulinic acid via solid supported acid catalysis", TETRAHEDRON LETTERS, ELSEVIER, AMSTERDAM , NL, vol. 52, no. 44, 4 September 2011 (2011-09-04), Amsterdam , NL, pages 5891 - 5893, XP028301592, ISSN: 0040-4039, DOI: 10.1016/j.tetlet.2011.09.013 *
RODRIGUEZ QUIROZ NATALIA, NORTON ANGELA M., NGUYEN HANNAH, VASILEIADOU EFTERPI, VLACHOS DIONISIOS G.: "Homogeneous Metal Salt Solutions for Biomass Upgrading and Other Select Organic Reactions", ACS CATALYSIS, AMERICAN CHEMICAL SOCIETY, US, vol. 9, no. 11, 1 November 2019 (2019-11-01), US, pages 9923 - 9952, XP055820913, ISSN: 2155-5435, DOI: 10.1021/acscatal.9b01853 *
SADULA SUNITHA, ATHALEY ABHAY, ZHENG WEIQING, IERAPETRITOU MARIANTHI, SAHA BASUDEB: "Process Intensification for Cellulosic Biorefineries", CHEMSUSCHEM, WILEY-VCH, DE, vol. 10, no. 12, 22 June 2017 (2017-06-22), DE, pages 2566 - 2572, XP055820922, ISSN: 1864-5631, DOI: 10.1002/cssc.201700183 *
SU JIALEI, SHEN FENG, QIU MO, QI XINHUA: "High-Yield Production of Levulinic Acid from Pretreated Cow Dung in Dilute Acid Aqueous Solution", MOLECULES, vol. 22, no. 2, 14 February 2017 (2017-02-14), XP055820910, DOI: 10.3390/molecules22020285 *
WANG JINGHUA, CUI HONGYOU, WANG YONG, ZHAO RONGRONG, XIE YUJIAO, WANG MING, YI WEIMING: "Efficient catalytic conversion of cellulose to levulinic acid in the biphasic system of molten salt hydrate and methyl isobutyl ketone", GREEN CHEMISTRY, ROYAL SOCIETY OF CHEMISTRY, GB, vol. 22, no. 13, 6 July 2020 (2020-07-06), GB, pages 4240 - 4251, XP055820923, ISSN: 1463-9262, DOI: 10.1039/D0GC00897D *
WANG YINGXIONG; PEDERSEN CHRISTIAN MARCUS; QIAO YAN; DENG TIANSHENG; SHI JING; HOU XIANGLIN: "In situNMR spectroscopy: Inulin biomass conversion in ZnCl2molten salt hydrate medium—SnCl4addition controls product distribu", CARBOHYDRATE POLYMERS, APPLIED SCIENCE PUBLISHERS , LTD BARKING, GB, vol. 115, 18 September 2014 (2014-09-18), GB, pages 439 - 443, XP029019657, ISSN: 0144-8617, DOI: 10.1016/j.carbpol.2014.09.011 *
WEI WEIQI; WU SHUBIN: "Depolymerization of cellulose into high-value chemicals by using synergy of zinc chloride hydrate and sulfate ion promoted titania catalyst", BIORESOURCE TECHNOLOGY, ELSEVIER, AMSTERDAM, NL, vol. 241, 13 July 2017 (2017-07-13), AMSTERDAM, NL, pages 760 - 766, XP085129416, ISSN: 0960-8524, DOI: 10.1016/j.biortech.2017.06.004 *
YANG HUI, WANG LIQING, JIA LISHAN, QIU CHENCHAO, PANG QI, PAN XINWEI: "Selective Decomposition of Cellulose into Glucose and Levulinic Acid over Fe-Resin Catalyst in NaCl Solution under Hydrothermal Conditions", INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, AMERICAN CHEMICAL SOCIETY, vol. 53, no. 15, 16 April 2014 (2014-04-16), pages 6562 - 6568, XP055820916, ISSN: 0888-5885, DOI: 10.1021/ie500318t *

Also Published As

Publication number Publication date
US20220306562A1 (en) 2022-09-29
CN110963908B (zh) 2021-03-09
CN110963908A (zh) 2020-04-07

Similar Documents

Publication Publication Date Title
CN110950750B (zh) 熔盐水合物中纤维素水解制备乙酰丙酸的方法
JP4604194B2 (ja) 触媒を用いたセルロースの加水分解方法および触媒を用いたグルコースの生産方法
JP7149332B2 (ja) 繊維系バイオマスからセルロース、低分散のヘミセルロース及びリグニン解離ポリフェノールを製造する方法
CN104250237B (zh) 利用固体催化剂催化果糖转化制备5‑羟甲基糠醛的方法
CN107162899B (zh) 一种微波辅助磷钨酸或及其盐催化生物质碳水化合物醇解合成乙酰丙酸酯的方法
CN113402485A (zh) 复合熔盐水合物中纤维素转化制备5-羟甲基糠醛的方法
CN103435577A (zh) 生物质制备乙酰丙酸或同时联产γ-戊内酯的方法
WO2019114527A1 (zh) 一种生产高活性木质素和副产糠醛的方法及应用
CN102336728A (zh) 利用复合型固体酸催化纤维戊聚糖水解液制备糠醛的方法
CN103694203B (zh) 纤维素基磺酸催化剂催化果糖制备5-羟甲基糠醛的方法
WO2021115264A1 (zh) 基于熔盐水合物的纤维素水解制备乙酰丙酸的方法
CN102010293A (zh) 钛硅分子筛催化合成1,2-戊二醇的方法
CN114272932B (zh) 一种镍铈生物炭催化剂及其制备方法、应用
CN108014782A (zh) 一种催化解聚木质素的方法
CN102850303A (zh) 介孔固体酸催化剂的一种新用途和用法
CN112121818B (zh) 一种磁性炭基催化剂及制备方法和应用
CN104447353A (zh) 一种苯与羟胺盐反应直接制备苯胺的方法
CN112500296A (zh) 一种盐酸金刚烷胺及其制备方法
CN109369367B (zh) 一种木质素制备4-(3-羟基苯基)-4-氧代丁酸的方法
CN114031583A (zh) 一种绿色高效茯苓多糖、五羟甲基糠醛联产的方法
CN110681379A (zh) 单原子钯催化剂及其制备和在Suzuki反应中的应用
Ding et al. High-efficiency depolymerization of microcrystalline cellulose in 1-butyl-3-methylimidazolium chloride over a magnetically recoverable cellulase-mimetic resin catalyst
CN111100098A (zh) 一种以co2催化果糖脱水生成5-hmf的方法
CN114588919B (zh) 用于糖苷键水解的高效水相稳定多孔性陶瓷固体酸催化剂及其应用
CN115106111B (zh) 一种碳化钼粒径依赖型氮掺杂碳材料催化剂及其制备方法和应用

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20897813

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20897813

Country of ref document: EP

Kind code of ref document: A1