CN108774542A - 一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法 - Google Patents

一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法 Download PDF

Info

Publication number
CN108774542A
CN108774542A CN201810725218.1A CN201810725218A CN108774542A CN 108774542 A CN108774542 A CN 108774542A CN 201810725218 A CN201810725218 A CN 201810725218A CN 108774542 A CN108774542 A CN 108774542A
Authority
CN
China
Prior art keywords
phenolic compound
hydrogenation deoxidation
hydro carbons
lignin depolymerization
ferrous
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
CN201810725218.1A
Other languages
English (en)
Inventor
张兴华
陈强
马隆龙
张琦
王晨光
陈伦刚
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangzhou Institute of Energy Conversion of CAS
Original Assignee
Guangzhou Institute of Energy Conversion of CAS
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 Guangzhou Institute of Energy Conversion of CAS filed Critical Guangzhou Institute of Energy Conversion of CAS
Priority to CN201810725218.1A priority Critical patent/CN108774542A/zh
Publication of CN108774542A publication Critical patent/CN108774542A/zh
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/06Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
    • C10G1/065Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation in the presence of a solvent
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/745Iron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/20Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
    • B01J35/23Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16Reducing

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

本发明公开了一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法,利用纳米铁作为催化剂,酚类化合物能高效地转化为烃类化学品,且催化剂原料丰富、价格低廉,制备条件温和、制备方法简单,催化活性优异、加氢脱氧效率高,具有成本低、效率较高,可大规模推广应用的优点。

Description

一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃 类的方法
技术领域:
本发明涉及生物质液体燃料和化工品制备技术领域,具体涉及一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法。
背景技术:
木质素是生物质的主要组成部分,是纤维素乙醇工业和造纸工业的主要副产物,由于得不到充分利用,变成了环境污染物,给环境带来了很大压力。因此,木质素高效地转化为液体燃料或化学品对提高生物质碳资源的利用率,改善生物质利用技术的经济性有着重要意义。一般地,通过催化解聚得到单环酚类平台化合物,再经加氢脱氧可以实现木质素向烃类燃料或化学品的转变。
酚类化合物加氢脱氧的催化剂种类较多。其中研究较早的是以硫化态金属为活性相的双功能催化剂(如负载的MoS2、NiMoS2、CoMoS2等催化剂)。该类催化剂反应过程中容易积炭失活。此外,反应体系中必须持续提供一定浓度的H2S以维持硫化态,避免催化剂活性中心的流失。H2S的引入导致产物中引入了大量硫元素。
Pd、Pt、Ru、Rh、Ir等贵金属具有很高的催化加氢活性,在温和的氢解条件下,能选择性的断裂木质素及其模型化合物,将原料降解成单体,二聚体和低聚物化合物。例如,在Al-SBA-15负载的Pd,Pt,Ru和Pd作用下玉米秸秆木质素选择性的氢解成4-乙基苯酚。然而,在苛刻的木质素降解条件下,该类催化剂很不稳定,容易失活;此外,该类贵金属催化剂的价格昂贵,并不适合进行大规模的工业生产。
除贵金属外,过渡态和其他副族金属也在木质素解聚及木质素衍生物加氢脱氧反应中存在活性。如钼的氧化物、氮化物和碳化物等早在20世纪80年代就作为催化剂用于木质素和酚类模型化合物的加氢脱氧反应。过渡态金属Co、Ni等金属及CoMo、NiMo等双金属催化剂在酚类化合物的加氢脱氧反应中也很常见。
发明内容:
本发明的目的是提供一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法,利用纳米铁作为催化剂,酚类化合物能高效地转化为烃类化学品,且催化剂原料丰富、价格低廉,制备条件温和、制备方法简单,催化活性优异、加氢脱氧效率高,具有成本低、效率较高,可大规模推广应用的优点。
本发明是通过以下技术方案予以实现的:
一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法,该方法以木质素解聚产物中含量较高的苯酚、苯甲醚、愈创木酚、苄醚、二苯醚、茴香烯、4-苄氧基苯酚、苯并呋喃等单环酚类化合物为原料,正辛烷为溶剂在纳米铁粉催化剂的作用下将原料进行加氢脱氧反应转化为烃类产品,反应温度为260-340℃,反应时间为1-20h,反应体系中氢气压力为2.0-6.0MPa;所述纳米铁粉催化剂通过室温环境中液相化学还原法制备,具体制备方法如下:加入pH值为8-10的NaOH溶液及柠檬酸钠,搅拌,搅拌速率为600rpm,通入氮气形成惰性保护气氛,依次滴加NaBH4和亚铁离子(Fe2+)溶液,搅拌30min后,用磁铁分离即得到黑色的纳米颗粒催化剂;其中NaBH4和亚铁离子的摩尔比小于2,柠檬酸钠为亚铁离子摩尔数的0.1-0.15倍。
所述的亚铁离子溶液优选地硫酸亚铁或氯化亚铁溶液。
本发明的有益效果如下:纳米铁粉催化剂原料丰富、价格低廉,制备条件温和、制备方法简单,催化活性优异、加氢脱氧效率高,可重复使用,在纳米铁粉催化剂作用下,酚类化合物能高效地转化为烃类化学品。
具体实施方式:
以下是对本发明的进一步说明,而不是对本发明的限制。
实施例1:催化剂的制备
在三口烧瓶中加入pH值为9的NaOH溶液及柠檬酸钠,搅拌,搅拌速率为600rpm,通入氮气形成惰性保护气氛,依次滴加0.2mol L-1的NaBH4和0.5mol L-1亚铁离子(Fe2+)溶液,搅拌30min后,用磁铁分离即得到黑色的纳米颗粒催化剂;其中NaBH4和亚铁离子溶液的体积比为1:1,柠檬酸钠为亚铁离子摩尔数的0.15倍。
实施例2:
将实施例1制备得到的2.0g纳米铁粉,1.0g的木质素解聚产物苯酚和30.0ml的正辛烷放入到100ml高压反应釜中,密封反应釜,用H2置换釜内气体5次,充H2增压至4.0MPa。开启搅拌桨(700rpm),以3℃/min的加热速率将反应釜升温至300℃,开始计时反应。反应时间为8h。烃类产物收率为94%。
实施例3-15:
参考实施例2,不同之处在于反应温度、压力和时间不同,具体参见表1:
表1
实施例16-22:纳米铁粉催化剂对苯酚加氢脱氧制备烃类产物的重复性反应
参考实施例2,催化剂重复使用次数及反应结果见表2。
表2
实施例 催化剂利用次数 烃类收率(%)
16 1 94
17 2 94
18 3 93
19 4 87
20 5 79
21 6 72
22 7 70
实施例23-29:不同酚类化合物加氢脱氧制备烃类产物的反应
参考实施例2,不同之处在于为其它酚类化合物,反应结果见表3。
表3
对比例1-2:
对比例1:
参考实施例2,不同之处在于催化剂为铁,结果参见表4.
对比例2:
参考实施例23,不同之处在于催化剂为CN105461498B公开的催化剂,结果参见表4.
表4
对比例 反应物 催化剂 烃类收率(%)
1 苯酚 13
2 愈创木酚 Fe/Ni/HY 26.53

Claims (2)

1.一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法,其特征在于,该方法以木质素解聚产物中单环酚类化合物为原料,正辛烷为溶剂,在纳米铁粉催化剂的作用下将原料进行加氢脱氧反应转化为烃类产品,反应温度为260-340℃,反应时间为1-20h,反应体系中氢气压力为2.0-6.0MPa;所述纳米铁粉催化剂通过室温环境中液相化学还原法制备,具体制备方法如下:加入pH值为8-10的NaOH溶液及柠檬酸钠,搅拌,搅拌速率为600rpm,通入氮气形成惰性保护气氛,依次滴加NaBH4和亚铁离子溶液,搅拌30min后,用磁铁分离即得到黑色的纳米颗粒催化剂;其中NaBH4和亚铁离子的摩尔比小于2,柠檬酸钠为亚铁离子摩尔数的0.1-0.15倍;所述单环酚类化合物选自苯酚、苯甲醚、愈创木酚、苄醚、二苯醚、茴香烯、4-苄氧基苯酚、苯并呋喃中的任一种。
2.根据权利要求1所述的催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法,其特征在于,所述的亚铁离子溶液为硫酸亚铁或氯化亚铁溶液。
CN201810725218.1A 2018-07-04 2018-07-04 一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法 Pending CN108774542A (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810725218.1A CN108774542A (zh) 2018-07-04 2018-07-04 一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810725218.1A CN108774542A (zh) 2018-07-04 2018-07-04 一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法

Publications (1)

Publication Number Publication Date
CN108774542A true CN108774542A (zh) 2018-11-09

Family

ID=64030973

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810725218.1A Pending CN108774542A (zh) 2018-07-04 2018-07-04 一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法

Country Status (1)

Country Link
CN (1) CN108774542A (zh)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110128247A (zh) * 2019-05-23 2019-08-16 南京林业大学 一种木质素催化解聚的方法
WO2023184037A1 (en) * 2022-04-01 2023-10-05 Sixring Inc. Method to manufacture biofuel

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102676202A (zh) * 2011-03-18 2012-09-19 赵晨 一种从木质素裂解油制备高品质汽油和柴油的方法
WO2012083236A3 (en) * 2010-12-16 2012-10-26 Energia Technologies, Inc. Catalysts, methods of preparation of catalyst, methods of deoxygenation, and systems for fuel production
CN104254418A (zh) * 2011-11-03 2014-12-31 克拉里安特国际有限公司 用于制备金属纳米颗粒分散体的方法、金属纳米颗粒分散体及其用途

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012083236A3 (en) * 2010-12-16 2012-10-26 Energia Technologies, Inc. Catalysts, methods of preparation of catalyst, methods of deoxygenation, and systems for fuel production
CN102676202A (zh) * 2011-03-18 2012-09-19 赵晨 一种从木质素裂解油制备高品质汽油和柴油的方法
CN104254418A (zh) * 2011-11-03 2014-12-31 克拉里安特国际有限公司 用于制备金属纳米颗粒分散体的方法、金属纳米颗粒分散体及其用途

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
吕晓书等: "《纳米零价铁材料:制备方法、性能表征及应用实例》", 31 August 2017, 西南师范大学出版社 *
宁远涛等: "《钯》", 31 December 2017, 中南大学出版社 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110128247A (zh) * 2019-05-23 2019-08-16 南京林业大学 一种木质素催化解聚的方法
CN110128247B (zh) * 2019-05-23 2022-05-06 南京林业大学 一种木质素催化解聚的方法
WO2023184037A1 (en) * 2022-04-01 2023-10-05 Sixring Inc. Method to manufacture biofuel

Similar Documents

Publication Publication Date Title
Wang et al. Progress in hydrogen production coupled with electrochemical oxidation of small molecules
Du et al. Electrochemical lignin conversion
He et al. Water‐enhanced synthesis of higher alcohols from CO2 hydrogenation over a Pt/Co3O4 catalyst under Milder conditions
Zhang et al. Self-hydrogen transfer hydrogenolysis of β-O-4 linkages in lignin catalyzed by MIL-100 (Fe) supported Pd–Ni BMNPs
Du et al. Hydrogen‐Independent reductive transformation of carbohydrate biomass into γ‐valerolactone and pyrrolidone derivatives with supported gold catalysts
CN104744204A (zh) 一种木质素催化加氢脱氧制备芳香烃的方法
Li et al. Review on the preparation of fuels and chemicals based on lignin
CN108774542A (zh) 一种催化木质素解聚产物中单环酚类化合物加氢脱氧制备烃类的方法
CN101774930A (zh) 一种间氯苯胺的制备方法
CN113117688A (zh) 一种mof前驱体钼镍催化剂、其制备方法以及其在木质素降解中的应用
CN108101751B (zh) 一种两步法降解木质素制备酚类化合物的方法
CN105837391B (zh) 一种无金属加氢催化剂在催化苯加氢反应中的应用
CN106495974A (zh) 一种低氢气分压下催化单环酚类平台化合物加氢脱氧制备芳烃的方法
CN103638938A (zh) 一种用于生物油加氢脱氧的催化剂的制备方法
More et al. Selective catalytic hydrodeoxygenation of vanillin to 2-Methoxy-4-methyl phenol and 4-Methyl cyclohexanol over Pd/CuFe2O4 and PdNi/CuFe2O4 catalysts
Gao et al. Highly dispersed PdCu supported on MCM-41 for efficiently selective transfer hydrogenation of furfural into furfuryl alcohol
Ge et al. Selective hydrodeoxygenation of guaiacol to cyclohexanol over core-shell Cox@ C@ Ni catalysts under mild condition
CN114177930A (zh) 一种分子筛负载钌镍催化剂催化木质素加氢解聚的方法
CN104226358B (zh) 一种催化酚类化合物加氢脱氧制备烷烃的方法及催化反应体系
Wang et al. Synthesis of Ni–Mo–N catalysts for removing oxygen from acetophenone
CN110028393A (zh) 一种纤维素催化加氢制备丙酮醇和羟基丁酮的方法
CN114182294B (zh) 一种电化学降解生物质精炼有机废弃物产氢的双催化剂体系和方法
CN109369366A (zh) 一种丙三醇催化脱氢制备乳酸的方法
CN112794797B (zh) 制备癸醛的方法
CN114471666A (zh) 一种铬锌改性分子筛负载双金属催化剂及其制备与在木质素解聚中的应用

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20181109

RJ01 Rejection of invention patent application after publication