CN114950438B - 提高生物质焦油低温重整性能的镍基催化剂的制备方法 - Google Patents

提高生物质焦油低温重整性能的镍基催化剂的制备方法 Download PDF

Info

Publication number
CN114950438B
CN114950438B CN202210500077.XA CN202210500077A CN114950438B CN 114950438 B CN114950438 B CN 114950438B CN 202210500077 A CN202210500077 A CN 202210500077A CN 114950438 B CN114950438 B CN 114950438B
Authority
CN
China
Prior art keywords
nickel
based catalyst
sea
preparation
temperature
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.)
Active
Application number
CN202210500077.XA
Other languages
English (en)
Other versions
CN114950438A (zh
Inventor
盖超
刘振刚
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.)
Research Center for Eco Environmental Sciences of CAS
Original Assignee
Research Center for Eco Environmental Sciences 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 Research Center for Eco Environmental Sciences of CAS filed Critical Research Center for Eco Environmental Sciences of CAS
Priority to CN202210500077.XA priority Critical patent/CN114950438B/zh
Publication of CN114950438A publication Critical patent/CN114950438A/zh
Application granted granted Critical
Publication of CN114950438B publication Critical patent/CN114950438B/zh
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/393Metal or metal oxide crystallite size
    • 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
    • B01J23/755Nickel
    • 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
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/396Distribution of the active metal ingredient
    • B01J35/399Distribution of the active metal ingredient homogeneously throughout the support particle
    • 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
    • B01J37/009Preparation by separation, e.g. by filtration, decantation, screening
    • 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
    • B01J37/04Mixing
    • 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
    • B01J37/08Heat treatment
    • B01J37/082Decomposition and pyrolysis
    • B01J37/084Decomposition of carbon-containing compounds into carbon
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/22Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
    • C01B3/24Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
    • C01B3/26Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using catalysts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0205Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02Processes for making hydrogen or synthesis gas
    • C01B2203/0205Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)

Abstract

本发明涉及生物质焦油重整催化剂的制备技术领域,具体涉及提高生物质焦油低温重整性能的镍基催化剂的制备方法。具体技术方案为:提高生物质焦油低温重整性能的镍基催化剂的制备方法,以海相页岩固体干酪根为原料,通过提质预处理后,经干燥、研磨、筛分后与六水合硝酸镍溶液混合后制得催化剂前驱体;将催化剂前驱体在氮气氛围下高温煅烧后即得镍基催化剂。本发明解决现有镍基催化剂低温重整焦油性能较差的问题。

Description

提高生物质焦油低温重整性能的镍基催化剂的制备方法
技术领域
本发明涉及生物质焦油重整催化剂的制备技术领域,具体涉及提高生物质焦油低温重整性能的镍基催化剂的制备方法。
背景技术
精细化学品、燃料、药物、合成纤维、塑料、化肥等几乎所有人类所需的化学工业品主要源于煤炭、石油和天然气等化石能源,然而这些传统化石能源利用过程带来许多问题,包括污染生态环境、资源匮乏等,因此以可持续发展的新能源替代传统化石能源势在必行。
生物质能是仅次于煤炭、石油、天然气的世界第四大能源,是唯一可再生的碳资源。相对传统化石能源,生物质能具备资源丰富、分布广泛、可再生和碳零排放等优势。采用热解气化技术将丰富的生物质资源转化为清洁燃气,既可为生活生产直接燃用,也可并网发电,具有高效率、低成本和易于规模生产的优点,发展潜力十分广阔。然而,生物质气化过程不可避免产生焦油等副产物,降低气化效率,影响燃气质量。
催化裂解气化可显著降低焦油含量,提高能源转化效率。目前主要研究热点集中于焦油重整催化剂的合成与调控。镍基催化剂以其优异的活化C-C键能力被认为是最具应用潜力的焦油重整催化剂。其载体多为白云石、橄榄石等天然矿石或氧化铝、氧化镁等金属氧化物。然而这类镍基催化剂低温重整焦油性能较差,常采用提高重整温度以提高活性,导致焦油净化能耗过高,严重制约了生物质气化技术的推广应用。
干酪根是沉积岩中不溶非氧化型酸、碱和非极性有机溶剂的分散有机质,是原始有机物质经过生活作用和物化作用改造而成,且是页岩中有机质的主体。干酪根具有丰富的孔隙网络,较高的比表面积以及对有机物优良的吸附性。我国页岩气勘探开发主要集中于上扬子区下古生界龙马溪组页岩。因此,龙马溪组页岩干酪根具有作为催化剂载体的巨大潜质。
发明内容
针对现有技术的不足,本发明提供了一种提高生物质焦油低温重整性能的镍基催化剂的制备方法,以干酪根衍生碳材料负载纳米镍催化剂,解决现有镍基催化剂低温重整焦油性能较差的问题。
为实现以上目的,本发明通过以下技术方案予以实现:
本发明公开了提高生物质焦油低温重整性能的镍基催化剂的制备方法,以海相页岩固体干酪根为原料,通过提质预处理后,经干燥、研磨、筛分后与六水合硝酸镍溶液混合后制得催化剂前驱体;将催化剂前驱体在氮气氛围下高温煅烧后即得镍基催化剂。
优选的,所述海相页岩固体干酪根提质预处理的过程为:在水浴条件下,将海相页岩固体干酪根与硫酸混合搅拌,并用去离子水洗涤至中性,并用纳滤膜过滤以获得提质后的海相页岩固体干酪根。
优选的,在58~62℃的水浴条件下,海相页岩固体干酪根与15%硫酸按质量比1:14~1:15混匀并搅拌10~12h。
优选的,所述六水合硝酸镍溶液的浓度为2.5~5.5mol/L,所述海相页岩固体干酪根与六水合硝酸镍溶液的质量比为1:6~1:8。
优选的,所述催化剂前驱体在450~550℃下煅烧1.5~4h。
相应的,一种镍基催化剂,根据上述制备方法制备的镍基催化剂。
本发明具备以下有益效果:
1.本发明制备的镍基催化剂在500℃重整温度条件下对生物质气化焦油中典型难降解组分萘、蒽等多环芳烃的重整率均>95%,所得小分子产物中H2体积分数高于60%。
2.本发明方法中以海相页岩固体干酪根为催化剂前驱体,变废为宝,原料成本低。因此,制备的催化剂具有成本低廉、制备方法简单、孔隙结构发达、以及优异的焦油低温重整活性和稳定性等特点。
3.本发明制备的镍基催化剂,可有效提高生物质焦油在低温条件下的重整降解效率,并将其转化为富氢可燃气,既可有效提高燃气热值,又大幅降低气化合成气净化能耗及成本。
附图说明
图1为实施例1制备的镍基催化剂的电镜扫描图;
图2为实施例1制备的镍基催化剂的透射电镜图;
图3为实施例4制备的镍基催化剂的电镜扫描图;
图4为实施例4制备的镍基催化剂的透射电镜图;
图5为实施例5制备的镍基催化剂的电镜扫描图;
图6为实施例5制备的镍基催化剂的透射电镜图。
具体实施方式
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。
若未特别指明,实施举例中所用的技术手段为本领域技术人员所熟知的常规手段。
本发明公开了一种提高生物质焦油低温重整性能的镍基催化剂的制备方法,以海相页岩固体干酪根为原料,通过提质预处理后,经干燥、研磨、过100目筛筛分后与2.5~5.5mol/L的六水合硝酸镍溶液混合后制得催化剂前驱体,海相页岩固体干酪根与六水合硝酸镍溶液的质量比为1:6~1:8;将催化剂前驱体在氮气氛围下在450~550℃下煅烧1.5~4h即得镍基催化剂。
具体的:海相页岩固体干酪根原料要求:
a.热演化程度/热成熟度(R0):1.1~1.4%(等效镜质体反射率分布频率);
b.平均TOC含量2.0~2.3%;
c.化学成分元素原子比范围:O/C:0.14~0.16;H/C:0.75~0.79;
d.比表面积:4.95~7.58m2/g
海相页岩固体干酪根提质预处理的过程为:在58~62℃(优选为58℃)的水浴条件下,将海相页岩固体干酪根与15%的硫酸混合搅拌10~12h(优选为12h),以去除碳酸盐和硅酸盐,海相页岩固体干酪根与硫酸的质量比为1:14~1:15(优选为1:15);然后用去离子水洗涤至中性,并用纳滤膜截留已去除碳酸盐和硅酸盐的样品中的硫酸根以获得提质的海相页岩固体干酪根。
由于干酪根中碳酸盐和硅酸盐煅烧后生成的CaO、SiO2等氧化物会覆盖催化剂孔道结构中的活性位点,从而降低焦油分子在孔道内活性位点的重整反应速率,抑制催化剂低温重整焦油性能。因此,通过上述预处理步骤去除碳酸盐和硅酸盐,可有效提高干酪根前驱体中有机质含量,进而显著增强煅烧后所得镍基催化剂的金属-载体界面相互作用,从而提高镍基催化剂对生物质焦油的低温重整性能。
下面结合具体的实施例对本发明进行进一步的阐述。
实施例1
(1)催化剂前驱体制备:以海相页岩固体干酪根为原料,通过提质预处理后,经干燥、研磨、筛分(100目)处理,进而将其与2.5mol/L浓度的六水合硝酸镍溶液按质量1:7比例混合并搅拌均匀,制得混合物料。
(2)催化剂制备:将混合物料干燥后置入石英管式炉,在N2气氛下于500℃煅烧1.5h,获得镍基催化剂,其电镜扫描图如图1所示,透射电镜图如图2所示。从图1、2中可看出,孔隙结构非常丰富,纳米镍粒子分布的十分均匀,且尺寸分布较一致。
(3)焦油低温催化重整实验:选取多环芳烃萘、蒽为典型焦油难降解组分的模型化合物,以水蒸气发生器制备的高温水蒸气(180℃)为催化反应介质,开展镍基催化剂低温重整焦油反应实验,重整反应温度设置为500℃。
(4)焦油低温催化重整产物分析:利用集气袋收集焦油催化重整反应后的气相产物,依据国标GB/T10410-2008(人工煤气和液化石油气常量组分气相色谱分析法)对气相产物组分进行定量分析。
实施例2
催化剂前驱体制备中除了步骤(1)将提质预处理后的海相页岩固体干酪根与5.0mol/L浓度的六水合硝酸镍溶液按质量1:7比例混合并搅拌均匀,制得混合物料之外,其余与实施例1相同。
实施例3
催化剂制备中除了步骤(2)将混合物料干燥后置入石英管式炉,在N2气氛下于500℃煅烧3.5h,获得镍基催化剂之外,其余与实施例1相同。
对比例1
催化剂前驱体制备中除了步骤(1)将提质预处理后的海相页岩固体干酪根与1.2mol/L浓度的六水合硝酸镍溶液按质量1:9比例混合并搅拌均匀,制得混合物料之外,其余与实施例1相同。获得的镍基催化剂,其电镜扫描图如图3所示,透射电镜图如图4所示。从图3、4可看出,孔隙结构较少,纳米镍粒子分布不均匀,且尺寸分布不一致。
对比例2
催化剂制备中除了步骤(2)将混合物料干燥后置入石英管式炉,在N2气氛下于700℃煅烧5h,获得镍基催化剂之外,其余与实施例1相同。获得的镍基催化剂,其电镜扫描图如图5所示,透射电镜图如图6所示。从图5、6可看出,孔隙结构一般,纳米镍粒子分布相对均匀,但尺寸分布不一致。
对比例3
催化剂前驱体制备中除了将海相页岩固体干酪根原料换为常规镍基催化剂所用生物质废弃物前驱体木屑,其余与实施例1相同。
各实施例和对比例的检测结果见表1所示。
表1焦油低温重整转化效率及裂解小分子气体组分实验结果
Figure BDA0003631132160000051
Figure BDA0003631132160000061
以上所述的实施例仅是对本发明的优选方式进行描述,并非对本发明的范围进行限定,在不脱离本发明设计精神的前提下,本领域普通技术人员对本发明的技术方案做出的各种变形和改进,均应落入本发明权利要求书确定的保护范围内。

Claims (3)

1.提高生物质焦油低温重整性能的镍基催化剂的制备方法,其特征在于:以海相页岩固体干酪根为原料,通过提质预处理后,经干燥、研磨、筛分后与六水合硝酸镍溶液混合后制得催化剂前驱体;将催化剂前驱体在氮气氛围下高温煅烧后即得镍基催化剂;
所述海相页岩固体干酪根提质预处理的过程为:在水浴条件下,将海相页岩固体干酪根与硫酸混合搅拌,并用去离子水洗涤至中性,并用纳滤膜过滤以获得提质后的海相页岩固体干酪根;所述催化剂前驱体在450~550℃下煅烧1.5~4h;
所述海相页岩固体干酪根中,化学成分元素原子比范围:O/C:0.14~0.16;H/C:0.75~0.79,比表面积:4.95~7.58m2/g;热演化程度/热成熟度:1.1~1.4%,平均TOC含量2.0~2.3%;
所述六水合硝酸镍溶液的浓度为2.5~5.5mol/L,所述海相页岩固体干酪根与六水合硝酸镍溶液的质量比为1:6~1:8。
2.根据权利要求1所述的提高生物质焦油低温重整性能的镍基催化剂的制备方法,其特征在于:在58~62℃的水浴条件下,海相页岩固体干酪根与15%硫酸按质量比1:14~1:15混匀并搅拌10~12h。
3.一种镍基催化剂,其特征在于:根据权利要求1~2任一项所述方法制备的镍基催化剂。
CN202210500077.XA 2022-05-07 2022-05-07 提高生物质焦油低温重整性能的镍基催化剂的制备方法 Active CN114950438B (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210500077.XA CN114950438B (zh) 2022-05-07 2022-05-07 提高生物质焦油低温重整性能的镍基催化剂的制备方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210500077.XA CN114950438B (zh) 2022-05-07 2022-05-07 提高生物质焦油低温重整性能的镍基催化剂的制备方法

Publications (2)

Publication Number Publication Date
CN114950438A CN114950438A (zh) 2022-08-30
CN114950438B true CN114950438B (zh) 2023-06-20

Family

ID=82980881

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210500077.XA Active CN114950438B (zh) 2022-05-07 2022-05-07 提高生物质焦油低温重整性能的镍基催化剂的制备方法

Country Status (1)

Country Link
CN (1) CN114950438B (zh)

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101468316A (zh) * 2007-12-24 2009-07-01 湖南众薪生物能源科技有限公司 一种促进生物质气体中焦油转化的催化剂及其制备方法
CN102133528A (zh) * 2010-01-27 2011-07-27 华北电力大学 一种生物质气化焦油裂解复合催化剂的制备方法
CN105251492B (zh) * 2015-10-09 2018-07-31 张家港中科景盛材料科技有限公司 一种黏土改性制备Ni基催化剂的方法
CN107129818B (zh) * 2017-06-21 2020-06-12 华中科技大学 一种固体废弃物与镀镍废水的综合处理方法
CN107715887A (zh) * 2017-10-24 2018-02-23 江门绿润环保科技有限公司 一种改性白云石负载的镍基催化剂的制备方法及其应用
CN109126799B (zh) * 2018-08-07 2021-04-23 淮阴工学院 一种用于生物质焦油裂解重整的红砖粉负载镍催化剂及制备方法
CN112536037A (zh) * 2020-12-31 2021-03-23 淮阴工学院 生物质炭负载镍铜纳米合金催化剂的制备方法及其在催化裂解焦油中的应用
CN113600198A (zh) * 2021-07-06 2021-11-05 同济大学 一种生物质焦油重整催化剂及其制备方法

Also Published As

Publication number Publication date
CN114950438A (zh) 2022-08-30

Similar Documents

Publication Publication Date Title
Chang et al. Study on products characteristics from catalytic fast pyrolysis of biomass based on the effects of modified biochars
CN112898997B (zh) 一种利用废旧锂电池热处理产物催化生物质热解的方法
Vichaphund et al. Selective aromatic formation from catalytic fast pyrolysis of Jatropha residues using ZSM-5 prepared by microwave-assisted synthesis
CN109759064A (zh) 一种Co@C/生物质催化剂及其制备方法和应用
CN107469802A (zh) 一种用于生产富芳烃生物燃油的催化剂及其制备方法
CN115558517A (zh) 一种利用废旧锂电池热处理产物异位催化生物质热解的方法
CN105800556A (zh) 一种煤焦气化与甲烷重整耦合工艺联产活性炭和氢气的方法
CN106807436A (zh) 一种微波改性Ca‑Zr/H‑ZSM‑5酸碱催化剂的制备方法
CN107233888B (zh) 生物质制备燃气多功能催化剂及制备方法
CN114950438B (zh) 提高生物质焦油低温重整性能的镍基催化剂的制备方法
KR101536623B1 (ko) 술폰산기(-so3h)가 도입된 산점을 포함한 정렬된 구조의 중형기공성탄소에 담지된 귀금속 촉매, 그 제조방법 및 상기 촉매를 이용한 리그닌 모델 화합물 분해 방법
CN101899339B (zh) 一种以煤为原料制备高甲烷含量气体的方法
CN109456801B (zh) 生物质富氢高能燃气联产纳米二氧化硅复合材料的方法
CN112158805B (zh) 利用生物质制备氢气的方法和系统
CN111377398B (zh) 生物质热解气化制取氢气和一氧化碳的方法
CN115584283B (zh) 一种由粗芴制备金刚烷类高密度燃料的方法
Samanta et al. Advanced Hydrogen Production through Methane Cracking: A Review
CN113998668A (zh) 超薄二氧化钛纳米片作为光催化剂在太阳能分解木质纤维素制氢的应用
CN108620075A (zh) 一种新型生物质基功能纳米材料的制备方法及其应用
CN220223597U (zh) 一种废弃物高值化利用联产氢气-碳纳米材料的集成系统
CN115608409B (zh) 一种镁铝复合氧化物/ hzsm-5双功能催化剂及其制备方法与应用
CN117208846B (zh) 一种慢速热解与快速热解耦合的热解重整制氢方法
CN117654513A (zh) 一种高温抗烧结生物炭基焦油重整催化剂及其制备方法
LU102649B1 (en) A method for producing hydrogen by catalytic reforming of biogas slurry
LU502470B1 (en) Method for green recycling and comprehensive utilization of red mud waste and lignin waste

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
GR01 Patent grant
GR01 Patent grant