NTP耦合Ni/HAP-Fe单原子催化剂强化焦油重整及协同抑制积碳机理研究
批准号:
52106252
项目类别:
青年科学基金项目(C类)
资助金额:
30.0 万元
负责人:
孟俊光
依托单位:
学科分类:
可再生能源与新能源转化利用
结题年份:
2024
批准年份:
2021
项目状态:
已结题
项目参与者:
孟俊光
中文摘要
焦油是制约生物质气化技术进一步发展的最主要瓶颈。低温等离子体(NTP)和催化是焦油重整的有效手段,针对两者单独作用对焦油中难转化的无支链芳香环结构化合物(苯、萘、菲等)裂解率低、副产物多及催化剂易积碳等问题,本申请提出NTP耦合催化反应体系,通过NTP产生的高活性粒子撞击苯环C-C键使其断裂,利用催化剂的活性位定向转化裂解中间产物。依据该机制设计一系列结构可控的Fe掺杂Ni/HAP-Fe单原子催化剂,系统考察催化剂的构筑方法与其酸(碱)位分布、金属离子尺寸、落位配位结构等在NTP耦合催化过程中对焦油重整反应历程及产物分布的调控规律,建立NTP与催化剂活性位对焦油转化的耦合/解耦机制。结合催化剂积碳的多维度表征,探讨NTP、催化剂及反应气氛(CO2、H2O等)对积碳形成/演化的作用规律及NTP耦合催化剂对积碳抑制/消除的协同作用。为NTP耦合催化转化生物质气化焦油提供理论基础和技术支撑。
英文摘要
Biomass tar is the most important bottleneck restricting the further development of biomass gasification. Non-thermal plasma (NTP) and catalysis are effective means of tar cracking/reforming. Aiming at the problem of the most difficult to convert unbranched aromatic ring compounds (benzene, naphthalene, phenanthrene, etc.) in tar have low cracking rate, many by-products and the catalysts are easily deactivated by carbon deposition when NTP and catalysis are used separately. The present application proposes an NTP coupled catalytic reaction system, in which the high-activity particles generated by NTP collied with the benzene ring to break the C-C bond, and the intermediate products are directionally converted by using the active sites of the catalyst. Then, a series of Fe doped Ni/HAP-Fe single-atom catalysts with controllable structure are constructed according to this mechanism. The effects of the method of constructing the catalyst and its acid (base) position distribution, metal ion size and coordination structure are investigated systematically on tar reforming and its product distribution during NTP coupled catalysis. The coupling/decoupling mechanism between NTP and catalyst surface characteristics for tar conversion are established. Combined with the multi-dimensional and multi-scale characterization of catalyst carbon deposition, the mechanism of NTP, catalyst and reaction atmosphere (CO2, H2O, etc.) in the formation and evolution of carbon deposition and the synergistic effect of NTP coupling catalyst on the inhibition /elimination of carbon deposition are discussed. The completion of this project will provide theoretical basis and technical support for the NTP coupled catalytic cracking of biomass gasification tar.
低温等离子体(NTP)和催化是生物质气化焦油重整的有效手段,针对两者单独作用对焦油中难转化的无支链芳香环结构化合物(苯、萘、菲等)裂解率低、副产物多及催化剂易积碳等问题,提出NTP耦合催化反应体系,通过NTP产生的高活性粒子撞击苯环C-C键使其断裂,利用催化剂的活性位实现中间产物定向转化。本项目通过不同方法合成了一系列Ni基羟基磷灰石载体(HAP)催化剂并成功应用于NTP耦合催化重整焦油体系:发现活性金属与HAP载体中的Ca实现了离子交换,成功嵌入载体骨架,形成更强的金属-载体相互作用,载体中分布均匀的缺陷位对于反应物的吸附和转化起着关键作用,表现出强稳定性和抗积碳性能;第二金属Mo,Co,Fe的添加能够增强与Ni的协同作用,进一步提升了催化剂的反应性能,新增的金属氧化物成为催化剂“自活化”阶段晶格氧的主要来源,也为反应过程中积碳的消除提供了“活性氧源”;NTP耦合催化体系成功解决了单独NTP催化的目标产物选择性差和单独热催化所需反应能耗高的难题,实现了中低温下(200-600℃)焦油的高效定向转化,NTP高能量氛围中催化剂结构和活性位点的稳定至关重要,产生离子交换的HAP载体催化剂表现出了优异的催化活性;首次提出分级NTP耦合催化(GPPC)体系,将NTP和催化剂分级分温区控制,解决了NTP和催化剂温度设置的矛盾,充分发挥NTP和催化剂的固有优势,有效缓解了催化剂表面积碳;载氧型催化剂在NTP耦合催化体系中具备优异的催化-氧化和氧离子传输能力,氧空位的存在提升了晶格氧的流动性,对催化剂表面积碳的消除极为有利,制备时先介入载氧型金属Ce,后介入活性位金属Ni,对载氧体活性和稳定性提升最大,中温条件下(550℃)NTP的存在将NiMn2O4的苯转化率大幅提升。项目共发表第一标注论文11篇(其中SCI论文10篇),授权(申请)发明专利4项,项目的实施为中温条件下生物质乃至有机固废气化制备高品质合成气开辟新途径,对于维护国家能源安全,实现双碳战略目标和乡村振兴战略目标具有意义,应用前景广阔。
国内基金
海外基金