Research Progress in Biomass-based Monolithic Catalytic Microreactors
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摘要: 天然生物质材料因其来源广泛、固碳能力强、机械强度较高、可再生性、环境友好性以及其具有的独特精细构造、化学组成，在多相催化领域备受青睐。生物质材料固有的孔道系统和化学组分既可以提升化学反应速率，又可以与催化剂复合参与到多相催化反应中。本文简述了竹、木和藤材等生物质材料作为催化剂载体的资源优势、结构优势和化学优势，综述了生物质基整体式催化微反应器的基本概念、催化剂类型、与催化剂的复合策略与机制、催化活性与失效机制及其在水处理、能源产生、化学合成、费托合成、生物分析等先进功能领域的研究进展。最后，针对目前研究的局限性及存在的问题，在复合策略优化、功能催化剂设计、结构调控提升和稳定性能改善等方面对生物质基整体式催化微反应器未来发展趋势进行了展望，以期为“双碳”战略目标下生物质复合材料功能界面构建与高效利用提供全新的科学思路与技术借鉴。Abstract: Natural biomass materials are favored in the field of heterogeneous catalysis due to their wide resources, strong carbon sequestration capacity, high mechanical strength, renewability, environmental friendliness, as well as their unique fine structure and chemical composition. The inherent pore channel system and chemical compositions of biomass materials can not only improve the chemical reaction rate, but also participate in the heterogeneous catalytic reaction as the catalysts carrier. The resource, structural and chemical advantages of biomass such as bamboo, wood and rattan as catalyst carriers were briefly introduced in this paper. The basic concepts, types of catalysts, construction strategies and mechanisms, catalytic activity and failure mechanism of biomass-based monolithic catalytic microreactors were reviewed, as well as the research progress in advanced functional fields such as water treatment, energy generation, chemical synthesis, Fischer-Tropsch synthesis, and bioanalysis. Finally, in view of the limitations and existing problems of the current research, the future development trend of biomass-based monolithic catalytic microreactor is prospected in terms of construction strategy optimization, functional catalyst design, structure regulation improvement and stability performance improvement, in order to provide new scientific ideas and technical references for the construction and efficient utilization of functional interfaces of biomass materials under the strategic goals of carbon peak and carbon neutrality.
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Key words:
- biomass materials /
- composites /
- catalysts /
- microreactors /
- nanomaterials
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图 2 (a)天然木材和Pd/木材膜照片；(b)天然木材浸入PdCl2水溶液中在80℃下加热12 h后的照片，木材样品颜色变黑，证实了在木材通道内Pd的原位形成；(c)脱除木质素的木材浸入PdCl2水溶液中在80℃下加热12 h后的照片，表明脱除木质素的木材颜色未变黑；(d)木材中Pd纳米颗粒的TEM图像，插图为其粒径分布；(e) Pd/木材的SAED图像；(f) HRTEM图像显示Pd的(111)晶格面间距离为0.23 nm[6]
Figure 2. (a) Photo images of natural wood and the Pd NPs/wood membrane. (b) A photo image of a piece of natural wood immersed in an aqueous solution of PdCl2 and heated for 12 h at 80℃. The wood sample became black in color confirming the in situ formation of Pd NPs forming within the wood channels. (c) A photo image of a piece of a white wood (with lignin removed) which was treated with the same Pd NP strategy as the control study. The result indicates that the wood without lignin does not undergo a color change. (d) TEM image of Pd NPs within the wood. Inset shows the size distribution of the Pd NPs. (e) SAED pattern of the Pd NPs/wood. (f) The HRTEM image exhibits the (111) lattice plane of Pd with an interplanar distance of 0.23 nm[6]
图 3 (a)多孔Ag/藤材复合微反应器的合成过程及其重力驱动催化还原对硝基苯酚(4-NP)示意图；(b) Ag-3/R的μ-CT图像以及纳米Ag沉积在后生木质部和原生木质部微通道上的三维μ-CT图像；(c)原始藤材和Ag/藤材复合微反应器数码图像；(d)原始藤材及其局部放大SEM图像；(e) Ag-2/R和(f)Ag-3/R的SEM图像；(g) Ag-3/R的EDS图像[23]
Figure 3. (a) Schematic of the synthetic procedure of the porous Ag/rattan filter and its gravity-driven catalytic function in the 4-NP reduction reaction.(b) Nano-CT images of Ag-3/R. 3D nano-CT images (without the vegetal biomass) of Ag NPs depositions onto the microchannels of metaxylem and protoxylem. (c) Digital images of naked rattan and Ag/rattan nanocomposites. (d) SEM image of naked rattan. Magnified SEM images of (1) a protoxylem vessel and (2) a metaxylem vessel. Magnified SEM images of (e) Ag-2/R and (f) Ag-3/R. (g) EDS spectrum for the Ag-3/R nanocomposite[23]
图 7 (a)次氯酸钠水溶液循环流动脱除木材中的木质素以及脱木质素前后的木质素含量；(b)木材孔道中连续流负载Au纳米颗粒的示意图、实验照片以及Au/木材复合材料的TEM图像[45]；(c)在未添加任何还原剂的条件下竹材微通道中连续流负载Ag纳米颗粒的示意图以及Ag/竹材复合材料的HAADF-STEM图像[46]
Figure 7. (a) Delignification of wood by the circular flow of NaClO aqueous solution. Lignin content of wood before and after delignification. (b) Scheme of the continuous-flow generation of Au NPs on the channel of wood. Digital picture of the continuous flow system. TEM image of the Au/wood.[45] (c) The continuous-flow synthesis of Ag NPs on the walls of microchannels of bamboo without adding any external reductant and its HAADF-STEM image[46]
图 8 (a)纳米Pd修饰的椴木复合反应器用于水处理；(b)木材长通道中导管和穿孔板的SEM图像；(c) Pd/木材膜复合催化水处理演示；(d)亚甲基蓝溶液流过Pd/木材膜前(红色线)后(蓝色线)的UV-vis光谱图；(e)不同pH值和(f)不同浓度亚甲基蓝溶液的降解效率；(g) SEM图像显示在木材的径向截面长而不规则的通道。(h)真空辅助下水处理实验装置图，黑色的Pd/木材膜用作过滤器；(i)不同处理速率下的降解效率；(j)与文献报道的其他Pd基复合材料相比，Pd/木材膜的TOF值比较[6]
Figure 8. (a) Basswood decorated with Pd NPs for water treatment. (b) SEM image of the long wood channels with vessels and perforation plates. (c) Demonstration of water treatment using a Pd NPs/wood membrane. (d) UV−vis spectra of the methylene blue solution before (in red) and after (in blue) flowing through Pd NPs/wood membrane. The degradation efficiency at different (e) pH values and (f) concentrations of the methylene blue solution, respectively. (g) SEM image showing long and irregular channels in the radial section of the wood. (h) Experimental setup for the water treatment tests, where vacuum is applied to control water flow rates. The black Pd NPs/wood membrane (thickness = 10 mm; effective diameter = 34 mm), which was used as a filter. (i) Degradation efficiency as a function of various treatment rates. (j) Turnover frequency (TOF) of the Pd NPs/wood membrane compared to other Pd-based materials reported in the literature[6]
图 9 (a)反应溶液流经微通道示意图；(b)不同结构和催化位点微反应器的催化和吸附性能比较；(c)不同厚度Pd/木材气凝胶复合微反应器的催化性能比较[30]；(d)Mn3O4/TiO2/木材复合微反应器的催化降解示意图；(e)TiO2/木材在H2O2和Mn3O4/TiO2/木材在H2O2和无H2O2作用下的通量比[34]；(f)不同浓度亚甲基蓝溶液的降解效率及自制亚甲基蓝降解过滤装置的照片[55]
Figure 9. (a) Schematic illustration of the reaction solution flowing through the microchannel. (b) Comparison of the catalytic and adsorption performance of microreactors with different structures and catalytic sites. (c) Comparison of the catalytic performance of Pd-aerogel wood microreactors with different wood thicknesses.[30] (d) Model of the catalytic degradation process in Mn3O4/TiO2/wood matrix as a microreactor. (e) Flux ratio of TiO2/wood with H2O2 and Mn3O4/TiO2/wood matrix with and without H2O2.[34] (f) The degradation efficiency at different concentrations of the methylene blue solution and the digital photograph of the home-made filtration device for methylene blue degradation[55]
图 10 (a)连续流催化生物反应器的构建与通道内流体运动；(b)反应pH和(c)反应温度对游离酶和固定化酶反应的影响；(d)反应前后对硝基苯酚溶液的UV-vis光谱图；(e)木材微流控反应器再利用性能；(f)与其他固定化漆酶材料的性能比较[56]
Figure 10. (a) Construction of continuous fluid catalytic bioreactor and fluid movement in the channel. (b) The effect of pH on the reaction of free and immobilized enzymes. (c) The effect of temperature on the reaction of free and immobilized enzymes. (d) UV spectrum variation of the 4-NP degradation reaction catalyzed by fluid. (e) Determination of wood microfluidic reactor reusability. (f) Comparison with other immobilized laccase materials[56]
图 11 (a)原始甘蔗海绵和不同制备时间制得的ZIF-67/甘蔗海绵；(b)ZIF-67/甘蔗海绵复合微反应器在不同运行条件下的连续流催化性能；(c)ZIF-67/甘蔗海绵复合微反应器催化活化PMS产生活性自由基的机制示意图；(d)设计的三种甘蔗微反应器对亚甲基蓝的催化降解性能比较；(e)组装而成的催化搅拌器和连续流催化过滤器[32]
Figure 11. (a) Digital photographs of the sugarcane (SC) sponge, ZIF-67@SC sponge-1, ZIF-67@SC sponge-2, ZIF-67@SC sponge-3, and ZIF-67@SC sponge-4 composites (The end number means the assembly times). (b) The catalytic performance of flow filtration of ZIF-67@SC sponge catalytic microreactor and the influence of operating conditions on catalytic activity. (c) Schematic illustration of the mechanism for ZIF-67@SC sponge catalytic filter activating PMS to generate active free radicals. (d) Comparison of the performance of three different sugarcane filter designs in terms of the catalytic degradation of methylene blue. (e) The digital photos of the reactor with the catalytic agitator (Up) and a homemade flow-through catalytic filtration device (Down)[32]
图 12 (a)氨硼烷催化分解制氢性能[28]；(b)Pt/木材碳膜复合催化剂的水下推进性能[27]；(c)基于三维Ni/木材碳整体式催化微反应器的生物质焦油重整性能[37]
Figure 12. (a) Hydrogen generation performance in ammonia borane catalytic decomposition.[28] (b) The performance of the Pt/activated carbonized wood catalyst for practical underwater propulsion applications.[27] (c) The performance of the flow-through reactor with a low tortuosity for biomass tar reforming based on 3D wood-carbon monolith[37]
图 13 (a)铜功能化的竹基复合微反应器用于连续流叠氮化物和末端炔烃之间进行铜(I)催化的1,3-偶极环加成(CuAAC)点击反应[64]；(b) Ag/竹材复合催化微反应器的照片；(c) Ag-3/B CMR催化转化2-NP、2-NA和4-NA；(d) Ag-3/B CMR的长期稳定性和可重用性[46]
Figure 13. (a) Copper functionalized bamboo for continuous-flow CuAAC click reactions.[64] (b) A digital photograph of the flow Ag/bamboo catalytic capillary microreactor (CMR) during a catalytic process. (c) The catalytic conversion of 2-NP, 2-NA, and 4-NA in the Ag-3/B CMR.(d) Long-term stability and reusability of the Ag-3/B CMR[46]
图 14 (a)三维Co@C/CW复合催化剂的合成过程及费托合成中多通道催化作用示意图；(b) Co@C/CW-100复合催化剂在不同气时空速下的CO转化率和选择性；(c) Co@C/CW-100复合催化剂随时间变化的CO转化率.与其他已报道的MOFs、ZIF衍生催化剂进行了(d) CO转化率和(e) C5+选择性的比较[31]
Figure 14. (a) Schematic of the synthesis of 3D Co@C/CW catalysts and multi-channel catalysis during Fischer-Tropsch synthesis. (b) CO conversion and selectivity of Co@C/CW-100 catalyst at different GHSV. (c) CO conversions with time on stream of Co@C/CW-100 (T = 240 ℃, P = 2.0 MPa, H2/CO = 2, and GHSV = 10 L·h−1·gcat−1). (d) CO conversion and (e) C5+ selectivity compared with other reported MOFs, ZIF derivative catalyst[31]
图 15 (a)脱木素竹材支架上的酶固定作为绿色层级生物反应器；(b)用不同数量BGUs固定OBS进行的Hanes-Woolf实验图和Michaelis-Menten方程拟合(插图)；(c) BGU@OBS的可重用性；(d)游离BGU和BGU@OBS的储存稳定性(~4℃保存40天)；(e) GOx@OBS和HRP@OBS串联催化的生物反应器(1)原理图和(2)光学照片；(f)流速为10 L/min时回收率与收集体积的函数关系[66]
Figure 15. (a) Enzyme immobilization on a delignified bamboo scaffold as a green hierarchical bioreactor. (b) Hanes-Woolf plots of experiments performed with OBS immobilized with different amounts of BGUs and the fitting of the Michaelis-Menten equation (insert). (c) Reusability of BGU@OBS. (d) Storage stability of free BGU and BGU@OBS (~4℃ for 40 days). (e) Schematic diagram (1) and optical photograph (2) of the bioreactor for tandem catalysis with GOx@OBS and HRP@OBS. (f) Recovery percentage as a function of collection volume at 10 mL/min flow rate[66]
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