Romo Joelle E, Wu Ting, Huang Xinlei, Lucero Jolie, Irwin Jennifer L, Bond Jesse Q, Carreon Moises A, Wettstein Stephanie G
Department of Chemical and Biological Engineering, Montana State University, 306 Cobleigh Hall, Bozeman, Montana 59717, United States.
Chemical and Biological Engineering Department, Colorado School of Mines, 255 Alderson Hall, Golden, Colorado 80401, United States.
ACS Omega. 2018 Nov 29;3(11):16253-16259. doi: 10.1021/acsomega.8b02461. eCollection 2018 Nov 30.
SAPO-34 zeolite crystals were grown on zeolite 5A beads, characterized, and then used to produce furfural from xylose and 5-hydroxymethylfurfural (HMF) from glucose. The SAPO-34/5A bead catalysts resulted in moderate furfural and HMF yields of 45% from xylose and 20% from glucose (463 K; 3 h) and were easier to recover than the SAPO-34 powder catalyst. At 463 K, the SAPO-34/5A beads were more selective than 0.02 M sulfuric acid for producing HMF and, unlike the sulfuric acid system, no levulinic acid was formed. The SAPO-34/5A bead catalysts had no significant loss in activity after three rounds of recycle when water washed or heated overnight between reactions; however, the heat-treated beads did show signs of thermal stress after the second reuse. The SAPO-34/5A bead catalysts show promise for dehydration reactions to produce furfural and HMF from xylose and glucose, respectively, and tailoring the catalyst and the support bead could lead to even higher selectivities and yields.
SAPO-34沸石晶体生长在5A沸石珠上,进行表征后,用于由木糖生产糠醛以及由葡萄糖生产5-羟甲基糠醛(HMF)。SAPO-34/5A珠催化剂使木糖的糠醛产率和葡萄糖的HMF产率适中,分别为45%和20%(463K;3小时),并且比SAPO-34粉末催化剂更易于回收。在463K时,SAPO-34/5A珠在生产HMF方面比0.02M硫酸更具选择性,并且与硫酸体系不同,不会生成乙酰丙酸。当在反应之间进行水洗或过夜加热时,SAPO-34/5A珠催化剂在三轮循环后活性没有显著损失;然而,经过热处理的珠子在第二次重复使用后确实出现了热应力迹象。SAPO-34/5A珠催化剂有望分别用于由木糖和葡萄糖脱水反应生产糠醛和HMF,并且对催化剂和载体珠进行调整可能会带来更高的选择性和产率。