Synergistic Effect of Acid Sites and a Gallium-Based Modified Meso-/Microporous Catalyst for the Pyrolysis of Biomass

2021 ◽  
Author(s):  
Xiaocui Wei ◽  
Yang Cao ◽  
Li Jin
Author(s):  
Muhammad Zahid ◽  
Jiang Li ◽  
Ahmed Ismail ◽  
Francisco Zaera ◽  
Yujun Zhu

PtCo/MIL-101(Cr) with high uniform dispersion Pt–Co IMNs synthesized by a polyol reduction method show higher activity for selective catalytic hydrogenation of α,β-unsaturated aldehydes due to the synergistic effect of PtCo and MIL-101(Cr) support.


Author(s):  
Sorin Avramescu ◽  
Cristian D. Ene ◽  
Madalina Ciobanu ◽  
Josefine Schnee ◽  
François Devred ◽  
...  

Catalytic activity of TiO2, 2%Re-TiO2 and 10%Re-TiO2 in the conversion of carbohydrates into levulinic acid under autoclave conditions was evaluated. These materials were prepared by aerogel method and characterized by...


2015 ◽  
Vol 5 (9) ◽  
pp. 4378-4389 ◽  
Author(s):  
Huimin Zhan ◽  
Shouying Huang ◽  
Ying Li ◽  
Jing Lv ◽  
Shengping Wang ◽  
...  

The synergistic effect of Cu0 and Brønsted acid sites remarkably facilitates the carbonylation of dimethyl ether to form methyl acetate.


Nanomaterials ◽  
2019 ◽  
Vol 9 (9) ◽  
pp. 1192
Author(s):  
Jianbing Wu ◽  
Sen Wang ◽  
Haitao Li ◽  
Yin Zhang ◽  
Ruiping Shi ◽  
...  

A series of zeolites with different topology structures, including SAPO-34, SUZ-4, ZSM-5, USY, MOR, and beta, were used to synthesize polyoxymethylene dimethyl ethers (PODEn) from dimethoxymethane (DMM) and trioxymethylene (TOM). The influence of acidic properties and channel systems were studied by activity evaluation, characterization, and theoretical calculation. The results confirmed that pore mouth diameter larger than a TOM molecule was an essential prerequisite for the synthesis of PODEn over zeolites, and the synergistic effect between medium-strong Brønsted acid sites (Brønsted MAS) and the maximal space of zeolites available determined the catalytic performance of all studied zeolites. DMM and TOM were firstly decomposed into methoxymethoxy groups (MMZ) and monomer CH2O over Brønsted MAS. Subsequently, the steric constraint of the maximum included sphere, with an appropriate size in zeolite channels, can promote the combination of CH2O and MMZ to form transition species ZO(CH2O)nCH3, which reacted with the methyl-end group to form PODEn over Brønsted MAS. Moreover, the reaction temperature showed different effects on the product selectivity and distribution, which also mainly depends on the size of the maximum space available in zeolite channels.


RSC Advances ◽  
2015 ◽  
Vol 5 (80) ◽  
pp. 65408-65414 ◽  
Author(s):  
Pouya Sirous Rezaei ◽  
Hoda Shafaghat ◽  
Wan Mohd Ashri Wan Daud

In catalytic pyrolysis of biomass feedstocks over zeolites, larger catalyst pores result in lower thermal coke. Besides, catalytic coke formation is suppressed by a small internal pore space or low density of acid sites.


2020 ◽  
Vol 849 ◽  
pp. 34-39
Author(s):  
Dijan Supramono ◽  
Syafira Tiaradiba

The non-oxygenated fraction of bio-oil is precursor of the formation of biofuel because it contains hydrocarbon only. Zeolite catalysts have been proved to improve the yields of non-polar fraction of bio-oil in case of fast co-pyrolysis. In the present work, the catalysts were applied to slow co-pyrolysis to investigate their effect on the yields and compositions of non-oxygenated fractions of bio-oil. The co-pyrolysis was conducted in a stirred tank reactor using non catalyst (thermal co-pyrolysis), natural zeolite and H-beta zeolite catalysts with heating rate of 5°C/minute from ambient temperature to 500°C and PP composition in combined feed varied 0, 50, and 100% weight of PP. As biomass, the present study used corn cobs. The results show that synergistic effect on the yield of non-oxygenated fraction in co-pyrolysis involving natural zeolite was lower than that in thermal co-pyrolysis and co-pyrolysis involving H-beta-zeolite exhibited negative synergistic effect. H-NMR analysis of the fraction from co-pyrolysis involving 50% weight of PP shows that the bio-oil contained approximately methyl H of about 55% by mol, methine H of 20% and methylene H of about 15% irrespective of catalysts used. This composition was closer to that of commercial gasoline rather than commercial diesel compositions.


Author(s):  
Xuelong Lv ◽  
Songcai Cai ◽  
Jin Chen ◽  
Dong-Xu Yan ◽  
Mingzhu Jiang ◽  
...  

Enhancing the surface acidity has been seen as an effective strategy to optimize the performance of catalysts for the degradation of chlorinated volatile organic compounds (CVOCs). Herein, a series of...


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