Hydrogen production from aqueous-phase reforming of glycerol, sorbitol, and glycine over Pt/Al2O3 catalyst in a fixed-bed reactor

IF 1.5 4区 化学 Q4 CHEMISTRY, PHYSICAL International Journal of Chemical Kinetics Pub Date : 2024-07-02 DOI:10.1002/kin.21752
Vinayak N. Kalekar, Prakash D. Vaidya
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Abstract

Aqueous-phase reforming (APR) is an interesting technique for generating hydrogen (H2) from biofeeds. In this work, APR of model compounds of wet biomass for H2 production was investigated. Glycerol, sorbitol, and glycine were the chosen model compounds. They represent polyols and amino acids in wet biomass such as waste sludge and microalgal biomass. The Pt/Al2O3 catalyst was preferred and it was characterized using nitrogen adsorption–desorption, scanning electron microscopy (SEM), transmission electron microscopy (TEM), x-ray diffraction (XRD), and x-ray photoelectron spectroscopy (XPS) techniques. APR trials were performed in a continuous fixed-bed reactor. The reaction conditions chosen for this work were: temperature (T) 453–498 K, pressure (P) 1.2–2.4 MPa, feed concentration 5–15 wt%, and weight hourly space velocity (WHSV) 0.15–0.6 g reactant/(g catalyst h). The best conditions for H2 production by the APR process were found to be T = 498 K, P = 2.4 MPa, and feed concentration = 15 wt%. Among the chosen model compounds, glycerol exhibited the highest H2 selectivity (82.7%) and H2 yield (21.6%) at 498 K. The analysis of kinetic data suggested first-order reaction kinetics for all the model compounds. The values of activation energy for the reactions with glycerol (55.4 kJ/mol), sorbitol (51.6 kJ/mol), and glycine (45.7 kJ/mol) were determined. Thus, APR is a promising route for effectively producing H2-bearing gaseous products with high heating value from wet biomass.

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在固定床反应器中以 Pt/Al2O3 催化剂对甘油、山梨醇和甘氨酸进行水相重整制氢
水相重整(APR)是一种利用生物原料产生氢气(H2)的有趣技术。在这项工作中,研究了湿生物质模型化合物的水相重整制氢。甘油、山梨醇和甘氨酸被选为模型化合物。它们代表了湿生物质(如废弃污泥和微藻生物质)中的多元醇和氨基酸。采用氮吸附-解吸、扫描电子显微镜(SEM)、透射电子显微镜(TEM)、X 射线衍射(XRD)和 X 射线光电子能谱(XPS)技术对 Pt/Al2O3 催化剂进行了表征。APR 试验是在连续固定床反应器中进行的。反应条件为:温度 (T) 453-498 K,压力 (P) 1.2-2.4 MPa,进料浓度 5-15 wt%,重量小时空间速度 (WHSV) 0.15-0.6 g 反应物/(g 催化剂 h)。通过 APR 工艺生产 H2 的最佳条件是 T = 498 K、P = 2.4 MPa 和进料浓度 = 15 wt%。在所选的模型化合物中,甘油在 498 K 时表现出最高的 H2 选择性(82.7%)和 H2 产率(21.6%)。测定了与甘油(55.4 kJ/mol)、山梨醇(51.6 kJ/mol)和甘氨酸(45.7 kJ/mol)反应的活化能值。因此,APR 是利用湿生物质有效生产具有高热值的含 H2 气体产品的一条可行途径。
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来源期刊
CiteScore
3.30
自引率
6.70%
发文量
74
审稿时长
3 months
期刊介绍: As the leading archival journal devoted exclusively to chemical kinetics, the International Journal of Chemical Kinetics publishes original research in gas phase, condensed phase, and polymer reaction kinetics, as well as biochemical and surface kinetics. The Journal seeks to be the primary archive for careful experimental measurements of reaction kinetics, in both simple and complex systems. The Journal also presents new developments in applied theoretical kinetics and publishes large kinetic models, and the algorithms and estimates used in these models. These include methods for handling the large reaction networks important in biochemistry, catalysis, and free radical chemistry. In addition, the Journal explores such topics as the quantitative relationships between molecular structure and chemical reactivity, organic/inorganic chemistry and reaction mechanisms, and the reactive chemistry at interfaces.
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