共 3 条
Characteristics and catalytic properties of WO 3 supported on zeolite A-derived from fly ash of sugarcane bagasse via esterification of ethanol and lactic acid
被引:3
|作者:
Tohdee, Kanogwan
[1
,2
]
Semmad, Surat
[3
]
Nonthawong, Jirawadee
[4
]
Praserthdam, Piyasan
[1
,2
]
Pungpo, Pornpan
[4
]
Jongsomjit, Bunjerd
[1
,2
]
机构:
[1] Chulalongkorn Univ, Fac Engn, Ctr Excellence Catalysis & Catalyt React Engn, Dept Chem Engn, Bangkok, Thailand
[2] Chulalongkorn Univ, Fac Engn, Biocircular Green Econ Technol & Engn Ctr, Dept Chem Engn,,BCGeTEC, Bangkok, Thailand
[3] Rajamangala Univ Technol Tawanok, Fac Engn & Architecture, Dept Construct Engn, Bangkok, Thailand
[4] Ubon Ratchathani Univ, Fac Sci, Dept Chem, Ubon Ratchathani 34190, Thailand
关键词:
Solid catalyst;
Esterification;
Ethanol;
Lactic acid;
Ethyl lactate;
Zeolite;
-A;
Ammonium meta-tungstate;
ETHYL LACTATE;
OLEIC-ACID;
HETEROGENEOUS CATALYST;
SURFACE MODIFICATION;
BIODIESEL PRODUCTION;
OXIDE CATALYSTS;
OXIDATION;
MONTMORILLONITE;
ISOPROPANOL;
PERFORMANCE;
D O I:
10.1016/j.sajce.2024.06.006
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
In the current trend of industrial manufacturing processes, an interest in utilization of industrial and agricultural wastes for producing green chemistry, eco-friendly product, has been increased. Therefore, this study aimed to produce ethyl lactate using solid-acid catalyst WO 3 /zeolite-A via esterification. Various analytical techniques, including XRF, BET, XPS, FTIR, NH 3 -IR, NH 3 -TPD, SEM-EDX, ICP-OES, XRD, TGA-DTA, and TEM, were employed to analyze the physical and chemical properties of zeolite -A and tungsten-supported on zeolite -A. The results revealed that after five reuse cycles, the lactic acid conversion rates were 20.1 % and 10.3 % for WO 3 /zeolite-A and Amberlyst-15, respectively. The spent WO 3 /zeolite-A exhibited a reduction in surface acid site, declining from 1,591.8 mu mol/g in the first run to 690.1 mu mol/g in the fifth run. The decline in efficiency was attributed to impurities blocking of active sites, structural alterations, and partial leaching of active species. XRD and FTIR analyses confirmed decreased crystallinity and structural changes in spent catalysts. TEM, SEM-EDS, and ICPOES analyses showed the loss of active tungsten species and the deposition of reaction intermediates leading to a decrease in ethyl lactate yield (decreased from ca. 44 to 20 %). Despite structural changes affecting catalytic performance, WO 3 /zeolite-A demonstrated a good promising catalyst for ethyl lactate production over five successive cycles (with ca. 50 % decrease).
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页码:273 / 284
页数:12
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