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Volumn 16, Issue 11, 2010, Pages 3296-3299

Shift of multiple incompatible equilibriums by a combination of heterogeneous catalysis and membranes

Author keywords

Heterogeneous catalysis; Membranes; Renewable resources; Sequential reactions transesterification

Indexed keywords

CHEMICAL EQUATIONS; HETEROGENEOUS CATALYSIS; HETEROGENEOUS CATALYST; RENEWABLE RESOURCE; SEQUENTIAL REACTION; SEQUENTIAL REACTIONS TRANSESTERIFICATION; SUSTAINABLE PROCESS;

EID: 77949297543     PISSN: 09476539     EISSN: 15213765     Source Type: Journal    
DOI: 10.1002/chem.200902759     Document Type: Article
Times cited : (18)

References (30)
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    • 1 is in the range of 0.03-0.12, demonstrating the need for a large excess of methanol.
    • 1 is in the range of 0.03-0.12, demonstrating the need for a large excess of methanol.
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    • d) V. Millot, US Pat. 6869986 (2005).
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    • 33746286331 scopus 로고    scopus 로고
    • Angew. Chem. Int. Ed. 2006, 45, 2209-2212;
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  • 21
  • 29
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    • The composition (FAME/monoglycerides/diglycerides ratio) of simple transesterification reaction mixtures is 5123:56:1 (MeOH/oil 30:1), 421:5:1. (MeOH/oil 15:1), and 133:1:2 (MeOH/oil 6:1).
    • The composition (FAME/monoglycerides/diglycerides ratio) of simple transesterification reaction mixtures is 5123:56:1 (MeOH/oil 30:1), 421:5:1. (MeOH/oil 15:1), and 133:1:2 (MeOH/oil 6:1).


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.