Continuous Acid-Catalyzed Methylations in Supercritical Carbon Dioxide: Comparison of Methanol, Dimethyl Ether and Dimethyl Carbonate as Methylating Agents

2010 ◽  
Vol 14 (2) ◽  
pp. 411-416 ◽  
Author(s):  
Peter N. Gooden ◽  
Richard A. Bourne ◽  
Andrew J. Parrott ◽  
Han S. Bevinakatti ◽  
Derek J. Irvine ◽  
...  
2006 ◽  
Vol 32 (8) ◽  
pp. 737-747 ◽  
Author(s):  
Seung Tae Hong ◽  
Hyung Sang Park ◽  
Jong Sung Lim ◽  
Youn-Woo Lee ◽  
Masakazu Anpo ◽  
...  

2006 ◽  
Vol 23 (1) ◽  
pp. 111-116 ◽  
Author(s):  
D. Ballivet-Tkatchenko ◽  
R. A. Ligabue ◽  
L. Plasseraud

2003 ◽  
Vol 2003 (9) ◽  
pp. 549-551 ◽  
Author(s):  
Tao Jiang ◽  
Buxing Han ◽  
Guoying Zhao ◽  
Yanhong Chang ◽  
Liang Gao ◽  
...  

The synthesis of dimethyl carbonate (DMC) by oxidative carbonylation of methanol with PdCl2 as a catalyst was investigated in the room temperature ionic liquid 1-butyl-3-methylimidazolium hexafluorophosphate ([bmim][PF6]). The products were recovered in situ using supercritical carbon dioxide. Enhanced selectivity of DMC over this catalyst was observed in the synthesis in [bmim][PF6] compared with the situation without the ionic liquid (IL). The mixture of catalyst and [bmim][PF6] could be recycled.


Foods ◽  
2021 ◽  
Vol 10 (6) ◽  
pp. 1223
Author(s):  
Hideki Kanda ◽  
Yuji Fukuta ◽  
Wahyudiono ◽  
Motonobu Goto

Soya beans contain a variety of lipids, and it is important to selectively separate neutral lipids from other lipids. Supercritical carbon dioxide extraction has been used as an alternative to the selective separation of neutral lipids from soya beans, usually using non-polar hexane. However, supercritical carbon dioxide extraction has a high operating pressure of over 40 MPa. On the other hand, liquefied dimethyl ether extraction, which has attracted attention in recent years, requires an operating pressure of only 0.5 MPa, but there is concern about the possibility of an explosion during operation because it is a flammable liquefied gas. Therefore, this study aims to reduce the operating pressure by using a non-flammable solvent, supercritical carbon dioxide extraction mixed with liquefied dimethyl ether as an entrainer. The extraction rate and the amount of neutral lipids extracted increased with increasing amounts of added liquefied dimethyl ether. In the mixed solvent, the amount of neutral lipids extracted was higher at an operating pressure of 20 MPa than in pure supercritical carbon dioxide extraction at 40 MPa. The mixing of liquefied dimethyl ether with supercritical carbon dioxide allowed an improvement in the extraction of neutral lipids while remaining non-flammable.


Tetrahedron ◽  
1999 ◽  
Vol 55 (40) ◽  
pp. 11949-11956 ◽  
Author(s):  
Neil S Isaacs ◽  
Brian O'Sullivan ◽  
Carla Verhaelen

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