Phase Behaviour and Physical Property Measurements for VAPEX Solvents: Part II. Propane, Carbon Dioxide and Athabasca Bitumen

2009 ◽  
Vol 48 (03) ◽  
pp. 57-65 ◽  
Author(s):  
A. Badamchi-Zadeh ◽  
H.W. Yarranton ◽  
B.B. Maini ◽  
M.A. Satyro
2009 ◽  
Vol 48 (01) ◽  
pp. 54-61 ◽  
Author(s):  
A. Badamchi-Zadeh ◽  
H.W. Yarranton ◽  
W.Y. Svrcek ◽  
B.B. Maini

1996 ◽  
Vol 211 (1) ◽  
pp. 173-179 ◽  
Author(s):  
J. A. Duffy ◽  
H. M. Fretwell ◽  
A. P. Clarke ◽  
S. B. Dugdale ◽  
M. A. Alam

2010 ◽  
Vol 42 (6) ◽  
pp. 797-801 ◽  
Author(s):  
Irede Dalmolin ◽  
Marcio A. Mazutti ◽  
Eduardo A.C. Batista ◽  
M. Angela A. Meireles ◽  
J. Vladimir Oliveira

2006 ◽  
Vol 59 (3) ◽  
pp. 225 ◽  
Author(s):  
Liang Gao ◽  
Tao Jiang ◽  
Buxing Han ◽  
Baoning Zong ◽  
Xiaoxin Zhang ◽  
...  

The oxidation of cyclohexane with H2O2 in a compressed CO2/acetic acid binary system was studied at 60.0 and 80.0°C, at pressures up to 18 MPa, and with the zeolite TS-1 as catalyst. The phase behaviour of the reaction system was also observed. There are three fluid phases in the reaction system at lower pressure but two at higher pressures. In the three-phase region the yields of the products, cyclohexanol and cyclohexanone, increase considerably with increasing pressure and reaches a maximum near the phase-separating pressure. CO2 can thus enhance the reaction effectively. However, the effect of pressure on the yield is very limited after the transition to a two-phase system.


2019 ◽  
Vol 98 (1) ◽  
pp. 404-411
Author(s):  
Ahmad Alizadeh ◽  
Robert Gordon Moore ◽  
Raj Mehta ◽  
Hossein Nourozieh

2017 ◽  
Vol 130 ◽  
pp. 56-62 ◽  
Author(s):  
Renata Vardanega ◽  
Irede A. Dalmolin ◽  
Gislaine C. Nogueira ◽  
Tahmasb Hatami ◽  
M. Angela A. Meireles

2010 ◽  
Vol 42 (2) ◽  
pp. 229-233 ◽  
Author(s):  
João P. Bender ◽  
Mirian Feitein ◽  
Marcio A. Mazutti ◽  
Elton Franceschi ◽  
Marcos L. Corazza ◽  
...  

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