Phase Equilibrium and Density of CO2 + Acetic Acid Systems from 308.15 to 338.15 K and 15 to 45 MPa-Reference-Cited by-同舟云学术

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Phase Equilibrium and Density of CO2 + Acetic Acid Systems from 308.15 to 338.15 K and 15 to 45 MPa

Published:2021-03-05 Issue:10 Volume:6 Page:6663-6673
ISSN:2470-1343
Container-title:ACS Omega
language:en
Short-container-title:ACS Omega

Author:

Zhu Teng¹,Li Yuming²,Gong Houjian³^ORCID,Dong Mingzhe⁴

Affiliation:

1. State Key Laboratory of Heavy Oil Processing, College of Science, China University of Petroleum, Beijing 102249, PR China

2. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, PR China

3. School of Petroleum Engineering, China University of Petroleum (East China), Qingdao, Shandong 266580, PR China

4. Department of Chemical and Petroleum Engineering, University of Calgary, Calgary, Alberta, Canada T2N 1N4

Funder

National Natural Science Foundation of China

Natural Science Foundation of Shandong Province

China University of Petroleum, Beijing

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acsomega.0c05462

Reference59 articles.

1. Experimental optimization of SC-CO2 extraction of carotenoids from Dunaliella salina

2. Concentration of Ruta graveolens active compounds using SC-CO 2 extraction coupled with fractional separation

3. Quaternary solubility of acetic acid, diacetin and triacetin in supercritical carbon dioxide

4. Phase Behavior and Modeling of Supercritical Carbon Dioxide−Organic Acid Mixtures

5. High-pressure (vapor+liquid) equilibrium in binary mixtures of (carbon dioxide+water or acetic acid) at temperatures from 313 to 353 K

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