| 1 |
Catalytic oligomerization of isobutyl alcohol to jet fuels over dealuminated zeolite Beta
Guo XY, Guo LS, Zeng Y, Kosol R, Gao XH, Yoneyama Y, Yang GH, Tsubaki N
Catalysis Today, 368, 196, 2021 |
| 2 |
Succinic Anhydride로부터 N-Hydroxysuccinimide의 친환경 생산공정 개발
구본석, 백정연, 박화인, 정인찬, 김우선
Clean Technology, 26(2), 91, 2020 |
| 3 |
Vapor-liquid equilibrium in the ternary system isobutyl alcohol plus isobutyl acetate plus N, N-dimethyl acetamide and the binary systems isobutyl alcohol plus N, N-dimethyl acetamide, isobutyl acetate plus N, N-dimethyl acetamide at 101.3 kPa
Bai X, Cui XB, Yu XF, Zhang Y, Feng TY, Liu HF, Zhang K, Fu YL, Cheng QL
Fluid Phase Equilibria, 449, 130, 2017 |
| 4 |
Isobutyl-Acetate와 Isobutyl-Alcohol 이성분계의 압력변환증류 공정 최적화 연구
조성진, 신재선, 최석훈, 이의수, 박상진
Korean Chemical Engineering Research, 52(3), 307, 2014 |
| 5 |
Liquid-liquid equilibria of the systems isobutyl acetate plus isobutyl alcohol plus water and isobutyl acetate plus isobutyl alcohol plus glycerol at different temperatures
Chafer A, de la Torre J, Monton JB, Lladosa E
Fluid Phase Equilibria, 265(1-2), 122, 2008 |
| 6 |
Study of liquid-liquid equilibrium of the systems isobutyl acetate plus acetic acid plus water and isobutyl alcohol plus acetic acid plus water at different temperatures
Chafer A, Lladosa E, de la Torre J, Burguet MC
Fluid Phase Equilibria, 271(1-2), 76, 2008 |
| 7 |
Liquid-liquid phase behaviour, liquid-liquid density, and interfacial tension of multicomponent systems at 298 K
Garcia-Flores BE, Trejo A, Aguila-Hernandez J
Fluid Phase Equilibria, 255(2), 147, 2007 |
| 8 |
Separation of isobutyl alcohol and isobutyl acetate by extractive distillation and pressure-swing distillation: Simulation and optimization
Munoz R, Monton JB, Burguet MC, de la Torre J
Separation and Purification Technology, 50(2), 175, 2006 |
| 9 |
Catalytic application of Al-MCM-41 in the esterification of acetic acid with various alcohols
Jermy BR, Pandurangan A
Applied Catalysis A: General, 288(1-2), 25, 2005 |
| 10 |
Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol plus isobutyl acetate and tert-butyl alcohol plus tert-butyl acetate at 20 and 101.3 kPa
Monton JB, Munoz R, Burguet MC, de la Torre J
Fluid Phase Equilibria, 227(1), 19, 2005 |
