Welcome to visit The Chinese Journal of Process Engineering, Today is
Institute of Process Engineering,Chinese Academy of Sciences
Toggle navigation
Home
Introduction
About Journal
Address from the Editor-in-Chief
Honor
Editorial Board
Previous Editorial Board
Current Editorial Board
Subscription
Guidelines
Publishing Ethics
Journal Online
Just Accepted
Current Issue
Archive
Most Read Articles
Most Download Articles
Most Cited Articles
Download
Contact Us
中文
Image/Table Caption
Advanced options
Journals
Article DOI
ALL
The Chinese Journal of Process Engineering
Publication Year From
Publication Year To
FromYear
2001
2002
2003
2004
2005
2006
2007
2008
2009
2010
2011
2012
2013
2014
2015
2016
2017
2018
2019
2020
2021
2022
2023
ToYear
2023
2022
2021
2020
2019
2018
2017
2016
2015
2014
2013
2012
2011
2010
2009
2008
2007
2006
2005
2004
2003
2002
2001
Volume
Issue
Author
Institution
Journals
Publication Years
Fig.1
Structure diagram of typical organic phosphorus extractants
Table 1 Comparison of main bond lengths of three acid extractants in dimers (Unit: nm)
[
25
]
Table 2 Comparison of the charge of three acid extractants at the main center of dimer (Unit: C)
[
25
]
Fig.2
Schematic diagram of combined forms of synergistic extraction of phosphorus extractants
[
33
]
Fig.3
Neutral extractant and extraction electron orbit
Table 3 Energy comparison of three acid extractants and dimers
(Unit: kJ/mol)
[
25
]
Table 4 Comparison of molecular frontier orbitals and energies of dimers of three acid extractants
(Unit: eV)
[
25
]
Fig.4
Co-extraction of Zn
Fig.5
Co-extraction of Fe
Fig.1
Schematic diagram of a typical ethane furnace
[
12
]
Fig.5
Metal oxygen intermediate
[
36
]
Fig.6
Benzaldehyde as an oxy transfer promoter
[
37
]
Fig.7
Halide ion stabilizes metal oxygen intermediate and catalyzes the carboxylation of epoxide
[
37
]
Fig.8
The equilibrium between the structure of catalyst [C
n
C
m
Im][HCO
3
] and its derived carbene-CO
2
(C
n
C
m
-CO
2
)
[
38
]
Fig.9
Structure of catalyst
[
39
]
Fig.10
Catalytic mechanism diagram
[
41
]
Fig.11
Catalytic process of molybdenum acetylacetonate [MoO
2
(acac)
2
] and TBAB
[
43
]
Table 1 Comparison of cracking furnace configuration
[
16
]
Table 3 Comparison of ethylene plant investment, cost and relative energy consumption with different cracking raw materials
[
18
]
Fig.2
Principle diagram of catalytic coke
[
62
]
page
Page 1 of 9
Total 162 records
First page
Prev page
Next page
Last page