1949
DOI: 10.1038/164834a0
|View full text |Cite
|
Sign up to set email alerts
|

Autoxidation of Isopropylbenzene

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1

Citation Types

0
3
0

Year Published

1957
1957
2006
2006

Publication Types

Select...
8

Relationship

0
8

Authors

Journals

citations
Cited by 11 publications
(3 citation statements)
references
References 0 publications
0
3
0
Order By: Relevance
“…Four variables were studied: temperature, sodium naphthenate concentration, ozone partial pressure, and initiation time. Their influences on overall conversion of Knopf, 1966;Sotelo et al, 1984" Simanov and Nemtsov, I960;6 Armstrong et al, 1949* Wagner, 1965Sotelo et al, 1983;* Hock and Lang, 1944 " T = 115 °C. 6Transition-metal oxides or organic salts. "…”
Section: Resultsmentioning
confidence: 99%
“…Four variables were studied: temperature, sodium naphthenate concentration, ozone partial pressure, and initiation time. Their influences on overall conversion of Knopf, 1966;Sotelo et al, 1984" Simanov and Nemtsov, I960;6 Armstrong et al, 1949* Wagner, 1965Sotelo et al, 1983;* Hock and Lang, 1944 " T = 115 °C. 6Transition-metal oxides or organic salts. "…”
Section: Resultsmentioning
confidence: 99%
“…The findings of Hock and Lang lead to the technical method of cumene-phenol processing by the decomposition of cumene hydroperoxide to phenol and acetone through strong acids. Oxidation of cumene was later carried out in aqueous-alkaline emulsion at 80-140°C and later by homogenous oxidation 19,20 at 120-130°C.…”
Section: Introductionmentioning
confidence: 99%
“…The effects of the catalyst type and concentration on the yield and product distribution in the decomposition reaction of 2-IPNHP are not available in the literature. However, the decomposition ofsthe key intermediate of the analogous reaction pathwayscumene hydroperoxide (CHP) into phenol and acetone has been extensively studied in the presence of H 2 SO 4 (Armstrong, 1950;Kharasch et al, 1950;Topchiev et al, 1964;Pujado et al, 1976;Hatch and Matar, 1978;Wallace, 1996), and this catalyst is currently used in several industrial phenol production plants (Pujado, 1990;Shelpakova et al, 1991;Jordan et al, 1991;Weissermel and Arpe, 1993;Wallace, 1996). The catalytic activities of HClO 4 and HCl in the CHP decomposition process are also reported (Kharasch et al, 1950;Tobolsky and Mesrobian, 1954;Kislina et al, 1988;Kislina et al, 1990;Vinnik et al, 1990).…”
Section: Introductionmentioning
confidence: 99%