1,1,2,2,3,3-六氟环丙烷合成路线 （共 25 条）
反应条件
T=300°C; 4 h; sealed tube in vacuo;
参考文献
Journal of Fluorine Chemistry, , vol. 15, p. 487 - 496
反应条件
T=290°C; 0.5 h; sealed tube in vacuo; Further byproducts given. Yields of byproduct given;
参考文献
Birchall, J. Michael; Fields, Roy; Haszeldine, Robert N.; McLean, Reginald J.
Journal of Fluorine Chemistry, 1980 , vol. 15, p. 487 - 496
反应条件
aluminum chlorofluoride T=100°C; 4 h; Yield given. Yields of byproduct given. Title compound not separated from byproducts;
参考文献
Journal of Fluorine Chemistry, , vol. 77, # 2 p. 138 - 142
反应条件
T=294°C; 1 h; sealed tube in vacuo;
参考文献
Birchall, J. Michael; Fields, Roy; Haszeldine, Robert N.; McLean, Reginald J.
Journal of Fluorine Chemistry, 1980 , vol. 15, p. 487 - 496
反应条件
T=296°C; 1 h; sealed tube in vacuo;
参考文献
Birchall, J. Michael; Fields, Roy; Haszeldine, Robert N.; McLean, Reginald J.
Journal of Fluorine Chemistry, 1980 , vol. 15, p. 487 - 496
反应条件
T=300°C; 4 h; sealed tube in vacuo;
参考文献
Birchall, J. Michael; Fields, Roy; Haszeldine, Robert N.; McLean, Reginald J.
Journal of Fluorine Chemistry, 1980 , vol. 15, p. 487 - 496
反应条件
T=700 - 900°C; 0.000330556 h; Reactor consisting platinum-lined tubePyrolysis; Product distribution / selectivity;
参考文献
Honeywell International Inc.
Patent: US2005/245774 A1, 2005 ;
Location in patent: Page/Page column 5 ;
反应条件
T=700 - 900°C; 0.000330556 h; Reactor consisting platinum-lined tubePyrolysis; Product distribution / selectivity;
参考文献
Honeywell International Inc.
Patent: US2005/245774 A1, 2005 ;
Location in patent: Page/Page column 5 ;
反应条件
T=700 - 900°C; 0.000330556 h; Reactor consisting platinum-lined tubePyrolysis; Product distribution / selectivity;
参考文献
Honeywell International Inc.
Patent: US2005/245774 A1, 2005 ;
Location in patent: Page/Page column 5 ;
反应条件
T=296°C; 0.75 h; sealed tube in vacuo; Further byproducts given;
参考文献
Birchall, J. Michael; Fields, Roy; Haszeldine, Robert N.; McLean, Reginald J.
Journal of Fluorine Chemistry, 1980 , vol. 15, p. 487 - 496
