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    • 59. 发明专利
    • CH581092A5
    • 1976-10-29
    • CH1297473
    • 1973-09-11
    • ICI LTD
    • B01J21/06B01J23/00B01J23/34B01J27/18B01J27/20C07C81/02
    • A process for the manufacture of nitroso compounds of the benzene series which comprises heating an aromatic nitrobenzene compound with an aldehyde, ketone or alcohol in the presence of a catalyst having a lattice consisting of a heavy metal selected from antimony, bismuth, cerium, chromium, cobalt, copper, germanium, gold, iron, lanthanum, lead, manganese, mercury, molybdenum, neodymium, nickel, rhenium, silver, tantalum, thallium, thorium, tin, titanium, tungsten, vanadium and zirconium, in association with oxygen atoms or hydroxyl, carbonate or phosphate ions and having at least one other of said heavy metals forming impurity atoms in the lattice. This process is related to those described in U.S. Pat. Nos. 3,578,720 and 3,700,605 but replaces the carbon monoxide used as reducing agent by an aldehyde, ketone or alcohol, especially a lower aliphatic alcohol, with consequent advantages in lower toxicity and ease of control of the process. The preferred reducing agent is methanol.
    • 60. 发明专利
    • FR2200242B3
    • 1976-08-13
    • FR7332993
    • 1973-09-13
    • ICI LTD
    • B01J21/06B01J23/00B01J23/34B01J27/18B01J27/20C07C81/02
    • A process for the manufacture of nitroso compounds of the benzene series which comprises heating an aromatic nitrobenzene compound with an aldehyde, ketone or alcohol in the presence of a catalyst having a lattice consisting of a heavy metal selected from antimony, bismuth, cerium, chromium, cobalt, copper, germanium, gold, iron, lanthanum, lead, manganese, mercury, molybdenum, neodymium, nickel, rhenium, silver, tantalum, thallium, thorium, tin, titanium, tungsten, vanadium and zirconium, in association with oxygen atoms or hydroxyl, carbonate or phosphate ions and having at least one other of said heavy metals forming impurity atoms in the lattice. This process is related to those described in U.S. Pat. Nos. 3,578,720 and 3,700,605 but replaces the carbon monoxide used as reducing agent by an aldehyde, ketone or alcohol, especially a lower aliphatic alcohol, with consequent advantages in lower toxicity and ease of control of the process. The preferred reducing agent is methanol.