摘要:
The present invention provides an unsupported catalyst with superior crush strength for use in a vapor phase reaction for the high yield conversion of lower aliphatic hydrocarbons such as n-butane to corresponding monocarboxylic acids used as acetic acid. The catalyst is prepared by the reduction of a vanadium oxide containing chromium catalyst.
摘要:
A vapor phase process is provided for high conversion of C.sub.4 -hydrocarbons to acetic acid in the presence of a catalyst comprising a calcined coprecipitate of a molybdenum compound and one or more compounds of metal elements selected from titanium, zirconium, tin, hafnium, niobium and tantalum.
摘要:
A butene may be oxidized in the vapor phase at elevated temperatures to produce acetic acid by reacting the butene with molecular oxygen in the presence of a catalyst comprising a composition of the empirical formula:V.sub.f Sb.sub.g X.sub.h Me.sub.i O.sub.Jwherein V is vanadium, Sb is antimony, and O is oxygen, wherein X represents a metal which is one or more of Bi, Nb, Co, Nd, Sm, Zn, Zr or Cr, and wherein Me represents a metal which is one or more of Al, Fe or Sn, the metal represented by Me being optionally present.
摘要:
The present invention provides a vapor phase process for high yield conversion of C.sub.4 -hydrocarbons to maleic acid and acetic acid with a heteropolymolybdic acid catalyst.
摘要:
Pyridine is prepared by reacting acetaldehyde, ammonia and oxygen at elevated temperatures and in the presence of a condensation catalyst, the oxygen (or air) oxidatively demethylating, in situ, the picolines and/or higher condensation products produced along with pyridine. A second embodiment includes incorporating methanol in the above reaction mixture. A third embodiment includes incorporating isobutyraldehyde in the above reaction mixture. These processes obviate the need for formaldehyde as a reactant.
摘要:
A butene may be oxidized in the vapor phase at elevated temperatures to produce acetic acid by reacting the butene with molecular oxygen in the presence of a catalyst comprising a composition of the empirical formula:V.sub.f Sb.sub.g X.sub.h Me.sub.i O.sub.jwherein V is vanadium, Sb is antimony, and O is oxygen, wherein X represents a metal which is one or more of Bi, Nb, Co, Nd, Sm, Zn, Zr or Cr, and wherein Me represents a metal which is one or more of Al, Fe or Sn, the metal represented by Me being optionally present.
摘要:
An improvement in the process wherein carbon monoxide and hydrogen are reacted in the liquid phase in the presence of a cobalt carbonyl catalyst whereby increased amounts of ethanol may be produced, which improvement comprises conducting the reaction in the presence of a non-polar, substantially inert, oxygenated hydrocarbon solvent.
摘要:
The present invention provides a supported catalyst for use in a vapor phase reaction for the high yield conversion of lower aliphatic hydrocarbons such as butane to corresponding monocarboxylic acids such as acetic acid. The catalyst is prepared by the carbon monoxide reduction of a vanadium pentoxide-impregnated, inert porous carrier.
摘要:
The present invention provides a highly efficient process for use in the high pressure catalytic vapor phase reaction for the high yield conversion of lower aliphatic hydrocarbons such as n-butane to corresponding monocarboxylic acids such as acetic acid. The oxidation reaction takes place under hydrocarbon rich conditions. The increased efficiency in this process is realized by the judicious use of steam and the catalyst systems set forth in the instant invention.