Abstract:
1. PROCESS FOR THE PREPARATION OF ACRYLONITRILE WHILD COMPRISES CONTACTING, AT A TEMPERATURE OF FROM 300*C. TO 500*C., A GASEOUS MIXTURE OF PROPYLENE, AMMONIA AND OXYGEN IN THE PRESENCE OF A CATALYST CONSISTING ESSENTIALLY OF A MIXTURE OF URANIUM OXIDE AND TELLURIUM OXIDE WHEREIN THE TE/U ATOMIC RATIO IS IN THE RANGE FROM 2 TO 5.
Abstract:
A process is disclosed whereby a silver containing catalyst is produced, in a particle size ranging from 300 to 1,500 A, through the pulsed electrolysis of a solution of a silver salt (e.g., silver nitrate) in the presence of a complexing agent (e.g., ammonia) wherein current is fed to the solution for spaced periods of a few seconds duration. Advantageously, after about 10-15 cycles of feeding and interrupting the current to the solution, a current inversion lasting from a few seconds is effected. The silver is obtained in the form of a powder which, after washing, can be used directly or supported on a ceramic material as catalyst for the production of ethylene oxide.
Abstract:
A PROCESS IS DISCLOSED FOR DISPROPORTIONATING AN OLEFIN HAVING FROM 3 TO 30 CARBON ATOMS, WHEREIN THE OLEFIN IS CONTACTED WITH A CATALYST CONSISTING ESSENTIALLY OF AN OXIDE OF TUNGSTEN AND COPPER OR OF TUNGSTEN AND A METAL OF THE 8TH GROUP OF THE PERIODIC SYSTEM, PREFERABLY IRON, COBALT OR BICKEL, IN WHICH THE RATIO OF METAL TO TUNGSTEN IS IN THE RANGE OF 1:3 TO 5:1. THE CATALYST IS ADVANTAGEOUSLY SUPPORTED BY A CARRIER SUCH AS SILICA AND ITS CONTACT WITH THE OLEFIN IS EFFECTED AT A TEMPERATURE IN THE RANGE OF 400 TO 700*C, AT A PRESSURE IN THE RANGE OF 1 TO 50 ATMOSPHERES AND FOR A CONTACT TIME IN THE RANGE OF 0.1 TO 60 SECONDS.
Abstract:
A process for disproportionating olefins is disclosed which employs a catalyst which includes tungsten and bismuth in the form of oxides or other forms.
Abstract:
1. A PROCESS FOR THE PREPARATION OF SILVER USEFUL AS A CATALYST BY SILVER ELECTROCHEMICAL DEPOSITION COMPRISING: COMPLEXING A SILVER COMPOUND WITH A MEMBER SELECTED FROM THE GROUP CONSISTING OF AMMONIC AND FLUOBORIC IONS, ELECTROLYTICALLY DEPOSITING THE SILVER COMPOUND ON A CATHODE, AND CONCURRENTLY REMOVING THE DEPOSITED SILVER FROM SAID CATHODE WHEREBY THE REMOVED SILVER HAS A SIZE OF LESS THAN 1500 A.
Abstract:
Me2 in good to excellent yields over cryst. SiO2 catalysts contg. 1 or more oxides of amphoteric elements Cr, Be, Ti, V, Mn, Fe, Co, Zn, Zr, Rh, Ag, Sn, Sb or B and/or optionally Al2O3, in their crystal lattices. Thus, a mixt. of (EtO)4Si and Cr (NO3)3 hydrolyzed and calcined gave a catalyst contg. 90.5 wt.% SiO2 and 6.0 wt.% Cr2O3, with sp. surface 300m2/g. Methyl-t-butylether passed over this catalyst at 13.3 LHSV, 270oC and 6 bar was 97.8% converted with 99.5% selectively to CH2:CMe2.
Abstract:
The dehydration of aliph. alcs. to the resp. ethers at 200-400≦̸C was catalyzed by WSiXYZ [W, X, Y, and Z are R (R = hydrogen, methyl, ethyl, isopropyl, n-propyl, n-buthyl, isobuthyl, cyclohexyl, cyclopentyl, phenyl, phenylcyclohexylalkylphenyl), OR, Cl, Br, SiH3, COOR, SiHnClm(n and m are 1-3) Thus, MeOH was contacted with (EtO)4Si/Al2O3 at 300≦̸C to give Me2O.
Abstract:
Me2O was prepd. in high conversion and yield by hydrogenation of CO over Si compd. stabilized catalysts contg. Al, Cr, Ta, Mn, Cu, and/or Zn at 300-330≦̸C, 50-100 kg/cm2, and space velocity 1,000-10,000/h. Thus, passing 3:1 H- CO over a Cu-Zn-Cr catalyst on stabilized Al2O3 at 300≦̸C, 50kg/cm2, and space velocity 3,500/h gave CO conversion 56% and selectivity for Me2O 61.3, MeOH 3.3, and CO2 35.4%
Abstract:
Compds. of formula Al2(OH)2Cly, where X is 1-4 and Y is 5-2, are made by reaction Al2O3 or Al(OH)3 at 160-270≦̸C under pressure with 30-7% HCl in an amt. equiv. to Al2(OH)3Cl3. In an example, Al2O33H2O 50 and 33% HCl 110kg were placed in an autoclave under 0.5 atm. N, heated to 180≦̸C in 30 min, and held there for 4 hr. more, the final pressure being 8 atm. The product was a soln, of Al2(OH)3Cl3 with a density of 1.40 at 20≦̸C contg. 19.5% Al2O3 and 21% C at pH 0.9
Abstract:
The mechanical and thermal properties of aluminium oxides were improved by treating with a hydrozable Si compd. Aluminium oxides were dipped in Si compd. and heated in an inert atmosphere for reaction with Si compd. The products and excess Si compd. were removed by vaporization. The residual Si compd. was hydrolyzed by water vapor, and the hydrolyzed products in the vapor phase were removed.