摘要:
Diamines of the formula ##STR1## where R.sup.1, R.sup.2 and R.sup.3 are each hydrogen, alkyl, aryl, alkoxy, aralkyl or cycloalkyl and X is a group of the formula(CR.sup.4 R.sup.5).sub.m (II)where R.sup.4 and R.sup.5 have the meanings given above for R.sup.1 and m is from 1 to 12, are prepared by a process in which a diamine of the formula ##STR2## where R.sup.1, R.sup.2 and X are the groups described above, is reacted with an olefin of the formula ##STR3## where R.sup.6 and R.sup.9 are each hydrogen or alkyl which is straight-chain in the .alpha.-position, in the presence of a zeolite as a catalyst.
摘要:
A silver catalyst containing lithium and cesium as promoters for the direct oxidation of ethylene with oxygen to give ethylene oxide is applied to a porous carrier and essentially consists of .alpha.-alumina and contains certain amounts of soluble calcium, aluminum, potassium and sodium salts. The carrier has a BET surface area of from 0.4 to 0.8 m.sup.2 /g, a pore volume of not less than 0.45 ml/g, the pores being equally accessible to cold and warm water, a bulk density of less than 700 kg/m.sup.3 and a shape which, in the reactor, provides a geometrical surface area of not less than 600 m.sup.2 /m.sup.3, on which more than 13% by weight of silver are applied as active component and more than 115 kg of silver are available per m.sup.3 of reactor, and from 100 to 300 ppm by weight of lithium and from 200 to 600 ppm by weight of cesium are present as promoters. A process for the preparation of the silver catalyst and its use for the oxidation of ethylene are described.
摘要翻译:含有锂和铯作为用于直接氧化乙烯以产生环氧乙烷的促进剂的银催化剂被施加到多孔载体上,并且基本上由α-氧化铝组成并含有一定量的可溶性钙,铝,钾和钠盐。 载体的BET表面积为0.4至0.8m2 / g,孔体积不低于0.45ml / g,孔隙对于冷和热水均等可及,堆积密度小于700kg / m 3, 在反应器中,形成不小于600m 2 / m 3的几何表面积的形状,其上以13重量%以上的银作为活性组分,每立方米反应器可获得超过115kg的银 和100〜300重量ppm的锂和200〜600重量ppm的铯作为助催化剂存在。 描述了用于制备银催化剂的方法及其用于乙烯氧化的用途。
摘要:
A silver catalyst for the direct oxidation of ethylene with oxygen to give ethylene oxide is applied on a porous carrier and essentially consists of .alpha.-alumina and contains certain amounts of soluble calcium, aluminum, potassium and sodium salts. The carrier has a BET surface area of from 0.2 to 0.8 m.sup.2 /g, a pore volume of not less than 0.5 ml/g, the pores being equally accessible to cold and warm water, and a bulk density of less than 650 kg/m.sup.3, and has a shape which, in the reactor, provides a geometric surface area of not less than 600 m.sup.2 /m.sup.3, on which more than 13% by weight of silver are applied as the active component, more than 110 kg of silver being available per m.sup.3 of reactor.
摘要翻译:用于用氧直接氧化乙烯以产生环氧乙烷的银催化剂被施加到多孔载体上,并且基本上由α-氧化铝组成并含有一定量的可溶性钙,铝,钾和钠盐。 载体的BET表面积为0.2至0.8m2 / g,孔体积不小于0.5ml / g,孔隙对于冷和温水均等可及,并且堆积密度小于650kg / m 3 ,并且具有在反应器中提供不小于600m 2 / m 3的几何表面积的形状,其上施加超过13重量%的银作为活性组分,可获得超过110kg的银 每立方米反应堆。
摘要:
A molded catalyst for reactions carried out under heterogeneous catalysis consists of a catalytically active material shaped into hollow cylinders, or of an inert carrier which is shaped into hollow cylinders and onto which catalytically active material is applied the external diameter of the hollow cylinders being from 3 to 20 mm, the internal diameter being from 0.1 to 0.7 times the external diameter and the length being from 0.2 times to twice the external diameter. The end faces of the hollow cylinder are curved so that the radius of curvature is from 0.4 to 5 times the external diameter.The novel catalysts are particularly useful for partial oxidation in the gas phase.
摘要:
C.sub.2 -C.sub.4 -olefins are prepared by catalytic conversion of methanol and/or dimethyl ether in the presence of a zeolite catalyst at elevated temperatures, by a process in which the catalyst used is a pure borosilicate zeolite which has been tableted or extruded without a binder and treated with hydrofluoric acid and hydrochloric acid. The treatment of the catalyst with hydrofluoric acid is carried out using 0.001-1N HF, and that with hydrochloric acid is carried out using 3-25% strength acid. The time-on-stream of the catalyst is improved.
摘要:
An oxidation catalyst wherein the catalytically active component has the general formulaMo.sub.12 P.sub.a Rh.sub.b Cu.sub.c V.sub.d Cs.sub.e X.sub.f Y.sub.g Z.sub.h O.sub.x,where X is Cr and/or Fe, Y is Nb, Z is Na, Li, K and/or Rb, a is 0.1-4, b is 0.001-1, c is 0.05-2, d is 0.05-4, e is 0.1-5, f is 0-2, g is 0-3 and h is 0-2, and x is the number of oxygen atoms required to saturate the valencies of the other constituents, is very suitable for the preparation of methacrylic acid by gas phase oxidation of methacrolein with an oxygen-containing and steam-containing gas mixture.
摘要:
A crystalline SiO.sub.2 --modification, which is characterized by an X-ray diffraction diagram having certain diffraction lines, and a process for the preparation of this crystalline SiO.sub.2 --modification by crystallizing reactive amorphous SiO.sub.2 under hydrothermal conditions in the presence of hexamethylenediamine. Sodium ions, phosphate ions and/or sulfate ions may be added for the crystallization.
摘要:
Wood preservatives for protecting wood or wood-base materials against animal pests, and which contain a perfluoroalkane sulfonate of the formula C.sub. n F.sub.2n+1 --SO.sub.3 M where n is one of the integers from 1-14 and M denotes hydrogen or a cation, and a process for protecting wood or wood-base materials against animal pests with these compounds.
摘要:
A catalyst for decomposing dinitrogen monoxide which is pure or present in gas mixtures comprises metallic silver applied to an alumina carrier with a BET surface area of from 5 to 25 m.sup.2 /g.
摘要:
Unsaturated nitriles are prepared from lactones and NH.sub.3 by a process in which the reaction of the lactone with NH.sub.3 is carried out in the presence of a zeolite as a catalyst.A particularly suitable starting material is caprolactone and particularly suitable catalysts are zeolites of the pentasil type, for example aluminosilicate zeolites.