Abstract: Disclosed is a method of making a catalyst containing vanadium antimony and tin in the oxide state which comprises making an aqueous slurry of a mixture of source batch materials comprising compounds of the elements to be included in the final catalyst followed by drying and heat calcining the mixture to an active catalyst, using as the source batch material for tin a stannous salt of a C.sub.1 to C.sub.18 acyclic, monocarboxylic acid containing no ethylenic or acetylenic carbon-to-carbon unsaturation.

Abstract: Disclosed is a process for making an .alpha., .beta.-unsaturated mononitrile by the catalytic reaction of a paraffin containing 3-5 carbon atoms with molecular oxygen and ammonia by catalytic contact of the foregoing reactants in a reaction zone with a metal oxide catalyst containing the elements indicated by the empirical formula,Cr.sub.a Mo.sub.b Te.sub.c M.sub.d O.sub.x (formula 1)whereM=one or more of Mg, Ni, Sb, Ti, La, P, Ce, Fe, Nb, W, V, and Cu, each of a, b & c is 0.1 to 10d is zero to 10a+b+c>1.5d, andx is determined by the valence requirements of the other elements present, andwherein the reactants fed to the reaction zone contain a mole ratio of said paraffin:NH.sub.3 in the range from 2.5 to 16 and a mole ratio of said paraffin:O.sub.2 in the range from 1 to 10.

Abstract: Disclosed is a method which comprises introducing into a reaction zone a feed which comprises a hydroxyl compound reactant, R"OH at least one amide reactant selected from R--CONH.sub.2 and R--CONHR', and a Lewis base as catalyst, thereby reacting R"OH with said amide reactant to produce a reaction mixture containing at least one disubstituted amide selected from R--CONR".sub.2 and R--CONR'R", whereineach of R, R' and R" contains no acetylenic unsaturation and 1 to 30 carbon atoms;each of R, R' and R" is selected from a hydrocarbyl groups and a hydrocarbyl group that is substituted with a group selected from carbamoyl, hydrocarbylcarbamoyl, dihydrocarbylcarbamoyl, and hydroxyl.

Abstract: A catalyst which is substantially free of alkali and alkaline earth metals and comprises an effective amount of a platinum group metal on a silicalite support; characterised in that the catalyst also comprises tin. There is also provided a process for the dehydrogenation of a C.sub.2 to C.sub.10 paraffin to yield an alkene product, which comprises contacting the paraffin under dehydrogenation conditions with a catalyst according to the invention.

Abstract: Disclosed is a method which comprises the reaction in a reaction zone of a nitrile, RCN, with a hydroxyl compound, R'OH, in the presence of water introduced into the reaction zone in the amount of more than 0.15 mole and up to 10 moles, per mole of RCN introduced to the reaction zone, thereby producing a reaction mixture containing at least one amide selected from R--CONHR' and R--CON(R').sub.

Abstract: Disclosed is a method which comprises the reaction in a reaction zone of a nitrile, RCN, with a hydroxyl compound, R'OH, in the presence of a Lewis base as catalyst introduced into the reaction zone, thereby producing a reaction mixture containing at least one amide selected from R--CONHR' and R--CON(R').sub.2, whereineach of R and R' contains no acetylenic unsaturation and 1 to 30 carbon atoms,each of R and R' is independently selected from a hydrocarbyl group and a hydrocarbyl group that is substituted with a group selected from cyano, carbamoyl, hydrocarbylcarbamoyl, dihydrocarbylcarbamoyl, and hydroxyl.

Abstract: Disclosed is a process for making an activated antimony and vanadium-containing catalyst in oxide form having an atomic ratio of Sb:V in the range from 0.8-4, which comprises calcining such an oxidic vanadium and antimony-containing composition at a temperature of over 750.degree. C., and thereafter contacting said calcined catalyst with a hydroxy compound in liquid form selected from (1) cyclohexanol, (2) cyclopentanol, (3) a monohydroxy, acyclic hydrocarbon having 1-8 C atoms, and (4) a dihydroxy, acyclic hydrocarbon having 2-4 carbon atoms, and separating as a liquid said compound from said catalyst insofar as it is present beyond the amount wetting said catalyst, and thereafter drying said catalyst.

Abstract: Disclosed is a process for making an .alpha., .beta.-unsaturated monoitrile by the catalytic reaction of a paraffin containing 3-5 carbon atoms with molecular oxygen and ammonia by catalytic contact of the foregoing reactants in a reaction zone with a metal oxide catalyst containing the elements indicated by the empirical formula,V.sub.v A.sub.a D.sub.d Sn.sub.m Sb.sub.n Cu.sub.c O.sub.x (formula 1)in the relative atomic proportions indicated by the subscripts, whereA is selected from Te and BiD is one or more optional elements selected from Mo, W, Ti, Ge, Ce, La, Cr, Mn, Mg, Ca, Co, Ni, Fe, Nb, Ta, Ag, Zn, Cd, B, P, Na, K and Cs, anda is 0.001 to 30d is zero to 30c is 0.001 to 30m is 0.1 to 60n is 0.1 to 60n/v is>12 and<100m+n is.gtoreq.v+a+c+d, andx is determined by the valence requirements of the elements present, andwherein the reactants fed to the reaction zone contain a mole ratio of said paraffin:NH.sub.3 in the range from 2 to 16 and a mole ratio of said paraffin:O.sub.

Abstract: Disclosed is a method which comprises the reaction in a reaction zone of a nitrile, RCN, with a hydroxyl compound, R'OH, in the presence of an inorganic catalyst introduced into the reaction zone, thereby producing a reaction mixture containing at least one amide selected from R--CONHR' and R--CON(R').sub.2, whereineach of R and R' contains no acetylenic unsaturation and 1 to 30 carbon atoms,each of R and R' is independently selected from a hydrocarbyl group and a hydrocarbyl group that is substituted with a group selected from cyano, carbamoyl, hydrocarbylcarbamoyl, dihydrocarbylcarbamoyl, and hydroxyl,wherein said inorganic catalyst is selected from phosphates and sulfates of Be, Ng, Al and B, and mixtures thereof.

Abstract: A mechanical actuator operated by electrical power suitable for actuating down hole equipment in a well, e.g. down hole safety valves, has an electric motor, a gear assembly with a mechanical advantage of at least 30:1, a two-part drive sleeve, the parts being connected by, e.g. splines so that the two parts can rotate together while capable of relative axial movement, an actuating sleeve moved axially by rotation of the drive sleeve, and a releasable lock operated by a solenoid to lock the two parts of the drive sleeve against relative axial movement. Rotation of the motor in one direction primes the actuator, rotating in the other direction actuates the equipment and the solenoid-operated releasable lock holds the equipment in the actuating position. If the solenoid is switched off, deliberately or by power failure, the lock is released allowing the equipment to return to its fail-safe position.

Abstract: Disclosed is a process for making 3-methylpyridine by contacting 2-methylglutaronitrile in admixture with hydrogen gas with a supported solid catalyst containing palladium metal promoted with at least one of Cr, W, Ni, Co and Ge.

Abstract: Disclosed is a method which comprises introducing into a reaction zone a feed which comprises a hydroxyl compound reactant, R"OH, at least one amide reactant selected from R-CONH.sub.2 and R-CONHR', and an inorganic catalyst, thereby reacting R"OH with said amide reactant to produce a rection mixture containing at least one disubstituted amide selected from R-CONHR".sub.2 and R-CONHR'R", whereineach of R, R' and R" contains no acetylenic unsaturation and 1 to 30 carbon atoms,each of R, R' and R" is selected from a hydrocarbyl group and a hydrocarbyl group that is substituted with a group selected from carbamoyl, hydrocarbylcarbamoyl, dihydrocarbylcarbamoyl, and hydroxyl,wherein said inorganic catalyst is selected from phosphates and sulfates of a Group 13 element and of a Group 2 metal having an atomic weight less than 145, and mixtures thereof.

Abstract: A fail safe annulus valve for fluids has a valve area across the annulus with inlet and exit ports and a slide valve in the area capable of sliding to open or close the ports. The slide valve is biased to its fail safe position by a spring, is susceptible to being opened by independent pressure apparatus, and is also susceptible to movement by differential annulus fluid pressure across the valve. Thus while it fails safe, it can always be moved by differential annulus pressure. The valve may be used for the annuli of oil or gas wells (e.g. annuli used for artificial lift) and may be mounted on a packer of the annulus. It may also be used for closing other types of annuli.

Abstract: Disclosed is a process for making ethylamines by the hydrogenation in a reaction zone of acetonitrile contained in a basic aqueous solution which also contains HCN, which comprises continuously passing hydrogen gas in contact with a flowing stream containing acetonitrile, water and HCN, which stream is in contact with a solid hydrogenation catalyst, wherein the hydrogen contact time is in the range from 0.5 seconds to 20 minutes and the molar ratio of H.sub.2 to acetonitrile charged to said reaction zone is in the range 2-200:1.

Abstract: Disclosed is the ammoxidation of methyl substituted pyridines to make cyanopyridines using a complex metal oxide catalyst containing P, V and Mo.

Abstract: Disclosed is a process for making an .alpha., .beta.-unsaturated mononitrile, acrylonitrile or methacrylonitrile, by the catalytic reaction in the vapor phase of a paraffin selected from propane and isobutane with molecular oxygen and ammonia and optionally a gaseous diluent, by catalytic contact of the foregoing reactants in a reaction zone with a catalyst, the feed to said reaction zone containing a mole ratio of said paraffin to NH.sub.3 in the rnage from 2.5 to 16 and a mole ratio of said paraffin to O.sub.2 in the range from 1 to 10, said catalyst having the elements and the proportions indicated by the empirical formula:VSb.sub.m A.sub.a D.sub.d O.sub.xwhereA is one or more Ti, Sn, Fe, Cr, GaD is one or more Li, Mg, Ca, Sr, Ba, Co, Ni, Zn, Ge, Nb, Zr, Mo, W, Cu, Te, Ta, Se, Bi, Ce, In, As, B, Mn andm is 0.8-4a is 0.01-2d is 0-2x is determined by the oxidation state of the cations present,which catalyst has been heated at a calcination temperature of at least 780.degree. C.

Abstract: Apparatus for the preparation of emulsions of oil in water comprises:(a) an oil feed line,(b) a source of concentrated surfactant solution,(c) a source of water,(d) a first low shear mixer for mixing concentrated surfactant and water to form a dilute surfactant solution,(e) means for uniting the flows of dilute surfactant solution and oil in a controlled manner,(f) a second low shear mixer for mixing the united flow streams of oil and dilute surfactant solution to form an emulsion of oil in water,(g) a third low shear mixer for mixing the emulsion of oil in water to form a dilute emulsion, and,(h) an arrangement of water feed lines and control valves such that, firstly, water can be supplied either to the first low shear mixer only or, secondly, to both first and third low shear mixers.The apparatus is particularly suitable for the preparation of emulsions of fuel oil in water from oils within a wide range of viscosities which burn with low emissions of NO.sub.x and particulates.

Abstract: Disclosed is a method of making a tri- or tetrahydrocarbylammonium hexahydroxyantimonate,[R.sub.3 R'N]Sb(OH).sub.6 .multidot.xH.sub.2 O (1)containing 3 to 30 C atoms, which process comprises the steps of (1) contacting a compound selected fromR.sub.3 N and R.sub.4 NOHwith the H.sup.+ form of a solid cation exchange resin, and allowing the amine or the tetrahydrocarbylammonium hydroxide to react with the cation exchange resin, and thereafter (2) contacting the reacted resin with an aqueous solution of KSb(OH).sub.6,wherein each R contains 1-10 C atoms and is independently selected from alkyl, aralkyl and alkylaralkyl, R' is H or H, and wherein x is an indeterminate number of moles of H.sub.2 O.

Abstract: A catalyst which is substantially free of alkali and alkaline earth metals and comprises an effective amount of a platinum group metal on a silicalite support; characterized in that the catalyst also comprises tin. There is also provided a process for the dehydrogenation of a C.sub.2 to C.sub.10 paraffin to yield an alkene product, which comprises contacting the paraffin under dehydrogenation conditions with a catalyst according to the invention.

Abstract: Disclosed is a process f9or making an .alpha., .beta.-unsaturated mononitrile by the catalytic reaction of a paraffin containing 3-5 carbon atoms with molecular oxygen and ammonia by catalytic contact of the foregoing reactants in a reaction zone with a metal oxide catalyst composition that has 10-90 weight percent of a diluent/support and 90-10 weight percent of a catalyst containing the elements indicated by the empirical formula,A.sub.a D.sub.d Bi.sub.c Fe.sub.f Mo.sub.12 O.sub.xin the proportions indicated by the said formula, said diluent/support containing 10 to 100 weight percent Al.sub.2 O.sub.3 and zero to 90 weight percent SiO.sub.2 whereinA is one or more of Li, Na, K, Rb, Cs, Tl B, W, Sn and La;D is one or more of Cr, Sb, Pb, P, Cu, Ni, Co, Mn and Mg;a is zero to 10;c is 0.1 to 10;d is zero to 10; andf is 0.2 to 10; andwherein the reactants fed to the reaction zone contain a mole ratio of said paraffin:NH.sub.3 in the range from 2 to 16 and a mole ratio of said paraffin to O.sub.