Abstract: A turbine has a rotatable outer casing with an inlet and an outlet therein. A casing rotation control causes the casing to rotate about a central point thereof such that the inlet consistently faces an incoming flow of ambient fluid. The casing has two spaced-apart portions in shapes of oppositely-disposed concave arcs (also referred to as “deflector plates” of a same circle. In some embodiments, each concave arc of the casing forms a unitary structure with a respective convex arc, the two spaced-apart convex arcs lying on either side of the outlet. In some embodiments, each concave arc is connected to a respective second concave arc at an endpoint thereof, the second concave arcs being rotatable about the point of connection.

Abstract: A turbine has a rotatable outer casing with an inlet and an outlet therein. A casing rotation control causes the casing to rotate about a central point thereof such that the inlet consistently faces an incoming flow of ambient fluid. The casing has two spaced-apart portions in shapes of oppositely-disposed concave arcs (also referred to as “deflector plates” of a same circle. In some embodiments, each concave arc of the casing forms a unitary structure with a respective convex arc, the two spaced-apart convex arcs lying on either side of the outlet. In some embodiments, each concave arc is connected to a respective second concave arc at an endpoint thereof, the second concave arcs being rotatable about the point of connection.

Abstract: The Present Invention is directed to a composition, its synthesis and a process for adsorptive separation of carbon monoxide from gas mixtures using adsorbents, which comprise cuprous compounds on amorphous oxide macroporous supports. The compositions are prepared by impregnating cupric compounds on supports followed by reduction of the cupric compound to the corresponding cuprous compound. The reduction can be performed by the use of a reducing gas, preferably synthesis gas at relatively low temperatures up to 150.degree. C., preferably preceded by the use of elevated temperature above 250.degree. C. All the adsorbents described in this invention consist of CuCl particles of finite size supported on macroporous support materials including alumina and silica gel. Among the ingredients used to form supported CuCl fine particles are support materials of low dispersing power, high copper loading, absence of dispersants, and proper post heat-treatment. The bulk nature of the active component (i.e.

Abstract: The present invention is directed to an at least binary exchanged X-zeolite having lithium and zinc cations in a ratio of preferably 5% to 40% zinc and 50% to 95% lithium, wherein the sum of the lithium and zinc ion exchange is at least 65% of the exchangeable ion content. Theses adsorbents are useful in a process for separating nitrogen from gas mixtures containing nitrogen and less strongly adsorbed components such as oxygen, hydrogen, argon or helium.

Abstract: The present invention is directed to an at least binary exchanged X-zeolite having lithium and a divalent cation selected from the group consisting of cobalt, copper, chromium, iron, manganese, nickel and mixtures thereof in a ratio of preferably 5% to 50% of the divalent cation and 50% to 95% lithium. Theses adsorbents are useful in a process for separating nitrogen from gas mixtures containing nitrogen and less strongly adsorbed components such as oxygen, hydrogen, argon or helium.

Abstract: The present invention is directed to a process for separating nitrogen from gas mixtures containing nitrogen and less strongly adsorbed components such as oxygen, hydrogen, argon or helium by use of an at least binary exchanged X-zeolite having lithium and a divalent cation selected from the group consisting of barium, cobalt, copper, chromium, iron, magnesium, manganese, nickel, zinc and mixtures thereof in a ratio of preferably 5% to 50% of the divalent cation and 50% to 95% lithium.

Abstract: The present invention is directed to a process for adsorptive separation of carbon monoxide or olefins from gas mixtures using adsorbents, which comprise cuprous compounds dispersed on amorphous oxide or carbon macroporous supports. The compositions are prepared by impregnating cupric compounds on, preferably pretreated, supports with the aid of an aqueous solution of an ammonium salt of a di- or polycarboxylic acid dispersant, such as ammonium citrate, followed by reduction of the cupric compound to the corresponding cuprous compound. The reduction can be performed either by the use of elevated temperature or by the use of a reducing gas preferably carbon monoxide at relatively low temperatures up to 150.degree. C. Methods of synthesis are also disclosed.

Abstract: The present invention is directed to a process for adsorptive separation of carbon monoxide or olefins from gas mixtures using adsorbents, which comprise cuprous compounds dispersed on amorphous oxide or carbon macroporous supports. The compositions are prepared by impregnating cupric compounds on, preferably pretreated, supports with the aid of an aqueous solution of an ammonium salt of a di- or polycarboxylic acid dispersant, such as ammonium citrate, followed by reduction of the cupric compound to the corresponding cuprous compound. The reduction can be performed either by the use of elevated temperature or by the use of a reducing gas preferably carbon monoxide at relatively low temperatures up to 150.degree. C. Methods of synthesis are also disclosed.

Abstract: The present invention is directed to a process for separating nitrogen from gas mixtures containing nitrogen and less strongly adsorbed components such as oxygen, hydrogen, argon or helium by use of an at least binary exchanged X-zeolite having lithium and calcium and/or strontium ions in ratio of preferably 5% to 50% calcium and/or strontium and 50% to 95% lithium.

Abstract: Carboxamides having the structural formula:R.sup.1 CHR.sup.2 CH(OR.sup.3)NHCR.sup.4 Owherein:R.sup.1 is H, C.sub.1 -C.sub.6 alkyl or aryl;R.sup.2 is H, C.sub.1 -C.sub.6 alkyl;R.sup.3 is benzyl, C.sub.1 -C.sub.8 alkyl or hydroxyalkyl; andR.sup.4 is H, C.sub.1 -C.sub.6 alkyl or aryl;are synthesized by reacting an aldehyde having the structural formula: R.sup.1 CHR.sup.2 CHO wherein R.sup.1 and R.sup.2 are as defined above, with an alcohol having the structural formula: R.sup.3 OH, wherein R.sup.3 is as defined above, and an amide having the structural formula: R.sup.4 CONH.sub.2 wherein R.sup.4 is as defined above, in the presence of a strong acid catalyst at a temperature in the range of 0.degree.-200.degree. C.

Abstract: Secondary formamides having the structural formula:R.sup.1 CHR.sup.2 CH(OR.sup.3)NHCHOwhereinR.sup.1 is H, C.sub.1 -C.sub.6 alkyl or aryl;R.sup.2 is H, or C.sub.1 -C.sub.6 alkyl; andR.sup.3 is benzyl, C.sub.1 -C.sub.8 alkyl or hydroxyalkyl;are synthesized by reacting an acetal having the structural formula: R.sup.1 CHR.sup.2 CH(OR.sup.3).sub.2 wherein R.sup.1, R.sup.2 and R.sup.3 are as defined above, with formamide in the presence of a strong acid catalyst at a temperature in the range of 0.degree.-200.degree. C.

Abstract: Amides having different molecular kinetic diameters or heats of adsorption, such as formamide and N-(1-alkoxyethyl)formamide, are separated under mild conditions with a molecular sieve which selectively adsorbs one of the amides, such as formamide. N-vinylformamide can be purified by removing formamide remaining in synthesis process streams using this technique. The adsorbed amide can be desorbed by heating the molecular sieve in either inert or reactive atmospheres. Preferred molecular sieves include the zeolites of types A, X, Y, molecular sieves of the MFI topology, chabazite, and mordenite. Calcium chabazite is particularly versatile and effective.

Abstract: Ethylidene bisformamide is produced in high selectivity by the reaction of formamide with vinyl acetate in a molar ratio of at least 1:1 at a temperature from about 60.degree. to 150.degree. C. in the presence of a catalyst comprising an acid salt of mercury of which the parent acid has a pKa less than about 3.8.

Abstract: The present invention is a process for selectively aminating alcohols wherein a mixture of an amine and a primary or secondary alcohol or diol is contacted with a catalytically effective amount of a phosphorus-containing catalyst which has been impregnated or titrated with a metal cation salt composition represented by the formula:M.sub.a.sup.m.spsp.+ X.sub.b.sup.n.spsp.-wherein M.sup.m+ is a cation selected from Group Ia and IIa of the Periodic Table of the elements having a valence m, X.sup.n- is an organic or inorganic anionic species having a valence n, and a and b are integers such that the ratio of a to b provides a neutral salt. A typical reaction includes the amination of ethanol with piperidine to form N-ethylpiperidine.

Abstract: The present invention relates to a process for the catalytic amination of 1.degree. and 2.degree. alcohols and diols wherein an amine is reacted with an alcohol or diol in the presence of a non-acidic cationic hydroxyapatite catalyst. A typical reaction includes the amination of ethanol with piperidine to form N-ethylpiperidine. The hydroxyapatite catalyst provides high conversion and selectivity toward the N-alkylated product. Product selectivity can be controlled by adjusting the ratio of cation to phosphorus in the hydroxyapatite catalyst.

Abstract: Silicon carbide protective films are produced on the surface of metallic or metal-impregnated substrates. A silicide or silicon diffusion coating is initially formed on the surface of the substrate, and subsequently said surface is treated with a gas stream which is reducing to the coating and substrate and contains a gaseous carbon source at a temperature greater than 500.degree. C.

Abstract: This present invention is a process for alkylating aromatic amines to form ortho-alkylated products in high selectivity relative to N-alkylated products. Aromatic amines are contacted with an olefin or an alcohol in the presence of an ion exchanged zeolite in which at least a portion of the exchangeable ion sites have been exchanged with Al cations.

Abstract: A silicon diffusion coating is formed in the surface of a metal article by exposing the metal article to a reducing atmosphere followed by treatment in an atmosphere of 1 ppm to 100% by volume silane, balance hydrogen or hydrogen inert gas mixture. Hydrogen with a controlled dew point is utilized as a surface preparation agent and diluent for the silane.

Abstract: Alkylated aromatic primary amines undergo disproportionation and transalkylation in the presence of a carbon-containing catalyst at a temperature between 200.degree. C. and 500.degree. C. The carbon-containing catalyst may have carbon as the only active component, or optionally, may also contain a Group VIIIA metal, such as platimum, palladium, nickel, cobalt or mixtures thereof.

Abstract: This invention relates to a process for producing ring alkylated aromatic amines. In accordance with this process an aromatic amine is reacted with an olefin, diolefin or an alcohol using a non-zeolitic molecular sieve as a catalyst. Under the conditions of the process the catalyst is extremely active, and with aromatic amines that are capable of alkylation at the ortho and para positions, high selectivity to the ortho alkylated isomer can be achieved.