Abstract:
A process for preparing alkylsilyl and arylsilyl ethers of formula: (R-O-SiR R R ) wherein R, R , R and R are independently selected from the group consisting of hydrogen, alkyl groups containing one to twenty carbon atoms, substituted alkyl groups containing one to twenty carbon atoms, aryl groups containing six to eighteen carbon atoms, substituted aryl groups containing six to eighteen carbon atoms, hetero aryl groups containing four to eighteen carbon atoms, and substituted hetero aryl groups containing four to eighteen carbon atoms, with the proviso that R is never hydrogen, by reacting, in a hydrocarbon solvent, a chlorosilane of formula: R R R Si-Cl wherein R , R , and R are independently selected from hydrogen, alkyl groups containing one to twenty carbon atoms, substituted alkyl groups containing one to twenty carbon atoms and aryl groups containing six to eighteen carbon atoms, substituted aryl groups containing six to eighteen carbon atoms, hetero aryl groups containing four to eighteen carbon atoms, and substituted hetero aryl groups containing four to eighteen carbon atoms with an alcohol of the formula ROH wherein R is an alkyl group containing one to twenty carbon atoms, a substituted alkyl group containing one to twenty carbon atoms, an aryl or substituted aryl group containing six to eighteen carbon atoms, or a hetero aryl or substituted hetero aryl group containing four to eighteen carbon atoms, in the presence of an organic acid acceptor (base) in a hydrocarbon solvent.
Abstract translation:制备式(R 2 -SR R 1 R 3)的烷基甲硅烷基和芳基甲硅烷基醚的方法,其中R 1,R 2,R 2和R 3独立地选自 由氢,含有1-20个碳原子的烷基,含有1-20个碳原子的取代烷基,含有6-18个碳原子的芳基,含有6-18个碳原子的取代芳基,含有4至18个碳原子的杂芳基组成 原子和含有4至18个碳原子的取代的杂芳基,条件是R不是氢,通过在烃溶剂中使下式的氯硅烷:R 1 R 2 R 3 Si- Cl其中R 1,R 2和R 3独立地选自氢,含有1-20个碳原子的烷基,含有1-20个碳原子的取代烷基和含有6-18个碳原子的芳基 含有6-18个碳原子的取代芳基,杂原子 含有四至十八个碳原子的芳基和含有四至十八个碳原子的取代杂芳基与式ROH的醇反应,其中R是含有1-20个碳原子的烷基,含有1-20个碳原子的取代烷基 ,含有6至18个碳原子的芳基或取代的芳基,或含有4至18个碳原子的杂芳基或取代的杂芳基,在有机酸受体(碱)存在下,在烃溶剂中。
Abstract:
A process for producing Caro's acid by reaction of at least 85 % by weight sulfuric acid and at least 50 % by weight hydrogen peroxide wherein the sulfuric acid (9) and hydrogen peroxide (1) are fed through separate feed lines (11 and 3), respectively, into a funneling zone (17) open to the atmosphere, the feed lines (11) and (3) having air gaps between their ends and the funneling zone (17); passing the hydrogen peroxide (1) and sulfuric acid (9) by gravity flow from the funneling zone (17) into one end of a reaction zone (22) whose size permits a pressure drop which is at least 8 times the theoretical pressure drop for such reaction zone (22) and removing a mixture containing Caro's acid (28) from the exit end (26) of the reaction zone (22).
Abstract:
A marschmallow-type confection which is rendered heat stable to 400 DEG F (250 DEG C) by the inclusion of microcrystalline cellulose (MCC), and which optionally includes at least one natural gum. In additional embodiments, the inventive confection [1] comprises entirely vegetal matter by the replacement of the animal-origin gelatin normally present with a vegetal gum, and/or [2] comprises a reduced calorie confection by the replacement of higher calorie sugars by non-caloric and/or lower-calorie bulking agents comprising additional amounts of MCC and, optionally, lower calorie sugar.
Abstract:
A process for quickly preparing easily separable solutions of lithium alkylamides, as exemplified by the formula (I): (R3M)xNLi(R1)y.(LB)z wherein M is silicon or carbon, R and R are C1-C8 alkyl, cycloalkyl or alkylene groups, LB is a Lewis base, x and y are integers equaling 2, and z is greater than 1, comprising the steps of reacting lithium metal in bulk form with an alkylamine in mole ratios of metal to alkylamine ranging from 2 to 1 to 10 to 1 in a solvent selected from ethereal or selected from the group consisting of conjugated dienes, vinyl aromatic and polycyclic aromatic compounds, under an inert atmosphere at elevated temperatures for 1 to 10 hours, cooling the product and separating the product solution from the unreacted lithium metal in the reactor.
Abstract:
Stable, redispersible, high internal phase w/o emulsion concentrates having a weight ratio of water: oil from about 3.5:1 to about 19:1 are prepared under low shear using 0.5 to 3 wt.%, based on the weight of the oil phase, of an emulsifier that is a polyglycerol ester of polycondensed ricinoleic acid. These concentrates may be used, for example, as fat mimetics in the food industry, as clouding agents for beverages, and in cosmetic and pharmaceutical compositions. The concentrates may further be used in and includes w/o/w emulsion compositions.
Abstract:
Refractory ore is crushed (2) conveyed to a pug mill mixer (6) and mixed with sulfuric acid. Nitric acid is then added to the ore in a second pug mill mixer (12) and a third mixer (20). The ore is then conveyed to a curing/oxidation rotary mixer (28) where NOx (30) is evolved and recycled to an HNO3 regenerator (94). The ore is then conveyed to a permeable bed (36) and then a pug mill (48) where CaO is added for neutralizing acid before it is conveyed to a cyanide heap leach (54) for leaching the precious metals which are absorbed with carbon (68) and the precious metals then recovered (74).
Abstract:
Combinations of bifenthrin with azadirachtin-containing neem seed extracts are synergistic in controlling acarids, especially pyrethroid-resistant mites, over a wide range of azadirachtin to bifenthrin ratios.
Abstract:
This invention provides a family of insecticidally effective proteins and particular members of that family which may be isolated from the venom of the spider Filistata hibernalis, DNA encoding such proteins, insecticidal compositions of these proteins or the DNA encoding them, and methods for controlling invertebrate pests. Recombinant expression vectors and host cells and methods for producing insecticidally effective peptides are also provided.
Abstract:
A process for producing soda ash (47) from a brine (1) containing sodium carbonate and sodium bicarbonate obtained by contacting water with an underground trona formation by heating the brine at 100 DEG C to 140 DEG C to evaporate water (6 A), convert sodium bicarbonate to sodium bicarbonate to sodium carbonate and drive off resulting carbon dioxide (7), reacting the brine with reduced sodium bicarbonate (8) with an aqueous sodium hydroxide solution (8 A) in amounts to convert essentially all of the remaining sodium bicarbonate in the brine to sodium carbonate, cooling to 5 DEG C to 25 DEG C to precipitate sodium carbonate decahydrate crystals (21 A), separating the crystals from their mother liquid (24 A), melting the separated crystals (35 A) to form a sodium carbonate solution (38), heating the solution to from above 60 DEG C to below 110 DEG C to evaporate water and precipitate sodium carbonate monohydrate crystals (38 A), separating the sodium carbonate monohydrate crystals from their mother liquor (41 A), and calcining them (44 A) to soda ash (47).
Abstract:
A process is provided for detoxifying an aqueous solution containing weak acid-dissociable cyanide metal complexes. The process comprises incorporating hydrogen peroxide and at least 1 mole of citric acid per mole of complexed metal ion and maintaining the pH of the solution between 8 and 12.