Abstract: In the field of automatic boiling in a pan in which the consistency of massecuite is controlled in accordance with method steps, intermittent boiling is used as an effective way to improve the boiling time and quality of products with supplying of appropriate amounts of water or solution into the pan to control the consistency each time it has reached a set value. This invention provides a novel method for controlling the consistency of the massecuite, wherein two curves are established defining the upper limit and lower limit, respectively, of an allowable range of consistency and within which the consistency is maintained, whereby a product of high quality is obtained safely, simply and within a minimum amount of time.

Abstract: 2-Isopropyl-2-(2-methylphenyl)-5-(N-methylhomoveratrylamino)-valeronitrile ("mepamil") of the Formula I: ##STR1## preferably administered in the form of water-soluble acid addition salts such as e.g. hydrochloride. The claimed compound is advantageously prepared by alkylation of 2-(2-methylphenyl)-3-methylbutyronitrile with 3,3-diethoxypropylchloride. Subsequently, the obtained 5,5-diethoxy-2-isopropyl-2-(2-Methylphenyl)-valeronitrile is mildly, acidically hydrolisized to yield the appropriate aldehye, i.e. 2-isopropyl-2-(2-methylphenyl)-5-oxovaleronitrile. This aldehyde is then reacted with N-methylhomoveratrylamine under conditions of reductive alkylation, suitably by catalytic hydrogenation over a platinum or palladium catalyst or by chemical reduction with the use of formic acid as a reducing agent. The resulting base is optionally converted by neutralization with a pharmaceutically acceptable organic or inorganic acid, i.e. hydrochloric or fumaric acid, into the corresponding acid addition salt.

Abstract: Asphaltenes are separated from hydrocarbon oil by bringing the oil into contact with formic acid or a water-soluble organic acid consisting of carbon, hydrogen and oxygen and having at least two functional groups.

Abstract: Process for the preparation of crystalline maltitol comprising successively:catalytic hydrogenation of a saccharified starch milk in a vessel 203,a step of chromatographic fractionation of the hydrogenated syrup in a vessel 204,crystallation and separation of the maltitol crystals in vessels 206 and 207 andrecycling through a pipe 309 emerging from the vessel 207 of the crystallization mother-liquors to the head of the chromatographic fractionation step.

Abstract: Lower olefinic hydrocarbons are produced from methanol in a high yield and with a high selectivity by bringing methanol into contact with a metallosilicate catalyst of the formula Si/Me wherein atomic ratio of Si/Me is 25-3200 and Me is Fe, Ni or Co at a temperature of 250.degree.-400.degree. C., a space velocity of 2000-8000 hr.sup.-1 and a pressure of atmospheric pressure -50 kg/cm.sup.2.

Abstract: A method for separating and purifying branched beta-cyclodextrins from aqueous solution. The process entails adding a beta-cyclodextrin complexant to a starting solution, recovering the precipitate so formed, dissolving the resulting precipitate in water, adding a second dose of beta-cyclodextrin complexant to the solution and recovering branched beta-cyclodextrin from the resulting liquor.

Abstract: A sugar-cooking apparatus of the type having a standing pipe coil surrounded by a heating jacket. The coiled pipe is of flattened cross-section for improved heat transfer. During use, a mixture of sugar, water and additives is passed through the coiled pipe and rapidly heated therein to form a sugar solution.

Abstract: A process for the degradation of granular starch employing hydrogen peroxide and a catalytic amount of manganese ions in an alkaline slurry reaction is disclosed. The manganese ions catalyze the degradative reaction so that the desired amount of degradation of the granular starch can be brought about in a shorter reaction period as opposed to a reaction run without manganese ions.

Abstract: Olefinic feedstocks which contain catalyst contaminants or poisons such as sulfur containing compounds may be oligomerized to a desired product by effecting the reaction in the presence of an added amount of hydrogen to the feedstock. The catalyst which is employed to effect this oligomerization will remain stable and will not deactivate due to the presence of the aforementioned poisons. The catalyst composite will comprise a porous support which has been impregnated with a catalytically effective amount of an iron group metal compound and, if so desired, a compound containing a metal of the Group IVA of the Periodic Table. In addition, the catalyst composite will also contain in combination therewith, a catalytically effective amount of an alkyl aluminum compound and, if so desired, an aluminum alkoxy or aluminum halide compound.

Abstract: The steam and thermal cracking of hydrocarbons is facilely carried out by in situ generating a stream of hot combustion gases including steam, advantageously in the configuration of a downstream axially extending, axially symmetrical helical flowstream, by combustion of steam-producing reactants in a combustion first reaction zone, and serially directly contacting and intimately admixing a liquid hydrocarbon feedstock with said gas of combustion in a downstream isodistribution, non-multi-tubular second reaction zone, advantageously first at a zone of reduced pressure thereof, the momentum of said gas of combustion at the point of direct contact being such as to provide all of the thermal and mechanical energy and heat transfer required to autogenously vaporize, entrain and effect cracking therein of said liquid hydrocarbon feedstock.

Abstract: A ceramic catalyst carrier has a honeycombed structure which comprises a plurality of elongated parallel preferably square channels and thin, porous walls. The thickness of the walls is between 0.4 mm and 1.2 mm. The open cross-sectional area of the channels is greater than 80% of the total cross-section of the carrier body. Besides an intended low primary porosity, a secondary porosity is produced by an opening material. The pores of the secondary porosity which enlarge the active surface for the catalyst show a selected pore size distribution curve with negative skewness and a modal value ranging from 4,000 nm to 60,000 nm. The total true porosity amounts preferably between 50 and 70 Vol. % of the ceramic, whereby the ratio between total and secondary porosity is in the range of 1:1 to 6:1. By ceramic fibres the mechanical strength of the thin walls of the soft green clot and of the fired porous structure can be improved.

Abstract: A process is disclosed for oligomerizing light olefins or their mixtures, which consists in reacting said olefins, possibly diluted with an inert gas, by means of synthetic zeolites containing oxides of silicon, titanium and aluminum, which have, in their calcined and anhydrous state, the following empirical formula:pHAlO.sub.2 .multidot.qTiO.sub.2 .multidot.SiO.sub.2'wherein p has a vlue larger than zero and smaller than, or equal to, 0.050 and g has a value larger than zero and smaller than, or equal to, 0.025, and the H.sup.+ of HAlO.sub.2 can be at least partially substitutable or substituted with cations.

Abstract: A process is disclosed for oligomerizing light olefins or mixtures thereof, which consists in reacting said olefins, possibly diluted with an inert gas, by means of synthetic zeolites containing oxides of silicon, titanium and iron, having, in their calcined and anhydrous state, the following empirical formula:pHFeO.sub.2. qTiO.sub.2.SiO.sub.2,wherein p has a value larger than zero and smaller than, or equal to, 0.050 and g has a value larger than zero and smaller than, or equal to 0.025, and the H.sup.+ of HFeO.sub.2 can be at least partially substitutable or substituted with cations.

Abstract: Heavy crude oil is recovered from tar sand by treating the tar sand with a low concentration emulsion of a solvent in water containing 0.5 to 15% by volume of the solvent. Suitable solvents include hydrocarbons and halogenated hydrocarbons. Solvent-in-water emulsions are efficient in extracting bitumen with the major advantage of greatly reduced solvent: tar sand ratios.

Abstract: A carboxamide compound of the formula: ##STR1## wherein R.sup.1, R.sup.2, R.sup.3, R.sup.4 and X are as defined and pharmaceutically acceptable salts thereof, and composition containing the compound are disclosed.The compound is useful as a calcium antagonistic agent and an antiinflammatory agent.

Abstract: This new process provides for the treatment of a gas containing a light fraction and a heavy fraction, so as to extract at least a portion of the heavy fraction.The process is characterized in that the gas to be treated (1) is contacted with a solvent (8) under cooling conditions to selectively absorb at least a portion of the heavy fraction of the gas in the solvent; the light unabsorbed fraction is discharged (16) and the solution of the heavy fraction in the solvent (18) is subjected to desorption (B.sub.1): the solvent (6) is recycled and the evaporated heavy fraction (9) is condensed (C), expanded (V.sub.1) and evaporated in thermal exchange contact (E.sub.2) with the mixture of the gas and the solvent to be cooled; the heavy fraction is discharged (14).The process may be used for the treatment of gas on the field (associated gas, natural gas) and/or in refining and petrochemical operations.

Abstract: A process for upgrading residual portions of crude oils comprising metal contaminants and Conradson Carbon contributing components by the combination of thermal visbreaking with fluid inert solids and catalytic upgrading of naphtha and higher boiling components of thermal visbreaking in separate systems of riser conversion and solids regeneration is discussed. Heat management of the regeneration systems is restricted in substantial measure by a novel external solids heat exchange apparatus arrangement utilized to partially cool hot regenerated solids utilized in the solids regeneration systems.

Abstract: The invention relates to a process for accomplishing specific chromatographic separation of lactose from milk. Milk is treated in a column with a cation exchange resin balanced in such a manner that its cationic composition corresponds to the cationic composition of milk at a temperature of about 50.degree. to about 80.degree. C., and the column is eluted with water to recover a protein containing fraction and lactose fraction.

Abstract: A piggy back evaporator is sealably coupled in open box form overlying a sugar maple sap evaporator and aligned with an upright flue pan of the conventional sugar maple sap evaporator which, when fired, boils off vaporizable constituents of the sap. The piggy back evaporator includes a drip pan sealably mounted to the flue pan. The drip pan includes an oblique condensate drain sheet extending over the major length of the same. A steam hole within the condensate drain sheet allows steam to reach the lower surface of a bottom wall of a piggy back pan. The piggy back pan bottom wall is corrugated to define a series of laterally spaced troughs on its upper face and flues on its lower face. A hood overlies the piggy back pan and seals off the interior thereof.

Abstract: A scraper for a sugar centrifuge comprises a scraper blade mounted on an arm which is moved down into and pivoted within the centrifugal bowl, such that the edge of the scraper blade is moved against but out of contact with the bowl wall for scraping off the sugar adhering to the bowl wall. After the scraping edge, the scraper blade has an afterscraper in direct or indirect contact with the bowl wall. The afterscraper comprises in one embodiment a block whose boundary plane facing the scraping edge forms an acute angle with the tangential plane along the line of contact of the block with the bowl wall.