ITS OPTICALLY ACCEPTABLE ISOMERS, THEIR PHARMACEUTICALLY ACTIVE ACID ADDITION SALTS, PROCESSES FOR THE PREPARATION THEREOF, PHARMACEUTICAL COMPOSITIONS CONTAINING THEM AND THE THERAPEUTIC USE THEREOF FOR THE TREATMENT OF CALCIUM DEFICIENCY.
Abstract:
Wrapping films capable of forming peelable seals, comprising by weight 20 to 80% of heat-sealable rigid polymers (A) which, in film form, have an elasticity modulus in excess of 3000 kg/cm2, measured according to the ASTM D 88227 standards; 0.1 to 50% of non-heat-sealable polymers (B) which do not form a solution with polymer (A); 0.1 to 30% of heat-sealable branched olefinic polymers (C) which, in film form, have an elasticity modulus below 3000 kg/cm2, measured according to the ASTM D 88227 standard; and 0 to 45% of polymers (D) compatible with polymers (A), (B) and (C), the sum of the polymers (A), (B), (C) and (D) representing 100% of the polymer material of the film, to which up to 45% of additives (E) and/or up to 10% of adjuvants (F) conventional for wrapping films may be added and process for the preparation thereof.
Abstract translation:能够形成可剥离密封件的包装薄膜包含按重量计20-80%的可热封刚性聚合物(A),其以膜形式具有超过3000kg / cm 2的弹性模量,根据ASTM D 88227标准 ; 0.1〜50%不能与聚合物(A)形成溶液的不可热封聚合物(B); 根据ASTM D 88227标准测量,其膜形式的弹性模量低于3000kg / cm 2的可热封支链烯烃聚合物(C)为0.1至30% 和与聚合物(A),(B)和(C)相容的聚合物(D)的0至45%,聚合物(A),(B),(C)和(D) 聚合物材料可以加入其中常规用于包装薄膜的多达45%的添加剂(E)和/或至多10%的佐剂(F)和其制备方法。
Abstract:
The present invention relates to the production of artificial paper of improved physical characteristics yet which retains the advantageous properties of cellulose paper. This novel artificial paper is comprised of (a) at least one of a specific class of rigid polyolefins, (b) at least one specific class of polymers incompatible with the rigid polyolefin and (c) at least one of a specific class of macromolecular materials which produce compatability of (a) and (b).
Abstract:
A CONTINUOUS PROCESS FOR EXTRACTING ALKALI PHOSPHATES AS CONCENTRATED, PURE SOLUTIONSDERVIED FROM THE ACIDIC ATTACK ON NATURAL ROCK COMPRISING IN T HAT IN A FIRST SERIES OF COUNTERCURRENT FLOW EXTRACTORS IMPURE SOLUTIONS OF PHOSPHORIC ACID ARE TREATED WITH A SOLVENT WHILE A STRONG ACID IS INTRODUCED AT ONE OR MORE POINTS IN THE FIRST SERIES OF EXTRACTORS, EXTRACTING THE SOLUTION OF PHOSPHORIC ACID IN SAID SOLVENT IN COUNTERCURRENT FLOW WITH AQUEOUS SOLUTIONS C ONTAINING PHOSPHATE IONS AND ALKALI IONS WITHIN A SECOND SERIES OF COUNTERCURRENT FLOW EXTRACTORS, FIRST WASHING AND PARTIALLY EXTRACTING THE SOLUTION OF PHOSPHORIC ACID IN SAID SOLVENT WITH A STREAM OF PURE WATER IN A THIRD SERIES OF COUNTERCURRENT FLOW EXTRACTORS, ADDING THE WATER STREAM LOADED WITH PHOSPHORIC ACID TO THE STARTING IMPURE SOLUTIONS OF PHOSPHORIC ACID IN THE FIRST SERIES OF EXTRACTORS, RECYCLING THE SOLVENT LEAVING THE SECOND SERIES OF EXTRACTORS TO THE FIRST SERIES OF EXTRACTORS, COLLECTING EXHAUSTED SOLUTIONS OF PHOSPHORIC ACID CONTAINING THE STRONG ACID WHICH HAS BEEN ADDED AT THE OUTLET OF THE FIRST SERIES OF EXTRACTORS, AND COLLECTING PURE ALKALI PHOSPHATES AS CONCENTRATED SOLUTIONS AT THE OUTLET OF THE SECOND SERIES OF EXTRACTORS.
Abstract:
CONTINUOUS PROCESS FOR THE PREPARATION OF MALEIC ANHYDRIDE WHICH COMPRISES: (A) CONCENTRATING A MALEIC ACID SOLUTION (E.G. FROM WASHING EFFUENT OF CATALYTIC OXIDATION OF BENZENE) AT 100-150*C. AND 400-760 MM. HG; (B) CONVERTIG THE DEHYDRATED MALEIC ACID FROM (A) AT 150-200*C. AND 40-300 MM. HG INTO A LIQUID PHASE OF IMPURE MALEIC ACID AND A PURIFIED GASEOUS PHASE OF MALEIC ANHYDRIDE AND WATER VAPOUR; (C) TREATING THE LIQUID PHASE FROM (B) WITH MALEIC ACID, FILTERING OFF THE IMPURITIES INCLUDING ANY FUMARIC ACID AND EITHER RECYCLING THE PURIFIED MALEIC ACID FILTRATE PARTLY TO (A) AND PARTLY TO (B) OR REMOVING SAID FILTRATE FORM THE SYSTEM; (D) CONDENSING THE GASEOUS PHASE FORM (B) AT A TEMPERATURE ABOVE THE DEWPOINT OF WATER GIVING SUBSTANTIALLY PURE MALEIC ANHYDRIDE AND WASHING THE RESIDUAL VAPOUR WITH WATER AND EVENTUALLY RECYCLING THE SOLUTION CONTAINING MALEIC ACID TO (A).
Abstract:
Adipic acid can be produced in a good yield and with only a small production of propionic acid by carrying out the alkali metal amalgam hydrodimerization of acrylic acid in dimethyl sulfoxide preferably admixed with water.