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1-13c-caprylic acid synthesis method |
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IPC classes for russian patent 1-13c-caprylic acid synthesis method (RU 2382025):
Antiinflammatory medications / 2365585
Invention relates to derivatives of 3-aminocaprolactam of formula (I): , where X represents -CO-R1 or -SO2-R2, R1 represents alkyl (with the exception of 5-methylheptanyl and 6-methylheptanyl, where radical R1 is bonded to carbonyl in position 1), halogenalkyl, alkoxy (with the exception of tret-butyloxy), alkenyl, alkinyl or alkylamino radical from 4-20 carbon atoms (for example, from 5-20 carbon atoms, 8-20 carbon atoms, 9-20 carbon atoms, 10-18 carbon atoms, 12-18 carbon atoms, 13-18 carbon atoms, 14-18 carbon atoms, 13-17 carbon atoms) and R2 is alkyl radical from 4-20 carbon atoms (for example, from 5-20 carbon atoms, 8-20 carbon atoms, 9-20 carbon atoms, 10-18 carbon atoms, 12-18 carbon atoms, 13-18 carbon atoms, 14-18 carbon atoms, 13-17 carbon atoms); or to its pharmacologically acceptable salt. Invention also relates to application and pharmacological composition, which has anti-inflammatory activity, based on said compounds.
Method of zirconium carboxylate production / 2332398
Invention relates to chemistry of derivative transition metal and can be used in chemical industry while producing transition metal carboxylate and refers to improved method of zirconium carboxylate production through interreacting of zirconium chloride with carboxylate derivatives of general formula RCOOM, where R-linear and branched alkyl CnH2n+1 or non-saturated acid residue, where n=0-16, and M - proton or cation of alcali metal, in which alkali acid of aliphatic or non-saturated acids are used as RCOOM compounds, interacting of zirconium chloride with the compounds leads to solvent absence in solid with mechanical activation at mole ratio ZrCl4: RCOOM within 1<m<4.5, where m is integral and broken number with the following extraction of derived zirconium carboxylate with an organic solvent.
Method for preparing saturated aliphatic carboxylic acids and methods for preparing their derivatives (variants) / 2311402
Invention relates to a method for synthesis of saturated aliphatic carboxylic acids with stable carbon isotopes (1-13C). Method involves the hydrocarboxylation reaction of α-olefins with carbon monoxide (13CO) and water at temperature 100-170°C and under pressure not exceeding 5 MPa in the presence of a solvent and catalytic system containing palladium compound as complex PdCl2(PPh3)2 and triphenylphosphine PPh3 taken in the ratio from 1:2 to 1:100, respectively. Synthesized carboxylic acids can be used as diagnostic test-preparations in medicine practice and in criminology, scientific investigations and in other fields. Invention provides synthesis of enanthic acid and caprylic acid labeled by stable carbon isotope 13C at position 1 for a single step, to increase yield of acids as measured for isotope raw, to decrease cost price of acids and to obtain derivatives of (1-13C)-caprylic acid - (1-13C0-caprylate sodium and (carboxy-13C)-trioctanoine.
Process of producing carboxylic acids, alcohols, or esters (options) / 2268872
Subject of invention is continuous carbonylation of long-chain aliphatic hydrocarbons to produce alcohols, acids, and other oxygen-containing products such as esters. Process comprises paraffin dehydrogenation, carbonylation, and fraction distillation-mediated end product recovery. Advantageously, mixture of paraffins containing different number of carbon atoms isolated from kerosene fraction is processed. Non-converted paraffins are recycled into dehydrogenation zone. Prior to be fed into carbonylation zone, stream is processed by selectively hydrogenating diolefins. In the carbonylation stage, homogenous catalytic system is used containing palladium/imidazole or palladium/triphenylphosphine complex, aliphatic acid (preferably formic acid), and solvent. Catalytic system further includes promoter selected from group: lithium iodide, zirconium chloride, tin chloride, and lithium bromide.
Method for preparing calcium stearate / 2259993
Invention relates to a method for preparing calcium stearate used for stabilization of plastic masses, in manufacture of paint and varnish materials, vitamin and medicinal preparations. Preparing calcium stearate is carried out by interaction of stearic acid and calcium oxide or hydroxide in the equimole ratio of reagents. The process is carried out in the solid phase under atmosphere pressure and intensive stirring without heating in the presence of zeolite of CaX type taken in the amount 6.7-16 wt.-%. Method provides simplifying technology due to a single stage process and improvement of economical indices.
The method of obtaining monocarboxylic acids (c4-c8 / 2242456
The invention relates to chemical technology, in particular to an improved method for producing a saturated monocarboxylic acids WITH4-C8by oxidation of the corresponding aldehydes with oxygen, aldehydes impose additional isopropanol at a volume ratio of isopropanol to the aldehyde, equal 0,0007-0,0038, and the reaction is carried out at a temperature of 50-700With
The method of obtaining the oil-soluble salts of the catalytically active metals / 2208603
The invention relates to an improved process for the preparation of oil-soluble salts of catalytically active metals in the form of a pasty mass, which are used as catalysts in oxosynthesis, condensation of aldehydes, oxidation of hydrocarbons, accelerators, curing polyester resins, driers, etc
Modified amino acids, compositions for delivery of biologically active agents in the selected biological system, the method of obtaining such compositions and pharmaceutical composition / 2203268
A mixture of branched primary alcohols, methods of obtaining, a mixture of biodegradable detergents, washing composition / 2198159
The invention relates to a mixture of branched primary alcohols from C11to C36and to mix them sulfates, alkoxylated, alkoxylates and carboxylates, which have high washing ability in cold water and good biological degradability
The method of obtaining cobalt salts of polyhydric carboxylic acids / 2194033
The invention relates to the field of synthesis of adhesive materials, in particular the technology of production of cobalt salts of polyhydric carboxylic acids, which are widely used in tire, rubber, paint and other industries
Manganese (ii) fumarate synthesis method / 2376278
Method of synthesis of manganese (II) fumarate through direct reaction of metal with acid is presented. The process is carried out in a vertical type bead mill with mass ratio of beads to the reaction mixture equal to 1:1, and the liquid phase is a solution of fumaric acid in an organic solvent with content of acid of 0.70-1.80 mol/kg. Manganese is taken in stoichiometric amount with acid or in deficiency of up to 5%. The process is started by loading the liquid phase solvent and acid and preparation of the acid solution in a bead mill, after which metal is loaded and the process is carried out at temperature ranging from 25 to 35°C while preventing spontaneous increase of temperature through forced cooling and controlling through sample taking and determination of manganese salt in the samples and residual amount of acid until attaining values close to calculated values during quantitative conversion of the reagent in deficiency. After that stirring and cooling are stopped. The suspension of the reaction mixture is separated from the glass beads, cooled to temperature between 5.2 and 6.2°C and filtered. The filtering residue is washed with the liquid phase solvent, cooled to approximately the same temperature, and taken for purification by recrystallisation. The filtrate and the washing solvent are returned to the repeated process.
Iron (ii) oxalate synthesis method / 2376277
Invention relates to a method of producing iron (II) oxalate by directly reacting metal with acid in the presence of atmospheric oxygen and a liquid phase while stirring. The process is carried out in a bead mill. The liquid phase solvent used is water with mass ratio of the liquid phase to glass beads equal to 1:1, content of oxalic acid in the initial load is between 0.5 and 2.0 mol/kg, and content of stimulating sodium chloride additive is between 0.02 and 0.10 mol/kg. Crushed grey cast iron which is stirred by a blade mixer is taken in amount of 30% of the mass of the rest of the load. The process is started and carried out at temperature in the interval from (50±2) to (93±2)°C while bubbling air under conditions for stabilising temperature using a heated liquid bath and controlling using a sample taking method and determination of content of iron (II) and (III) salts in the samples, and residual quantity of acid up to virtually complete conversion of the latter into salt. After that air bubbling, external heat supply for stabilising temperature and stirring are stopped. The suspension of the reaction mixture is separated from the glass beads and particles of unreacted metal alloy and filtered. The filtration residue is washed with distilled water and taken for further purification through recrystallisation, while the filtrate and the washing water are returned to the load for the repeated process. Iron (II) oxalate, which is separated from the reaction mixture by traditional filtering, is virtually the only product of conversion.
Method of producing iron (ii) fumarate / 2373217
Iron (II) fumarate can be used in different fields of chemical practice, in analytical control and in scientific research, through direct reaction of iron with fumaric acid in the presence of a catalyst, where the catalyst used is molecular iodine in amount of 0.025 to 0.1 mol/kg of the initial load, iron is taken in large excess in form of shells on the entire height of the reactor, false bottom and blade mixer, as well as in form of crushed cast iron and(or) reduced iron powder, the liquid phase solvent used is butylacetate, in which iodine and fumaric acid are at least partially dissolved, where fumaric acid is taken in amount of 0.8 to 1.2 mol/kg of the initial load, loading is done in the sequence: glass beads, liquid phase solvent, fumaric acid, iodine, and then crushed cast iron and(or) reduced iron powder; the process is started at room temperature and is carried out in a vertical type bead mill with ratio of mass of beads to mass of crushed cast iron and(or) reduced iron powder equal to 4:1, at temperature ranging from 18 to 45°C while bubbling air with flow rate of 0.95 l/min-kg of the liquid phase and using forced cooling and controlling using a sampling method until complete exhaustion of the loaded acid for formation of salt, after which stirring and cooling are stopped, the reaction mixture is separated from glass beads and unreacted crushed cast iron and(or) reduced iron powder and filtered, the residue is washed with butylacetate and taken for recrystallisation, and the filtrate and washing butylacetate are returned to the repeated process. Amount of acid used in extracting the product (without loss during purification) ranges from 89 to 96.5%, which depends on conditions for carrying out the process.
Method of producing basic phthalate of iron (iii) / 2373186
Invention relates to an improved method of producing basic phthalate of iron (III), which is used in chemical practice, analytical control and scientific research, through direct reaction of iron with atmospheric oxygen and phthalic acid in the presence of organic solvent, where the stimulating additive used is hydrochloric acid and inorganic chlorides in amount ranging from 0.013 to 0.062 mol/kg of the load. The liquid phase solvent is n-butyl alcohol iron which is crushed and moved in the reaction zone in form of steel balls with diametre ranging from 2.2 to 3.7 mm, alone or in combination with crushed cast iron in any mass ratio. Initial content of phthalic acid is varied from 1.0 to 1.5 mol/kg of the load. The reactor used is a vertical type bead mill with the grinding agent in form of steel balls and crushed alloy of iron together with glass beads in mass ratio of iron-containing reagent, beads and the rest of the load equal to 1:1:0.6 with a spill pipe as a bubbler during the process. Loading is done in the following sequence: grinding agent and moved metal, liquid phase solvent, phthalic acid, chlorine-containing stimulating agent, and the process itself starts with heating contents of the reactor to 35°, is carried out with self-heating in the range 35 to 50°C while stirring continuously, bubbling air at a rate of 2.3 to 3.1 l/(min kg of load), while maintaining temperature using a cooling liquid bath and controlling the process using a sampling method until exhaustion of all loaded acid, after which bubbling is stopped. Suspension of the reaction mixture is let to flow under gravity through a net lying in the field of a permanent magnet into the receiving tank of a vacuum filter, after which it is filtered. The residue is washed with the liquid phase solvent and taken for purification, and the primary filtrate and washing solvent are returned to the repeated process.
Mechano-activated amorphous and amorphous-crystalline calcium salts of gluconic acid, compositions, methods of production, pharmaceutical preparations and method of treatment based on said preparations / 2373185
Crystalline calcium salt of gluconic acid or its compound with excipients is processed in grinding activator devices, or to a value of supplied specific energy of not more than 10.4 kJ/g and achieving amorphous-crystalline state, or to a value of specific energy of not less than 10.5 kJ/g and achieving amorphous state. The obtained substances are analysed using X-ray diffraction, infrared, NMR, EPR spectroscopy, mass- and chromatography-mass spectrometry and differential thermal analysis.
Method of producing malonate and manganese (ii) succinate / 2373182
Invention relates to a method of producing malonate or manganese (II) succinate, which can be used in different areas of chemical practice, in analytical control and scientific research, through direct reaction of a metal and its dioxide with carboxylic acid in the presence of an organic solvent and stimulating iodine additive in a vertical type bead mill with a high-speed mixer and glass beads as grinding medium, where manganese, its dioxide and carboxylic acid in the initial load are taken in molar ratio 1+x):1:(2+x) so as to obtain (2+x)m moles of salt, where x in the given molar ratio of reagents equals 0.4±0.1 for amber acid and 1.0±0.1 for malonic acid, and m is the number of moles of manganese dioxide in the load; iodine is taken in amount of 0.05 mol/kg of the reaction mixture after loading organic solvent and acid, but before loading manganese dioxide and metal. Total mass of acid, metal and its dioxide lies between 15 and 25% of the mass of the initial load, and ratio of mass of beads to mass of the load is 1:1. The process is started at room temperature and carried out under forced cooling conditions at temperature ranging from room temperature to 40°C while controlling by taking samples until exhaustion of all loaded reagents into the target salt, after which the process is stopped. The suspension of the final reaction mixture is separated from the beads and filtered. The product residue is washed with a liquid phase solvent and taken for purification from trace metal and its dioxide through recrystallisation, and the filtrate and washing solvent are returned to the repeated process.
Method of producing manganese (ii) fumarate from manganese metal and manganese (iii) oxide / 2371430
Invention relates to an improved method of producing manganese (II) fumarate from manganese metal and its oxide (III) through direct reaction of the metal and its oxide Mn2O3 with an acid in the presence of a liquid phase and a stimulating iodine additive in a vertical type bead mill with glass beads as grinding agent. The metal and its oxide are loaded in molar ratio (2±0.1):1 in total amount of 7.87 to 10.93% of the mass of the load. Acid is added with 15 to 25% excess of the calculated value, equal to the number of moles of metal and twice the number of moles of metal oxide in the load. The base of the liquid phase is isoamyl alcohol, in which the iodine stimulating additive is dissolved in amount of 0.02 to 0.05 mol/kg. Glass beads are loaded first, in mass ratio to the reaction mixture of 1.35:1, and then later the liquid phase solvent, acid and stimulating additive, and after brief stirring, metal oxide and metal, stirring all the while. Taking this moment as the beginning of the process, forced cooling is introduced right away. Operating temperature is stabilised in the range 33 to 45°C and in this mode, the process is carried out until virtually quantitative conversion of metal and its oxide to the target salt, after which stirring and forced cooling are stopped. The reaction mixture is separated from the glass beads, cooled to temperature 5 to 6°C and kept at that temperature for 1 to 2 hours. The solid phase of the target salt is filtered off and washed with isoamyl on a filter cooled to approximately the same temperature, after which it is taken for purification by recrystallisation. The filtrate and the cleaning solvent, containing excess acid, the bulk of the stimulating additive and a certain amount of dissolved target salt, are returned for loading in the repeated process. The process is carried out in light temperature conditions. The target substance can be easily separated.
Reaction product of selenium dioxide and aliphatic haloid carboxylic acids, method for making product, solution of product and therapy of benign, virus, premalignant and malignant nonmetastasing skin affections, dysontogenetic lesions of visible mucous membranes and other skin diseases / 2366648
Invention refers to a new product in the form of solution for treatment of benign, virus, premalignant and malignant nonmetastasing skin affections, dysontogenetic lesions of visible mucous membranes, skin mycoses, wrinkle correction and senile pigment spots. The product represents a compound of general formula H2SeO3·x·[R-CXY-(CH2)m-COOH], where x=2-6 prepared from reaction of selenium dioxide and haloid carboxylic acids of general formula R-CXY-(CH2)m-COOH, where R = phenyl, alkyl of general formula CnH2n+1; n=1-5, X=H or Y, Y=F, CI, Br or J, m = 0-10. Besides, the invention concerns a product in the form of solution for treatment benign, virus, premalignant and malignant nonmetastasing skin affections, dysontogenetic lesions of visible mucous membranes, skin mycoses, wrinkle correction and senile pigment spots, containing 0.1-50 wt % of said product, 1-99 wt % of haloid carboxylic acids and the rest - water. Also the invention concerns method of treatment of various skin diseases, including topic applications of the product.
Method of obtaining nickel (ii) oxalate dihydrate / 2362763
Invention relates to improved method of obtaining nickel (II) oxalate NiC2O4·2H2O, which includes preparing of reaction water solution, which contains nickel (II), precipitation of nickel oxalate, separating of sediment from solution and its drying, in which as nickel source used are solutions of nickel chloride, nitrate, sulphate, and as reagent-precipator used is anionite AB-17-8 in oxalate form. Obtained product can be applied in industry for producing catalysts, metal films, polymetal alloys, ceramic-metal and ferromagnetic substances, as well as in production of electrovacuum devices.
Method for preparation of manganese oxalate (ii) / 2359956
Invention is related to improved method for preparation of manganese oxalate (II) by means of direct interaction of metal with acid in bead mill in presence of liquid phase, in which manganese and oxalic acid are loaded into bead mill in stoichiometric ratio in amount of 0.75-2.4 mole/kg of load at mass ratio of load and glass beads of 1:1.2, liquid phase dissolvent used is water or organic substance, or mixture of organic substances; loading is carried out in the following sequence: liquid phase dissolvent, acid, then metal; process is started at room temperature and is carried out under conditions of forced cooling in the temperature range of 18-39°C with control over procedure by sampling method to practically complete spend of loaded reagents for product making, afterwards mixing and cooling are terminated, suspension of reaction mixture is separated from glass beads and filtered, salt deposit is sent for product cleaning from traces of non-reacted metal, and filtrate is returned into repeated process.
Catalyst system / 2372989
Present invention relates to a new catalyst system, a new carbonylation reaction medium and to a method of carbonylation of ethylene-unsaturated compounds using the new catalyst system. The catalyst system, which is capable of catalysing carbonylation of an ethylene-unsaturated compound, can be obtained by combining: a) group VIIIB metal, or its compound, b) bidentate phosphinic or arsinic ligand and c) acid, where the said ligand is present in molar excess of at least 2:1, compared to the said metal or said metal in its compound, and the said acid is present in molar excess ranging from 5:1 to 95:1, compared to the said ligand. In another version the catalyst system, which is capable of catalysing carbonylation of an ethylene-unsaturated compound, can be obtained by combining: a) group VIIIB metal, or its compound, b) bidentate phosphic or arsinic ligand and c) acid, where molar ratio of the said ligand to the said metal or said metal in its compound lies in the range greater than 5:1 to 750:1, and the said acid is present in molar excess of at least 2:1, compared to the said ligand.
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FIELD: chemistry. SUBSTANCE: invention relates to a method for synthesis of 1-13C-caprylic acid which is used as a diagnostic preparation when diagnosing motor-evacuation functions of the stomach. The method involves hydrocarboxylation reaction of 1-heptene with carbon monoxide 13CO and water at temperature 100-170°C and pressure not above 5 MPa, in the presence of a solvent and a catalyst system which contains a complex compound of palladium and triphenylphosphine in ratio ranging from 1:2 to 1:100, where the solvent used is dioxane and/or aromatic hydrodrocarbon. EFFECT: obtaining 1-13C caprylic acid with high isotope purity, increased cost-effectiveness of the process owing to increased degree of utilisation of isotope material. 5 cl, 9 ex
The invention relates to organic chemistry, in particular to methods for saturated aliphatic carbolic acid containing stable carbon isotopes13With, and in particular 1-13With Caprylic acid. This compound is used as a diagnostic drug for the diagnosis of motor-evacuation function of the stomach. Analysis of scientific literature shows that there is a method of obtaining enanthic acid containing a radioactive isotope of carbon14In position 1 the molecules of acid (carbonyl carbon atom) (see, for example, Ammara, Delwilliams. "Syntheses of organic compounds with carbon isotopes". M., 1961, p.39). The known method is a multistage process of interaction of methyl iodide-14With dihydroisoquinolin potassium with the formation of 2-methyl-14C-dehydroretinal and then restoring it with a solution containing sodium hydroxide, diethylene glycol and 85%hydrazinehydrate with the formation of the 114With-enanthic acid with access to 39.6%, based on methyl iodide-14C. Unfortunately, there is a method of obtaining carboxylic acids is complicated by the fact that consists of several stages, and also the use of compounds with radioactive isotope of carbon14C. Another disadvantage of this method is low Ihad target product isotope raw materials. Previously we have proposed a method of obtaining the 113With Caprylic acid (U.S. Pat. RF 2311402, MKI7SS 51/14, 2007) reaction hydrocarbonsoluble 1-Heptene - its interaction with carbon monoxide13And water at a temperature of 100-170°C. and a pressure of not more than 5.0 MPa, in a mixed solvent - propionic acid and o-xylene in the presence of a catalytic system containing a compound of palladium in the form of a complex PdCl2(PPh3)2and triphenylphosphine h3taken in the ratio range of from 1:2 to 1÷100 respectively. Selectivity for Caprylic acid is 98%. Output 1-13With Caprylic acid in the calculation of the absorbed13WITH 100%. At the same time, the degree of isotopic enrichment was 80%, so the yield of the desired acid13WITH at 78.4% of theoretical. It is known that carboxylic acids in the conditions of the carbonylation of olefins in solution complexes of palladium and rhodium may be subject to decomposition (decarbonylation) with the release of carbon monoxide (J.Tsuji. Palladium. Reagents and Catalysts. Chichester: John Wiley & Sons: 1998, p.385, 537). In this case formed WITH unlabeled will also interact with the original olefin with the formation of the corresponding carboxylic acid, which could cause a reduction in the degree of isotopic enrichment (isotopic purity) in the pre is its us the way. The yield of 1-13With Caprylic acid source13WITH will be lower due to the decline in the share of initial reagents into the target 1-13With Caprylic acid. Thus, the disadvantage of this method is the low degree of isotopic enrichment of the 113With Caprylic acid. In the framework of the present invention solves the task of developing a one-step method of obtaining Caprylic acid with a stable isotope of carbon13In position 1 the molecules of acid (carbonyl carbon atom) with isotopic purity not less than 98%, increased yield of the desired acid in the calculation of the isotopic raw materials, improve the economic efficiency of the process. The problem is solved in that Caprylic acid stable isotope of carbon13In position 1 is obtained by reaction of hydrocarbonsoluble 1-Heptene - its interaction with carbon monoxide13And water at a temperature of 100-170°C. and a pressure of not more than 5.0 MPa, in the solution of a catalytic system containing a complex compound of palladium and triphenylphosphine h3taken in the ratio range of from 1:2 to 1:100, using as solvent dioxane, or aromatic hydrocarbons - benzene, toluene, xylene or their mixtures with dioxane. The problem is solved also by the fact that the use of giving is giving 13WITH from 0.5 to 1.0 MPa. The problem is solved by using the temperature from 140 to 160°C. The problem is solved also by the fact that use of the catalytic system with a ratio of complex compounds of palladium and triphenylphosphine in the range from 1:10 to 1:40. The task is solved in that the reaction mixture is further added hydrochloric acid. When carrying out the process at temperatures below 140°C, the reaction proceeds slowly, and at temperatures above 160°C breaks down complex compounds of palladium with separation of metallic palladium. At pressures below 0.5 MPa decreases the speed of the process, and when the pressure is higher than 1.0 MPa decreases the selectivity of the process. When the ratio of the complex compound of palladium:triphenylphosphine less than 1:10 decreases the stability of the catalyst, and when the ratio is about 1:40 decreases the speed of the process. The invention is illustrated by the following examples. Example 1 In a stainless steel autoclave with a volume of 200 ml, placed on the table of the magnetic prevented, put 0.07 g PdCl2(PPh3)2, 2,62 g PPh3and 5.7 ml of 1-Heptene, 0,36 ml of N2O. as solvent a mixture consisting of 9.6 ml of o-xylene and 4.7 ml of dioxane. The autoclave is pressurized, vacuum, fill with carbon monoxide13CO and heated on the temperature of 150°C. Then bring pressure to work (0.5 MPa) and constant support during the whole experience. After 3 hours, turn off the stirring and heating, the autoclave is cooled to room temperature and relieve pressure. The autoclave unload and analyzing the reaction mixture by gas chromatography (GC). Chromatographic analysis of the products of the synthesis is performed on a gas chromatograph with a flame ionization detector; use metal column size 3 m×3 mm, filled with Chromaton N-AW-DMCS (0,16-0,20 mm) with 3% H3RHO4soaked in 10% polyethyleneglycoladipinate. As an internal standard using hexadecane. To determine the isotopic purity of the 113With Caprylic acid it is recovered from the reaction mass by vacuum distillation and analyzed by the method of NMR nuclei13With (25°C, the solution in CDCl3). Use the NMR spectrometer AM-360 (Bruker) with an operating frequency of 360 MHz. The selectivity of the reaction by Caprylic acid was 95.5%, while the degree of transformation13WITH close to 100%. The isotopic purity of the target 1-13With Caprylic acid is 99%, and its yield per absorbed13CO - 94.5% of theoretical. During the reaction the catalyst is stable and is not destroyed with the release of metallic palladium. Example 2 The reaction is carried out in the same way as the example 1, however, in the original mixture of 0.02 ml of Hcl conc. and conduct a reaction for 4 hours. The selectivity of the reaction by Caprylic acid were 96.7%. The isotopic purity of the obtained 1-13With-Caprylic acid - 99%, and its output at full conversion13CO - 95,7% of theoretical. The catalyst is not destroyed. Example 3 The reaction is carried out as in example 1, however, the operating pressure of carbon monoxide13WITH is 1.0 MPa. The selectivity of the reaction by Caprylic acid increased by 91.9%. Output 1-13With Caprylic acid per13CO - 90,1% of theoretical, its isotopic purity 98%. In the process, the catalyst is stable. Example 4 The reaction is carried out as in example 1, but in the solvent used to 14.3 ml of dioxane, and conducting the reaction for 6 hours. The selectivity of the reaction by Caprylic acid amounted to 94.5%. The isotopic purity of the obtained 1-13With Caprylic acid is 99%, and its output at full conversion13CO - 93.6% of theoretical. The catalyst is stable and is not destroyed with the release of metallic palladium. Example 5 The reaction is carried out as in example 1, but in the solvent used to 14.3 ml of o-xylene and conducting the reaction for 11.5 hours. The selectivity of the reaction by Caprylic acid was 81.0%. Output 1-13With Aprilovo acid per 13WITH no absorption - 79,4% of theoretical, its isotopic purity 98%. During the reaction the catalyst is stable. Example 6 The reaction is carried out as in example 1, but in the solvent used to 14.3 ml of benzene and conduct a reaction for 8 hours. The selectivity of the reaction by Caprylic acid amounted to 92.2 per cent. The isotopic purity of the obtained 1-13With Caprylic acid is 99%, and its output per13CO - 91,3% of theoretical. The catalyst is stable. Example 7 The reaction is carried out as in example 1, but in the solvent used to 14.3 ml of toluene and conduct a reaction for 5 hours. The selectivity of the reaction by Caprylic acid amounted to 94.8%. Output 1-13With Caprylic acid per13WITH no absorption - 92.9% of theoretical, its isotopic purity 98%. During the reaction the catalyst is stable. Example 8 The reaction is carried out as in example 1, but in the solvent used to 14.3 ml of n-xylene and carry out reaction for 10 hours. The selectivity of the reaction by Caprylic acid was 81,5%. Output 1-13With Caprylic acid per13WITH no absorption - 80.7% of theoretical, its isotopic purity 99%. The catalyst is not destroyed during the process. Example 9 The reaction is carried out in the same way, to the to in example 1, however, as the catalytic system using 0.07 g of the complex PD(SLA)2(h3)2and 1.31 g h3and conduct the reaction at a temperature of 110°C for 4 hours. The selectivity of the reaction by Caprylic acid made 94.0%. The isotopic purity of the obtained 1-13With Caprylic acid is 99%, and its output at full conversion,13CO - 93.1% of from theoretical. The catalyst is stable and is not destroyed with the release of metallic palladium. The advantage of this method is that it allows a single stage, and in a fairly mild conditions (0.3 to 1.0 MPa) to obtain 1-13With Caprylic acid with high isotopic purity of 98-99% is due to the replacement of propionic acid used as a component of the solvent, dioxane, or an aromatic hydrocarbon from a number of: benzene, toluene, xylene, or a mixture of dioxane. The method allows to increase the economic efficiency of the process of obtaining the 113With Caprylic acid by increasing the degree of usage (output) isotopic raw13WITH. Furthermore, the method allows to obtain isotopic diagnostic preparations, not containing dangerous radioactive isotopes. 1. The method of obtaining Caprylic acid with a stable isotope of carbon (1-13C) reaction of hydrocarbonsoluble 1-Heptene with carbon monoxide13 And water at a temperature of 100-170°C. and a pressure of not more than 5 MPa, in the presence of solvent and catalyst system comprising a complex compound of palladium and triphenylphosphine in the value taken from the range from 1:2 to 1:100, characterized in that the solvent used dioxane and/or aromatic hydrocarbon. 2. The method according to claim 1, characterized in that the process is carried out at 140-160°C. 3. The method according to claim 1, characterized in that the process is performed under a pressure of 0.5-1.0 MPa. 4. The method according to claim 1, characterized in that the ratio between the complex compound of palladium and triphenylphosphine taken from the range from 1:10 to 1:40. 5. The method according to claim 1, characterized in that the reaction mixture is further added hydrochloric acid.
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