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1-hydroxyadamantanon-4-one preparation method |
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IPC classes for russian patent 1-hydroxyadamantanon-4-one preparation method (RU 2319688):
The method of producing cycloalkanones c8-c12 / 2154050
The invention relates to the production of cycloalkanones C8-C12promising intermediates in the synthesis of lactams, aliphatic dicarboxylic acids, Daminov - monomers for the production of polyamide fibers, plastics and plasticizers new types and other valuable materials
Method for preparing xanthophyll / 2284992
Invention relates to the improved method for preparing xanthophylls, in particular, to a method for preparing mono- or polyoxidized xanthophylls. Method involves oxidation of carotinoid in a lower oxidation state as compared with xanthophylls to be prepared from hydrogen peroxide aqueous solution and organic solvent wherein indicated solvent represents a water-insoluble solvent. Indicated reaction is carried out in the presence of iodine-containing compound chosen from the group including iodine, iodine halide derivative and metal iodide. Method allows avoiding using danger and expensive substances and formation of large amounts of salts. The proposed invention is used mainly for oxidation of beta-carotene to form canthaxanthine and oxidation of lutein and zeaxanthine wherein the end substances represent important agents used in preparing food compositions and supplements in animal fodder.
Method for production of carbonyl compounds / 2270185
Claimed method includes reaction of nitrous oxide with alkenes in presence of inert gas as diluent. Reaction is carried out in gas phase at 401-700°C and under pressure of 2-300 atm. Target compounds represent value intermediates for precise and base organic synthesis.
A method of obtaining a monocyclic ketones7-c20 / 2227136
The invention relates to a method for producing monocyclic ketones7-C20
The method of producing cyclopentanone / 2227135
The invention relates to a method of producing Cyclopentanone
The method of obtaining substituted monocyclic ketones / 2227134
The invention relates to a method for producing substituted monocyclic ketones4-C20
The method of obtaining carbonyl compounds / 2227133
The invention relates to a method for producing carbonyl compounds with the number of atoms2-C40
A method of producing aldehydes / 2212396
The invention relates to a method for producing an aldehyde intermediate of organic synthesis
Solid acid catalyst, process for its production and its use / 2190465
The invention relates to a solid molded the catalysts are easily separated from the reactants and re-used in the reactions of alkylation, esterification and isomerization
Method for production of carbonyl compounds / 2270185
Claimed method includes reaction of nitrous oxide with alkenes in presence of inert gas as diluent. Reaction is carried out in gas phase at 401-700°C and under pressure of 2-300 atm. Target compounds represent value intermediates for precise and base organic synthesis.
Method for preparing xanthophyll / 2284992
Invention relates to the improved method for preparing xanthophylls, in particular, to a method for preparing mono- or polyoxidized xanthophylls. Method involves oxidation of carotinoid in a lower oxidation state as compared with xanthophylls to be prepared from hydrogen peroxide aqueous solution and organic solvent wherein indicated solvent represents a water-insoluble solvent. Indicated reaction is carried out in the presence of iodine-containing compound chosen from the group including iodine, iodine halide derivative and metal iodide. Method allows avoiding using danger and expensive substances and formation of large amounts of salts. The proposed invention is used mainly for oxidation of beta-carotene to form canthaxanthine and oxidation of lutein and zeaxanthine wherein the end substances represent important agents used in preparing food compositions and supplements in animal fodder.
1-hydroxyadamantanon-4-one preparation method / 2319688
Invention provides a method for preparation of 1-hydroxyadamantanon-4-one (Kemantan), which can be used as immunostimulating drug effective to treat vascular system diseases, limbs autoimmune genesis extremities, tuberculosis, infection-allergic bronchial asthma, chronic aphthous stomatitis, herpes, as well as anticataleptic agent and intermediate for synthesis of 1,4-bifunctional derivatives of adamantane. Method comprises oxidation of adamantanone by means of sulfuric/nitric acid mixture in the form of complex oxidation-activating system including sulfuric, nitric, and acetic acids, molar ratio adamantanone/sulfuric acid/nitric acid/acetic acid being 1: (1.75) : (8.43-12.62) : (0.25-1). Process is carried out when stepwise raising temperature: first, at 35°C, nitric acid is measured out to reaction mass for 1-1.5 h, after which temperature is raised to 50-55°C for 12-16 h.
Method of producing 1-acetyl-4- propionylbenzene / 2374217
Invention relates to a method of producing 1-acetyl-4-propionylbenzene, which is starting material for making medicinal agents and dipyrrolylbenzenes, used in synthesis of conducting interlinked polymer systems, which can be used as electrode materials for energy accumulators, biosensors, photoluminescent materials, electroluminescent materials and electromagnetic shields. The method involves using propionyl chloride and ethylbenzene as starting material in an organic solvent medium, and carrying out the reaction in the presence of anhydrous aluminium chloride at temperature between 25 and 40°C for 20 to 60 minutes, with formation of an intermediate product 1-propionyl-4-ethylbenzene, which is separated and oxidised with potassium permanganate in an aqueous solution of magnesium nitrate at temperature between 65 and 80°C for 3 to 5 hours, forming the desired product which is extracted using toluene, with subsequent recrystallisation from n-hexane or petroleum ether. The method uses non-toxic and readily available components, which makes the proposed method suitable for industrial use.
4,4'-difluorobenzophenone synthesis method / 2394016
Present invention relates to a method for synthesis of 4,4'-difluorobenzophenone, the main raw product for synthesis of aromatic polyester-ketones. The method involves a first step where fluorobenzene reacts with formaldehyde under conditions for catalysis with organic sulphonic acids to form difluorodiphenylmethane. The product is extracted and oxidised with nitric acid at the second step to 4,4'-difluorobenzophenone.
Method of producing acrolein, acrylic acid or mixture thereof from propane / 2429218
According to method A) an input stream of the reaction gaseous mixture A is fed into the input of the first reaction zone A, where the input stream is obtained by merging at least four different gaseous initial streams 1, 2, 3 and 4, where the gaseous initial streams 1 and 2 contain propane, gaseous initial stream 4 is molecular hydrogen and gaseous initial stream 3 is fresh propane, the input stream of the reaction gaseous mixture A is passed at least through one catalyst layer of the first reaction zone A on which, if needed, when feeding other gaseous streams, as a result of heterogeneous catalytic partial dehydrogenation of propane, a stream of products of gaseous mixture A forms, which contains propane and propylene, the stream of products of gaseous mixture A comes out of the first reaction zone A through the corresponding outlet, while splitting said stream into two partial streams 1 and 2 of products of the gaseous mixture A with identical composition, and the partial stream 1 of products of the gaseous mixture A is returned to the first reaction zone A as the gaseous initial stream 1, the partial stream 2 of products of the gaseous mixture A, if needed, is directed to the first separation zone A, in which a portion or more of components contained therein, which are different from propane and propylene, are separated, as a result of which a stream of products of gaseous mixture A' which contains propane and propylene, B) partial stream 2 of products of the gaseous mixture A or a stream of products of gaseous mixture A' is used in a second reaction zone B for supplying at least one oxidation reactor, in which propylene contained in the partial stream 2 of products of gaseous mixture A or in the stream of products of gaseous mixture A' undergoes selective heterogeneously catalysed partial gas-phase oxidation with molecular oxygen to obtain a stream of products of a gaseous mixture B, which contains acrolein, acrylic acid or mixture thereof as the desired product, unconverted propane and, if needed, unconverted propylene, as well as molecular oxygen, the stream of products of gaseous mixture B comes out of reaction zone B, the desired product contained in separation zone B is separated in said separation zone B and at least a portion of residual gas formed after separation and containing unconverted propane, molecular oxygen and, if needed, unconverted propylene, is returned to reaction zone A as gaseous initial stream 2. Gaseous initial streams 2, 3 and 4 as well as, if needed, additional gaseous initial streams different from the gaseous initial stream 1, are merged into a gaseous stream of the working mixture, after which, using this gaseous stream of the working mixture as the working stream, a jet pump is activated, said pump having a nozzle, a mixing section, a diffuser and a suction inlet. Movement of the working stream which is throttled through the nozzle, the mixing section and the diffuser to the input of the first reaction zone A, as well as the suction effect of the suction inlet takes place in the direction of outlet of the stream of products of gaseous mixture A from the first reaction zone A. The pressure drop created in the suction nozzle with splitting of the stream of products of the gaseous mixture A into two partial streams 1 and 2 results in suction of the partial stream 1 of products of the gaseous mixture A, its movement through the diffuser with simultaneous mixture with the working stream on the mixing section and inlet of the formed reaction stream of gaseous mixture A at its inlet point into the first reaction zone A, characterised by that a gaseous initial mixed stream is formed first by merging in random sequence gaseous initial streams 2 and 3, as well as, if needed, additional gaseous initial streams different from gaseous initial streams 1 and 4, and only after that the gaseous initial stream 4 is added to the formed gaseous initial mixed stream to obtain a gaseous mixed working stream.
Method of conducting continuous process of producing acrolein, acrylic acid or mixture thereof from propane in stable operating mode / 2429219
Invention relates to a method of conducting a continuous process of producing acrolein, acrylic acid or mixture thereof from propane in a stable operating mode, according to which: A) propane in a first reaction zone A undergoes heterogeneously catalysed dehydrogenation in the presence of molecular oxygen to obtain a gaseous mixture of products A containing propane and propylene, B) the gaseous mixture of products A, if needed, is fed into a first separation zone A in which a portion or more of components different from propane and propylene is separated therefrom and a gaseous mixture of products A' containing propane and propylene remaining after separation is obtained, C) the gaseous mixture of products A or gaseous mixture of products A' is fed into at least one oxidation reactor of the second reaction zone B, in which propylene contained therein undergoes partial selective heterogeneously catalysed gas-phase oxidation with molecular oxygen to obtain a gaseous mixture of products B, which contains acrolein, acrylic acid or mixture thereof as the desired product, unconverted propane, excess molecular oxygen and, if needed, unconverted propylene, D) in the second separation zone B, the desired product contained therein is separated from the gaseous mixture of products B, and at least a portion of the remaining gas containing propane, molecular oxygen and, if needed, unconverted propylene is returned to the reaction zone A as circulation gas 1 containing molecular oxygen, E) fresh propane is fed into at least one continuous flow process zone selected from a group comprising reaction zone A, separation zone A, reaction zone B and separation zone B, where the said fresh propane is fed at a rate characterised by a given stationary value when realising the process in a stable operating mode, and F) content of molecular oxygen in the gaseous mixture of products B is continuously determined and said value is compared with the desired stationary value needed to realise the process in stable operating mode, characterised by that if at a certain moment in time, content of molecular oxygen in the gaseous mixture of products B exceeds the given desired stationary value, fresh propane is fed into the process right away at feed rate higher than its stationary value, and if at a certain moment in time, content of molecular oxygen in the gaseous mixture of products B is lower than the corresponding given desired stationary value, fresh propane is fed into the process right away at feed rate lower than its stationary value.
Method for direct conversion of lower c1-c4 paraffins to oxygenates / 2485088
Invention relates to a method for direct conversion of lower C1-C4 paraffins to oxygenates such as alcohols and aldehydes, which are valuable intermediate products of organic synthesis and can be used as components of engine fuel and/or starting material for producing synthetic gasoline and other engine fuels. The method involves passing a mixture consisting of a lower paraffin or oxygen, diluted with an inert gas or air or pure oxygen, through a catalyst bed at temperature not higher than 350°C. The catalyst used is a catalyst system for heterogeneous reactions, which contains microfibre of a high-silica support and at least one active element, the active element being in form of either a MeOxHalv composite or a EwMezOxHaly composite, wherein the element Me in both composites is selected from a group which includes transition metals of groups 5-12 and periods 4 and 5, or elements of lanthanum or lanthanide groups or, preferably, ruthenium; element Hal is one of the halogens: fluorine, chlorine, bromine, iodine, but preferably chlorine; element E in the EwMezOxHaly composite is selected from a group which includes alkali, alkali-earth elements, or hydrogen, and indices w, z, x and y are weight fractions of elements in given composites and can vary in the following ranges: z - from 0.12 to 0.80, x - from 0.013 to 0.34, y - from 0.14 to 0.74, w - from 0 to 0.50.
Method of vanillin manufacturing / 2519550
Method consists in air oxygen oxidation of lignin, obtained by fermentative hydrolysis of wood of coniferous species or wood, affected by brown or mottled rot, with content of lignin 40-90 wt % in water-alkali medium at higher temperatures and pressure. The process is carried out in presence of catalysts on the basis of copper hydroxide with continuous supply of alkali solution into reactor for 1-150 minutes.
1-hydroxyadamantanon-4-one preparation method / 2319688
Invention provides a method for preparation of 1-hydroxyadamantanon-4-one (Kemantan), which can be used as immunostimulating drug effective to treat vascular system diseases, limbs autoimmune genesis extremities, tuberculosis, infection-allergic bronchial asthma, chronic aphthous stomatitis, herpes, as well as anticataleptic agent and intermediate for synthesis of 1,4-bifunctional derivatives of adamantane. Method comprises oxidation of adamantanone by means of sulfuric/nitric acid mixture in the form of complex oxidation-activating system including sulfuric, nitric, and acetic acids, molar ratio adamantanone/sulfuric acid/nitric acid/acetic acid being 1: (1.75) : (8.43-12.62) : (0.25-1). Process is carried out when stepwise raising temperature: first, at 35°C, nitric acid is measured out to reaction mass for 1-1.5 h, after which temperature is raised to 50-55°C for 12-16 h.
Method of obtaining 1-hydroxyadamanthan-4-on / 2342358
Claimed invention relates to method of obtaining 1-hydroxyadamanthan-4-on, which is immuno-stimulating means, efficient for treatment of limbs vascular system diseases of autoimmune genesis, chronic stomatitis, herpes, etc. Method lies in catalytic oxidation of adamanthon-2. Here as oxidant agent, hydrobromous acid is used, which is generated in situ from carbon tetrabromide and water, and oxidation is performed in presence of catalysts - compounds of molybdenum Mo(CO)6 or tungsten W(CO)6, with molar ratio[Mo(CO)6 or W(CO)6]: [adamanthon-2]:[CBr4]:[H2O]=1:100:100:1000-4000 at temperature 140-160°C during 6-10 hours.
Method of producing 1-hydroxyadamantan-4-one / 2491270
Present invention relates to a method of producing 1-hydroxyadamantan-4-one, having immunostimulating action. The method involves oxidising adamantane with a mixture of CCl4, water and an amide of propionic acid in the presence of a tungsten catalyst - W(CO)6 for 6 hours at 150°C with molar ratio [W]:[AdH]:[CCl4]:[CH3CH2CONH2]:[H2O] - 1:20:100:100:1000.
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FIELD: organic synthesis and pharmaceutical industry. SUBSTANCE: invention provides a method for preparation of 1-hydroxyadamantanon-4-one (Kemantan), which can be used as immunostimulating drug effective to treat vascular system diseases, limbs autoimmune genesis extremities, tuberculosis, infection-allergic bronchial asthma, chronic aphthous stomatitis, herpes, as well as anticataleptic agent and intermediate for synthesis of 1,4-bifunctional derivatives of adamantane. Method comprises oxidation of adamantanone by means of sulfuric/nitric acid mixture in the form of complex oxidation-activating system including sulfuric, nitric, and acetic acids, molar ratio adamantanone/sulfuric acid/nitric acid/acetic acid being 1: (1.75) : (8.43-12.62) : (0.25-1). Process is carried out when stepwise raising temperature: first, at 35°C, nitric acid is measured out to reaction mass for 1-1.5 h, after which temperature is raised to 50-55°C for 12-16 h. EFFECT: increased yield of 1-hydroxyadamantanon-4-one and improved its purity. 7 ex
The invention relates to pharmaceutical industry and relates to a method of obtaining a 1-hydroxyadamantane-4-it (Kelantan) - immunostimulating agent, effective in the treatment of diseases of the vascular system, limbs autoimmune dysfunction, chronic bronchitis, tuberculosis, infectious-allergic bronchial asthma, chronic aphthous stomatitis, herpes, and is also used as anticatholicism means and intermediate for the synthesis of 1,4-bifunctional substituted adamantane. There are several ways to obtain 1-hydroxyadamantane-4-it, including the oxidation of 2-hydroxyadamantane 70%sulfuric acid, followed by repeated extraction of the mixture of oxidation products and the additional oxidation of the obtained mixtures with chromic anhydride [H.W.Geluk, Tetrahedron, 24, s-5377, 1968]. The disadvantage is the low yield of the target product. The output in this case 1-hydroxyadamantane-4-it is not more than 25%. In other ways the target product obtained by oxidation of adamantanone with chromic anhydride in acetic, propionic or triperoxonane acids [CS, patent No. 163671, CL SS 49/38, 1976], or by oxidation of adamantanone 12-fold excess of nitric acid [H.W.Geluk, Tetrahedron, 24, s-5368, 1968]. The disadvantages of these methods are low yields of final product, using large is icesta oxidants, fire explosive reagents. The oxidation of adamantanone nitric acid, as shown by Helucom [H.W.Geluk, Tetrahedron Letters, No. 47, C-4476, 1971], form rather stable complexes with oxygen-containing adamantane derivatives with nitric acid. In terms of the allocation of product on the way, they are not completely decomposed, and getting rid of their impurities by crystallization also fails. There is also known a method hydroxylation derivatives of adamantanone by a mixture of nitric and sulfuric acids in the presence of catalysts (sodium nitrite, manganese dioxide). The reaction is carried out mainly at 35°C, the reaction product is extracted with chloroform and allocate it after evaporation of the solvent [RU NO. 2104994 SS 49/487, 1998.02.20]. The disadvantage of this method of synthesis is the use of a considerable excess of 67.7%nitric acid of 3.46 mol, a 94.6%sulfuric acid - representing 22.06 mole and 0,8125 mol of sodium nitrate (as catalyst) on 1 mol of adamantanone and relatively low output Kelantan - 72%. The closest analogue is the way hydroxylation derivatives aminoadamantana and oxidation of adamantanone by a mixture of nitric and sulfuric acids [SU inventor's certificate No. 974757, SS 49/24, SS 45/00, 1995.09.27]. The reaction is carried out mainly at 20°C. the Reaction mass by this method, after dilution with water, n is italist 40%sodium hydroxide solution, extracted with chloroform and isolated product after evaporation of the solvent. The disadvantage of this method is the low productivity due to low response speed, and complex instrumentation process due to the formation in the form of a precipitate of a large number of salts after alkalizing, which complicates the extraction of the target product. The technical result of our proposed method is to develop a technologically advanced method of producing 1-hydroxyadamantane-4-it is with high yield and purity. The technical result is achieved by oxidation of adamantanone using a mixture of sulfuric and nitric acids, with use of the complex oxidation-activating system, including sulfuric, nitric, acetic acid at a molar ratio:adamantane:nitric acid:sulfuric acid:acetic acid 1:1,75-2:8,43-12,62:0.25-1, and the process is carried out at step increase in temperature, first at 35°With metered into the reaction mass nitric acid for a period of 1-1 .5 hours, then increase the temperature to 50-55°and within 12-16 hours. To reduce the amount of acidic waste and improving the selectivity of the oxidation process to a known system containing nitric and sulfuric acid (used for Kelantan) proposed to add acetic acid, The speed and selectivity of the process can increase due to an improved homogenization of the reaction mixture and education "softer" oxidative particles of nitrone-cation solvated mixture of acetic and sulfuric acids. This results in improved yield and purity of the target product, improves the manufacturability of the process. Conducting the reaction in a stepwise temperature increases initially at a temperature of 35°justified by the fact that when adding nitric acid 15-30 minutes, it begins to leak response education adamantoise cation (exothermic reaction) in this regard, it is necessary to control the temperature of the speed of the dosing acid within 1-1 .5 hours. The choice of temperature range due to the fact that at the reaction temperature below 50°there is incomplete conversion of adamantanone and decreases the yield of the target product, and when the temperature rises above 55°there is also a decrease of the output 1-hydroxyadamantane-4-it from leaking further oxidation leading to the formation of trudnosgoraemyh products. The optimal duration of the reaction is 12-16 hours. Decrease or increase the length reduces the yield of the target product. When using acetic acid in a molar ratio of less than 0.25 to 1 mol of adamantanone n is observed a significant reduction in the degree of conversion source adamantanone. When the ratio of acetic acid above equimolar also observed a decrease in output due to the difficulty of the selection of the target product. When studying the effect of the content of nitric acid in the reaction mass to the output of Kelantan we have found that when using a molar ratio adamantane:nitric acid less than 1:1,75 observed a significant reduction of the yield of the target product and increase the duration of the process. The discovered patterns can be explained by the fact that the oxidation of adamantanone nitric acid, as shown by Helucom [H.W.Geluk, Tetrahedron Letters, No. 47, C-4476, 1971], form rather stable complexes with oxygen-containing adamantane derivatives with nitric acid in a molar ratio of 1:1. With increasing molar ratio adamantane:nitric acid above 1:2 there was a decrease of the yield of the desired product due to the formation of side products pereokislenie of adamantanone, soluble in water. When studying the effect of the content of sulfuric acid in the reaction mass on the yield of the target product, we have found that using a molar ratio adamantane:sulfuric acid is less than 1:8,43 reduces the yield of the desired product due to the reduction of the pH and the increase of this ratio above 1:br12.62 also p is nijaat yield of the target product, because excessive acidity of the environment leads to peroxidation of the source reagent. The novelty of the invention lies in the fact that they use a complex oxidation-activating system containing nitric, sulfuric, acetic acid. Due to this it is possible to increase the selectivity of the process due to an improved homogenization of the reaction mixture and education "softer" oxidative particles of nitrone-cation solvated mixture of acetic and sulfuric acids. This results in improved yield and purity of the target product, improves the manufacturability of the process. The method is implemented as follows. To a solution of sulfuric acid or acetic acid is added gradually adamantane and maintaining the temperature not above 35°C, was added dropwise nitric acid for 1-1,5 hours. After adding all of nitric acid, the temperature of the reaction mass was raised to 50-55°C. Maintain the reaction mass in 12-16 hours, then poured on to ice, filtered off unreacted adamantane, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°C to stop the allocation of nitrogen oxides within 2-4 hours. Weakly acidic reaction mass (pH 5-6) is filtered and then the filtrate is extracted Kelantan with methylene chloride. The solvent is evaporated and get the target product output 65-87,4%. Example 1. the solution in the 95.8 ml (1,80 mole) of 94.6%sulfuric acid and 4.6 ml (range : 0.08 mole) of acetic acid is gradually added 24 g (0,16 mol) of adamantanone and maintaining the temperature not above 35°C, was added dropwise within 1-1 .5 hours 19,0 ml (0,28 mol) 66,2%nitric acid. After adding all of nitric acid, the temperature of the reaction mass was raised to 50-55°C, incubated for 12 hours, poured onto 200 g of ice, filtered 1.2 g of adamantanone, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°before the termination of the allocation of nitrogen oxides (2-4 hours), extracted with 3 times 100 ml of methylene chloride, the solvent evaporated and get 22,3 g Kelantan, the yield of 84.0%, TPL 318-320°C (recrystallized from CCl4). The purity of Kelantan 98,3-99,0% (according to GC). The molar ratio of reagents:adamantane:nitric acid:sulfuric acid:acetic acid: 1:1,75:11,25:0,5. Example 2. To the solution of the 95.8 ml (1,80 mole) of 94.6%sulfuric acid and 2.3 ml (0.04 mol) of acetic acid is gradually added 24 g (0,16 mol) of adamantanone and maintaining the temperature not above 35°C, was added dropwise within 1-1 .5 hours 19,0 ml (0,28 mol) 66,2%nitric acid. After adding all of nitric acid, the temperature of the reaction mass was raised to 50-55°C, incubated for 12 hours, poured onto 200 g of ice, filtered 4,2 g adamantanone, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°before the termination of the allocation of nitrogen oxides (2-4 hours), extracted with 3 times 100 ml METI what inflorida, the solvent is evaporated and get a 20.2 g Kelantan, output 76,1%, TPL 318-320°C (recrystallized from CCl4). The purity of Kelantan 97,3-98,0% (according to GC). The molar ratio of the reagents adamantane:nitric acid:sulfuric acid:acetic acid 1:1,75:11,25:0,25. Example 3. To the solution of the 95.8 ml (1,80 mole) of 94.6%sulfuric acid 8,76 ml (0,16 mol) of acetic acid is gradually added 24 g (0,16 mol) of adamantanone and maintaining the temperature not above 35°C, was added dropwise within 1-1 .5 hours 19,0 ml (0,28 mol) 66,2%nitric acid. After adding all of nitric acid, the temperature of the reaction mass was raised to 50-55°C, incubated for 12 hours, poured onto 200 g of ice, filtered off 0.8 g of adamantanone, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°before the termination of the allocation of nitrogen oxides (2-4 hours), extracted with 3 times 100 ml of methylene chloride, the solvent evaporated and get 22,4 g Kelantan, the yield of 84.3%, TPL 318-320°C (recrystallized from CCl4). The purity of 98.3-99,0% (according to GC). The molar ratio of reagents:adamantane:nitric acid:sulfuric acid:acetic acid: 1:1,75:11,25:1. Example 4. To the solution in 72 ml of 1.35 mol) of 94.6%sulfuric acid and 4.6 ml (range : 0.08 mole) of acetic acid is gradually added 24 g (0,16 mol) of adamantanone and maintaining the temperature not above 35°C, was added dropwise during the course the e 1-1,5 hours 19,0 ml (0,28 mol) 66,2%nitric acid. After adding all of nitric acid, the temperature of the reaction mass was raised to 50-55°C, maintain the reaction mass 12 hours, poured onto 200 g of ice, filtered 5,4 g of adamantanone, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°before the termination of the allocation of nitrogen oxides (2-4 hours), extracted with 3 times 100 ml of methylene chloride, the solvent evaporated and obtain 17.3 g of Kelantan, the output of 65.1%, TPL 318-320°C (recrystallized from CCl4). The purity of Kelantan 98,3% (according to GC). The molar ratio of reagents:adamantane:nitric acid:sulfuric acid:acetic acid 1:1,75:8,43:0,5. Example 5. To a solution of 107 ml (2,02 mole) of 94.6%sulfuric acid and 4.6 ml (range : 0.08 mole) of acetic acid are added gradually, 24 g (0,16 mol) of adamantanone and maintaining the temperature not above 35°C, was added dropwise within 1-1 .5 hours 19,0 ml (0,28 mol) 66,2%nitric acid. After adding all of nitric acid, the temperature of the reaction mass was raised to 50-55°C, incubated for 12 hours, poured onto 200 g of ice, filtered off 0.8 g of adamantanone, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°before the termination of the allocation of nitrogen oxides (2-4 hours), extracted with 3 times 100 ml of methylene chloride, the solvent evaporated and get 23,2 g Kelantan, the output of which is 87.4%, TPL 318-320° (paracrystalline the see of CCl 4). The purity of Kelantan 98,7% (according to GC). The molar ratio of the reagents adamantane:nitric acid:sulfuric acid:acetic acid 1:1,75: 12,62:0,5. Example 6. To the solution of the 95.8 ml (1,80 mole) of 94.6%sulfuric acid and 4.6 ml (range : 0.08 mole) of acetic acid are added gradually, 24 g (0,16 mol) of adamantanone and maintaining the temperature not above 35°C, was added dropwise within 1-1 .5 hours of 21.7 ml of 0.32 mol) 66,2%nitric acid. After adding all of nitric acid, the temperature of the reaction mass was raised to 50-55°C, incubated for 12 hours, poured onto 200 g of ice, filtered off 1.0 g of adamantanone, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°before the termination of the allocation of nitrogen oxides (2-4 hours), extracted with 3 times 100 ml of methylene chloride, the solvent evaporated and get 21 g of Kelantan, output 79,1%, TPL 318-320°C (recrystallized from CCl4). The purity of 98.3-99,0% (according to GC). The molar ratio of reagents:adamantane:nitric acid:sulfuric acid:acetic acid 1:2:11,25:0,5. Example 7. To the solution of the 95.8 ml (1,80 mole) of 94.6%sulfuric acid and 4.6 ml (range : 0.08 mole) of acetic acid are added gradually, 24 g (0,16 mol) of adamantanone and maintaining the temperature not above 35°C, was added dropwise within 1-1 .5 hours 19,0 ml (0,28 mol) 66,2%nitric acid. After adding all of nitric acid, the temperature of reaction the th mass raised to 50-55° C, maintain the reaction mass 16 hours, poured onto 200 g of ice, filtered off 0.8 g of adamantanone, the filtrate is neutralized with sodium hydroxide, keeping the temperature 50-55°before the termination of the allocation of nitrogen oxides (2-4 hours), extracted with 3 times 100 ml of methylene chloride, the solvent evaporated and get 22,9 g Kelantan, the yield of 86.2 per cent, TPL 318-320°C (recrystallized from CCl4). The purity of Kelantan 98,3-99,0% (according to GC). Molar ratio of reactants:adamantane:nitric acid:sulfuric acid:acetic acid 1:1,75:11,25:0,5. Conclusions: Thus, the developed technological method of synthesis of 1-hydroxyadamantane-4-it, which makes it possible to reduce the consumption of sulfuric acid at 45% and increase the yield of the target product from 72 to 87.4 per cent compared with the prototype. A method of obtaining a 1-hydroxyadamantane-4-she oxidation of adamantanone using a mixture of sulfuric and nitric acids, characterized in that use complex oxidation-activating system consisting of sulphuric, nitric and acetic acid at a molar ratio adamantane: nitric acid: sulfuric acid: acetic acid equal to 1:1,75-2:8,43-12,62:0,25-1, moreover, the process is carried out at step increase in temperature, first at 35°With metered into the reaction mass nitric acid for a period of 1-1 .5 hours, then increase the temperature to 50-55°during the 12-6 o'clock
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