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The way to get calcium acetate |
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IPC classes for russian patent The way to get calcium acetate (RU 2156757):
The method of obtaining crystalline sodium acetate from waste products chemical products / 2024486
The invention relates to waste disposal and the simultaneous achievement of commercial products and can be used in other industries where liquid wastes with a content of acetic acid
Salt-(4-hydroxy-3,5-di-tert-butylphenyl)-propionic acid as stabilizers of pvc and method of production thereof / 2150463
The invention relates to ORGANOMETALLIC chemistry, namely to new connections, particularly to salts (4-hydroxy-3,5-di-tert-butylphenyl)-propionic acid of General formula
< / BR> where R = C(CH3)3, Me is a metal selected from the group of Zn, Ba, Ca, Cd, Al, Sn, Mg, Cr+3, Mn+2, n is the valence of the metal, n = 2 to 4, which can find use as a stabilizer for polymers and additives to oils
The method of production of synthetic drying oils on the basis of naphthenic acids / 2145594
The invention relates to the production of paint and varnish materials, namely, synthetic drying oils on the basis of naphthenic acids
The method of obtaining 2-ethylhexanoate metals / 2137751
The invention relates to the field of synthesis of organic metal salts, such as 2-ethylhexanoate metals, which are used in the production of polymeric materials, stabilizers and modifiers, allowing you to modify the rheological properties of polymer materials, and also as additives to paints, varnishes, lubricants and raw materials for thin film deposition of complex oxides
The allocation method fluorinated carboxylic acid / 2131408
The invention relates to a method for allocation of fluorinated carboxylic acids, allowing you to get them with a high degree of purity
Salts of alkaline earth metals, salts of transition metals or transition metal complexes ketocarboxylic acids, method for their preparation and composition for coating and method for the protection of the corroding metal substrate / 2130010
The method of obtaining 2-ethylhexanoate metals / 2127250
The invention relates to the field of electrochemical synthesis of organic compounds, in particular 2-ethylhexanoate metals that are used in the manufacture of polymeric materials as stabilizers and modifiers
The method of obtaining aluminium derivatives of salicylic and acetylsalicylic acids / 2124498
The invention relates to the field of pharmacy, the synthesis of salts of polyvalent metals with salicylic and acetylsalicylic acids and can be used to obtain practical pharmacopoeial forms of salicylates aluminum in pharmaceutical laboratories
The method of obtaining calcium stearate / 2124495
The invention relates to petrochemical synthesis, namely the method of obtaining calcium stearate used as a stabilizer for polyvinyl chloride, and also in the manufacture of varnishes, surface-active compounds that are used as flotation agents
The method of obtaining the sodium salt of monochloracetic acid / 2109006
The invention relates to the field of technology organochlorine compounds, and in particular to a method for producing sodium salt of monochloracetic acid used in the production of monochloracetic acid used in the production of sodium salt of carboxymethyl cellulose, dyes, herbicides, vitamins b6and medicines
The method of producing rare earth oxalates or transplutonium elements / 2089538
The invention relates to radiochemical technology and can be used in technologies for radionuclides and rare earth transplutonium elements and manufacturing, as well as in preparative inorganic and analytical chemistry
Preparation comprising water-soluble triterpenic acid salts and method for its preparing / 2244426
Invention relates to a method for preparing the preparation comprising triterpenic acid water-soluble salts and additionally added protein-containing product and vegetable raw, the source of triterpenic acids taken in the following ratio of components, wt.-%: protein-containing product, 10-17; triterpenic acid sodium salts, 4-5, and vegetable raw, the balance. Method involves mixing triterpenic acid-containing vegetable raw with the protein-containing product taken in the ratio = (9-11):(1-2), mechanical-chemical treatment of this mixture in activator device, mixing of prepared semi-finished product with sodium carbonate or sodium hydrocarbonate taken in the ratio = (92-97):(3.5-8.3) and repeated treatment in the activator device. Method involves applying flow-type ball vibration-centrifugal or ellipse-centrifugal mills as the activator device that provide the acceleration of milling bodies up to 170-250 m/c2 and time for treatment for 1.5-3 min. Invention provides simplifying the process and the complex processing waste in lumber industry.
Method for preparing copper (ii) acetate monohydrate / 2246480
Invention relates to a method for preparing copper (II) acetate monohydrate that represents organic carboxylic acid salt. Copper (II) acetate monohydrate is prepared by crystallization from solution obtained by mixing acetic acid, alkaline metal acetates or ammonium with copper-containing spent solution used in etching printing boards. Method provides reducing cost of the proposed method for preparing copper (II) acetate monohydrate, retaining purity of product with simultaneous utilization of toxic waste in electronic engineering manufacture - the spent solution in etching printing boards. Also, invention provides reducing material consumptions in preparing copper (II) acetate monohydrate, expanding assortment of materials used for its preparing and utilization of toxic waste in electronic engineering manufacture. Product obtained by the proposed method can be used as pigment, fungicide and copper microfertilizer in agriculture, as catalyst in processes of polymerization, as a stabilizing agent of artificial fibers, for preparing galvanic solutions and preparing other copper compounds.
Method for preparing nickel oxalate / 2256647
Invention relates to the improved method for preparing nickel oxalate that can be used in preparing catalysts, ceramic materials and in manufacturing electric vacuum devices. Method involves preparing the reaction solution containing nickel (II) and oxalate, crystallization of product, separation of precipitate from solution and its drying. The reaction solution is prepared by mixing reagent as source of oxalate and spent solution from chemical nickel plating taken in the amount providing the mole ratio in the reaction solution nickel (II) : oxalate = 1.0:(0.8-2.8). Spent solution of chemical nickel plating contains as main components nickel (II), ligand for nickel (II), reducing agent and product of its oxidation. As spent solution of chemical nickel plating method involves using solution containing nickel (II), ligand for nickel (II), hypophosphite, phosphite as main components and pH value in the reaction solution is brought about from 2.5 to 7.5. As spent solution of chemical nickel plating method involves using solution containing nickel (II) and ligand for nickel (II) as main components. As a reducing agent method involves using substance taken among the group including hydrazine, borohydride, hydrazine borane, alkylaminoborane, dithionite, hydroxymethyl sulfinate, thiourea dioxide, product of reducing agent oxidation and pH value in the reaction solution is brought about 0.0 to 8.5. Invention provides reducing material consumptions for preparing nickel oxalate, expanded assortment of materials used for preparing nickel oxalate, utilization of manufacture waste, reduced cost of product and simultaneous utilization of the spent solution of chemical nickel plating representing toxic waste of manufacturing.
Method for preparing copper (ii) salts with dicarboxylic acids / 2256648
Copper (II) salts with dicarboxylic acids are prepared by crystallization from reaction aqueous solution obtained by mixing reagent as source of dicarboxylic acid anion and waste from radio-electronic manufacturing - spent solution in etching printed boards. Solutions containing copper (II), ammonia or mineral acid, ammonium salts and other substances are used as the spent solution in etching printed boards. Dicarboxylic acid, dicarboxylic acid anhydride, dicarboxylic acid salt with sodium, potassium, ammonium or aqueous solutions of these substances are used as reagent representing the source of dicarboxylic acid anion. Prepared copper (II) salts can be used in manufacturing high-temperature superconductors, as fungicides and copper microfertilizers in agriculture, medicinal agents in veterinary science, for antibacterial treatment of water and in other fields. Invention provides reducing cost of products, retention of their purity, utilization of waste in radio-electronic manufacturing (spent solution in etching printed boards of different composite).
Method of production of zinc oxalate dihydrate / 2259347
Product obtained by this method may be used as pigment for production of catalysts of synthesis of inorganic and organic substances, manufacture of ceramic articles and production of oxide and other compounds of zinc. Proposed method includes preparation of reaction solution containing zinc (II) and oxalate, crystallization of target product, separation of sediment from solution and drying the sediment; reaction solution is prepared by mixing the solution of zinc plating process and oxalate-containing reagent; use is made of used solution of zinc plating process and reaction solution containing zinc (II) and oxalate at mole ratio of 1.0: (0.8-3.0) is prepared.
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.
Preparing aromatic carboxylic acid ammonium salts / 2272805
Invention relates to the improved method for preparing aromatic carboxylic acid ammonium salts by reaction of aromatic carboxylic acid with ammonia in aprotonic solvent medium. Method involves carrying out the reaction in the closed vessel by continuous addition of aromatic carboxylic acid in aprotonic solvent medium and passing gaseous ammonia under condition providing maintenance of ammonia partial pressure in the range from 0.1 to 3 bars and elimination of ammonium salt suspension in aprotonic solvent. Method allows preparing ammonium salts as crystals of a definite size that exhibit narrow distribution by size.
Method for preparing neodymium organic salts (variants) / 2278107
Invention relates to the improved methods (variants) for preparing salts formed by neodymium and organic acids that are used as components on preparing metal-chelating catalysts. Method for preparing neodymium organic salts from neodymium oxide and carboxylic acid involves conversion of neodymium oxide to a water-soluble salt by heating at temperature 50-150°C with inorganic ammonium salt aqueous solution with simultaneous distillation of water and ammonia. Then carboxylic acid is converted to water-soluble ammonium salt by mixing with distilled ammonia and water. In mixing prepared aqueous solutions of inorganic neodymium salt with organic ammonium salt the neodymium organic salt and inorganic ammonium salt aqueous solution are prepared. After isolation of the end neodymium organic salt an aqueous solution of ammonium inorganic salt is recirculated to the process. Method for preparing neodymium organic salts from neodymium oxide and carboxylic acids (variant) involves conversion of neodymium oxide to water-soluble inorganic salt by heating at temperature 50-150°C with inorganic ammonium salt aqueous solution and with simultaneous distillation of water and ammonia. Then carboxylic acid and hydrocarbon solvent are added to neodymium inorganic salt aqueous solution followed by addition of distilled ammonia at intensive stirring. After ceasing the stirring the reaction mixture if separated for aqueous and organic layers. Aqueous layer representing inorganic ammonium salt solution is recirculated to the process and the end product is isolated from an organic layer representing neodymium organic salt solution in hydrocarbon solvent, or solution of the definite concentration is prepared. Proposed methods (variants) provides excluding consumption of additional reagents and creates conditions for wasteless production of neodymium organic salts from neodymium oxide and organic acids.
Method of extraction of copper (ii) from waste printed circuit board pickling solutions / 2287595
Cleaning is performed by adding to waste solution reagent containing monocarbonic acid of aromatic series or its salt, or anhydride at subsequent forming of sediment of salt of copper (II) with anion of monocarbonic acid of aromatic series.
Method for preparing rare-earth element carboxylates / 2288213
Invention relates to the improved method for synthesis of rare-earth element carboxylates. Method involves interaction of rare-earth element oxide or oxides with carboxylic acid or mixture of carboxylic acids at increased temperature in the presence of rare-earth element salt or mixture of rare-earth elements wherein the mole ratio rare-earth element salt or mixture of rare-earth element salts : rare-earth element oxide or rare-earth element oxides is maintained as = 1:(20-150). The end substances can be used as catalysts used in polymerization of coupled dienes based on rare-earth element carboxylates and can be used in synthesis of cis-1,4-homopolymers and cis-1,4-copolymers in industry of synthetic rubbers. Method shows the simplified technology and improved ecology.
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(57) Abstract: The invention relates to the production of salts of acetic acid. Calcium acetate is produced by processing the oxide, hydroxide, carbonate or mixtures thereof 52-65% acetic acid with the stoichiometric ratio of the starting components with subsequent crystallization and drying of the product. The crystallization is carried out by exposure of the product for at least 16 h, and drying is carried out at 80-100°C. as a result, the output acetate calcium rises to 88-96%, and thus attain a high degree of purity of the product. 1 C.p. f-crystals, 1 table. The invention relates to methods of producing salts of acetic acid, in particular calcium acetate. A method of obtaining calcium acetate, which consists in the interaction of calcium carbonate with acetic acid under heating, followed by filtration of the solution and evaporation of the filtrate under constant acidification. After cooling of the filtrate precipitated crystals of calcium acetate is separated in a Buechner funnel and dried at 60-70oC. the Yield of the target product is 53% of the stoichiometric value, purity approximately 100% (Karyakin Y. I., Angels, I. I., Pure substances, M, Chemistry, 1974, S. 153). The implementation of this method is rather complicated and energy-intensive. Implementation (development) of this method in large-tonnage production is impractical for several reasons. The main disadvantages of the method of crystallization of calcium acetate from dilute solutions the following:1) low yield of hydrated calcium acetate because of its high solubility in water (~ 30%); 2) separation of the crystals on the filter; 3) the presence of leachate with a high content of dissolved calcium acetate; 4) the problem of determination of calcium acetate from a solution of the filtrate (by evaporation), 5) processing and recycling of the liquid phase (filtrate). All of the above problems are removed, if the reaction is carried out in solid phase. A method of obtaining acetate calcium-magnesium interaction dolomite with glacial acetic acid. This method is chosen by the applicant for the prototype (Application Germany 3705618, C 07 C 53/10, 1988). The method consists in the following. The oxides or hydroxides of calcium and magnesium (calcined dolomite and/or limestone, respectively hydrated) is treated with a slight excess (2-10% better 5% relative to the stoichiometric amount) 85-100% acetic acid, the reaction is carried out in the mixer G is removed at a temperature of 110-160oC in the dryer with a movable layer of the substance. The purity of the finished product is ~ 70% of the content of soluble impurities ~ 30%. This method is quite technologically advanced, since the reaction is carried out in the solid phase. However, the final product is of low purity (low content of basic substance) as the excess of acetic acid leads to the formation of acid salts. In addition, used in the known method, the amount of acetic acid (relative to the amount of dolomite), and the duration of mixing dolomite with acetic acid do not provide the full completion of the neutralization of acetic acid with dolomite, because in these conditions the reaction proceeds only on the surface of solid particles, and the acid diffusion inside the particles is difficult because of the formation of calcium acetate on their surface. As a consequence, the final product is a mixture of acetate calcium-magnesium (~ 70%) and unreacted hydroxides to oxides of calcium-magnesium, as evidenced by the presence of insoluble impurities in the target product. The finished product has a technical purpose, it is used for mixing, lowering the freezing point of water. Such conditions of synthesis of acetate calcium help to improve the purity of the final product, because they ensure full reaction of interaction of calcium compounds with acetic acid. However, the processing of calcium compounds acetic acid in a selected ratio leads to the formation of the intermediate product, containing no liquid phase, which allows the process without filtering. The concentration of acetic acid 52-65% is optimal for the reaction without filtering, because the concentrations of acetic acid below 52% is obtained liquid paste, which should be filtered with the mission of the Department of solid crystals of calcium acetate from a solution containing 25-30% of dissolved calcium acetate. When the acetic acid concentration is above 65% obreshetochnye, as the reaction proceeds on the surface of solid particles, and the acid diffusion inside the particles is difficult because of the resulting acetate on their surface, resulting in the final product is a mixture of acetate calcium source calcium compound. When dissolved in water this product is insoluble residue CaO, Ca(OH)2or GaCO3. When the concentration of the acid 52-65% and the stoichiometric ratio of the starting components is formed a thick paste that does not contain an excess of the liquid phase. When the shutter product synthesis to drying for at least 16 h in a reaction vessel formed of white needle crystals of calcium acetate, soluble in water. Reducing the exposure time does not allow for the neutralization reaction to the end, as evidenced by the decrease in purity of acetate calcium and the presence of impurities of the source of calcium (Ca(OH)2, CaO, CaCO3) in the finished product. Extract product is much more than 16 hours (according to experimental data up to 1.5 months in a closed container) does not affect its quality. The way in experienced production as follows: to a reactor filled stoichiometric quantity of a solution of acetic acid and poured slowly the source connection of the th portions, with stirring, poured a calcium compound within 15-30 minutes and add the remaining amount of acetic acid, cooled the reaction mass to room temperature, the semi-product is left in the reactor or unload in a plastic container and incubated at room temperature in closed containers for at least 16 hours during this time, the formation of crystals of calcium acetate. Wet acetate is dried at a temperature of 80-100oC and atmospheric pressure for 4-5 hours Drying is possible at temperatures below 80oC, however, at the same time, dehydration increases in 2-3 times. Drying at temperatures above 100oC is impractical, because there is a decomposition of calcium acetate calcium oxide and acetone. Example 1. Synthesis of CaO The synthesis is carried out in the mixer brand CM-25 of 25 liters, equipped with a jacket for cooling water and two Z - shaped agitators. Calcium oxide by weight of 4.5 kg is weighed on a dial scale. Measure 16.5 l a 55% aqueous solution of acetic acid. From this amount is poured into the mixer 8.5 l, serves cooling water in the jacket of the mixer includes a mixer and small portions sprinkled 4.5 kg CaO for 25-30 minutes the Reaction proceeds with pratury 40-50oC poured the remaining acetic acid 8,0 l When the temperature reached in the reaction mass 25oC, the finished product is unloaded in the intermediate tank with a volume of 30-50 l, cover with a lid and incubated at atmospheric pressure and room temperature for 16 hours Example 2. Synthesis of Ca(OH)2< / BR> For synthesis take 6,0 kg Ca(OH)2and 16.7 l a 55% aqueous solution of acetic acid. Synthesis is carried out as in example 1. Example 3. Synthesis of CaCO3< / BR> For synthesis take 6,0 kg CaCO3and 12.4 l a 55% aqueous solution of acetic acid. Synthesis is carried out as in example 1. Example 4. Synthesis of acetate from a mixture of calcium oxide, hydroxide and calcium carbonate carried out as in example 1, with the necessary volume of 50% acetic acid are calculated according to the formula V.acid =aCaO3,67+BCa(OH)22,78+CCaCO3to 2.06< / BR> whereaCaO,BCa(OH)2,CCaCO3- mass fraction of the components CaO, Ca(OH)2and CaCO3respectively; V.acid - volume acetic acid. For example, for the synthesis of take 6 kg of mixture (2 kg CaO, Ca(OH)2and CaCO3and V. acid =2kgCaO3,67+2kgCa(OH)2and the qualitative characteristics of the target product are presented in table where in examples 1-11 shows the data related to the claimed invention. Examples N 12-23 shown for comparison and contain data about the synthesis conditions outside the declare. The table below shows results show the following: 1. Purity offered by way of acetate calcium is 100,1-101,4%, which is considerably higher than by a known method. The yield is from 88.1 to 96.4% 2. When using acetic acid above the stoichiometric ratio is formed sour salt (examples 12-14), which reduces the purity of the product; 3. If the shutter speed is wet acetate less than 16 h recrystallization of the product does not pass to the end and when dissolved in water dry acetate there insoluble impurity source of calcium, in this case, the removed product purity and yield (examples 15-17); 4. With increasing acetic acid concentration is above 65%, the reaction in the solid phase does not pass until the end and when dissolved in water dry acetate is also available insoluble impurity source of calcium, in this case decreases the purity of the product and output (examples 18-20); 5. Increasing drying temperature of more than 100oC reduces BP is LASS="ptx2"> Literature
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