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Method to produce polyacrylamide hydrogel |
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IPC classes for russian patent Method to produce polyacrylamide hydrogel (RU 2493173):
Polymerisation of isoolefin with polymorphogenates regulated with respect to polydispersity / 2491299
Invention relates to method of polymerisation of monomers with obtaining isoolefin polymers and copolymers, polymerisation system for polymerisation of such monomers, catalytic system for carbocationic polymerisation of isoolefins, isoolefin polymer or copolymer, obtained by said method and with application of said catalytic system. Method of polymerisation of monomers with obtaining isoolefin polymers and copolymers includes polymerisation of one or more monomers in polymerisation medium, including one or more monomers, diluents and catalytic system. Diluent includes one or more halogenated hydrocarbons. Catalytic system includes one or more Lewis acids and multiple modifiers, which include one or more initiators and one or more polymorphogenates, which contain molecular oxygen or organic oxygenate. If polymorphogenate represents initiator, catalytic system includes second initiator. Regulation of concentration of said one or more polymorphogenates in said polymerisation medium is performed by regulated distribution of molecular mass (PMM) of isoolefin polymers and copolymers, constituting more than 2.0. Polymerisation medium is supplied in form of one or more raw material flows into reactor for polymerisation. Mixture of polymer and diluents is removed from reactor. Diluent is separated from mixture in order to separate polymer. Separated diluent is returned into one or more raw material flows, supplied into reactor. One or more polymorphogenates are added into at least one or more raw material flows.
Polymerisation of isoolefin with polymorphogenates regulated with respect to polydispersity / 2491299
Invention relates to method of polymerisation of monomers with obtaining isoolefin polymers and copolymers, polymerisation system for polymerisation of such monomers, catalytic system for carbocationic polymerisation of isoolefins, isoolefin polymer or copolymer, obtained by said method and with application of said catalytic system. Method of polymerisation of monomers with obtaining isoolefin polymers and copolymers includes polymerisation of one or more monomers in polymerisation medium, including one or more monomers, diluents and catalytic system. Diluent includes one or more halogenated hydrocarbons. Catalytic system includes one or more Lewis acids and multiple modifiers, which include one or more initiators and one or more polymorphogenates, which contain molecular oxygen or organic oxygenate. If polymorphogenate represents initiator, catalytic system includes second initiator. Regulation of concentration of said one or more polymorphogenates in said polymerisation medium is performed by regulated distribution of molecular mass (PMM) of isoolefin polymers and copolymers, constituting more than 2.0. Polymerisation medium is supplied in form of one or more raw material flows into reactor for polymerisation. Mixture of polymer and diluents is removed from reactor. Diluent is separated from mixture in order to separate polymer. Separated diluent is returned into one or more raw material flows, supplied into reactor. One or more polymorphogenates are added into at least one or more raw material flows.
Mercaptan mixture / 2491275
Disclosed is a novel mixture consisting of 2,2,4,6,6-pentamethylheptane thiol-4, 2,4,4,6,6-pentamethylheptane thiol-2, 2,3,4,6,6-pentamethylheptane thiol-2 and 2,3,4,6,6- pentamethylheptane thiol-3, a method for production and use thereof as a chain-terminating agent when producing synthetic rubber. The method of producing the mixture involves reacting hydrogen sulphide with triisobutene during a continuous process at temperature of 0-60°C, wherein before reaction, hydrogen sulphide is dried, the triisobutene used has water content of at most 40 ppm, and the catalyst used is boron trifluoride in amount of 0.6-0.9 wt % with respect to triisobutene used; conversion is carried out in the absence compounds which form complexes with boron trifluoride, and at the end of the reaction, the reaction mixture is brought into contact with aqueous alkaline solution, and the catalyst is separated, wherein the triisobutene used for reaction with hydrogen sulphide contains four isomers: 2,2,4,6,6-pentamethylheptene-3, 2-(2,2-dimethylpropyl)-4,4-dimethylpentene-1, 2,4,4,6,6-pentamethylheptene-2 and 2,4,4,6,6-pentamethylheptene-1, wherein hydrogen sulphide and triisobutene are taken in molar ratio ranging from (1.1-5.0):1 and boron trifluoride is added in gaseous form with excess pressure ranging from 5 to 10 bar.
Gas-phase polymerisation of alpha-olefin / 2490281
Invention relates to a method for gas-phase polymerisation of alpha-olefin and an internal circulation fluidised-bed polymerisation reactor for realising said method. The method for gas-phase polymerisation of alpha-olefin involves cycled gas containing one or more alpha-olefins and an inert gas into a polymerisation reactor; polymerising the alpha-olefin to polyolefin in the presence of a catalyst in two separate polymerisation zones in the polymerisation reactor; and removing the obtained polyolefin from the polymerisation reactor. The internal circulation fluidised-bed polymerisation reactor has one outlet pipe which is mounted in the reactor, in which at least one through-hole is formed, said through-hole connecting the inner and outer parts of the outlet pipe, and a gas-distributing plate which is mounted with inclination from the outer part of the outlet pipe to the side wall of the polymerisation reactor. The polymerisation reactor is divided into two polymerisation zones by the outlet pipe and the inner part of the outlet pipe forms a riser in which polyolefins rise during fast fluidisation. The outer part of the outlet pipe forms an annular gap in which polyolefins passing through the riser descent under gravity. Polyolefins passing through the annular gap are again fed into the bottom part of the riser and are polymerised during circulation between the riser and the annular gap. The alpha-olefin is a compound of formula CH2=CHR, where R is a hydrogen atom or a hydrocarbon radical with 1-12 carbon atoms.
Polymer films / 2489454
Film is made by extrusion from an ethylene and alpha-olefin compolymer. Said ethylene and alpha-olefin copolymer is obtained during a gas-phase polymerisation process with formation of particles in the presence of a monocyclopentadienyl metallocene complex, a co-catalyst of general formula (L*-H)+ d(Ad-), where L* is a neutral Lewis base, (L*-H)+ d is a Brоnsted acid, Ad- is a non-coordinating associative anion, having a charge d- and the anion includes an aryl-substituted borate, and d is an integer ranging from 1 to 3, of carrier material and alpha-olefin. Polymer film contains less than 300-600 gels/m2 with size from 100 to 2000 mcm according to the invention of an optical inspection system.
High melt flow rate, impact-resistant propylene copolymer and method for production thereof / 2487897
Polymerisation method involves contacting propylene and optionally at least one other olefin with a catalyst composition in a first polymerisation reactor under gas-phase polymerisation conditions, the catalyst composition containing a procatalyst, a cocatalyst and a mixed external electron donor (M-EED) containing a first selectivity control agent (SCA1), a second selectivity control agent (SCA2), and an activity limiting agent (ALA); forming, in a first polymerisation reactor, an active propylene-based polymer having a melt flow rate greater than about 100 g/10 min as measured in accordance with ASTM D1238-01 (230°C, 2.16 kg); contacting the active propylene-based polymer with at least one olefin in a second reactor under polymerisation conditions; and obtaining an impact-resistant propylene copolymer having a melt flow rate greater than about 60 g/10 min. A version of the method and the polymer is disclosed.
Catalyst suspension flow splitter and methods for use thereof / 2487894
Catalyst composition suspension feeding system includes a) a primary suspension feeding system which includes a primary suspension flow metre and a primary catalyst injecting device; b) a secondary suspension feeding system which includes a secondary suspension flow metre, a secondary carrier liquid, a secondary carrier liquid flow control device, a secondary catalyst injecting device and further includes a secondary carrier liquid flow metre, a secondary carrier liquid controller and a secondary suspension flow controller. The primary suspension flow metre measures the flow rate of the primary suspension of the catalyst composition arriving at the primary catalyst injecting device. The secondary suspension flow metre measures the flow rate of the secondary suspension of the catalyst composition arriving at the secondary catalyst injecting device. The secondary carrier liquid flow control device controls a method parameter of the secondary suspension feeding system based on the ratio of the flow rate of the primary suspension of the catalyst composition to the flow rate of the secondary suspension of the catalyst composition. The method parameter, which is controlled by the secondary carrier liquid control device, is the flow rate of the secondary carrier liquid measured by the secondary carrier liquid flow metre. The secondary carrier frequency controller controls the secondary carrier liquid control device based on the flow rate of the secondary carrier liquid and the flow rate set by the secondary carrier liquid flow controller. The invention also discloses a catalyst composition suspension feeding system in which a carrier gas is used instead of a carrier liquid as well as corresponding devices, and a method of controlling flow of a catalyst suspension.
Solid extractant for extraction of scandium and method of its production / 2487184
Solid extractant is proposed (SEX) for extraction of scandium from scandium-containing solutions, containing a styrene divinyl benzene matrix with di-(2-ethyl hexyl)phosphoric acid. At the same time it additionally contains dibenzo-18-crown-6 at the following ratio of components, wt %: di-(2-ethyl hexyl)phosphoric acid 28-30, dibenzo-18-crown-6 28-30, styrene divinyl benzene - balance, besides, the ratio of styrene and divinyl benzene in the matrix is equal to 65÷70:30÷35. There is a method also suggested for production of the above extractant.
Method of producing active base for anti-turbulence additive based on homo- and copolymerisation of α-olefins / 2487138
Described is a method of producing polymer bases for anti-turbulence additives. The method involves polymerisation of C6-C30 α-olefins in the presence of a product of reducing titanium tetrachloride with an organoaluminium compound as a catalyst, and a complex based on 3-thia-1,5-diazabicyclo[3.2.1]octane and dimethylaluminium chloride as a cocatalyst. Reactants are in the following molar ratios: α-olefin 1, catalyst 0.002-0.004, cocatalyst 0.02-0.04. The polymerisation reaction is carried out at temperature ranging from -20° to +20°C for 8-12 hours.
Catalyst feed systems and methods of their application / 2486952
Invention relates to catalyst feed systems and methods of their application. Catalyst feed systems for olefin polymerisation comprises catalyst feed vessel and heat exchange system to maintain vessel catalytical system temperature of 27°C or lower, is lower that flow critical temperature. Heat exchange system comprises flexible connection intended for coolant feed into vessel jacket. Coolant includes of the following substances: air, liquid nitrogen, liquid carbon dioxide, glycol, water, liquid alkanes, coolants, and mixes thereof. Invention covers also the method of improving fluidity of heterogeneous solid or applied catalytic system in catalyst feed system wherein catalytic system in the form of particles flows through catalyst feed system. Invention covers also the method of olefin polymerisation including sustaining applied catalyst temperature inside vessel, feeding the catalyst into polymerisation reactor and binging catalyst in contact with olefin to produce polyolefin.
Method of producing sulphur-containing polyacrylamide derivatives / 2465287
Invention relates to a method of producing a sulphur-containing polyacrylamide derivative, having in three types of elementary units in the macrochain:
Polycomponent flocculating systems for removing paint materials from recycled water / 2430930
Invention relates to a system of reagents for extracting paint materials from recycled water, based on acrylic, melamine, polyurethane, nitrocellulose, epoxy and alkyde film-forming agents and can be used in wood processing, machine building, motorcar and other industries. Disclosed is a flocculant consisting of (wt %) polyacrylamide (6-10), activating additive selected from aminotriazole, guanidine carbonate and semicarbazide (0.1-1.5), hydrazine hydrate (0.1-1.5) and water (the rest).
Method of preparing polymer hydrogel / 2378290
Invention relates to synthesis of polymers with high water absorption based on acrylamide and can be used in production of sanitary and hygiene items, dehydrating agents for the coal industry, water-retaining agents for agriculture. Copolymerisation of an aqueous solution of monomers containing acrylamide and a crosslinking agent is carried out in the presence of ammonium persulphate as a radical copolymerisation initiator with the following ratio of components in the solution of monomers, wt %: acrylamide 85-95, guanidine methacrylate 5-15. The crosslinking agent used is guanidine methacrylate.
Water-soluble powdered cation-agent polymer compound, method of production and application / 2352590
There is disclosed water-soluble powdered cation-agent polymer compound containing at least two cationic polymers differing by cationic types with the first cationic polymer made of composing monomers by radical polymerisation in aqueous solution with the second cationic polymer added. The first cationic polymer is polymerised in an aqueous solution of the second cationic polymer by adiabatic gels-polymerisation. Ratio of the second cationic polymer to the first cationic polymer is 0.01:10 to 1:4. Additionally there is disclosed method of producing this polymeric compound applied as an auxiliary flocculative agent in solid/liquid separation.
Water-soluble cation-active powdered polymer composition, method of production and application / 2351614
There is disclosed water-soluble cation-active powdered polymer composition contains, at least, two cationic polymers of different molecular weight. The first cationic polymer consists of component monomers by radical polymerisation in aqueous solution with the second cationic polymer added whereat cation link types of the first and second polymers are matched. The first cationic polymer is a copolymer of cationic and nonionic monomers. Apparent molecular weight of the first cationic polymer is more than 1 million. The first cationic polymer is polymerised in aqueous solution of the second cationic polymer by adiabatic gel polymerisation method. Ratio of the second cationic polymer to the first cationic polymer is 0.01:10 to 1:3. Besides, there is described method of making these polymer compositions and their application as a flocculating additive for solid substance/liquid isolation.
Acrylamide water solution, which contains saccharide / 2343161
Acrylamide water solution contains from 40 wt % to 60 wt % of acrylamide and from 0.1 ml/l to 60 ml/l of saccharide, obtained by cultivation of strain J1 FERM BP-1478 of microorganism Rhodococcus rhodochrous. Reaction of acrylonitryl with biocatalyst, which has nitrylhydratase activity, containing saccharide, and obtained from strain J1 FERM BP-1478 culture of microorganism Rhodococcus rhodochrous, expressing nitrylhydratase, is carried out. Method of polyarcrylamide obtaining includes two stages. At first stage said water solution of arcrylamide is obtained. At second stage polymerisation of arcrylamide water solution in presence of initiator is carried out.
Polymer composition and a method for preparation thereof / 2245349
Invention relates to water-soluble powder polymer compositions useful as flocculants for dehydration of solids-containing slurries or sludges. Compositions are prepared via continuous polymerization of at least one unsaturated monomer, wherein at least one polymerization-affecting parameter is varied in accordance with a repetitive scheme. For instance, monomer concentration, molecular weight regulator amount, monomer solution pH value, and/or monomer solution composition can be varied.
Aqueous dispersion of water-soluble polymer and its preparation / 2218355
The invention relates to a composition and method for producing a non-ionic and anionic water-soluble polymers in the form of finely dispersed particles of the polymer in aqueous salt environment
A method of manufacturing paper / 2194818
The invention relates to the manufacture of paper, and more particularly, to a method of making paper, which paper add weight cationic organic polymer containing a hydrophobic group and an anionic material microecology
The method of obtaining water-soluble (co)polymers of acrylic series / 2192434
The invention relates to the production of water-soluble polymers of acrylic series, which can be used in several branches of engineering and technology, namely as a dressing for finishing textiles, coal mining, and in the processes of purification and clarification of drinking, industrial and waste water as a flocculant, in the drilling technique as a protective means in the chemical industry as the thickening agent
Method of preparing polymer hydrogel / 2378290
Invention relates to synthesis of polymers with high water absorption based on acrylamide and can be used in production of sanitary and hygiene items, dehydrating agents for the coal industry, water-retaining agents for agriculture. Copolymerisation of an aqueous solution of monomers containing acrylamide and a crosslinking agent is carried out in the presence of ammonium persulphate as a radical copolymerisation initiator with the following ratio of components in the solution of monomers, wt %: acrylamide 85-95, guanidine methacrylate 5-15. The crosslinking agent used is guanidine methacrylate.
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FIELD: biotechnologies. SUBSTANCE: method is realised by polymerisation of an aqueous solution containing 7-15 wt % of acrylamide and 0.5-1.5 wt % of N,N'-methylenebisacrylamide, in presence of polymerisation initiator, besides, the polymerisation initiator is a mixture of 4,4'-azobis(4-cyanopentane acid) and ammonium salt of 4-8-dithiobenzoate of 4-cyanopentane acid with their content in the aqueous solution as 0.03-0.07 wt % and 0.07-0.35 wt %, accordingly, and polymerisation is performed at temperature of 70-80°C and pH 3.0-4.0. EFFECT: increased structural homogeneity of a hydrogel. 2 tbl, 5 ex
The invention relates to the field of polymer chemistry, biochemistry and medicine, namely to a process for the preparation of polyacrylamide hydrogel, which is due to the high porosity is used as the separating medium in liquid chromatography, as a carrier of immobilized biologically active substances, as well as for the manufacture of implants soft tissue. A method of obtaining polyacrylamide hydrogel by γ-irradiation dose of 0.5 to 5.0 Mrad powdered polyacrylamide followed by the addition of water and mechanical homogenization of the mixture [RF patent 2114867, C08F 120/56, 1998]. The disadvantage of this method is the heterogeneous structure of the obtained hydrogel, due to the presence of pores of different sizes. All the pores of the hydrogel accessible to molecules of insulin with a molecular mass (MM) 6000 and molecules of serum albumin with MM 67000, 70-80% of the pores accessible to molecules of alcohol dehydrogenase with MM is 141,000 and 40-50% of the pores accessible to molecules of fibrinogen with MM 340000. The closest in technical essence and the achieved results is the method of obtaining a polyacrylamide hydrogel by polymerization of an aqueous solution containing 7-15 wt.% acrylamide and 0.5 to 1.5 wt.% N,N'-methylenebisacrylamide, in the presence of initiator, polymerizati [research Methods in immunology, Ed. by I. Lefkovits and of B. Pernis World Moscow, s-107]. As an initiator of polymerization using a redox system: ammonium persulfate and N,N,N',N'-tetramethylethylenediamine, and polymerization was performed at room temperature. The disadvantage of this method is the structural heterogeneity of the obtained hydrogel, due to the wide range of pore sizes. Depending on the amount of acrylamide and N,N'-methylenebisacrylamide obtained hydrogels swollen in the state contain 80-95% water, all the pores of hydrogels available for molecules of insulin, 90-95% of the pores accessible to molecules of ovomucoid with MM 31000, 80-90% of the pores accessible to molecules of serum albumin, 50-60% of the pores accessible to molecules of alcohol dehydrogenase and 30-40% of the pores accessible to molecules of fibrinogen. The objective of the invention is to increase the structural homogeneity of the hydrogel. The technical result that is achievable with the use of the invention is to increase the structural homogeneity of the hydrogel. The technical result is achieved in that in the method of obtaining a polyacrylamide hydrogel by polymerization of an aqueous solution containing 7-15 wt.% acrylamide and 0.5 to 1.5 wt.% N,N'-methylenebisacrylamide, in the presence of a polymerization initiator as a polymerization initiator, a mixture of 4,4'-azobis(4-cyanopentanoate acid) and ammonium salts of 4-S-dithio is enzoate 4-cyanopentanoate acid in their content in an aqueous solution of 0.03-0.07 wt.% and 0.07 and 0.35 wt.% accordingly, and the polymerization is carried out at a temperature of 70-80°C and pH 3.0 to 4.0. Example 1. In to 89.5 ml of water at pH of 3.6 dissolve 10 g of acrylamide (AA), 0.5 g of N,N'-methylenebisacrylamide (BIS), 0,065 g of 4,4'-azobis(4-cyanopentanoate acid) (CTC) and 0.07 g of ammonium salt of 4-S-dithiobenzoate 4-cyanopentanoate acid (DTB). The vacuum solution with 10-3mm Hg and incubated for 20 hours at 78°C. the resulting gel is crushed by pushing through a sieve with a pore diameter of 1 mm and washed with 10-fold excess of distilled water. The water content of the hydrogel assessed by weighing the swollen hydrogel in water and lyophilized hydrogel. To assess content in the hydrogel pores of different size to 2 ml of gel add 4 ml of the protein solution and the mixture was incubated for 48 hours at 4°C. the Concentration of the original protein solution and the protein solution after contact with the hydrogel was measured spectrophotometrically at 280 nm using pre-built calibration dependence. Given the volume ratio of hydrogel and solution of protein, counting the number of pores available for each protein, taking as 100% the number of pores available for water. The properties of the hydrogel are shown in table 2. Examples 2-4. The process is conducted according to example 1, using different numbers of components. The compositions of the reaction mixture and the polymerization conditions are shown in table 1. Example 5 (the end of the roll, the prototype). At room temperature and stirring in 89 ml of distilled water was dissolved 10 g of acrylamide and 0.5 g of N,N-methylenebisacrylamide. After complete dissolution the solution was added 0.08 g of ammonium persulfate. The solution is vacuum at 10-12 mm Hg, to it add 0,08 ml of N,N,N',N'-tetramethylethylenediamine and incubated at room temperature (18-21°C) for 5 hours. The obtained gel is then removed from the vessel, crushed by pushing through a sieve with a pore diameter of 1 mm and washed with 10-fold excess of distilled water.
It is seen that using as an initiator of polymerization of a mixture of 4,4'-azobis(4-cyanopentanoate acid) and ammonium salts of 4-S-dithiobenzoate 4-cyanopentanoate acid in the process of copolymerization of acrylamide and N,N'-methylenebisacrylamide results in a more homogeneous porous hydrogels, in which very little of the content of pores of large size. So, if the hydrogel obtained by the method prototype, all the pores have dimensions that provide access for water molecules and protein molecules with 6000 MM, of which 38 % is available for protein molecules with MM 360000, hydrogels, the scientists on the proposed method, the number of pores available for protein molecules with MM 360000, reduced 3.8-7.6 times. The limiting values of the components of the initiator due to the fact that at concentrations below these values, the polymerization proceeds at a very slow speed, and at concentrations above these values, the hydrogel is formed. Only at pH values of 3.0 to 4.0 is possible to obtain a homogeneous solution all used compounds. At temperatures above 80°C the polymerization is explosive in nature, and at temperatures below 70°C it does not leak. A method of obtaining a polyacrylamide hydrogel by polymerization of an aqueous solution containing 7-15 wt.% acrylamide and 0.5 to 1.5 wt.% N,N'-methylenebisacrylamide, in the presence of a polymerization initiator, characterized in that as the initiator of polymerization, a mixture of 4,4'-azobis(4-cyanopentanoate acid) and ammonium salts of 4-S-dithiobenzoate 4-cyanopentanoate acid in their content in an aqueous solution of 0.03-0.07 wt.% and 0.07 and 0.35 wt.%, respectively, and the polymerization is carried out at a temperature of 70-80°C and pH 3.0 to 4.0.
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