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Method of preparing polymer materials with specified porosity via treatment with carbon dioxide in supercritical state followed by heat treatment at atmospheric pressure |
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IPC classes for russian patent Method of preparing polymer materials with specified porosity via treatment with carbon dioxide in supercritical state followed by heat treatment at atmospheric pressure (RU 2266305):
A method of obtaining a foamed polystyrene / 2073693
The invention relates to methods of producing a stable foam, used as heat insulator
The method of obtaining medicinal healing sponges / 2104008
The invention relates to pharmaceutical industry
Absorbent porous polymeric macrostructure, absorbent and method for producing porous absorbent polymer macrostructure / 2099093
Absorbent polymer composition / 2091081
The invention relates to an improved particulate, absorbent, polymeric compositions
Composition for microporous material krasavicaaaaa / 2057150
The invention relates to the production of PVC plastisols with coloured compounds, which serve as the basis for the manufacture of krasavitsa materials in the form of various rollers of printing machines, stamp pad, marking stamps, etc
Ultraflexible pipeline insulation / 2248378
Invention relates to method for production of physically foamed heat-retention polyolefin foam and expanded material made from the same. Polyolefin foam is obtained by extrusion of expanded material composition containing (mass %): metallocene polyethylene 77-92; antipyrene 5-10; cell stabilizer 3-8; and other additives 0-5 % using physical foaming agent. Flexible expanded material of present invention has wide-range application, in particular it is useful as insulator for thin and/or twisted pipelines. Forasmuch foam is obtained using physical foaming agents and is not chemically cross-linked it may be reprocessed for reutilization.
Composition for the production of rigid polyurethane foam / 2226538
The invention relates to techniques for the production of compositions for the manufacture of rigid polyurethane foam intended for the manufacture of heat-insulating elements
Gravitationa foam billet / 2225873
The invention relates to the manufacture graphitizing foam blanks, which can then be compacted to obtain a friction material
Sheet polypropylene foam, moldable when heated / 2219198
The invention relates to a method for producing an extruded foamed sheet thermoplastic, which, in particular, serve as the raw material for molding containers, vats, substrates, ceilings vehicle or packaging panels, pallets
Foamed porous membrane of thermoplastic polymers, and a method and apparatus for their manufacture / 2203127
The invention relates to foamed porous membrane made of thermoplastic polymers, characterized by a great volume of voids and a high proportion of open pores, and also to a method and apparatus for the manufacture of such membranes
A method of manufacturing a civil, structural or packaging material, a device for implementing the method and the product obtained by this method / 2105776
Dielectric polymeric foam and its utilization in production of lenses for radio waves / 2263124
The invention is pertaining to a dielectric polymeric foam and its utilization in production of lenses for radio waves. The dielectric polymeric foam is intended for utilization in the capacity of different dielectric materials, including as the material for production of spherical lenses for radio waves and Luneberg lens. The polymeric foam has a dielectric permeability of no less than 1.5 at 12 GHz and 25 °C and is produced by a foaming of the polymeric composition, which contains a synthetic polymetric compound and one or more dielectric inorganic filler. The filler is selected from a fibrous titanate of the alkaline-earth metal and a lamellar titanate of the alkaline-earth metal. The produced dielectric polymeric foam has good and uniform dielectric features.
Method of preparing physically foamed polyolefin foams and heat-insulation plastic foams manufactured therefrom / 2247755
Invention, in particular, relates to polyolefin foams, which are resistant to temperatures as high as 160°C. Method comprises stirring and melting of polyolefin, melting range of which is 85-170°C (as measured according to differential scanning calorimetry technique at heating rate 10°C /min), or a mixture of one or several such polyolefins. Resulting homogenous mixture consists of a single individual phase with melting temperature within the range 120-160°C (measured as above). The mixture is fed into extruder being heated to melting temperature in the first section of extruder. Molten mixture is further mixed, in the second section of extruder at elevated pressure, with foaming agent containing substance, which is liquid at temperature and pressure in extruder but vaporizes when pressure is lowered. Molten mixture is then cooled to a temperature, at which liquid mixture transforms to semicrystalline phase, and extruded through in cold state through die such as to foam the mixture as a result of evaporation of foaming agent to produce foamed polyolefin.
Linking vinylaromatic polymers and foam / 2213101
The invention relates to binding monomineralic aromatic polymer resins and their use as polymer and foam products in the form of sound or thermal insulation, construction foam, packaging
A method of obtaining a self-extinguishing foam plates / 2190638
The invention relates to the production of self-extinguishing foamed slabs of polystyrene, molded extrusion method
The material for the manufacture of containers and the containers on its basis / 2183557
The invention relates to materials for the manufacture of containers and to containers on its basis intended for beverages and other food products, which can be applied by stamping circuit configuration and create the shape of the container by bending sheet
Foam strip obtained from a homogeneous olefin polymers / 2179563
The invention relates to a foam gasket and method of forming
Expanded onto a polyolefin composition (options), the composition a stabilizing reagent for foam, the product of foamed polyolefin and method of preparation of penopoliuretana / 2174991
The invention relates to a polyolefin composition capable of foaming, i.e
Thin draped stagnant having a uniform thickness of the adhesive film, molded product based on the film (options), and a method of manufacturing a molded product / 2127291
The method of obtaining extruded polystyrene / 2114131
The invention relates to the technology of plastics processing, the method of production of polystyrene by extrusion, which is widely used as insulation material in industrial and civil construction, construction of roads and Railways
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FIELD: polymer materials. SUBSTANCE: method is comprised in saturating polymer material sample, placed in high-pressure cell, with carbon dioxide under supercritical conditions at pressure 250 atm and temperature 40-120°C, cooling the cell to room temperature and slowly lowering pressure to its atmospheric value. Foaming of polymer sample saturated with carbon dioxide under supercritical conditions proceeds during 60 min of further heat treatment at atmospheric pressure. Final porosity of polymer sample is determined by heat treatment temperature. EFFECT: essentially preserved mechanical properties of initial polymer due to that, during heat treatment operation, outside layer of CO2-saturated polymer sample is foamed. 9 dwg, 1 tbl, 6 ex
The invention relates to a method for producing polymeric materials with a specified pore volume through treatment with carbon dioxide in supercritical state at a pressure of 250 atmospheres and a temperature of 40-120°and further heat treatment at a temperature of 40-210°and atmospheric pressure. Today, the development of methods of polymeric matrices with a given porosity attracts much attention of research groups around the world. This is because porous polymers and materials based on them have an extremely wide range of applications. For example, in the scientific literature describes the use of porous polymers as a filter to trap organic matter [My, WM., Irvine RL. Polyurethane foam based biofilter media for toluene removal. Water. Sci. Technol. 2001; 43(11): 35-42] and the volatile components of smell [Avison SJ, Gray DA, Davidson GM, Taylor AJ. Infusion of volatile flavor compounds into low-density polyethylene. J. Agric. Food. Chem. 2001 Jan; 49(1): 270-5.], as adsorbents for the separation of biomolecules [Mayr, Tessadri TR., Post E, Buchmeiser MR. Metathesis-based monoliths: influence of polymerization conditions on the separation of biomolecules. Anal. Chem. 2001 Sep 1; 73(17): 4071-8]in a microfluidic chromatography and capillary electrophoresis [Gusev I, Huang X, Horvath C. Capillary columns with in situ formed porous monolithic packing for micro high-performance liquid chromatography and capillary electrochromatography. J. Chomatogr. A 1999 Sep 3; 855(1): 273-90], in optical electronic devices [Wirnsberger G, Yang P, Scott BJ, Chmelka BF, Stucky GD. Mesostructured materials for optical applications:from low-k dielectrics to sensors and lasers. Spectrochim Acta A Mol. Biomol. Spectrosc. 2001 Sep 1; 57(10): 2049-60] and electrochemical power sources [Sotiropoulos, S., Brown, I.L., Akay G., Lester E. Nickel incorporation into a hollow fibre microporous polymer: a preparation route for novel high surface area nickel structures. Materials Letters 35 (1998) 383-391]. Of great interest is the use of such materials in medicine. Here the main areas of application of porous polymers are: the creation of sources for slow dosing in humans drugs (Drug delivery) [Dziubia TD, Torjman MC, Joseph L, Murphy-Tatum M, Lowman AM. Evaluation of porous networks of poly(2-hydroxyethyl methacrylate) as interfacial drug delivery devices. Biomaterials 2001 Nov; 22(21): 2893-9], using as the basis for growth and tissue regeneration [Choueka j, Charvet J.L., Koval K.J., Alexander H., James for K.S. Canine bone response to tyrosine-derived polycarbonates and poly(L-lactid acid). J. Biomed. Mater. Res., May; 31(1): 35-41 (1996)] and implants with improved survival [Gosain AK, Song L, Riordan P, Amarante MT, Nagy PG, Wilson CR, Toth JM, Ricci JL. A 1-year study of osteoinduction in hydroxyapatite-derived biomaterials in an adult sheep model: part I. Plast. Reconstr. Surg. 2002 Feb; 109(2): 619-30]. The above examples do not exhaust the whole range of possible applications of porous polymeric materials, but they clearly show that the need for such materials today is quite high and will increase in the future. One of the promising methods for creating porosity in polymer matrices is the handling of carbon dioxide in gazoo is different, liquid or supercritical state. Although this method of obtaining porosity is applied relatively recently, to date, published a large number of works devoted to this topic. In these studies, the process of creating porosity was carried out in two stages: the first stage polymer is saturated with gaseous, liquid or supercritical CO2at high pressure, the second saturated CO2the polymer was wspanialy using rapid heating at atmospheric pressure. So, in [Handa, Y.P.; Zhang, Z.J. A new technique for measuring retrograde vitrification in polymer-gas systems and for making ultramicrocellular foams from the retrograde phase. Polym. Sci. Part B: Polym. Phys. 2000, Vol.38, p.716-725.] described obtaining in this way a porous polymethylmethacrylate (PMMA), in [Kumar, V.; Weller, J.E. Microcellular Foams; Khemani, K.S., Ed.; ACS: Washington, DC, 1997; Vol.669, p.101.] we studied the influence of temperature foaming porosity of the saturated CO2polycarbonate. The authors of [Wessling, M.; Borneman, Z.; Van den Boomgaard, T.; Smolders, S.A. Carbon dioxide foaming of glassy polymers, J. Appl. Polym. Sci. 1994, Vol.53, p.1497-1512.] we studied the process of steam formation in the films of polycarbonate, polyamide and polysulfone, it is shown that the saturation of these polymers gaseous CO2and subsequent foaming process steam formation is accompanied by the formation on the surface of the thin dense layer that covers the access to the pores in the thickness of the polymer. [Stafford, who .M.; Russel, TR; McCarthy, T. Expansion of polystyrene using supercritical carbon dioxide: effects of molecular weight, polydispersity, and low molecular weight components. J. Macromolecules 1999, Vol.32, p.7610-7616] studied the dependence of the average diameter of the pores saturated with supercritical CO2and foamed polystyrene from the molecular weight, polydispersity and quantity of low-molecular components in the original polymer. It is shown that all studied factors, only the presence of substantial amounts of low molecular weight substances influences the pore formation in polystyrene. In addition, there are a number of publications on obtaining in this way a porous polypropylene [Liang, M.-T.; Wang, C.-M. Production of Very Low Density Microcellular Polypropylene by Supercritical Carbon Dioxide: Nottinghma (UK), 1999, p.151.], polyethylene [Briscoe, .J.; Director, B.I.; Savvas, T. Cellular Polymers 1993, Vol.12, p.171.] and polyethylenterephtalate modified with glycol [Handa, Y.P.; Wong, W.; Zhang, Z.; Kumar, V.; Eddy, S.; Khemani, K. Polym. Eng. Sci 1999, Vol.39, p.55.]. In this application the invention to create for polymeric materials, the porosity of a given size is proposed using two-stage processing, allowing to obtain polymeric materials with a specified pore size. In the first stage, the polymer is saturated with carbon dioxide in supercritical state. The saturation of the polymer is conducted at the facility, the concept of which is shown in figure 1. The process of saturation in this installation done by ulali as follows: the polymer sample was placed in a cell E, then use pump N the cell was filled with carbon dioxide to a predetermined pressure, after which thermostat T was heated to a predetermined temperature. When experiment the cell was cooled to room temperature and slowly dumped pressure through an adjustable air restrictor PP. Data on the sorption of carbon dioxide with polymers at a temperature of 40°S-120°and a pressure of 250 ATM for 60 minutes processing are shown in table 1.
Presents data cover the temperature range below the glass transition temperature, saturation with carbon dioxide at values close to or above this temperature results in the sorption of extremely large quantities of carbon dioxide, which, in turn, leads to severe swelling (2.5-4 times compared to the initial volume) and almost complete loss of mechanical strength. For example, after processing of PMMA at a temperature of 100°With (amount of adsorbed carbon dioxide 28% by weight of polymer) of the polymer sample was loose and fragile. Processing of PMMA above this temperature led to mechanical destruction of the sample. Immediately after treatment with carbon dioxide, the sample was placed in a thermostat and kept for 60 minutes at a given temperature. During the heat treatment was foaming of the outer layer polymer saturated with carbon dioxide. While the core of the polymer did not undergo any changes, i.e. the sample was largely retained mechanical properties of the source material. The proposed procedure, in which education is the EC first processed with carbon dioxide, then extracted from the cells after cooling and slow pressure relief and then foams at thermostat, provides a number of advantages compared with the known method foaming directly in the cell when the pressure relief, namely: this procedure ensures strict control of all process parameters (process conditions in skso2the foaming temperature), which in turn, allows high accuracy to predict the final porosity of the material; when the two-stage processing more effectively used cell volume, because in this case no additional amount for expansion of the expandable polymer samples, which significantly reduces the cost of the porous polymeric material. As an illustration, figure 2, shows a photograph of a sample polimetilmetakrilata processed in supercritical carbon dioxide at a pressure of 250 atmospheres and a temperature of 40°C for 30 minutes and then foamed at different temperatures. Total pore volume of polymer materials was measured by filling them with water at room temperature and a pressure of 300 atmospheres. The measured values thus porosity of the samples polymethylmethacrylate depending on the temperature of the foaming is shown in the histogram (figure 3). The machining conditions and temperature in which peniana match, specified in figure 2. As can be seen in figure 3., the proposed method is two-stage processing of polymers makes it possible to obtain samples with porosities varying within wide limits depending on the heat treatment temperature at atmospheric pressure. In a similar manner there were obtained samples of different porosity high impact polystyrene (HIPS), polycarbonate, polystyrene, copolymer of acrylic-butadiene-styrene (ABS)copolymer of 94% of methyl methacrylate and 6% of methyl acrylate (datril 6). Data on the change in porosity of polymeric materials depending on the temperature treatment at atmospheric pressure is shown in figure 4 (polycarbonate), 5 (high impact polystyrene), 6 (polystyrol PSN-115), 7 (copolymer of Acrylonitrile-butadiene-styrene ABS), Fig (copolymer of datril 6). Specific processing conditions, and achieved the porosity indicated in the examples. To confirm the formation of the polymer porous structure of the samples before and after treatment were investigated by scanning electron microscopy. Figure 9 shows a micrograph of the initial and treated samples. The shots clearly shows that the treatment proposed method leads to the formation of polymer in the well-developed structure of pores. Example 1. Sample polymethylmethacrylate ×44×15 mm (PMMA) was placed in a cell that was processed in sorcity eskay carbon dioxide at a temperature of 40° C and a pressure of 250 psi for 60 minutes, then the cell was cooled to room temperature and slowly dropped the pressure to atmospheric. Then saturated with carbon dioxide sample was extracted from the cell and placed in thermostat, where is kept at a temperature of 80°C for 60 minutes. The resulting porous polymeric material has a total pore volume of 0.7 cm3/year Example 2. A sample of polycarbonate based on bisphenol a brand "Makrolon" (firm Bayer, Germany), in the form of granules (dcp=3-4 mm, total number of 24 pellets), was placed in a cell that was processed in supercritical carbon dioxide at a temperature of 120°and pressure of 250 psi for 60 minutes, then the cell was cooled to room temperature and slowly dropped the pressure to atmospheric. Then saturated with carbon dioxide sample was extracted from the cell and placed in thermostat, where is kept at a temperature of 190°C for 60 minutes. The resulting porous polymeric material has a total pore volume of 0.4 cm3/year Example 3. Sample high impact polystyrene (HIPS), in the form of granules (dcp=3-4 mm, total number of 32 granules), was placed in a cell that was processed in supercritical carbon dioxide at a temperature of 40°and pressure of 250 psi for 60 minutes, then the cell was cooled to room temperature and slowly lost pressure, the reduction to atmospheric. Then saturated with carbon dioxide sample was extracted from the cell and placed in thermostat, where is kept at a temperature of 140°C for 60 minutes. The resulting porous polymeric material has a total pore volume of 0.9 cm3/year Example 4. Sample polystyrol PSN-115 according to GOST 20282-86, in the form of granules (dcp=3-4 mm, total number of 32 granules), was placed in a cell that was processed in supercritical carbon dioxide at a temperature of 40°and pressure of 250 psi for 60 minutes, then the cell was cooled to room temperature and slowly dropped the pressure to atmospheric. Then saturated with carbon dioxide sample was extracted from the cell and placed in thermostat, where is kept at a temperature of 120°C for 60 minutes. The resulting porous polymeric material has a total pore volume of 1.05 cm3/year Example 5. A sample of the copolymer of Acrylonitrile-butadiene-styrene (ABS), in the form of granules (dcp=3-4 mm, total number of 24 pellets), was placed in a cell that was processed in supercritical carbon dioxide at a temperature of 50°and pressure of 250 psi for 60 minutes, then the cell was cooled to room temperature and slowly dropped the pressure to atmospheric. Then saturated with carbon dioxide sample was extracted from the cell and placed in thermostat, where is kept at a temperature of 120°for the of 60 minutes. The resulting porous polymeric material has a total pore volume of 0.9 cm3/year Example 6. The cylindrical sample (d=7 mm, l=20 mm) of a copolymer of methyl methacrylate with methyl acrylate dakril 6, weight percentage of methyl acrylate 6%, was placed in a cell that was processed in supercritical carbon dioxide at a temperature of 40°and pressure of 250 psi for 10 minutes, then the cell was cooled to room temperature and slowly dropped the pressure to atmospheric. Then saturated with carbon dioxide sample was extracted from the cell and placed in thermostat, where is kept at a temperature of 100°C for 60 minutes. The resulting porous polymeric material has a total pore volume of 1.78 cm3/year 1. The method of obtaining porous polymeric materials with a specified volume of pores, wherein a sample of the polymer material is first placed in a high-pressure cell and saturated with carbon dioxide under supercritical conditions at a pressure of 250 atmospheres and temperatures 40-120°With, then the cell is cooled to room temperature and slowly relieve the pressure to atmospheric, then saturated with carbon dioxide polymer sample is subjected to heat treatment at atmospheric pressure for 60 min, and the final porosity of the sample is set by the temperature of heat treatment. 2. The method according to claim 1, featuring the the action scene, what were processed polymethylmethacrylate (PMMA), the saturation of carbon dioxide was carried out at a pressure of 250 atmospheres in the temperature range 40-100°With subsequent heat treatment conducted at temperatures 40-140°C for 60 min, the total porosity of the polymer samples of 0.05-0.9 cm3/g depending on the heat treatment temperature. 3. The method according to claim 1, characterized in that the processed polycarbonate (PC), the saturation of carbon dioxide was carried out at a pressure of 250 atmospheres in the temperature range of 40-120°With subsequent heat treatment conducted at temperatures 150-210°C for 60 min, the total porosity of the polymer samples of 0.01-0.4 cm3/g depending on the heat treatment temperature. 4. The method according to claim 1, characterized in that the processed high-impact polystyrene (HIPS), the saturation of carbon dioxide was carried out at a pressure of 250 atmospheres in the temperature range 40-100°With subsequent heat treatment conducted at temperatures 40-140°C for 60 min, the total porosity of the polymer samples of 0.1-0.9 cm3/g depending on the heat treatment temperature. 5. The method according to claim 1, characterized in that the processed polystyrene (PS), the saturation of carbon dioxide was carried out at a pressure of 250 atmospheres in the temperature range 40-100°With subsequent heat treatment was carried out at a temperature of 40-120°C for 60 min, the total porosity of the polymer is Bristow 0,21-1,05 cm 3/g depending on the heat treatment temperature. 6. The method according to claim 1, characterized in that the processed copolymer of Acrylonitrile-butadiene-styrene (ABS), the saturation of carbon dioxide was carried out at a pressure of 250 atmospheres in the temperature range 40-100°With subsequent heat treatment was carried out at a temperature of 40-120°C for 60 min, the total porosity of the polymer samples of 0.1-0.9 cm3/g depending on the heat treatment temperature. 7. The method according to claim 1, characterized in that the processed copolymer of 94% poly 6% for polymethylacrylate (datril 6), the saturation of carbon dioxide was carried out at a pressure of 250 atmospheres in the temperature range 40-80°With subsequent heat treatment was performed at temperatures of 40-100°C for 60 min, the total porosity of the polymer samples 0,35-1,78 cm3/g depending on the heat treatment temperature.
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