• 专利附录
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    • 专利摘要:

    公开号:SU805952A3
    申请号:SU782654151
    申请日:1978-08-29
    公开日:1981-02-15
    发明作者:Карчмарофф Петер；Форстер Эвальд；Шаффнер Армин
    申请人:Циба-Гейги Аг (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR OBTAINING A METAL SILICATE FORPOLYMER
    20 mm thick. After soaking for 10–15 hours, the dry mass is granulated on a wiper sieve with 3 mm holes. The granulate is again distributed on metal sheets and incubated 2 times for 15 hours with intermediate granulation at room temperature, the water content of the granules is reduced to 25-32% by weight. After shaking, this product is held in a chamber dryer with air circulation for 2-3 hours at 90 ° C until the water content drops to approximately 20% by weight. After regrinding, the product is treated for an additional 1-2 hours at a chamber temperature of 120 ° C until the water content drops to 11% by weight. Part of the grinding, continue to dry at a chamber temperature of 120 s, while the water content in it will be equal to 5 wt.%.
    B, To the resulting prepolymer with a water content of 5 wt.%, Add 1.0 wt.% Modified rock wax and grind in a pin mill. The pressing is performed in conventional steel forms with a surface of improved quality at a pressure of 800-1000 kg / cm and 250-2 ° C. 10 mm thick samples tested according to German Industrial Standard (SPS) standard 53470 require about 5 minutes of exposure during pressing and have high strength.
    V.V. the drying fluid mixer with a capacity of 20 liters is dosed and mixed for 2 minutes 3.30 kg of the obtained prepolymer with a water content of 11% by weight and 3.30 kg of calcium silicate (ground wollastonite). After that, another 3.30 kg of prepolymer with a water content of 11% by weight and 0.02 kg of ground zinc stearate are added and homogenized for 5 l of fluff. The resulting mass is pressed at 250-260 ° C according to Example 1.B in shaped parts.
    Press pressing to obtain samples tested in accordance with GSP 53470 (thickness 10 mm) is 5 minutes. Samples have the following properties:
    Specific weight, kg / cm 2.41 Compressive strength; MPa, (GSP 53455) 171
    Brinell hardness, MPa (01N 53456) 295
    Impact bending strength, kg / m
    (S1ShM 77103) 0.160
    Linear coefficient of thermal expansion at 25-150 C, KG -, SSGE 0304) 6.5-10
    D. In a 30-liter ball mill, 5.00 kg of the obtained prepolymer with a water content of 11 wt.% Is laid and homogenized for 6–8 hours.
    4.00 kg of calcium silicate (milled wollastonite), 1.00 kg of talc (residue after calcination at 95.7 wt.%), 0.01 kg of milled zinc stearate. The resulting g mass is compressed as described in example 1.B method in shaped parts.
    Test samples have the following properties:
    Specific gravity, g / cm 2.44 f. Compressive strength, MPa, (GSP 53454)
    150
    Brinell hardness
    MPa, (1 53454).
    162
    Impact strength when
    bending, kg / m 5 (SShPM 77103) 0.170
    Lightfastness, h 2000
    D. In a mixer with a capacity of 10 liters, 2.0 kg of the obtained prepolymer with a water content of 11 wt.%, 0 2.0 kg of asbestos fibers (washed without iron 3-10 mm), 1.0 kg of copper filings (O size, 6x1; 5x4; 0-12.0 mm) and then homogenized for 30 minutes. The obtained molding material is pressed into steel molds heated to 300 ° C into molded blanks of size 45x30x15 mm, and the pressing time is about 1-2 minutes per 1 mm of the thickness of the part. The obtained molded blanks are characterized by good mechanical indications and high abrasion resistance.
    E. On a calendering unit, artificial mineral fibers 3-10 mm long obtained by the product obtained in Example 1 with a water content of more than 35% by weight are impregnated. Impregnation is carried out so that the ratio of precondensate / artificial mineral 0 fiber is 1: 3-1: 2 . The impregnated material is sent directly to the belt conveyor of the tunnel kiln. In the zones of the furnace, temperatures of 90, 110 and 130 C 5 are set, respectively. The passage rate is adjusted so that a product with a water content of 1015% by weight is obtained. This product is pressed in other forms at 200 ° C and a pressure of 200 kg / cm into molded blanks with dimensions of 150x70x10 mm.
    The resulting compacts are characterized by strength and insulation.
    PRI me R. 2. A. Preparation of prepolymers
    In a tray mixer with a capacity of 20 liters, doses of 4.66 kg of a 37% aqueous solution of sodium silicate (molar ratio Na-0 / S i 0, 3, 3, pH 11) are injected with doses at intervals of about 10 minutes with continuous stirring, 4, 32 g of sodium silicate powder (residue after calcination at 900 s 82 wt.% 0.80 kg silicate powder
    5 potassium (residue after calcination, poi, 900 ° C, 99 wt.%). After the formation of a homogeneous mass, another 2.00 kg of sodium silicate solution, 4.00 kg of zinc oxide (in portions) and 0.05 kg of pigment are added with constant stirring. The water content in the mixture is 31.7 wt.%. The equipment is closed and the reaction mixture is homogenized at 25–30 ° C for 10–10 minutes. Then the homogenous mass is placed in metal drying sheets with a layer thickness of 20 mm. After being stacked in this position for about 15 hours, the dry mass is granulated on a wiper sieve with 5 mm holes. The granulate is again distributed on metal sheets and kept at room temperature for about 20 hours, with the water content of the granules being reduced to 2025 wt.%. After passing through the pin mill, the ground mass is kept in a chamber dryer with air circulation for 3-5 hours at 90 ° C until its water content drops to 12 wt.%. Part of this prepolymer was continued to dry in a convection drying chamber at 100 s, until the water content dropped to 7–8 wt.%. B. A spiral mixer is dosed and 2.0 kg of the obtained prepolymer is homogenized with a water content of about 12% by weight, as well as a mixture of 0.7 kg of calcium silicate (ground wollastonite), O, 3 kg of talcum residue after calcination at 95 , 7 wt.% And 0.01 kg of modified mountain wax. The mixture is sent directly to the compactor and transferred to the granulate. The press is pressed at 240-250 ° C and a pressure of 100012000 kg / cm - into molded blanks according to GSP 53470.. The obtained molded blanks have the following properties: Compressive strength, Mna, (DlN 53454) 170 Brinell hardness, MPa, (D1N 53456) 202 Impact strength under bending, 77103) 0,130 Tritz. A. Preparation of Odds of Polymers 1.15 kg of a 37% aqueous solution of sodium silicate (molar ratio 1: 3.3 pH 11), and 0.70 kg of sodium silicate powder (residue after calcination at 82 wt.% ). After a homogeneous mass is formed, 0.08 kg of emulsion gator (sodium alkyl alkyl sulfonate product), 0.40 kg of zinc oxide and 0.02 kg of pigment (cadmium yellow) are added and mixed thoroughly for approximately 10 minutes. Then, as a filler, 0.83 kg of artificial mineral fibers with 1.00 kg of silicate solution per: three are added and homogenized. The water content in the mixture is 38.3%. The shredded mass is placed on a metal-based drying sheets with a layer thickness of 30 mm. After soaking for 5-8 hours, the material is granulated on a cleaning sieve with 10 mm holes. The granulate is again distributed on metal sheets and incubated for about 15 hours at room temperature. The water content in the resulting product is 25-28. weight.%. After re-granulation, the product is kept in a chamber dryer with air circulation for 3-5 hours at 90 ° C until the water content drops to approximately 15% by weight. After continuing to dry on a roller mill, a product with a water content of 8 wt.% B is obtained. Use of prepolymers. The obtained for-polymer with a water content of 8% by weight is ground after mixing with 2.5% by weight of glycerol monostearate as a lubricant for separation from the mold, in a crusher with 5 mm holes. The crushed mass is used directly as a press-mass and pressed at 27ffc and a pressure of 600-700 kg / cmt molded blanks of 60x30x10 mm. molded blanks have good durability of types, heat resistance, non-inflammability and light resistance. PRI me R 4. A. receiving forpolymerv. In a tray mixer with a capacity of 20 liters, 2.36 kg of a 37% aqueous solution of sodium silicate (38 Be, molar ratio N33.0 / 5 i 02.: 3, 3, pH 11, technical product) and 1.15 kg of sodium silicate powder (residue after calcination at 900 ° C 82 wt.%). After the formation of a homogeneous mass, 2.00 kg of sodium silicate solution with 2.00 kg of zinc oxide and 0.03 kg of pigment are added over about 5 minutes, and then homogenized for 10 minutes. After that, approximately 6.20 kg of calcium silicate (milled wollastonite) are added together with 5.00 kg of a solution of 37% sodium silicate within 15 minutes. The water content in the homogenized mixture is 33.0 j.%. Then the mixture is continued to knead at 25-30 ° C for another 25 minutes. The homogenized material is placed on metal driers with a layer thickness of 20 mm. After soaking for about 20 hours, the pulp is granulated on a wiper sieve with 5 mm holes. The water content of the pellets is weight. % The granules are scattered on a conveyor belt of a tunnel furnace with 3 zones, in which the temperatures are 90, 120 and respectively. The ratio of the zone lengths is 2: 1: 1, respectively. The passage rate is then set so that at the end of the furnace a product can be removed in which the water content varies between 4 and 8% by weight, while the product from the middle zone contains about 12-18% by weight of water. The resulting prepolymer with a water content of from 4 to 8 wt.% Is milled in a pin mill, then 1.0 wt. % of zinc stearate and processed directly as a press-mass. Pressing is performed at a pressure of 800-1000 kg / cm and .- The samples made according to GSP 53470 have the following properties: Specific weight, kg / cm 2.65 Compressive strength, MPa, (GSP 53154 ) 365 Brinell MPa hardness, (01N 53456) 420 Impact bending strength, kg / m, (SSHMP 77107) 0.210 Flexural strength of MPa, (UPL 77103) 100 Linear coefficient of thermal expansion. A (CGE 0304) at 25-150 ° С8.5 .10 Approx. A. Getting the fore of lenders In tray mixer capacity. 20 liters of 1.25 kg of sodium silicate powder (residue after calcination at 82 wt.%) And 1.45 kg of deionized water are placed under constant stirring. After suspension for another 15 minutes, another 6.85 kg of sodium silicate powder is gradually added. After the formation of a viscous mass, 0.70 kg of zinc oxide and 0.02 kg of pigment are filled for about 10 minutes. After these substances are evenly distributed, another 1.45 K of deionized water and 0.85 kg of sodium silicate powder are added, to the paste obtained in approximately 10 minutes, doses are added in 10 minutes and followed by stirring for 20 minutes 3.44 kg of silicate calcium (milled wollastonite), and the temperature is between 30 and 45 ° C. The mass is placed on metal drying sheets with a layer thickness of 20 mm. After soaking for 15 hours, the pulverized mass is granulated on a strainer with 5 mm holes. The water content of the granules is 24–26 wt.%. The granulate is poured onto a belt conveyor of a tunnel kiln, which has 3 zones, in which the temperatures are 1 to 90-110 and 140 ° C respectively. The relative length of the zones is 2: 1: 1, respectively. The passage rate is then set so that at the end of the furnace a product can be removed, in which the water content varies between 4 and 6% by weight. As the product from the middle zone contains about 1016% by weight of water. B. Application of prepolymers. The resulting prepolymer with a water content of 4 to 6% by weight is ground after adding 1.0% by weight of zinc stearate in a pin mill and is directly processed. as a press mass. Pressing is performed at a pressure of 800 kg / cm and 250 ° C. Made molded blanks (60x30x10 cm) have high hardness, good impact resistance to bending, absolute incombustibility, as well as high heat and light resistance. Their specific weight is 2.60 g / cm. Example 6. A. Obtaining prepolymers. In a tray mixer with a capacity of 10 liters, 2.30 kg of a 37% aqueous solution of sodium silicate are laid with constant stirring (308%, molar ratio i 3, 3; pH 11 is a technical product and 0.66 kg of sodium silicate powder (residue after calcination at 82% by weight. After the formation of a homogeneous mass, after 10 minutes, another 1.50 kg of sodium silicate solution is added with 1.10 kg of zirconium oxide and homogenized for 10 minutes. Then, approximately, over 15 minutes, add 3, 50 kg of calcium silicate (milled wollastonite) together with a 1.50 kg 37% solution and sodium silicate. The water content in the compound is about 32.5 wt.%. Then the mixture should be mixed for another 25 minutes at 25-30 ° C. The homogeneous material is placed on the metal drying sheets with a layer of IVIM thickness 20. After being held in this position for 18 The dry mass is granulated on a 5 mm thick wiping sieve. The water content in the granules is 15% by weight. The granules are spread on a conveyor belt of a tunnel kiln having 3 zones in which the temperatures are 90, 120 and 150 ° C, respectively. The ratio of the lengths of zones 2: 1: -1, respectively. The passage rate is then set so that at the end of the furnace a product can be sown in which the water content varies between 7 and 8% by weight, while the product from the middle zone contains about 10% by weight of water. The resulting prepolymer with a water content of 7-8 wt.% Is ground after the addition of 1.0 wt.% Zinc stearate in a pin mill, and after that in a ball mill and directly processed as a press mass. Pressing is performed at a pressure of 800-1000 kg / cm and. Manufactured according to GSP 53470, the samples have the following properties: Specific weight, g / cm 2.23 Compressive strength, MPa, (GSP 53454) 86 Brinell hardness, MPa, (D1N 53456) 273 Flexural strength, kg / m ( СШМ 77107) 1,20 Flexural strength, MPa, (СШПМ 77103) 44 Example 7. A. Preparation of prepolymers. In a tray mixer with a capacity of 10 l, 2.20 kg of 37% aqueous solution of sodium silicate (38 ° Be, molar ratio of Na20 / S i 0-2.1: 3.3; pH C) 0 are placed under constant stirring; 64 g of sodium silicate powder (residue after calcination at 82 wt.%). After a homogeneous mass has been formed, approximately 1.50 kg of a solution of sodium silicate with 0.42 kg of magnesium oxide is added over about 15 minutes and homogenized for 10 minutes. Then approximately. For 15 minutes, doses of 3.45 kg of calcium silicate (milled wollastonite) are added along with 1.50 kg of a 37% sodium silicate solution. The water content in the compound is about 33.0 wt.%. Then the mixture is continued to stir for another 25 minutes at 25-30 ° C. The homogenized material is placed on metal drying sheets with a layer thickness of 20 mm. After soaking for 30 hours, the pulp is granulated on a wiper sieve with 5 mm holes. With water retention in the pellet, those are 20 wt.%. The granules are dispersed into a conveyor belt conveyor of a tunnel kiln, which has 3 zones, in which the temperatures are 90, 120 and 150 ° C, respectively. Length ratio zones 2: 1: 1 respectively. The passing rate is then set so that at the end of the furnace a product can be removed in which the water content varies between 8 and 10% by weight, while the product from the middle zone contains about 14% by weight water. The resulting prepolymer with a water content of 9.5 wt.% Is ground after the addition of 1.0 wt.% Zinc stearate in a pin mill and is directly processed as a press machine. Pressing is carried out at a pressure of 800-1000 kg / cm and. Samples manufactured according to GSP 53470 have the following properties: Specific gravity, g / cc 2.17. Compressive strength, MPa, (GSP 53454) 65 Brinell MPa hardness, (D1N 53456) 235 Impact strength under bending, kg / m (SHPM 77107), 0.07 Flexural strength, MPaDSSHPM 77103) 23 Example8. A. Preparation of prepolymers,. A tray mixer with a capacity of 10 liters is placed under constant stirring with 2.20 kg of 37% aqueous paicTBOpa sodium silicate (molar ratio i 0,, 3, pH 11) and 0.64 kg of sodium silicate powder (residue after calcination at 82 wt.%). After a homogeneous mass has been formed, approximately 1.50 kg of sodium silicate solution with 0.70 kg of iron oxide are added over about 10 minutes and homogenized for another 10 minutes. Then, over a period of 15 minutes, doses of 3.45 kg of calcium silicate (milled wollastonite) are added together with 1.50 kg of a 37% sodium silicate solution. The water content in the compound is about 34.0 wt.%. Then the mixture is continued to knead at 25-30 ° C for another 25 minutes. Homogenized material is placed on metal drying sheets with a layer thickness of 20 mm. After soaking for about 20 hours, the dry mass is granulated on a wiping sieve with 5 mm holes. The water content in the pellet is 16 wt.% Granulate is poured onto a belt conveyor of a tunnel kiln having 3 zones, in which the temperatures are 90, 120 and 150 s, respectively. The ratio of the lengths of zones 2: 1: 1, respectively. The passing rate is then set so that at the end of the furnace a product can be removed in which the water content varies between 7 and 8% by weight, while the product from the one zone contains about 10% by weight of water. To the resulting prepolymer with a water content of 7.5% by weight, 1.0% by weight of zinc stearate is added, then spread / spread on a pin mill and processed as a press. Pressing is performed at a pressure of 8001000 kg / cm and. Manufactured according to GSP 53470. The tested samples have the following properties: Specific weight, g / cm 2.55 Compressive strength, MPa, (GSP 53454) 300 Brinell hardness, MPa, (D1N 53456) .380 Bending strength, kg / m (SShPM 77107) 0.16. Flexural strength, MPa, (atsPM 77103) 103 Example 9. A, Preparation of prepolymers. A tray mixer with a capacity of 10 liters is placed under constant stirring, 2.70 kg of 37% aqueous sodium silicate solution (38 ° Be, molar ratio tJa2.0 / S i 3.3 pH 11) and 0.70 kg sodium silicate powder (residue after calcination at 900s 82 wt.%). After a homogeneous mass was formed, another 1.50 kg of sodium silicate solution was added with 1.75 kg of dried iron scrap for 10 minutes (composition of the composition of water to b wt.%) And homogenized for another 10 minutes. Then, within 15 minutes, doses of 3.80 kg of calcium silicate (milled wollastonite) are added together with 1.50 kg of a 37% strength sodium silicate solution. The water content of the compound is about 31.0% by weight. Then the mixture is continued to stir at 25-30 ° C for another 25 minutes. Homogenized material is placed on metal drying sheets with a layer thickness of 20 mm. After soaking for 22 hours, the pulp is granulated on a test tube sieve with 5 mm openings. The water content of the granules is 20 wt.%. The granules are spread onto a belt conveyor of a tunnel furnace, having 3 zones in which the temperatures are 90, 120 and respectively. The ratio of the lengths of zones 2:: 1: 1, respectively. The passage rate is then set so that at the end of the furnace a product can be removed in which the water content varies between 7 and 10% by weight, while the product from the middle zone contains about 17% by weight of water. The resulting prepolymer with an α-water content of 8.0% by weight is ground after adding 1.0% by weight of zinc tearate in a pin mill and is directly processed as raw metal. Pressing is performed at a pressure of 800-1000 kg / cm. The resulting molded blanks also have good mechanical strength. Thus, according to the proposed method, I obtain prepolymers of metal silicates, which can be used to obtain plastics with high mechanical strength. Formula of the invention. A method for producing a metal silicate prepolymer by reacting a metal oxide with a metal oxide in an aqueous medium, followed by heating the product obtained, characterized in that sodium silicate is used as the metal silicate prepolymer forming a material with high mechanical strength. potassium or I mix them with calcium or magnesium silicate with a content of water-soluble silicate of 30-33%, and as a metal oxide is a compound selected from the group including conductive ZnO, MgO, ZrO, Fe-jO, FeoO, and the reaction is carried out at 20 - 30 ° C and- AANII contains water in the initial mixture 10. : 50 wt.% Until the content of water in the reaction mixture is 0.1-25 wt.%, Followed by grinding the resulting product and heating it to. until the water content of the resulting prepolymer is 2-20% by weight. Sources of information taken into account in the examination 1. UK patent number 1077973, cl. C 4, pub. 1967 (prototype) ..
    权利要求:
    Claims (1)
    [1]
    Claim
    A method of producing a metal silicate prepolymer by reacting a metal silicate with metal oxide in an aqueous medium followed by heating the obtained product, characterized in that, in order to obtain a prepolymer for pressmasses 20 forming materials with high mechanical strength, sodium or potassium silicate is used as a metal silicate or a mixture thereof with calcium or magnesium silicate with a water-soluble silicate content of 30-33%, and as a metal oxide - a compound selected from the group consisting of ZnO, MgO, ZrO, Fe ^ Oj, Fe ^ O ^, and the interaction is carried out at 20-30 ° C and · containing 30% water in the initial mixture 10-. h 50 wt.% until the water content in the reaction mixture is 0.1-25 wt.%, followed by grinding the resulting product and heating it to .12'0 ° C 35 until the water content in the resulting prepolymer is 2-20 wt.%.
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    同族专利:
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
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    US3102037A|1957-12-16|1963-08-27|Aerojet General Co|Refractory cement composition|
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    DE1571607A1|1965-05-11|1970-12-23|Kurz Dr Fredrik Wilhelm Anton|Binding or impregnating agent based on water glass|
    DE1671266B1|1967-04-26|1971-06-09|Wasagchemie Ag|Process for the production of glass-like porous moldings|
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    US3990903A|1973-07-23|1976-11-09|Southwest Research Institute|Hydrothermal cement and method of cementing well bores|
    FR2361314B1|1976-08-10|1983-01-28|Southwest Res Inst|AT376444B|1982-06-04|1984-11-26|Drach Johann Ing|METHOD FOR PRODUCING AN ACTIVE SUBSTANCE FOR REDUCING OR. PREVENTION OF FLAMMABILITY OF ORGANIC MATERIALS|
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    NO170626C|1990-05-18|1992-11-11|Norsk Proco As|NON-PROTECTED, WATERPROOF AND ACID RESISTANT PRODUCT|
    CN1036774C|1994-06-03|1997-12-24|广西大学|Preparing method for zinc polysilicate flocculate agent and use|
    GB0125368D0|2001-10-23|2001-12-12|Dutiro Cathbert|Hybrid 01|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    CH1085477|1977-09-06|
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