• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The clarification of a sodium aluminate liquor in the Bayer Process, especially the liquor obtained by Kelly filter filtration of the supernatant from the primary settling stage, is improved by flocculation with a polymer of the formula CH2 = C (R<1>)CONHR<2>NR<3>R<4> wherein R<1> is hydrogen or methyl, R<2> is straight or branched chain C2-8 alkylene having at least 2 carbon atoms in the backbone and R<3> and R<4> are independently selected from C1-4 alkyl.
    公开号:SU1604152A3
    申请号:SU874202242
    申请日:1987-03-27
    公开日:1990-10-30
    发明作者:Родни Филд Джон；Мэри Муди Джиллиан；Кейт-Хантер Тревор
    申请人:Эллайд Коллоидс Лимитед (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to the production of alumina and can be used to separate solid particles suspended in aqueous liquors of the Bayer process,
    The purpose of the invention is to increase the efficiency of the process.
    The following polymers were tested in accordance with the present invention.
    A - homopolymer MARTAS (chlorinated-3-me takrylamidopropyltrim ethyl) ammonium), obtained by gel polymerization, with a characteristic viscosity of 5.1 dl / g;
    B - copolymer MARTAS and AST (acrylamide) with a ratio of 70 monomers:
    : 30 with a characteristic viscosity of 5.0 dl / g;
    С - copolymer MARTAS and Ast with a monomer ratio of 95: 5, obtained by reverse phase polymerization followed by azeotropic distillation with a characteristic
    bone 4.7 dl / g;
    D. - sodium polyacrylate.
    Example 1 To immitate the VIY production of alumina, Bayer prepared a suspension of 20 g / l kaolin in a 200 g / l sodium hydroxide solution. After sedimentation of the suspension 500 ml of supernatant with a turbidity of 20 NTU and a suspended particle content of less than 0.3 wt.%
    O) O 4
    JV Yu
    but
    cm
    stirred in a high beaker with a capacity of 600 ml, treated with the test flocculant A and subjected to vigorous stirring. After 2 minutes, the rotation speed of the stirrer was reduced and the stirring continued for another 15 minutes. During this time, stirring was stopped after 5, 10, and 15 minutes, the suspension was allowed to settle, and the turbidity of the supernatant was determined.
    In this case, the following results were obtained (Table 1).
    EXAMPLE 2. The process is carried out analogously to example 1 with flocculus B, and the following results were obtained (Table 2).
    Example 3 The process was carried out in the same manner as in Example 2, but the liquid temperature was 90 ° C. The results obtained are shown in Table 3.
    EXAMPLE 4 The process was carried out in the same manner as in the case of Example 3, with stirring for 10 minutes, using MAPTAC homopolymer and copolymers with different values of intrinsic viscosity. The results are shown in Table 4, in which the amounts of MAPTAS are indicated in% by weight,%, and the rest falls on polymers derived from acrylamide. The turbidity without the addition of a polymer was 20 NTU.
    The obtained results illustrate the advantage of the proposed method from the point of view of the size of the flakes, and consequently, the potential possibility of increasing the filtration rate when using MAPTAC copolymers with polyacrylamide,
    Example 3, the suspension was prepared and precipitated in the same manner as described in example 1. In the case where no copolymer was added, filtration continued for 32 seconds. When various copolymers were added (see Table 4) in an amount of 0.1–1 mg / l to the supernatant, the filtration time decreased by about 10 seconds or more,
    A sample, a 50% suspension. In an oil of copolymer 95% MAPTAC and 5% acrylamide with a characteristic viscosity of 4.7 was prepared by reverse phase polymerization followed by azeo
    0
    five
    0
    five
    0
    five
    0
    five
    0
    five
    hard rectification. The resulting product is designated as polymer K,
    A suspension of 10 g / l of kaolin in a solution of sodium hydroxide 200 g / l was prepared and then intensively mixed with a laboratory mixer for 10 minutes with polymer C, then product D was added to the suspension (sodium polyacrylate in an amount of 0.5 mg / l, continued vigorous stirring for another minute, and then the rotation speed of the agitator was reduced and the mixture was stirred at a low rotation speed for 15 minutes. The product was then allowed to stand and the turbidity of the supernatant was determined, I
    Products D and C were added after precipitation. The results are shown in tabLo5, in which turbidity before means turbidity when polymers D and C were added before, and turbidity after when they were added after precipitation.
    The above data is clearly il-. .. lyustruttot is an advantage achieved when using the proposed copolymer, in particular, gris, adding it before sedimentation.
    The proposed polymers have a high molecular weight, usually at least 500,000 and, as a rule, less than 30 million. The intrinsic viscosity should be at least 1, preferably at least 3 dl / g. Although it may be up to 30 dl / g, it usually does not exceed 8 or 10 dl / g. Good results are obtained with a viscosity of 4.5-8 dl / g, but results are often achieved when its values are г 5 dl / g,
    In accordance with the present invention, polymers can be prepared. by conventional methods, for example, by gel polymerization in an aqueous medium followed by drying and grinding or reverse phase polymerization, which is often followed by a stage of azeotropic distillation with the formation of a stable suspension of the polymer in a non-aqueous medium or a dry polymer layer, which is separated from the non-aqueous medium. It is often preferred to obtain a polymer in the form of a stable suspension of small (for example, less than 4 microns in size) particles in an oily liquid by means of a reverse phase 51
    after which azeotropic distillation is usually carried out,
    The resulting polymer can then be added to a solution of sodium aluminate in the usual manner, for example, as a diluted solution, obtained by dissolving the solid polymer in water or mixing with water a suspension of the polymer obtained by reverse phase polymerization, often in the presence of an emulsifier to obtain suspensions in water.
    This invention can be used to separate suspended solid inorganic particles from sodium aluminate solutions of any origin. In practice, the pH of such solutions is usually higher than 11, usually 13, for example 13.5, and more often not less than 14. The advantage of the proposed method is that it is quite effective even at liquid temperature, for example, at - re more than 60, and often above .80 С, Usually the treated liquid has a temperature of at least 95 ° С. Satisfactory results can be obtained at temperatures
    up to 115 C or higher temperatures,
    The sodium aluminate solution can be any such solution formed during the production of aluminum by the Bayer method, which must be cleaned of suspended solids in the suspended state. Preferably, however, this should be a suspension formed during leaching of bauxite with hot sodium hydroxide, followed by (if necessary) dilution. Red slurry is then separated from this suspension by primary sedimentation and washed once or several times. The liquid that is separated after the first settling, which usually contains less than 0.3 mass% of suspended solid inorganic particles, to further reduce their content and increase the transparency of the solution. subjected to filtration under pressure. The use of the polymer in accordance with the present invention is accomplished at this stage, thereby accelerating the phosphorus to a transparent solution with a low solids content.
    5 0 5 About
    The proposed method can be carried out by adding the polymer to the liquid after the primary precipitation stage, and conventional anionic or non-ionic flocculants can be used, such as
    five
    0
    45
    50
    55
    starch or sodium polyacrylate. However, good, and in many cases excellent, results can be obtained in this case, if the polymer is added before the primary precipitation stage. Although the separation of solid particles can be achieved by using a polymer as the only flocculant, one. . However, it is desirable to accelerate it by using the one specified in combination with a conventional ionic or anionic flocculant. Optimum results are achieved when a quaternized polymer is added first, and then anionic flocculus anionic nly is added. Suitable flo- ntami molecules that can be used in kombinatszta with the cationic polymer include starch and water soluble, synthetic polymers, e.g. go- mopolimery or copolymers of acrylic or methacrylic acid, or other carboxylic or sulfonic etilennenasshhennyh (obgano as a sodium or other water soluble salts), or sulfomethylated acrylamides.
    Filtration under pressure, as a rule, is carried out using Kelly filters, and the resulting filtrate is usually sent to the stage of precipitation of the AlHiNiO hydroxide from it.
    The proposed method makes it possible to increase the efficiency of the suspension thickening process.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    1, A process for thickening pshama, including treating the suspensions obtained in the Bayer process with water-soluble synthetic anionic and cationic flocculants, followed by separating the liquid phase from the solid phase, characterized in that, in order to increase the efficiency of the process, the polymer 3 is used as a cationic flocculant. -methacrylate-amidopropyltrimethyl ammonium or its copolymer with acrylamide, containing at least 25 wt.% of chloride units
    3-methacrylamidopropyltrimethyl ammonium, with cationic floc nt. taken with a characteristic viscosity of 2.9-10.5 dl / g and mol.Mo 500,000 - 30,000,000.
    2, the method according to claim 1, differing from that by the fact that the cationic flocculant is introduced into the suspension before the introduction of the anionic flocculant.
    3, the method according to ppp and 2, that is, so that after the introduction of the anionic frokulta, sedimentation of suspended solids is carried out followed by filtration of the liquid under
    pressure, g
    4, Method according to claims, 1 and 3, that is, that cationic flocculant is introduced before precipitating suspended solid particles with anionic flocculant .5. The method according to claims 1 and 3 , that is, after the cationic flocculating agent is introduced after sedimentation, suspended solid particles with anionic flocculant are introduced before the filtration stage.
    6. The method according to claim 1, in contrast to the fact that the cationic flocculant is added to the sodium aluminate solution containing less than 0.3% of suspended inorganic solid particles, after which the filtration is carried out under pressure.
    7. The method according to claims 1, 3 and 6, which means that the pressure filtration is carried out on a Kelly filter.
    8. Method no. Nl, o t; L and h and y and with the fact that the solution has a temperature of at least 60 ° C and a pH of at least 13..
    Table 1
    NTU - nephelometric determination of turbidity.
    Table 2
    T a b l and c a 3
    Redak, Tor A. Dolynich
    Will make ep N, Tselikova
    Tehred M.DidykKorrektor T. Malets
    Order 3395
    Circulation 410
    VNIIPI State Committee for Inventions and Discoveries at the State Committee on Science and Technology of the USSR 113035, Moscow, Zh-35, Raushsk nab. D. 4/5
    Production and publishing plant Patent, Uzhgorod, st. Gagarin, 101
    Table
    Table3
    Subscription
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    同族专利:
    公开号 | 公开日
    EP0232302B1|1989-09-20|
    JPS63500589A|1988-03-03|
    AU578544B2|1988-10-27|
    US4789485A|1988-12-06|
    HUT43012A|1987-09-28|
    CA1251917A|1989-04-04|
    WO1987000825A1|1987-02-12|
    DE3665702D1|1989-10-26|
    EP0232302A1|1987-08-19|
    BR8606788A|1987-10-13|
    HU199352B|1990-02-28|
    GB8519107D0|1985-09-04|
    AU6139286A|1987-03-05|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3023162A|1956-04-10|1962-02-27|Rohm & Haas|Dewatering aqueous suspensions with quaternized dialkylaminoalkyl acrylates or methacrylates|
    JPS5322938B2|1973-12-27|1978-07-12|
    US4137164A|1976-10-26|1979-01-30|American Cyanamid Company|Process for clarifying iron ore slimes|
    US4396752A|1977-05-16|1983-08-02|Societe Francaise Hoechst|Strong cationic polyelectrolytes in powder form based on acrylamide and quaternized or salified dimethylaminoethyl acrylate for flocculation of solid material suspensions and coalescence of emulsions|
    US4160731A|1978-04-18|1979-07-10|American Cyanamid Company|Process for dewatering sewage sludges disinfected with lime|
    US4275042A|1980-01-22|1981-06-23|Alcan Research And Development Limited|Removal of oxalate from Bayer process liquor|
    NZ201950A|1981-11-27|1984-12-14|Buckman Labor Inc|Water-soluble quaternary ammonium graft copolymers and uses therefor|
    US4545902A|1984-09-17|1985-10-08|Nalco Chemical Company|Flocculants for bauxite |
    US4578255A|1984-12-27|1986-03-25|Kaiser Aluminum Chemical Corporation|Purification of Bayer process liquors|
    US4678584A|1985-06-20|1987-07-07|Cx/Oxytech, Inc.|Method of removing heavy metal from wastewater streams|
    KR100799605B1|2006-05-04|2008-01-30|제일모직주식회사|Resin Composition Having Good Scratch Resistance|US4717550A|1986-10-09|1988-01-05|American Cyanamid Company|Process for purifying alumina|
    AU627469B2|1988-07-18|1992-08-27|Allied Colloids Limited|Recovery of alumina from bauxite|
    GB8824176D0|1988-10-14|1988-11-23|Allied Colloids Ltd|Recovery of alumina from bauxite|
    DE3909005A1|1989-03-18|1990-09-20|Basf Ag|USE OF NON-HYDROLYZED N-VINYLFORMAMIDE UNITS CONTAINING COPOLYMERISES AS FLAKING AND TEMPERATURES|
    DE4039053A1|1990-12-07|1992-06-11|Henkel Kgaa|POLYGLYCERINE IN THE BAYER PROCESS|
    US5133874A|1990-12-24|1992-07-28|American Cyanamid Company|Removal of humate from bayer alumina liquors|
    US5091159A|1991-06-10|1992-02-25|Nalco Chemical Company|Use of dextran as a filtration aid for thickener overflow filtration in Kelly filters in the Bayer process|
    US5368745A|1993-09-02|1994-11-29|Cytec Technology Corp.|Method of flocculating low metal oxide content solids in a liquid|
    US6077486A|1999-03-25|2000-06-20|Cytec Technology Corp.|Process for purifying alumina by mixing a Bayer process stream containing sodium aluminate with amidoxime polymer to reduce the level of iron|
    DE10119685A1|2001-04-20|2002-10-24|Stockhausen Chem Fab Gmbh|Removing water-insolubles from aqueous metal solution, e.g. in production of aluminum oxide by the Bayer process, involves adding water-soluble cationic polyelectrolyte based on dimethylaminopropyl-acrylamide|
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    US10427950B2|2015-12-04|2019-10-01|Ecolab Usa Inc.|Recovery of mining processing product using boronic acid-containing polymers|
    US20200031683A1|2018-07-27|2020-01-30|Solenis Technologies, L.P.|Systems and methods for alumina production|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB858519107A|GB8519107D0|1985-07-29|1985-07-29|Flocculation process|
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