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WO1996026976A1 - Copolymeres blocs thermoplastiques a proprietes anti-condensation - Google Patents

Copolymeres blocs thermoplastiques a proprietes anti-condensation Download PDF

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Publication number
WO1996026976A1
WO1996026976A1 PCT/US1996/001178 US9601178W WO9626976A1 WO 1996026976 A1 WO1996026976 A1 WO 1996026976A1 US 9601178 W US9601178 W US 9601178W WO 9626976 A1 WO9626976 A1 WO 9626976A1
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WO
WIPO (PCT)
Prior art keywords
cement
group
water
improved
concrete
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US1996/001178
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English (en)
Inventor
David Charles Darwin
Ellis Martin Gartner
Ahmad Arfaei
Xiaojia Zhang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
WR Grace and Co Conn
WR Grace and Co
Original Assignee
WR Grace and Co Conn
WR Grace and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by WR Grace and Co Conn, WR Grace and Co filed Critical WR Grace and Co Conn
Priority to AU49072/96A priority Critical patent/AU4907296A/en
Publication of WO1996026976A1 publication Critical patent/WO1996026976A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00—Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24—Macromolecular compounds
    • C04B24/26—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B24/2617—Coumarone polymers
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00—Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24—Macromolecular compounds
    • C04B24/26—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B24/2652—Nitrogen containing polymers, e.g. polyacrylamides, polyacrylonitriles
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00—Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24—Macromolecular compounds
    • C04B24/26—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B24/2664—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of ethylenically unsaturated dicarboxylic acid polymers, e.g. maleic anhydride copolymers
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00—Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24—Macromolecular compounds
    • C04B24/26—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B24/2688—Copolymers containing at least three different monomers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00—Chemical modification by after-treatment
    • C08F8/30—Introducing nitrogen atoms or nitrogen-containing groups
    • C08F8/32—Introducing nitrogen atoms or nitrogen-containing groups by reaction with amines
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2103/00—Function or property of ingredients for mortars, concrete or artificial stone
    • C04B2103/0045—Polymers chosen for their physico-chemical characteristics
    • C04B2103/0061—Block (co-)polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2800/00—Copolymer characterised by the proportions of the comonomers expressed
    • C08F2800/10—Copolymer characterised by the proportions of the comonomers expressed as molar percentages

Definitions

  • the present invention is directed to an improved hydraulic cement and to cement compositions having the subject improved cement therein.
  • the present invention relates to an improved hydraulic cement composition composed of a mixture of a hydraulic cement and an amino alkoxy derivative of maleic acid polymers, as fully described below, and the hydraulic cement compositions, such as mortar and concrete, capable of exhibiting high flowability and retention of flowability over a sustained period of time without imparting a significant delay in the initial set time of the composition.
  • cement supe ⁇ lasticizers include, for example, compounds, such as naphthalene sulfonate- formaldehyde condensates lignin sulfonates and the like.
  • copolymers of hydroxy-terminated allylether and maleic anhydride and their salt, or ester derivatives, such as disclosed in U. S. Patent 4,471,100, or copolymers of maleic anhydride and styrene which have been partially esterified, as disclosed in U. S. Patent 5,158,996, have been proposed as cement admixtures capable of enhancing slump.
  • the proposed cement admixture does not provide the desired combination of properties or only provides them in low degrees.
  • esterified acrylate copolymers while providing good slump enhancement, causes the treated cement composition to exhibit excessive set retardation.
  • the present invention i ⁇ directed to an improved hydraulic cement and to cement composition formed with said cement, wherein the cement contains an amino alkoxy derivative of maleic acid polymer or copolymers thereof.
  • the polymer can be represented by the general formula
  • R' represents a hydrogen atom or an aryl or substituted aryl group or a C 2 -C 10 (preferably a C 2 -C 4 ) oxyalkylene group, (BO), or a plurality (1-200, preferably from 1 to about 70) of said groups which is terminated with a C,- C 10 alkyl group, C 5 -C 6 cycloalkyl group or aryl group or mixture thereof;
  • X and Y each independently represent NHR', OH, O " M + where M is an alkali metal, or ammonium cation, or X and Y together represent -O ' lvTO - when NT * is an alkalene earth metal cation;
  • R" represents hydrogen atom or methyl group;
  • Z represents unsubstituted or substituted aryl or C 5 -C 6 cycloalkyl or a heterocyclic group or the group OR"', where R'" represents a C,-C 5 alkyl
  • cement compositions formed with the cement admixture of the present invention have been unexpectedly found to exhibit a high degree of slump over a sustained period of time while not having any significant set retardation.
  • the present invention is directed to an improved cement admixture and to cements and cement compositions formed with said cement admixture.
  • the presently described improved cement has been unexpectedly found to provide a cement composition, such as mortar or concrete, having high flowability over an extended period of time without imparting a significant delay in the initial set time of the composition.
  • the presently achieved cement compositions are capable of being readily formed into a desired shape, having substantial self-leveling properties and can be worked over an extended period from commencement of hydration.
  • the present cement composition does not exhibit extensive delay in set and, therefore, does not delay the timetable for forming the desired structure.
  • the improved cement of the present invention is composed of a substantially uniform mixture of an amino alkoxy derivative of maleic acid polymer, as fully described below, and a hydraulic cement.
  • the cement can be selected from any conventional hydraulic cement such as, for example, ordinary portland cement (meeting the requirements of ASTM C-150), high early strength portland cement, ultra high early strength portland cement, blast ⁇ furnace slag cement, fly-ash cement, blended portland cements, calcium aluminate cements, calcium sulfate cements, magnesium phosphate cements and the like.
  • the amino alkoxy derivative of maleic acid polymers and copolymers thereof have been unexpectedly found to provide an improved cement product and resultant cement composition.
  • the subject polymer of the present invention can be represented by the formula
  • R' represents a hydrogen atom or substituted or unsubstituted aryl group or a C 2 -C
  • X and Y each independently represent NHR', OH, O ' M + where M is an alkali metal or ammonium cation, or X and Y together represent -O ' JVTO - when NT * is an alkalene earth metal cation;
  • R" represents hydrogen atom or methyl group;
  • Z represents unsubstituted or substituted aryl or C 5 -C 6 cycloalkyl or a heterocyclic group or the group OR'", where R'" represents a C,-C 5 alkyl or C 5 -C 6 cycloalkyl group; and a, b and c each represent molar percentages of the polymer's structure such that in a particular polymer a has a value of 0 to 100 (preferably at least about 2), b has a value of from 0 to 100, the sum of a plus b is from about 20 to 100, and c has a value of from 0 to 80.
  • the subject formula can further contain small amounts (up to about 10%, preferably up to about 5%) of other ethylenically polymerizable units, such as acrylonitrile, butadiene, acrylamide, acrylic acid, acrylic acid ester of alkanols and ether alcohols, and the like.
  • other ethylenically polymerizable units such as acrylonitrile, butadiene, acrylamide, acrylic acid, acrylic acid ester of alkanols and ether alcohols, and the like.
  • the initial polymer may be a homopolymer of maleic anhydride or may be a copolymer of maleic anhydride and at least one other group (c) which is present in a molar ratio of from 5:1 to 1 :5, preferably from 1 :1 to 1 :4, provided there is sufficient maleic anhydride units present to be derivatized, as described below, and provide a water soluble resultant polymer.
  • the initial maleic anhydride polymers found useful herein are low molecular weight polymers. They should be selected so that the resultant derivatized polymer has a number average molecular weight of from about 1,000 to 100,000, preferably from about 1,500 to 50,000 most preferably 5,000 to 30,000.
  • the maleic anhydride polymer precursor of both homopolymer and copolymer character, are formed by conventional free radical polymerization.
  • the derivatized maleic acid polymer is formed by reacting the maleic anhydride polymer precursor with ammonia or an alkyl (preferred), cycloalkyl or aryl terminated alkoxy amine or aniline or substituted aniline, such as sulfanilic acid and the like.
  • an alkoxy amine is used as a reactant, the imidization may be carried out neat, as the maleic anhydride polymers are normally soluble in the amines. It is preferred to commence the reaction in the presence of small amounts of water as a solvent when the polymer has low solubility in the amine reactant.
  • the amine reactants found useful in forming the desired derivatized maleic acid polymer can be selected from ammonia, unsubstituted or substituted aniline, or an alkyl-terminated alkoxy amine (preferred) represented by the formula:
  • BO represents a C 2 -C, 0 (preferably a C 2 -C 4 ) oxyalkylene group
  • O represents an oxygen atom and B represents a C 2 -C 10 (preferably C 2 -C 4 ) alkylene group or mixture; and R"" represents a C r C, 0 (preferably C,-C 4 ) alkyl group and n is an integer selected from 1 to 200 preferably from 1 to 70.
  • the precursor polymer and amine reactant form the desired derivatized maleic acid polymer by heating the reactants either in a common solvent or neat at elevated temperatures of from about 100'C to 250 ° C preferably from 170 ° C to 200°C under ambient pressure or, under a pressure lower than ambient pressure with removal of water. Further, when the reaction is carried out under ambient or substantially ambient pressure it is preferred to pass air or nitrogen gas over the liquid reaction medium or by bubbling the gas through the medium to remove water and other low molecular weight by-products from the reaction zone.
  • the preferred imidized derivative of maleic acid polymer (where "a" of the polymer formula is a positive integer, most preferably at least about 2) is formed by carrying out the above reaction at elevated temperatures of 170°C to 200°C under anhydrous conditions.
  • the amine reactant is normally used in from about 5 to 100 molar equivalence and preferably from 10 to 40 molar equivalence based on the maleic acid units available in the precursor polymer.
  • the imidization reaction can be enhanced by conducting the reaction in the presence of a basic catalyst, an acid catalyst and/or a transamidation catalyst.
  • a basic catalyst such as dicyclohexylamine, 1,1,3,3- tetramethylguanidine, 1,3-diphenylguanidine, quinoline, isoquinoline, 4- benzylpyridine, 4-phenylpyridine, 2,3-benzodiazine, 1,4-benzodiazine, 1-benzazine, 1,3-benzodiazine, N,N'-dicyclohexyl-carbodiimide, 2,2'-bipyridyl, 2,3'-bipyridyl, 2,4'-bipyridyl or such catalyst can be selected from the group consisting of HC1, Sb 2 O 3 , Ti-(OC 4 Ho) 4 , NaNH 2 , SnO 2 , potassium or sodium alkoxides, manganese acetate,
  • the reactants are contacted with each other at the above described reaction conditions for from about 1 to 8 hours and preferably from about 1 to 2.5 hours.
  • water a by-product is removed to drive the reaction to imidization.
  • the derivatized maleic acid polymers may also be formed by initially reacting maleic anhydride with the amine reactant described above to produce an amino alkoxy derivative of maleic acid.
  • This derivatized material is then copolymerized with monomeric units capable of forming units (c) in the presence of an effective amount of a vinyl polymerization catalyst, such as a redox catalyst system or a free radical catalyst.
  • a vinyl polymerization catalyst such as a redox catalyst system or a free radical catalyst.
  • maleic anhydride can be reacted with an alkyl terminated alkoxyamine of Formula II at temperatures of from about 40 to 200°C. The higher temperature of from about 120-200°C is normally accompanied by removal of water.
  • the resultant maleic acid derivative is then mixed with a second monomer such as N-vinyl pyrrolidone, in the presence of a polymerization catalyst such as free radical catalysts of azobisisobutyronitrile, dibenzoyl peroxide, lauroyl peroxide and the like or redox catalyst systems such as sodium bisulfite, ascorbic acid, hydrogen peroxide and the like.
  • a polymerization catalyst such as free radical catalysts of azobisisobutyronitrile, dibenzoyl peroxide, lauroyl peroxide and the like or redox catalyst systems such as sodium bisulfite, ascorbic acid, hydrogen peroxide and the like.
  • the free radical polymerization should be done using catalyst capable of causing polymerization at temperatures of from about 40°C to 140°C.
  • the amino alkoxy derivative of maleic acid polymer is most preferably formed from a homopolymer of maleic acid or copolymers thereof having from at least about 5 to about 100 molar equivalence of -(BO) n R" units and preferably from about 10 to 40 molar equivalents based on the maleic acid units of the polymer and that B represents ethylene or propylene units or mixtures thereof.
  • the most preferred comonomeric units are methyl vinyl ether, styrene, sulfonated styrene, and N-vinyl pyrrolidone.
  • the resultant polymer of Formula I is normally a high-boiling viscous liquid which is substantially soluble in water.
  • the improved cement of the present invention is composed of a substantially uniform mixture of a hydraulic cement and the derivatized maleic acid polymer of Formula I, which are both described herein above.
  • the polymer should be present in from 0.005 to 5 (preferably from 0.03 to 1 and most preferably from 0.05 to 0.3) weight percent based on the weight of hydraulic cement.
  • the polymer can be mixed with the cement as an aqueous solution having from about 20 to 50 weight percent of the subject polymer solids in the solution.
  • the polymer treated cement can be formed at any stage of the cement's formation or use.
  • the polymer can be mixed at the cement mill with clinker cement raw material during its grinding to form cement powder. It can also be applied to the cement powder during its blending with other dry materials to prepare a specific type of cement, such as blended cement, pozzolanic cement and the like.
  • the improved cement can be formed in situ during the course of preparing a cement composition, such as a mortar mix (hydraulic cement, sand and water) or a concrete (hydraulic cement, sand, large aggregate, such as stone, and water).
  • the instant derivatized maleic acid polymer can be added (conventionally as an aqueous solution) as part of the water of hydration or can be added separately.
  • the water of the aqueous polymer solution should be calculated as part of the total water content of the cement composition.
  • the water to cement ratio (w/c) should be from about 0.3 to 0.7 and preferably from about 0.35 to 0.5.
  • the present polymer has been found capable of imparting a high degree of fluidity to an unset cement composition for sustained periods of time or, alternately, can be used to maintain the same slump as an untreated cement composition while permitting reduction in the w/c ratio to thus provide a stronger set cement composition structure or a combination of the above features.
  • the derivatized maleic polymer of the improved cement (whether as a dry blend of cement and polymer or as formed in situ as part of the formation of a wet unset cement composition) should be from 0.005 to 5, preferably from 0.03 to 1 and most preferably from 0.05 to 0.3 weight percent of solid polymer based on the weight of solid hydraulic cement of the cement composition.
  • cement compositions formed with the present improved cement have a significantly higher degree of flowability (higher degree of slump), than compositions formed with conventional hydraulic cement. Further, the present cement compositions are capable of retaining their high degree of slump over a sustained period of time giving the artisan an extended period to work the cement composition into its final shape. Finally, the present cement composition can achieve initial set without exhibiting excessive retardation. Thus, the use of this cement composition does not cause delay of the working time required to form a particular structure.
  • Conventional cement additives such as air entrainers, water proofing agents, strength enhancers, corrosion inhibitors, antifoaming agents and curing accelerators can be used with the subject cement additive. These additives can be mixed with the cement composition prior to, along with or subsequent to the addition of the present cement additive.
  • MAO A methoxy terminated polyalkoxy amine
  • Example 2 Using the procedure detailed in Example 1 , a series of derivatized copolymers were synthesized using various mole ratios of the maleic anhydride-methyl vinyl ether copolymer to the methoxy terminated polyoxyalkylene amine having a molecular weight of 2000. The resulting products were isolated as viscous liquids ("Polymers 2A, 2B, 2C").
  • Each of the polymers formed in Examples 1 and 2 above was formed into 50% aqueous solutions with deionized water. Each of these solutions was used in forming a cement composition composed of standard hydraulic portland cement and water. The polymer to cement weight ratio (solid polymer/solid cement, s/s) was 0.002 and the water to cement ratio was 0.48.
  • cement compositions were made with no polymeric admixture (blank) and with a conventional concrete supe ⁇ lasticizer agent, naphthalene sulfonate formaldehyde condensate ("NSFC") in dosages set forth in Table I.
  • NFC naphthalene sulfonate formaldehyde condensate
  • Example 1 1:0.31 0.2 22.1 22.4 22.7 22.7 20.7 422
  • Example 2A 1:0.375 0.2 21.0 21.5 21.9 21.1 19.2 396
  • Example 2B 1:0.25 0.2 22.0 22.3 22.2 22.3 21.3 438
  • Example 2C 1:0.10 0.2 18.0 17.5 16.0 15.0 14.0 322
  • a series of derivatized copolymers were formed by reacting a copolymer of styrene and maleic anhydride (1:1, SMA 1000, AtoChem) with three different methoxy terminated polyalkoxyamine materials of number average molecular weights 700, 1000, and 2000 having ethylene oxide to propylene oxide ratios of 13:2, 19:3, and 32:10 respectively (Jeffamines M-715, M-1000, and M-2070, respectively, Texaco). In each instance, the mixture was stirred under nitrogen and heated to 180°C for 1 hour with removal of water. Upon completion of the heating, homogeneous viscous liquids were formed, which were water-soluble on cooling to room temperature. Syntheses were performed using each of the three molecular weight methoxy terminated polyalkoxyamine materials at various ratios with respect to maleic anhydride. These products were used as cement fluidizers in Example 5 below.
  • Example 4 The reaction products of Example 4 were tested in cement compositions in the same manner as described in Example 3 above. Results of these tests are shown in Table II.
  • a second solution was formed by mixing 1360 parts water with 6480 parts of a 50% aqueous NaOH solution and 3969 parts maleic anhydride. This solution was then added to the above initially formed solution.
  • N-vinylpyrrolidone N-vinylpyrrolidone
  • MA maleic acid salt
  • MAJ maleic acid half sodium salt-half amide adduct of Jeffamine M-1000
  • An amino alkoxy derivative of maleic acid was formed in a similar manner to that described in Example 6 above.
  • the initial solution was formed by mixing 1840 parts water with 788 parts sulfanilic acid and then adding simultaneously 394 parts maleic anhydride and 322 parts of 50% aqueous solution of sodium hydroxide at a rate to maintain a temperature of 30-35°C.
  • a second solution was formed in which 250 parts of Jeffamine M-1000 was mixed with 859 parts water to which 24.7 parts maleic anhydride and 202 parts of 50% aqueous sodium hydroxide solution were simultaneously added.
  • the second solution was combined with the first solution.
  • the resultant solution had a polymer content of 30% and its pH was adjusted to 7 with addition of 50% sodium hydroxide solution. (Solution VILA)
  • N-vinyl pyrrolidone N-vinyl pyrrolidone
  • MAJ maleic acid- Jeffamine M-1000 half amide reaction product
  • MAS maleic acid-sodium salt, sulfanilic acid half amide adduct
  • a concrete mix was formed in the same manner as described above except the W/C ratio was 0.51.
  • the admixture polymers of Examples 6 and 7 were used in a dosage of 0.15% polymer based on solid cement of the concrete mix.
  • Table VI show that very high slump is achieved along with good air and compressive strength while the set time is not excessively retarded.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

Ciment hydraulique amélioré et compositions de ciment hydraulique dans lequel se trouve dispersé uniformément un polymère ou un copolymère à base d'un dérivé alkoxyaminé de l'acide maléique à terminaison alkyle.
PCT/US1996/001178 1995-02-27 1996-01-25 Copolymeres blocs thermoplastiques a proprietes anti-condensation Ceased WO1996026976A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU49072/96A AU4907296A (en) 1995-02-27 1996-01-25 Thermoplastic block copolymer with inherent anti-fog properties

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US39540595A 1995-02-27 1995-02-27
US08/395,405 1995-02-27

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WO1996026976A1 true WO1996026976A1 (fr) 1996-09-06

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010003867A1 (fr) * 2008-07-08 2010-01-14 Huntsman International Llc Dispersant destiné à disperser de la matière comprenant du gypse

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5223129A (en) * 1975-08-14 1977-02-21 Nippon Zeon Co Moistureereducing agent for cement compound
SU1070126A1 (ru) * 1981-05-05 1984-01-30 Научно-Исследовательский Институт Бетона И Железобетона Госстроя Ссср Бетонна смесь
JPS60191043A (ja) * 1984-03-09 1985-09-28 日本ゼオン株式会社 セメント用混和剤
US4662942A (en) * 1983-08-01 1987-05-05 Idemitsu Petrochemical Co., Ltd. Cement additives
EP0306449A2 (fr) * 1987-08-28 1989-03-08 Sandoz Ag Copolymères de styrène et de demi-esters de l'acide maléique, et application comme fluidifiants du ciment
US5134188A (en) * 1990-04-04 1992-07-28 Bayer Aktiengesellschaft Aqueous solutions or dispersions of hydroxy-functional copolymers and a process for their production
US5432212A (en) * 1993-04-05 1995-07-11 W. R. Grace & Co.-Conn. Dispersant composition for cement having excellent property in inhibition of slump-loss
US5476885A (en) * 1989-07-25 1995-12-19 Nippon Shokubai Co., Ltd. Cement additive, method for producing the same, and cement composition

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5223129A (en) * 1975-08-14 1977-02-21 Nippon Zeon Co Moistureereducing agent for cement compound
SU1070126A1 (ru) * 1981-05-05 1984-01-30 Научно-Исследовательский Институт Бетона И Железобетона Госстроя Ссср Бетонна смесь
US4662942A (en) * 1983-08-01 1987-05-05 Idemitsu Petrochemical Co., Ltd. Cement additives
JPS60191043A (ja) * 1984-03-09 1985-09-28 日本ゼオン株式会社 セメント用混和剤
EP0306449A2 (fr) * 1987-08-28 1989-03-08 Sandoz Ag Copolymères de styrène et de demi-esters de l'acide maléique, et application comme fluidifiants du ciment
US5476885A (en) * 1989-07-25 1995-12-19 Nippon Shokubai Co., Ltd. Cement additive, method for producing the same, and cement composition
US5134188A (en) * 1990-04-04 1992-07-28 Bayer Aktiengesellschaft Aqueous solutions or dispersions of hydroxy-functional copolymers and a process for their production
US5432212A (en) * 1993-04-05 1995-07-11 W. R. Grace & Co.-Conn. Dispersant composition for cement having excellent property in inhibition of slump-loss

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010003867A1 (fr) * 2008-07-08 2010-01-14 Huntsman International Llc Dispersant destiné à disperser de la matière comprenant du gypse

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