WO2000044487A1 - Sugar derivative composition for modifying properties of cement and cementitious compositions and processes for manufacturing same - Google Patents
Sugar derivative composition for modifying properties of cement and cementitious compositions and processes for manufacturing same Download PDFInfo
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- WO2000044487A1 WO2000044487A1 PCT/US2000/001834 US0001834W WO0044487A1 WO 2000044487 A1 WO2000044487 A1 WO 2000044487A1 US 0001834 W US0001834 W US 0001834W WO 0044487 A1 WO0044487 A1 WO 0044487A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/32—Polymers modified by chemical after-treatment
- C08G65/329—Polymers modified by chemical after-treatment with organic compounds
- C08G65/331—Polymers modified by chemical after-treatment with organic compounds containing oxygen
- C08G65/3311—Polymers modified by chemical after-treatment with organic compounds containing oxygen containing a hydroxy group
- C08G65/3314—Polymers modified by chemical after-treatment with organic compounds containing oxygen containing a hydroxy group cyclic
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
-
- 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
- C04B24/10—Carbohydrates or derivatives thereof
-
- 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
- C04B24/12—Nitrogen containing compounds organic derivatives of hydrazine
-
- 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
- C04B24/28—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C04B24/32—Polyethers, e.g. alkylphenol polyglycolether
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/32—Polymers modified by chemical after-treatment
- C08G65/329—Polymers modified by chemical after-treatment with organic compounds
- C08G65/333—Polymers modified by chemical after-treatment with organic compounds containing nitrogen
- C08G65/3332—Polymers modified by chemical after-treatment with organic compounds containing nitrogen containing carboxamide group
- C08G65/33327—Polymers modified by chemical after-treatment with organic compounds containing nitrogen containing carboxamide group cyclic
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- 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
- C04B2103/40—Surface-active agents, dispersants
- C04B2103/408—Dispersants
Definitions
- This invention relates to dispersing particles using a compound comprising a residue of a sugar or sugar derivative linked by an amine, amide, imide, or urea group to a non-sugar substituent comprising one or more alkyl, aryl, alkylaryl, oxyalkylene, or polyoxyalkylene groups, or a mixture thereof.
- the particles to be dispersed may be inorganic (e..g, calcium carbonate) and include hydratable cementitious binders such as Portland cement. More particularly, the invention involves methods for making the compounds, and methods for modifying properties of cementitious compositions.
- additives have been proposed to increase the flowability, or "slump," in cement compositions such as mortar and concrete, without increasing the water content of the initially formed compositions.
- Such additives or admixtures are classified as chemical “superplasticizers” or “water reducers,” and include compounds such as naphthalene sulfonate formaldehyde condensates, lignin sulfonates, and the like.
- Yamamoto et al. disclosed a concrete water reducer comprising a salt of naphthalenesulfonic acid-formaldehyde condensate and a gluconate-ethylene oxide adduct. This was said to offer high water-reducibility, to prevent deterioration of the concrete due to change of slump over time, and to avoid a set retarding effect that would hinder initial strength.
- a cement dispersing composition comprising a salt of naphthalenesulfonic acid-formalin condensate, a cement setting retarder such as an alkylene oxide adduct of a carboxycarboxylic acid or polyhydroxy compound (e.g., oxyalkylene adduct of gluconic acid), and an ester of glycol or glycerin and/or C 6 or lower aliphatic mono- or polycarboxylic acid.
- a cement setting retarder such as an alkylene oxide adduct of a carboxycarboxylic acid or polyhydroxy compound (e.g., oxyalkylene adduct of gluconic acid)
- an ester of glycol or glycerin and/or C 6 or lower aliphatic mono- or polycarboxylic acid e.g., oxyalkylene adduct of gluconic acid
- compositions of the invention comprise a binder and a compound having a residue of a sugar or sugar derivative linked by an amine, amide, imide, or urea group to a non-sugar substituent comprising one or more alkyl, aryl, alkylaryl, oxyalkylene, polyoxyalkylene groups, or a mixture thereof.
- cementitious composition will encompass compositions having a binder (cement, other cementitious binders); optionally po2-zolans, slag, clay, etc.; and at least one compound (whether termed an “additive” or “admixture” is not critically important) for modifying a property of the cementitious composition.
- An exemplary compound of the invention for use in modifying cementitious (or other particle-containing compositions) thus comprises: (A) at least one residue of sugar or sugar derivative; (B) at least one non-sugar substituent, such as an alkyl group (preferably one C j -Cg alkyl group, substituted or unsubstituted, per sugar residue in component (A)), an aryl or alkylaryl group (preferably having one C 6 -C 8 aryl or alkylaryl substituted or unsubstituted group per sugar residue in component (A)), and/or an oxyalkylene or polyoxyalkylene oligimer or polymer group (e.g., preferably having repeating C 2 -C 4 oxyalkylene groups, or, more preferably, repeating ethylene oxide and propylene oxide groups, wherein the number of repeating units is 2-200); and (C) a linking group comprising an amide, amine, imide, urea, or mixture thereof, for linking the sugar residue of
- Exemplary sugar residues of component (A) may be derived from hydroxycarboxylic acids such as aldonic acid (e.g., gluconic acid, heptogluconic acid), aldaric acid (e.g., glycaric acid, heptoglucaric acid), and uronic acid (e.g., glucuronic acid, heptoglucuronic acid), or their salts or their lactones (i.e. anhydrides); or may also be derived from aldoses or sugars (e.g., monosaccharides such as glucose, disaccharides such as sucrose, etc.), including corn syrup and molasses and their oxidized forms which could also serve as substrates for gluconamide formation.
- aldonic acid e.g., gluconic acid, heptogluconic acid
- aldaric acid e.g., glycaric acid, heptoglucaric acid
- uronic acid e.g., glu
- Exemplary non-sugar substituents of component (B) comprise at least one substituted or unsubstituted alkyl group, aryl group, and/or alkylaryl group, and/or an oxyalkyl or polyoxyalkylene group.
- Substituted alkyl, aryl, or alkylaryl groups may comprise a functional group such as a hydroxy group, alkene group, alkyne group, halide group, ether group, carbonyl group, aldehyde group, ketone group, ester group, carboxylic acid group, amide group, amine group, nitrite group, nitro group, sulfide group, sulfoxide group, amino acid group, sulfonate group, phosphonate group, or a mixture thereof, without deviating from the present invention.
- a functional group such as a hydroxy group, alkene group, alkyne group, halide group, ether group, carbonyl group, aldehyde group, ketone group, ester group, carboxylic acid group, amide group, amine group, nitrite group, nitro group, sulfide group, sulfoxide group, amino acid group, sulfonate group, phosphonate
- the alkyl group should preferably have from 1 to 8 carbons so as to provide suitable solubility and surface activity to the overall sugar residue compound derived.
- amides are most preferred for connecting sugar residue group(s) to non-sugar substituent group(s).
- a preferred exemplary compound of the invention for modifying cement, cementitious compositions, or other particle-containing compositions comprises at least one residue of sugar or sugar derivative; at least one non-sugar substituent comprising a C 2 -C 4 oxyalkylene groups, or, more preferably, repeating ethylene oxide and propylene oxide groups, wherein the number of repeating units is 2-200 (and more preferably 2-100); and a linking member, preferably an amide group, for linking the sugar residue(s) to the ethoxylated non-sugar substituent group(s).
- This compound may, for example, be sold as a cement additive (e.g., grinding) or as an admixture for use in cementitious compositions (e.g., concrete, mortar).
- the compound is also believed to be useful as a particle dispersant in non-hydratable particle-containing compositions (e.g., clay-containing mixes, latexes for paint; also patching, sealant, or coating compositions).
- the present invention particularly includes cement and other cementitious or other hydratable binder compositions (as well as nonhydratable compositions employing non-hydratable binders) comprising the above-described additive or admixture compound.
- the present invention also pertains to processes for modifying such compositions, as well as to processes for making the above-described compound.
- the above-described compounds may be used to modify other properties of cementitious compositions as well.
- the inventive compounds are useful as grinding aids for cement clinker; and thus a process of the invention involves introducing the compound during grinding of cement clinker.
- the compounds of the invention when used as a grinding aid, are useful for increasing the strength of materials and structures made from the processed cement.
- the above-described compounds are suitable for use as efficient water reducer additives or admixtures for use in or with cement, for use in the manufacture of cement, and for use in cementitious mixtures including concrete, mortar, or masonry.
- the compounds may be used to modify other properties of cementitious compositions.
- the compounds are believed to be useful as grinding aids for cement clinker; and, consequently, an exemplary process of the invention involves introducing the above-described additive compound during the grinding of cement clinker.
- exemplary methods of the involve incorporating the above- described compounds into an aqueous environment having a binder material.
- the composition may be introduced into a concrete or mortar as an admixture, either with a hydratable and/or nonhydratable binder material (e.g., cement and/or clay), or it can be introduced using mix water.
- compositions of the invention include a plurality of particles to be dispersed and a compound for dispersing the plurality of particles, the compound having at least one residue of sugar or sugar derivative, at least one non-sugar substituent, and a linking group.
- the invention also pertains to a method of dispersing nonhydratable solids such as polymer particles (e.g., synthetic polymers for latexes) or minerals (e.g., calcium carbonate) in an aqueous system, comprising introducing to said nonhydratable solids the compound described herein having the sugar residue connected to the non-sugar substituents by the linking group, as described above.
- nonhydratable solids such as polymer particles (e.g., synthetic polymers for latexes) or minerals (e.g., calcium carbonate) in an aqueous system
- an exemplary composition comprises a plurality of particles to be dispersed and a compound for dispersing said plurality of particles, said compound comprising (A) at least one residue of sugar or sugar derivative; (B) at least one non-sugar substituent, such as an alkyl group (preferably one C r C g alkyl group, substituted or unsubstituted, per sugar residue in component (A)), an aryl or alkylaryl group (preferably having one C 6 -C 8 aryl or alkylaryl substituted or unsubstituted group per sugar residue in component (A)), and/or an oxyalkylene or polyoxyalkylene oligimer or polymer group (e.g., preferably having repeating C 2 -C 4 oxyalkylene groups, or, more preferably, repeating ethylene oxide and propylene oxide groups, wherein the number of repeating units is 2-200); and (C) a linking group comprising an amide, amine, imide, urea, or mixture thereof
- An exemplary method comprises introducing into a mix tank a sugar derivative and an amine (and optionally a solvent) to form a reaction mixture; and forming a sugar amide reaction product.
- the sugar amide reaction product can then be separated from the reaction mixture solvent.
- the components may be added using conventional methods.
- the sugar derivative component may be incorporated into a mixing tank using a bulk solids hopper and feed system.
- Another exemplary process involves evaporating the reaction mixture solvent to isolate the sugar amide reaction product as a dry material.
- the evaporation may be achieved by decreasing pressure above the reaction mixture (e.g., applying a vacuum), whereby solvent is removed from the sugar amide reaction product.
- Solvent may also be removed by flowing a gas over or through the reaction mixture.
- the sugar amide reaction product forms a precipitate.
- the reaction product may optionally be chilled, before removing the resulting crystals by filtration. A dry product can then be obtained by evaporating the residual solvent.
- Another exemplary process of the invention involves the use of water to extract the sugar amide reaction product from the solvent.
- a water-immiscible solvent and reaction product are contacted with water, such as in a counter-current extraction, and the product is removed from the solvent phase resulting in an aqueous phase product.
- This exemplary approach provides advantages in terms of avoiding solids handling and eliminating the need to vaporize or distill solvents.
- a still further exemplary process of the invention involves the use of water to replace solvent after the reaction is completed.
- the solvent may be replaced with water using batch distillation.
- water is added, either continuously or all at once, to the mixture containing solvent and product.
- this solvent replacement process provides the advantage of eliminating solids handling and the need to condense solvent from a carrier stream.
- the components may be added into a continuous in-line mixing tank to obtain the sugar amide reaction product which, with solvent (and any residual amine), can then be fed continuously into a distillation column.
- the solvent is replaced by water that is heated and vaporized into the distillation column, and the reaction product may be removed from the column in aqueous form while the solvent is condensed, optionally refluxed, and purified for reuse (along with any residual amine) in the process.
- Fig. 1 is a graphic illustration of flow performance of cement compositions comprising various admixtures, including admixtures of the present invention
- Fig. 2 is a graphic illustration of set retarding performance of cement compositions comprising various admixtures, including admixtures of the present invention
- Fig. 3 is a diagram of an exemplary evaporation process of the invention for manufacturing a sugar amide composition of the present invention
- Fig. 4 is a diagram of an exemplary crystallization process of the invention for manufacturing a sugar amide composition of the present invention
- Fig. 5 is a diagram of an exemplary extraction process of the invention for manufacturing a sugar amide composition of the present invention
- Fig. 6 is a diagram of an exemplary solvent replacement process of the invention for manufacturing a sugar amide composition of the present invention
- Fig. 7 is a diagram of another exemplary solvent replacement process of the invention for manufacturing a sugar amide composition of the present invention.
- the present invention relates to compositions and methods involving particles to be dispersed (e.g., fillers such as calcium carbonate, binders such as cement, particles in slurries such as drilling mud) and compounds for dispersing or otherwise modifying the particles.
- particles to be dispersed e.g., fillers such as calcium carbonate, binders such as cement, particles in slurries such as drilling mud
- the present invention pertains to cementitious compositions comprising a cement binder and a modifying compound.
- pastes are mixtures composed of a hydratable cement binder (usually, but not exclusively, Portland cement, masonry cement, or mortar cement and may also include limestone, hydrated lime, fly ash, blast furnace slag, pozzolans, and silica fume or other materials commonly included in such cements) and water; mortars are pastes additionally including fine aggregate (e.g., sand), and concrete are mortars additionally including coarse aggregate (e.g., crushed gravel, stone).
- the cementitious compositions tested in this invention may be formed by mixing required amounts of certain materials, e.g., a hydratable cement, water, and fine and/or coarse aggregate, as may be applicable to make the particular cement composition being formed.
- Exemplary compounds for modifying one or more properties of cementitious compositions comprise, as summarized above, a residue of sugar or sugar derivative, a non-sugar substituent, and a linking member for connecting the sugar residue to the non-sugar substituent.
- a residue of sugar or sugar derivative a residue of sugar or sugar derivative
- a non-sugar substituent a non-sugar substituent
- a linking member for connecting the sugar residue to the non-sugar substituent.
- G represents at least one residue of sugar or sugar derivative; "g” is an integer of from 1 to 100, and more preferably “g” is from 1 to 50; X represents a linking group selected from amide, amine, imide, urea, or mixture thereof (preferably it is an amide); "x" is an integer of from 1 to 100 (and preferably equal to or less than "q”); Q represents a non-sugar substituent group selected from an alkyl (preferably having one C 2 -C 8 substituted or unsubstituted alkyl group per sugar residue in componet (G)), aryl or alkylaryl group (preferably having one C 6 -C 8 aryl or alkylaryl substituted or unsubstituted groups per sugar residue in component (G)), and/or an oxyalkylene or polyoxyalkylene oligimer or polymer group (e.g., preferably having repeating C 2 -C 4 oxyalkylene
- G can represent the same or similar groups, units, or compounds.
- sugar residue and non-sugar substituent components may be connected to the linking member (X), as well as to other similar or identical groups or compounds, as in the following structures:
- Q groups above can be connected, in turn, to G, Q, GX, XQ, and/or GXQ containing groups.
- sugar as employed herein means and refers to a sugar molecule (e.g., monosaccharide, disaccharide, polysaccharide, etc. as further described hereinafter) or derivative thereof which is capable of chemically-bonding to the linking group.
- a particularly preferred compound of the invention comprises a sugar amide
- the sugar residue "G” may be derived from hydroxycarboxylic acids such as aldonic acid (e.g., gluconic acid, heptogluconic acid), aldaric acid (e.g., glycaric acid, heptoglucaric acid), and uronic acid (e.g., glucuronic acid, heptoglucuronic acid or, as it is otherwise sometimes called, glucoheptonic acid), or their salts or their lactones (i.e.
- aldonic acid e.g., gluconic acid, heptogluconic acid
- aldaric acid e.g., glycaric acid, heptoglucaric acid
- uronic acid e.g., glucuronic acid, heptoglucuronic acid or, as it is otherwise sometimes called, glucoheptonic acid
- salts or their lactones i.e.
- the sugar residue may also be derived from aldoses or sugars (e.g., glucose, sucrose, tetrose, pentose, hexose, etc.), including corn syrup and molasses and their oxidized forms which could also serve as substrates for gluconamide formation.
- aldoses or sugars e.g., glucose, sucrose, tetrose, pentose, hexose, etc.
- corn syrup and molasses and their oxidized forms which could also serve as substrates for gluconamide formation.
- sugar residues are sugar acids having 3-10 carbons; more preferred are sugar acids having 4-8 carbons; and most preferred are those having 5-7 carbons.
- Sugar acids which are also preferred include -D-gluconic acid, -D-glucaric acid, and D- Glucuronic acid, and mixtures thereof.
- the non-sugar substituent "Q" group may comprise substituted alkyl and aryl groups having functional groups such as a hydroxy group, alkene group, alkyne group, halide group, ether group, carbonyl group, aldehyde group, ketone group, ester group, carboxylic acid group, amide group, amine group, nitrite group, nitro group, sulfide group, sulfoxide group, amino acid group, sulfonate group, phosphonate group, or a mixture thereof.
- functional groups such as a hydroxy group, alkene group, alkyne group, halide group, ether group, carbonyl group, aldehyde group, ketone group, ester group, carboxylic acid group, amide group, amine group, nitrite group, nitro group, sulfide group, sulfoxide group, amino acid group, sulfonate group, phosphonate group, or a mixture thereof.
- an alkoxylated amine which can be used for combining with the starting sugar acid to obtain the additive/admixture compounds of the invention, may be represented by the formula
- AO represents an alkoxy group, and preferably a C 2 -C 3 ethylene oxide/propylene oxide group
- "n” and “p” are integers whereby the sum of “n” and “p” are from 1 to 100, and “n” or “p” individually are integers of from 0 - 100
- R 1 can be connected to R 2 to form a cyclic polyoxyalkylene secondary amine, e.g. morpholine.
- an alkylamine which can be used for combining with the starting sugar acid to obtain additive/admixture compounds of the invention may be represented by the formula R 3
- R 3 and R 4 independently represented hydrogen or -Cjn alkyl group, a cycloalkyl group, or an aryl ring (e.g., as in benzyl amine).
- R 3 and R 4 may also form a cyclic structure such as in a cyclic secondary amine, e.g. piperadine, etc.
- R 3 and R 4 can also contain additional amine or other functional groups.
- the amine may be reacted with a sugar acid by thermal amidation with or without an amidation catalyst.
- the reaction temperature is preferably in the range of 80 to 180°C (more preferably 100-145°C ), and the reaction can be done in bulk or in solution.
- An azeotropic agent such as toluene, can be used to facilitate dehydration. Lactone formation can be minimized by using a slight to modest excess of the amine, and it is believed that any residual amine will not have an adverse effect upon cementitious materials into which the sugar residue containing compounds are incorporated.
- the derived sugar amide can be represented by the general formula:
- AO represents C 2 -C 4 alkoxyl group, and more preferably ethylene oxide and propylene oxide groups;
- R 1 and R 2 independently represent hydrogen or a C r C 3 alkyl group;
- "n" and "p” each independently represent an integer from 0 to 100; and the sum of "n” and "p” is an integer from 1 to 100, and
- R 3 and R 4 independently represent hydrogen or C r C 20 alkyl, cycloalkyl group, or an aryl ring (e.g., as in benzyl amine).
- R 1 , R 2 , R 3 , and R 4 may also contain functional groups.
- the amine may also be reacted with sugars or oligosaccharide having reactive aldehyde or ketone groups to form adducts.
- the reaction temperature is in the range of 0 to 120°C, preferably 20° to 100°C.
- the reaction can be done practically in bulk with a small amount of water (fusing a sugar with an amine), alcohols, alcohols containing water or in water.
- Acid catalysts such as hydrochloric acid, acetic acid, oxalic acid, etc., can be used to rearrange the sugar amine adducts into more stable form, known as Amadori derivatives (in the case of reaction of aldoses with an amine) or Heyns compounds (in the case of the reaction of ketoses with an amine).
- Exemplary sugar-amine adducts after being rearranged with an acid catalyst, can be represented by the general formulae:
- R 1 can be connected to R 2 to form a cyclic polyoxyalkylene secondary amine, e.g. morpholine.
- R 3 and R 4 independently represented hydrogen or C,-C 20 alkyl, cycloalkyl group, or aryl group (e.g., benzyl amine).
- R 1 , R 2 , R 3 , or R 4 may also contain other functional groups.
- Hydrogenation of the sugar amine adducts may also be done to stabilize the compounds as well as to improve their dispersing performance. Hydrogenation can be done simultaneously with amine adduct formation with or without a catalyst.
- the derived hydrogenated sugar-amine adducts can be represented by the general formulae:
- G represents a monomeric sugar residue after amination followed by hydration
- AO represents an alkoxy group, and preferably a C 2 -C 3 ethylene oxide/propylene oxide group
- n and p are integers whereby the sum of “n” and “p” are from 1 to 100, and “n” or “p” individually are integers of from 0 - 100
- R 1 can be connected to R 2 to form a cyclic polyoxyalkylene secondary amine, e.g. morpholine.
- R 3 and R 4 independently represented hydrogen or C,-C 20 alkyl, cycloalkyl group, or aryl group (e.g., benzyl amine).
- R 1 , R 2 , R 3 , or R 4 may also contain other functional groups.
- Cements and cement compositions of the invention comprise a mixture of a hydratable cement, or other cementitious binder, and from 0.001 to 5.0 weight percent based on the weight of the hydratable cement of the above-described sugar-amine derivative compound. More preferably, the amount of the sugar-amine derivative compound in the cement or cement composition is 0.0005 to 0.5 weight percent based on the weight of the hydratable cement or cementitious binder.
- the exemplary [G] g [X] x [Q] q compounds provide a particle attachment group (e.g., the sugar residue component G connected by an intervening linking group X to a non-sugar substituent component Q to provide steric hindrance and/or repulsion for enhancing the dispersion ability of the compounds and providing a beneficial adsorption rate relative to the cement particles being attached and dispersed within the aqueous matrix of a cementitious slurry. It is believed that such compounds described herein become uniformly dispersed throughout cementitious compositions, such as mortar or concrete, before being attached by, or entirely adsorbed onto, the cement.
- a particle attachment group e.g., the sugar residue component G connected by an intervening linking group X to a non-sugar substituent component Q to provide steric hindrance and/or repulsion for enhancing the dispersion ability of the compounds and providing a beneficial adsorption rate relative to the cement particles being attached and dispersed within the aqueous
- the present invention also provides novel processes for making compounds of the present invention, such as a sugar amide derivatives, useful for modifying hydratable compositions (e.g., mortar, concrete) and non-hydratable particle- containing composisitions alike.
- a sugar amide derivative useful for modifying hydratable compositions (e.g., mortar, concrete) and non-hydratable particle- containing composisitions alike.
- an exemplary process for producing a sugar amide derivative involves combining an amine component 10, a derivative of a sugar 12, and optionally a solvent 14 in a mix tank 20 to initiate a reaction wherein the amine component 10 and sugar derivative are linked by means of an amide bond.
- the product After the product is formed, it must then be separated or removed from the solvent, which acts to provide sufficient contact between the two reactants to facilitate formation of sugar amide derivative product, which is designated as at 22 in the solvent removed from mix tank 20.
- the amine component 10 can comprise a wide variety of primary alkyl amines, secondary alkyl amines, or aromatic amines.
- the amine may be added at about a 1:1 molar ratio to the sugar derivative component 12.
- a small excess of the amine e.g., 3 mol %) may be added to drive the reaction to completion.
- Amines of particular interest include primary and secondary amines as well as primary or secondary amines containing functional groups.
- the sugar derivative component 12 may consist of an acid derivative of a sugar or its salt or lactone (e.g., glucono-delta lactone).
- the solvent acts to provide adequate contact between the two reactants for the reaction to occur.
- the solvent 14 may be preferably selected so that it is miscible with the amine component 10. Dissolution of the sugar derivative 12, although not believed to be essential for product formation, may be advantageous in increasing the rate of reaction. Further, it may be advantageous in some isolation schemes if the nature of the solvent is such that, under reaction conditions, the reaction product is soluble in the solvent, but upon cooling (to room temperature or below) the product may precipitate or crystallize from the reaction solvent. Sufficient quantities of solvent 14 should be used to dissolve completely the amine component 10, and to dissolve or wet the sugar derivative 12.
- Solvents that are contemplated for use include alcohols and other polar organic solvents (such as chlorinated hydrocarbons, ethers, amides, nitriles), aromatic hydrocarbons, tertiary amines (.e.g, triethylamine, triethanolamine, methyldiethanolamine, trisopropanolamine, etc.), and the amine that is used as a reactant (e.g., as incorporated in the amine component 10). Methanol is most a preferred solvent in terms of facilitating the reaction. However, other solvents are also suitable and may facilitate the isolation step, as further discussed below.
- the mixing step (as designated at 20) may be conducted using at room temperature, or, more preferably, at slightly higher temperatures and/or atmospheric pressures.
- reaction itself gives rise to a temperature increase within the mixing tank 20 because the reaction is exothermic in nature. This may advantageously increase the rate of reaction/production. In some cases, gentle heating may be applied to increase the rate (e.g., in mix tank 20). It is contemplated that the reaction may be run using refluxing methanol, although this is not essential for the reaction to occur.
- Product isolation such as the drying step, designated as at 28 in Fig. 3, will be the step having the largest effect on the process scheme.
- the isolation of product 30 occurs by driving off the residual solvent, such as by using any known direct or indirect heating methods, and then applying a vacuum and/or sweep gas (designated as at 29) to remove solvent and obtain the separated dry reaction product 30.
- the solvent would then be condensed 32, and possibly purified 34 such as through distillation, filtration through activated carbon, or other known methods, before being returned to a solvent recovery tank 14 which is also used as a feed into the mixing tank 20.
- Off gases 35 from the condensor 32 are preferably recovered (e.g., scrubbed) and reused, as well, in the process.
- Solvent selection in this case is dictated by the ability of the process to evaporate off readily the residual material.
- Solvents of interest can include lower molecular weight alkyl alcohols, and in particular methanol, as mentioned above.
- FIG. 4 Another exemplary process for product isolation is shown in Fig. 4 wherein, after the reaction is initiated in the mixing tank 20, the sugar amide derivative reaction product-in-solvent is then crystallized, preferably in a separate tank as shown at 26, and optionally but preferably by using conventional cooling means in the separate crystallization tank 26 (or alternatively through cooling coils (designated at 24)).
- the crystallized or precipitated reaction product can then be filtered 27 from the bulk of the solvent, which can be returned to the solvent tank 14, preferably after purification
- Filtration can be accomplished by a wide range of approaches, such as batch cake filtering (e.g., pressure leaf or nutsche filters), continuous cake filtering (e.g., disk or horizontal vacuum filters), or centrifugation filtering (e.g., basket, peeler, or pusher).
- batch cake filtering e.g., pressure leaf or nutsche filters
- continuous cake filtering e.g., disk or horizontal vacuum filters
- centrifugation filtering e.g., basket, peeler, or pusher.
- Filtered solvent 27 can then be purified 34 such as by filtration using activated carbon, and reused in the process (by feeding back to the solvent tank
- the residual solvent remaining with the filtered reaction product is subjected to the drying step 28, wherein the residual solvent may be driven off by direct or indirect heating 28 to obtain the separated reaction product 30.
- a sweep gas, vacuum, or both 29 can be used to facilitate removal of the residual solvent, which then can be condensed 32, optionally purified 34 (as described above), and returned to the solvent tank 14 for reuse in the process.
- Off gas 35 may be recovered (e.g., scrubbed using condensers) and reused in the process as well.
- the crystallization approach provides advantages including significant reduction of the quantity of solvent condensed from the carrier stream.
- the number of solvent return steps illustrated for example in Fig. 4 illustrates this advantage.
- Solvent selection is important since the product should be soluble at reaction temperatures, but the reaction product is preferably nearly insoluble at the crystallization temperatures. Isopropanol and methanol are particularly useful solvents, providing nearly complete recovery of the product at ambient temperatures (e.g., about 70° Fahrenheit).
- an exemplary process for making a sugar amide derivative of the present invention comprises: introducing into a mix tank a sugar derivative, an amine, and a solvent to form a reaction mixture; forming a sugar amide reaction product; and separating said sugar amide reaction product from said reaction mixture solvent.
- the sugar derivative may, for example, comprise a sugar acid derivative of a sugar or its salt or its lactone.
- the amine component may comprise a primary amine, a secondary amine, or mixture thereof comprising a group selected from an aromatic, hydroxy, etheric, halogen, unsaturated alkyl, carbonyl, ester, amino, nitro, carboxylic, nitrilo, thio, or sulfone functional group.
- the solvent may comprise an alcohol, polar organic solvent (e.g., a chlorinated hydrocarbon, ether, amide, nitrile, or mixture thereof), aromatic hydrocarbon, an amine (e.g., preferably a tertiary amine, or mixture thereof.
- the mix tank 20, moreover, may comprise a batch mix tank, wherein a valve and/or pipe is opened after reaction is substantially completed (and/or periodically) whereby reaction-product/solvent (22) can be conveyed to the drying step 28; and the mix tank 20 may also be a continuous in-line tank, from the bottom of which the crystallized or precipitated reaction product is flowed in solvent to the drying step 28 on a continuous basis.
- the drying of the sugar amide reaction product, shown at 28, may be accomplished, as aforesaid, by heating (e.g., direct heat source applied such as by thermal energy, or by exposure to heated pipes), but it is advisable that sugar amide derivative not be charred by overheating or unnecessarily high thermal energy.
- the solvent is removed from sugar amide reaction product by flowing a gas through said reaction mixture, and/or by applying a vacuum.
- a cooling step 24 is preferably employed, after mixing together the amine 10, sugar derivative 12, and solvent 14, to crystallize or precipitate a reaction product. This facilitates the subsequent filtering of the reaction mixture solvent to separate the sugar amide reaction product from the solvent.
- Another exemplary process of the invention for manufacturing a sugar amide derivative involves the use of water to extract the product from the solvent. As diagrammatically illustrated in Fig. 5, the amine component 10, sugar derivative component 12, and solvent 14 are mixed together 20, and the resultant reaction product in solvent are fed to an extraction column or vessel 40. In the extraction column 40, the solvent containing reaction product is contacted with water which is flowed into the column 40 such that the reaction product flows in a direction that is counter-current to the direction of water flow. The reaction product may be removed as an aqueous product 44 from the bottom of the extraction column 40, and the solvent is then collected at the top of the extraction column 40 and returned, after optional purification step 34, to the solvent recovery tank 14 for reuse in the process.
- the solvent 14 used in the reaction step 20 must be immiscible in water to enable the extraction to work.
- a suitable solvent for this purpose is toluene.
- Other exemplary solvents that are also believed to be suitable include anisole, benzene, acetonitrile, xylene, and methyl butyl ether (preferably methyl-t-butyl ether).
- One important consideration in the exemplary extraction approach illustrated in Fig. 5 is that residual amine may degrade the reaction product in the presence of water. This may be overcome by adding a buffer, with the water 42 introduced into the extraction column 40, to control the pH.
- buffers and pH modifiers include conventional (commercially available buffer solutions), ionic polymers, acetic acid, hydrochloric acid, nitric acid, mineral and carboxylic acids, ammonium chloride, or a mixture thereof.
- a still further process for manufacturing a sugar amide derivative involves solvent replacement distillation.
- the solvent replacement distillation process provides the advantage of eliminating solids handling and the need to condense solvent from a carrier stream.
- the solvent 14 and amine component 10 are combined with the sugar derivative component 12 in the mixing tank 20, which in this case is a batch vessel.
- solvent is replaced with water 42, preferably along with a pH buffer, that is introduced continuously or in one dose directly into the mix tank 20 containing the solvent and reaction product.
- Solvent is driven off by heating, such as by employing a distillation column 50 connected to the mix tank 20, and is separated from the water using batch distillation.
- the reaction product is then recovered as an aqueous product 30.
- Solvent which travels through the distillation column 50 is condensed using a condensor apparatus 32 and may be refluxed in the column 50.
- recovered solvent may optionally (and preferably) undergo purification using activated carbon or other filtration methods before being reused in future batches.
- Solvent selection is important because the separation from water must be nearly complete for reuse in subsequent reactions.
- a solvent such as methanol is preferred since it does not form an azeotrope with water. Other alcohols can be utilized, but the reaction rate is inhibited because a small amount of water tends to be recycled with the solvent.
- an important consideration in the solvent replacement approach is that residual amine will degrade the product in the presence of water and also high temperatures. This can be overcome by adding a buffer with the water to control the pH, as previously mentioned. Alternatively, drawing a vacuum over the mixing tank (to lower the pressure) also helps to reduce degradation since the operating temperature decreases.
- a continuous reactor e.g., an in-line, continually stirred mix tank 22 is used for reacting continuously fed amine component 10, sugar derivative component 12, and solvent 14 together.
- the reaction product in solvent (20) is continuously fed to a distillation column 50 where water 42 replaces the solvent.
- the water 42 (optionally with one or more pH buffers) is introduced at or near the bottom of the distillation column 50 where a heating element or "reboiler" 52 is used to heat the distillation column.
- the water functions to replace the solvent, and the reaction product is removed in an aqueous form.
- the solvent is then condensed using a condenser 32 and optionally purified 34, using activated carbon filtration for example, and then solvent (with any unreacted amine) is recovered 14 and may be reused in the process.
- This approach (Fig. 7) has an additional advantage over the batch process (as shown in Fig. 6) since residual amine is removed before combining with significant amounts of water. This reduces degradation and may eliminate the need for a buffer or vacuum operation.
- the aforementioned compounds of the invention may be combined with conventional admixtures, such as alkoxylated polycarboxylates (such as "comb" type polymers used as water reducers or superplasticizers; e.g., superplasticizers commercially available from Grace Construction Products, Cambridge,
- ADVA® naphthalene sulfonate formaldehyde condensate, melamine sulfonate formaldehyde condensate, calcium or sodium lignosulfonate, alkali or alkaline earth metal nitrites or nitrate (e.g., calcium nitrite and/or calcium nitrate such as commercially available from Grace Construction
- shrinkage-reduction admixtures such as those containing alkyl ether oxyalkylene adducts and/or oxyalkylene glycols (e.g., such as commercially available from Grace Construction Products under the tradename
- the resultant solution pH was 5-6.
- Air content was measured in accordance with ASTM C185. After the test, the mortar mix was used for the measurement of setting time. Setting time was measured with an automatic penetrometer developed by W. R Grace & Co.-Conn. so that the measured setting time is equal to the initial set time defined by ASTM C 403/C403M-95.
- Results are provided below in Tables 1-4 below and Figures 1 & 2.
- the fluidity performance (flow (mm)) of Examples 1 and 5 is compared, as a function of dosage, to that of gluconic acid.
- the set retarding performance in terms of set time (hrs) as a function of dosage is shown for Examples 1, 5, and unmodified gluconic acid.
- Example 5 0.08 7.00 3.1 6h41m 8h33m
- Example 12
- a 10 gram sample of glucose was dissolved in 10 grams of water in a four- neck flask fitted with a mechanical stirrer, a DEAN- STARKTM trap with condenser, and a dry nitrogen inlet at 60 to 80°C.
- a homogenous syrup was obtained in less than 20 min.
- the homogeneous mixture was then heated in an oil bath at 110°C for 3 hours under slow continuous flow of nitrogen.
- the color of the homogenous mixture quickly turned into yellow to greenish, and then a dark yellow color, was obtained.
- the mortar testing results of the material appear in Table 7 along with that of D-glucose.
- the mortar testing procedure was the same as is described in Example 10.
- a 9.0 gram sample of glucose (50 mM) was fused with 3.0 grams of acetic acid (50 mM), and 2.0 grams of water in a four-neck flask fitted with a mechanical stirrer, a DEAN-STARKTM trap with condenser, and a dry nitrogen inlet at 60 to 80°C.
- a 5.06 grams of hexylamine (50 mM) was slowly added with 7 mL of methanol. The temperature was held at 65 - 68°C for 2 hours under a slow continuous nitrogen flow. Methanol was removed by rotary evaporation. A viscous, black syrup was obtained.
- the mortar testing procedure is the same as is described in Example 10.
- a 54 gram sample of corn syrup (dextrose equivalence 35%) was placed in a four-neck flask that was fitted with a mechanical stirrer, a DEAN-STARKTM trap with condenser, and a dry nitrogen inlet. The temperature was raised to 80°C and a 0.38 mL aliquot of 5N HCl aqueous solution were added to the syrup. 7.0 grams of monoethanolamine was then slowly added to the flask. The solution was continued to stirred for another 1 hour under slow nitrogen flow. A viscous, black syrup was obtained.
- the mortar testing results of the material are shown in Table 9 along with that from corn syrup. The mortar testing procedure is the same as is described in Example 10.
- the mortar testing results of the material are shown in Table 10 along with that of corn syrup (dextrose equivalence of 35%). The mortar testing procedure is the same as is described in Example 10.
- the blaine surface area (BSA) was measured periodically as described by ASTM C
- a sedimentation experiment was conducted wherein a dilute suspension of calcium carbonate powder (about .079 volume percent fraction) was made. (CaCO 3 powder from Aldrich, 10 micron ave. diameter).
- a small dosage of N-pentyl gluconamide (preparation was analogous to that of Example 9) was dosed into the suspension (0.75-1.60 % by wt based on calcium carbonate powder).
- the suspension was treated by ultrasonic exposure for precisely 5 minutes and then dispersed again by agitation.
- the suspension was then quickly transferred to a capped volumetric cylinder and left to stand for the sedimentation observation.
- the volume of the sediment was measured after 20 minutes, and the powder volume fraction in the sediment was calculated. The higher powder volume fraction in the sediment indicated that the sediment was more compact, suggesting better dispersion of the powder.
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Abstract
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AU27363/00A AU755918B2 (en) | 1999-01-29 | 2000-01-26 | Sugar derivative composition for modifying properties of cement and cementitiouscompositions and processes for manufacturing same |
JP2000595777A JP2002535232A (en) | 1999-01-29 | 2000-01-26 | Sugar derivative composition for changing properties of cement and cementitious composition and method for producing the same |
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US11792799P | 1999-01-29 | 1999-01-29 | |
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WO2001004185A1 (en) * | 1999-07-09 | 2001-01-18 | Mbt Holding Ag | Oligomeric dispersant |
US6478870B2 (en) | 2000-01-27 | 2002-11-12 | Dow Corning Corporation | Process aid for preparing a flowable slurry |
EP1308427A1 (en) * | 2000-08-11 | 2003-05-07 | Nippon Shokubai Co., Ltd. | Cement admixture and cement composition |
US6663745B1 (en) | 1999-01-29 | 2003-12-16 | Mykrolis Corporation | Method for manufacturing hollow fiber membranes |
WO2004024647A1 (en) * | 2002-09-16 | 2004-03-25 | Construction Research & Technology Gmbh | Oligomeric dispersant |
US6908955B2 (en) | 1999-07-09 | 2005-06-21 | Construction Research & Technology Gmbh | Oligomeric dispersant |
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JP3834736B2 (en) * | 2003-09-05 | 2006-10-18 | 第一工業製薬株式会社 | Anti-caking agent for granulated blast furnace slag |
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US5565420A (en) * | 1994-05-16 | 1996-10-15 | The Procter & Gamble Company | Granular detergent composition containing admixed fatty alcohols for improved cold water solubility |
US5583183A (en) * | 1993-09-29 | 1996-12-10 | W. R. Grace & Co.-Conn. | Cement and cement composition having improved rheological properties |
-
2000
- 2000-01-26 JP JP2000595777A patent/JP2002535232A/en active Pending
- 2000-01-26 AU AU27363/00A patent/AU755918B2/en not_active Ceased
- 2000-01-26 WO PCT/US2000/001834 patent/WO2000044487A1/en active Application Filing
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US5583183A (en) * | 1993-09-29 | 1996-12-10 | W. R. Grace & Co.-Conn. | Cement and cement composition having improved rheological properties |
US5565420A (en) * | 1994-05-16 | 1996-10-15 | The Procter & Gamble Company | Granular detergent composition containing admixed fatty alcohols for improved cold water solubility |
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JP2002535232A (en) | 2002-10-22 |
AU2736300A (en) | 2000-08-18 |
AU755918B2 (en) | 2003-01-02 |
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