[go: up one dir, main page]

CN100441531C - Sulfate dispersion chromate reducer - Google Patents

Sulfate dispersion chromate reducer Download PDF

Info

Publication number
CN100441531C
CN100441531C CNB2004800344494A CN200480034449A CN100441531C CN 100441531 C CN100441531 C CN 100441531C CN B2004800344494 A CNB2004800344494 A CN B2004800344494A CN 200480034449 A CN200480034449 A CN 200480034449A CN 100441531 C CN100441531 C CN 100441531C
Authority
CN
China
Prior art keywords
composition
cement
tin sulphate
chromium
water
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.)
Expired - Fee Related
Application number
CNB2004800344494A
Other languages
Chinese (zh)
Other versions
CN1882515A (en
Inventor
L·A·贾丁
C·R·科恩曼
D·T·吉尔里
V·古普塔
全炳和
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
Original Assignee
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 filed Critical WR Grace and Co
Publication of CN1882515A publication Critical patent/CN1882515A/en
Application granted granted Critical
Publication of CN100441531C publication Critical patent/CN100441531C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

A chromium VI reducing composition comprising particles of solid material selected from the group consisting of iron (II) sulfate and tin sulfate, the particles being substantially uniformly dispersed within a liquid carrier. Methods for modifying hydratable cementitious materials using the chromium reducing composition are also disclosed and provide advantages over dry powder or dissolved forms of sulfate compositions when used in cement manufacturing.

Description

Sulfate dispersion chromate reducer
Technical field
The present invention relates to the reductive agent of sexavalent chrome (VI), relate more particularly to cement additire, and be used for reducing the method for chromic salt of cement, described method relates to the solid sulphuric acid salt particle that is dispersed in the liquid vehicle.
Background technology
Chromium is the inevitable trace element in raw materials used when making cement clinker, and cement clinker is through grinding to make cement.Especially, sexavalent chrome (" Cr VI ") can form under the condition of the oxidation of cement kiln and alkaline sintering.Cr VI compound is classified as has utmost point toxicity, because their high oxidation gesture and can penetrate the ability of people tissue, thereby cause sensitization of skin, anaphylaxis and eczema.Because Cr VI compound has high-dissolvability and is released when cement and water are mixed together, so they tend to touch people's skin in handling wet cement and mortar process.
Hope is reduced to trivalent chromium (Cr III) with sexavalent chrome (Cr VI).This is because Cr III tends to come out as stable complex compound sediment from solution, thereby reduces the danger as serious skin irritant.In fact, known many reductive agents.Yet they tend in low pH level effective, and validity is relatively poor under the high pH environment of cementing compositions.
Ferrous sulfate (II) is generally used for reducing the chromium in the bonding system.In the process of reduction chromium, iron (Il) is oxidized to iron (III).Yet the actual dose of the ferrous sulfate (II) that the chromium reduction is required is required stoichiometric 10 times.This part ground be since ferrous sulfate (II) usually with dried forms, be added into to the dosage of 0.5 weight % with 0.3 weight % of cement, and can be by airborne this fact of moisture oxidation.In addition, the ferrous sulfate of this a large amount of adding dried forms (II) is in-problem.At first, in the cement operating process, be difficult to accurately add drying material.They also bring unmanageable dirt problems in the logistics, and cause the worry to the health risk that is caused by dust.
It is also important that excessive ferrous sulfate is unfavorable for bonding system,, and prolong setting time because increased the water requirement of workability.
Typically, exsiccant ferrous sulfate (II) can not be added in the cement under being higher than 80 ℃ temperature, otherwise has by the danger of a large amount of oxidations.When cement is discharged from grinding machine and is transported to temperature when surpassing 80 ℃ storer in the temperature that is up to 130 ℃, ferrous sulfate (II) must be added in the latter half of cement manufacturing and distribution process.The most normally, ferrous sulfate (II) must be about to add before the packaged transportation at cement.The other quality control step of these needs is used for checking the chromium content in the cement, and this increases trouble and cost to cement manufacturers.
As the surrogate of ferrous sulfate (II), can use tin sulphate as chromium reducing agent.The dosage of required solid sulphuric acid tin is than the dosage of ferrous sulfate II much lower (cement~0.02 weight %).When with process of lapping in cement when combination, believe tin sulphate how many easier uses and more heat-resisting and storage-stable.Yet the logistics that still exists similar tin sulphate with dry powder form to join in the cement operation is worried.
Although tin sulphate is water miscible, when being added in the cement as the aqueous solution, it loses dose effect rapidly.The actual requirement of tin sulphate is 2 times of aequum when tin sulphate is added into powder type at least.This discordance has considered to hinder the tin sulphate that uses the solution form from the economics viewpoint.
Therefore, consider above-mentioned shortcoming, the inventor believes to be needed new chromium reducing agent, this reductive agent to need low relatively dosage adding rate and can liquid form sends and distribute.
The invention summary
Compare with tin sulphate with the ferrous sulfate (II) of solubilized form that uses in the prior art or dry powder form, the invention provides a large amount of solid sulphuric acid salt particles, it is believed that its oxidation-resistance of being more convenient for distributing and having more.Therefore exemplary composition of the present invention comprises a large amount of solids, and described solids comprise ferrous sulfate (II), tin sulphate or its mixture, and described particle is dispersed in the liquid vehicle basically equably.
In a preferred composition, liquid vehicle is the water dispersion that comprises sulphate particles (as tin sulphate) and viscosity modifier (VMA).The example of VMA comprises welan gum (welan gum), xanthan gum, You Tan (diutan) glue and ether of cellulose.In another preferred composition, liquid vehicle can comprise alkanolamine, as the form of trolamine, tri-isopropanolamine, diethanolamine and salt thereof; And liquid vehicle can randomly comprise water.It is believed that in liquid composition of the present invention to comprise a large amount of vitriol, because when introducing water, in vitriol can be included in solids and two kinds of forms of dissolving simultaneously as liquid vehicle or as liquid vehicle a part of.
When comparing, use liquid vehicle that bigger tolerance range and accessibility is provided with drying material.In addition, liquid product provides bigger advantage in environmental health and secure context, because it has eliminated the possibility that the people sucks chemical dust.In addition, the dose effect when using liquid vehicle to cause the dose effect of tin sulphate to be not less than the tin sulphate that adds dried forms, the advantage that provides liquid to add simultaneously to tin sulphate.
The present invention is used for reducing the illustrative methods of cement chromium and comprises introduce the liquid composition that above-mentioned comprising is dispersed in the sulphate particles in the liquid vehicle in the mutual grinding operation of cement clinker.Or sulfate dispersion of the present invention can be added in cement and cementing compositions such as concrete, masonry mortar, gypsum, the sprayed concrete etc. with the form of adulterant composition.The present invention also provides the cementing compositions that comprises hydratability cement and aforesaid liquid composition.
Other illustrative methods of the present invention and composition also can comprise optional viscosity modifier, at least a or multiple following material except sulphate particles sexavalent chrome (" CrVI ") reductive agent: (A) at least a other hexavalent chrome reduction agent (as metal-salt); (B) be total to additive, comprise antioxidant, oxygen scavenger or its mixture; (C) at least a cement additire (as alkanolamine); Or (D) aforementioned any mixture.
Further advantages of the invention and feature will describe in further detail hereinafter.
Description of drawings
Fig. 1 uses various forms of tin sulphates for expression and reduces the legend of chromium, and described various forms comprises 20% solution (prior art), dry powder form (prior art) and two kinds of liquid vehicle dispersion forms of the present invention.
The detailed description of exemplary
Therefore, generalized as preceding institute, but the present invention relates to the chromium reducing composition of liquid dispersion, be used for reducing the method for chromium of matrix material and matrix material by using described chromium reducing composition to make.
Term used herein " cement " is meant the Portland cement (Portlandcement) that is used for building commerce, it is meant that described cement clinker is made up of the calcium sulfate that contains one or more forms (ASTM type i, II, III, IV or V) as levigate adulterating agent usually by grinding or grinding the hydratability cement that cement clinker is made mutually." bonding " material is such material, and they have when water exists individually solidifies and the hardened hydraulicity or hydratability cementing property.Matrix material comprises grinding granulated blast furnace slag (though some air cooled slag also can be considered to agglutinating) and Roman cement (as usual Portland cement)." bonding " material also can comprise gypsum (as calcium sulfate hemihydrate), aluminate cement, ceramic cement, oilwell drilling cement, reach other.
Solids sulfate dispersion of the present invention can be used in the cement manufactory, as directly being used in shredder (as ball mill, roll mill), separator, the classifier, or is used in bag technology of the package.Dispersion also can be used on cement neutralization after the manufacturing and is used in cementing compositions such as concrete, masonry mortar (mortar masonry), gypsum fire prevention body, sprayed concrete and other composition.
Except that Portland cement, the term " cement " that the present invention uses can comprise volcanic ash, its be have seldom or do not have cementing value (promptly, as tackiness agent) the material of siliceous or silicon-aluminum containing, but when water exists, the volcanic ash of form in small, broken bits and the calcium hydroxide generation chemical reaction that discharges by the Portland cement hydration, thus material formed with cementing property.For example referring to Dodson, V., Concrete Admixtures(Van Nostrand Reinhold, New York1990), 159 pages.Diatomite, Wingdale, clay (as metakaolin), shale, flying dust, siliceous smog and blast-furnace slag also are that some belong to the material in the known volcanic ash.Some grinds granular blast-furnace slag and high calcium flying dust and had not only had and coagulate rigid but also have cohesiveness.
The invention provides and comprise the liquid composition that is dispersed in the solid sulphuric acid salt particle in the liquid vehicle.It is believed that described vitriol based additive can be reduced into chromium III with chromium VI effectively, and it can be known as " chromium reducing agent " in this article sometimes.Illustrative methods of the present invention is included in and adds described liquid composition (sulphate particles chromium reducing agent) in the process of mutual grinding cement clinker in cement clinker, thereby makes hydratability cement.
An illustrative methods making described liquid composition merges as the water dispersion with at least a viscosity modifier (VMA) with liquid vehicle for the vitriol (as tin sulphate, ferrous sulfate (II)) with the solids form.VMA makes and might produce the concentration sulfate dispersion of homogeneous basically, even also be like this afterwards in the quite long shelf lives (as 28 days).Viscosity modifier (VMA) should provide the absolute dilution (sheerthinning) of being convenient to pumping liquid dispersion of the present invention feature.In addition, VMA should not can hinder the effect of cement admixture composition in the end using.
Term viscosity modifier used herein (" VMA ") is meant the reagent of dried enriched material form, or when it is dispersed in the water and become the reagent of high viscosity liquid thus.The suitable VMA of high viscosity liquid form it is believed that and be particularly suitable for purpose of the present invention, and it can be available from GraceConstruction Products, Cambridge, and Massachuetts, commodity are by name to be V-MAR
Figure C20048003444900081
3.This VMA is based on outstanding smooth glue (available from CP Kelco), and contains water and dispersion agent, as can be available from the commodity of Grace ADVA by name Those dispersion agents.
The present invention can use other viscosity modifier (VMA).They include but not limited to: (a) biological polymer polysaccharide is selected from welan gum, outstanding smooth glue, xanthan gum, sandlwood carbohydrate gum (rhamsan), gellan gum (gellan), dextran, amylopectin, heat polysaccharide (curdlan) and derivative thereof with fixed attention; (b) ocean glue is selected from phycocolloid, agar, carrageenin and derivative thereof; (c) plant secretion thing is selected from Viscogum BE, Sudan Gum-arabic, kuteera gum, yellow work glue, dawa gum (Ghatti) and derivative thereof; (d) seed glue is selected from guar gum, Viscogum BE, gumbo glue, plantago mucilage, mesquite gum and derivative thereof; (e) starch-based glue class is selected from ether, ester and derivative thereof (for example referring to US 6,1110,271, the 3 hurdles, 38-46 is capable); With their mixture; And (f) relevant thickening material, be selected from the urethane copolymers of the expandable acrylic copolymer of alkali, the hydrophobically modified of hydrophobically modified, based on the relevant thickening material of urethane, Mierocrystalline cellulose (for example Natvosol, carboxymethyl hydroxyethyl cellulose), polyacrylic ester and polyethers.
Tin sulphate is 330g/l (for example referring to Encyclopedia ofChemical Technology, the 4th edition .24 volume, the 129th page) 25 ℃ solubleness.The invention enables the concentration that will be loaded into the tin sulphate in the liquid vehicle to be higher than usually by described vitriol being dissolved in resulting concentration in the independent water.For example, when in the mixture that the solids tin sulphate is dispersed in water and viscosity modifier, might obtain to account for the tin sulphate dispersion of gross weight 56%, wherein 35% tin sulphate will be as solid dispersed, and 21% tin sulphate will be dissolved in the solution.On behalf of the amount of the tin sulphate of carrying with liquid form, this surprising increase is arranged.
Other the exemplary liquid vehicle of tin sulphate or ferrous sulfate of being used to suspend comprises alkanolamine, it can be nonaqueous, if or used water, then described liquid vehicle to be essentially the part water-based in addition.Exemplary alkanolamine comprises the form of trolamine, tri-isopropanolamine, diethanolamine and salt thereof.
Exemplary chromate reduction liquid composition of the present invention comprises: the chromate reduction active substance of solid sulphuric acid tin particulate forms (mean particle size is 0.001 to 1.0 micron), and its content is 40-70% based on the dry weight of composition; Water, its content is 5%-50% based on the gross weight of liquid composition; With biological polymer polysaccharide viscosity modifier, it is selected from outstanding smooth glue and xanthan gum, and the content of described biological polymer polysaccharide is 0.1%-10% based on the gross weight of liquid composition.
Other exemplary composition of the present invention except comprising ferrous sulfate (II) or tin sulphate (II), can further comprise other chromium reducing agent (as metal-salt), includes but not limited to tin protochloride, manganous sulfate, iron sulphide and/or iron protochloride.
The exemplary that the present invention is other except the sulphate particles that comprises the dispersion form, can further comprise at least a cement additire, and it comprises alkanolamine, glycol, sugar, chloride salt or its mixture.The consumption of one or more optional cement additires can be 5%-80% based on the gross weight of liquid composition.
In the present invention other exemplary composition and method, the contriver consider might with make ferrous sulfate (II) and/or tin sulphate solids more the sludge proof material coat or capsule seals described particle, these materials do not hinder described particle to be dispersed in equably in the aforesaid liquid carrier basically, and these materials do not hinder above-mentioned particle as the effect of chromium reducing agent in cementing compositions.Exemplary capsule closure material or coating material can comprise polysaccharide, starch, carbohydrate or its improved form; Polyethylene; With other polymer materials.
Other illustrative methods of the present invention, except the agent of sulfuric acid alkali hexavalent chrome reduction, further comprise and in cement clinker, introducing as the antioxidant, oxygen scavenger or its mixture that are total to additive, vitriol reagent is carried out in being introduced in before the described grinding or in the process of lapping of these materials: the ratio of additive is 99.5: 0.5 to 20: 80 altogether; More preferably ratio is 99: 1 to 50: 50; Most preferably be 95: 5 to 60: 40.
Though also inessential, preferably sulfuric acid alkali chromium reducing agent salt and optional common additive (antioxidant and/or oxygen scavenger) both are distributed in the same fluid additive composition.Not so not preferably, as before cement clinker grinds, in the process or add additive altogether afterwards discriminably.
Therefore, no matter be that combination is added or added respectively, the amount of total common additive (antioxidant and/or oxygen scavenger) should be 0.05 to 80.0% based on the gross weight of fluid additive composition, more preferably 0.5 to 50.0%, most preferably 1.0 to 30.0%.
Term used herein " antioxidant " is meant such composition, material or compound, particularly when they are incorporated in the fluid additive composition that contains above-mentioned sulfuric acid alkali chromium (VI) reductive agent, it reduces rate of oxidation or reduces unwanted oxygenizement to the hexavalent chrome reduction agent in others.For example United States Patent (USP) 5,211,875 disclose and it is believed that and be fit to antioxidant of the present invention, for example 2,6-two (tertiary butyl)-4-cresols (BHT), 2,2 '-methylene radical-two (the 6-tertiary butyl-p-cresol), the triphenyl phosphorous acid ester, three-(nonyl phenyl) phosphorous acid ester and dilauryl sulfo-malonic ester.Also it is believed that other antioxidant such as United States Patent (USP) 6,465, the sulfurous gas described in 065, THBP 2,4,5 trihydroxybutyrophenone and butylated hydroxy anisole also are fit to the present invention.Aforesaid, these antioxidants can be attached in the same fluid additive composition with vitriol, or, not so not preferably, before grinding, in the process or in cement or cement clinker, add these antioxidants afterwards respectively.The consumption of antioxidant should be preferably 0.05 to 80% based on the gross weight (if being attached in the composition) of fluid additive composition, and more preferably 0.5 to 50%, most preferably 1.0 to 30.0%.If separate adding with fluid additive, then the amount of antioxidant can be 0.1ppm to 1000ppm, more preferably 1.0-300ppm, most preferably 5-100ppm (based on the umber of per 1,000,000 parts of dry cement weight).
Term used herein " oxygen scavenger " is meant such composition, material or compound, when being comprised in the fluid additive composition that comprises sulfuric acid alkali CrVI reductive agent, they can remove deoxidation, for example (a) by staying the oxygen reaction or combine with carrying, or (b) obtain harmless product by catalytic oxidation.
Can be used as the exemplary oxygen scavenger of additive altogether of the present invention and include but not limited to that (a) contains the compound of ethylenically unsaturated hydrocarbons; (b) phenol or its salt or derivative; (d) azanol or hydrazine or derivatives thereof; (e) sulfurous acid or its salt or derivative; (f) transition metal complex; Or its mixture.
The exemplary oxygen-scavenging compositions of one class comprises ethylenically unsaturated hydrocarbons.Ethylenically unsaturated hydrocarbons can use separately or use with transition-metal catalyst.Ethylenically unsaturated hydrocarbons can be replacement or unsubstituted.As defined herein, unsubstituted ethylenically unsaturated hydrocarbons is anyly to have at least one aliphatic carbon-to-carbon double bond and comprise the carbon of 100 weight % and the compound of hydrogen.The ethylenically unsaturated hydrocarbons of the replacement of this paper definition is to have at least one aliphatic carbon-to-carbon double bond and comprise the carbon of about 50 weight %-99 weight % and the compound of hydrogen.Preferred replacement or unsubstituted ethylenically unsaturated hydrocarbons have the compound of two or more ethylenically unsaturated groups for those per molecules.
The preferred example of unsubstituted ethylenically unsaturated hydrocarbons includes but not limited to: diene polymer such as polyisoprene, (as using trans-polyisoprene), polyhutadiene (particularly 1, the 2-polyhutadiene, have more than or equal to 50% 1, the 2-microstructure), and multipolymer, as styrene butadiene.Described hydrocarbon also comprises polymer compound, as polypenthylene, poly-octene and other polymkeric substance by the olefin metathesis preparation; Diene oligomer such as squalene; And derive from Dicyclopentadiene (DCPD), norbornadiene, 5-ethylidene-2-norbornene or other contains polymer of monomers or the multipolymer that surpasses a carbon-to-carbon double bond (conjugation or unconjugated).These hydrocarbon comprise carotenoid such as β-Hu Luobusu further.
The preferred ethylenically unsaturated hydrocarbons that replaces includes but not limited to that those contain the compound of oxygen part, as ester, acid acid, aldehyde, ether, ketone, alcohol, superoxide and/or hydroperoxide.The composition that uses also can comprise the mixture of two or more above-mentioned replacements or unsubstituted ethylenically unsaturated hydrocarbons.
As mentioned above, ethylenically unsaturated hydrocarbons can advantageously use with transition-metal catalyst under many circumstances.Though be not bound by any particular theory, the proper metal catalyzer is those compounds of change between at least two kinds of oxidation state easily.Referring to Sheldon, R.A.; Kochi, J.K.; " Metal-Catalyzed Oxidations of Organic Compounds " (Academic Press, NeW York 1981).Preferably, transition-metal catalyst is the form of the salt that forms with the metal that is selected from the periodictable first, second or the 3rd transition series.Proper metal includes but not limited to manganese II or III, iron II or III, cobalt II or III, nickel II or III, copper I or II, rhodium II, III or IV and ruthenium.When metal is introduced in fluid additive or be introduced in the cement, the oxidation state that the oxidation state of metal need not activity form.Metal is preferably iron, nickel or copper.More preferably manganese, most preferably cobalt.The proper metal counterion includes but not limited to muriate, acetate, stearate radical, palm acid group, 2 ethyl hexanoic acid root, neodecanoic acid root or cycloalkanes acid group.
The unsaturated additive altogether of the olefinic of the replacement of preferred classes comprises enediol.The example of commercially available enediol comprises xitix and saccharosonic acid and salt (as sodium ascorbate, SODIUM ISOVITAMIN C) or derivative.Any stereoisomer of these compounds can be effective in the present invention.Xitix/the ascorbate salt of an alkali metal salt and alkaline earth salt such as potassium or sodium is preferred.
The exemplary of use enediol in addition comprises the activator of the oxygen scavenging capacity that is used to strengthen enediol.For example, United States Patent (USP) 4,524,015 discloses the particulate mixtures that uses ascorbate salt or xitix, alkaline carbonate, iron cpd, blackout and water.Therefore, these can be considered to useful enediol activator.
Illustrative methods that the present invention is other and composition can comprise the activator that is used to contain the enediol compound, as transistion metal compound, complex compound or inner complex.The more preferably transition metal of chosen from Fe, copper, cobalt or nickel.Most preferably iron or copper.Preferably supply form of transition metal is (1) compound as the ordinary salt of transition metal ion, or the poly-alkyl polyamine of (2) transition metal ion (" PAPA ") inner complex, big cyclammonium (" big ring ") inner complex or amino poly-carboxylate inner complex.Also may use other to contain the transition metal chelate of one or more amine, hydroxyl, carboxylate or sulfhedryl or its combination.
Metal catalyst can comprise simple transition metal salt such as iron protochloride or iron(ic) chloride, cuprous chloride or cupric chloride, ferrous sulfate or copper sulfate, Ferrous Gluconate, single nickel salt or cobalt chloride, and they are more preferably, most preferably copper sulfate.The transition metal amine of chelating is the metal catalyst that particularly suitable uses with ascorbate salt, because when using with suitable amount, they have oxygen scavenging matter, this has increased the oxygen scavenging matter of ascorbate salt, therefore makes metallo-chelate remove compound as second.And, but the oxygen of the transition metal ion catalysis ascorbate salt in the complex compound is removed activity.In the chelating ion complex compound, preferably poly-alkyl polyamine; More preferably those have the complex compound of the carbochain of symmetrical length between adjacent nitrogen atom, and most preferably those each described chains comprise 1-4, and the best is the complex compound of 2 carbon atoms.Also can use the transition metal chelate of ethylenediamine tetraacetic acid (EDTA) (" EDTA "), as Fe++/EDTA/ (2Na+).
Therefore other exemplary oxygen scavenger can comprise independent transition metal complex (as except with above-mentioned enediol uses).This material is by Aquanautics, Inc., Alameda, California exploitation.(referring to Packaging Technology, " OxygenEliminator Extends Shelf Life, " 1989 and " Extending the Life of a Bottleof Beer, " New York Times, Mar.29,1989).These materials (yet being not uniquely) especially are that those are at transition metal and United States Patent (USP) 4,959, the complex compound that forms between the poly-alkylamine of the what is called of describing in 135 (described document is merged in this paper as a reference), and those are at transition metal with as United States Patent (USP) 4, the complex compound that forms between " the big cyclammonium " described in 952,289 (described document is merged in this paper as a reference).
In the present invention, these transition metal complexes can and can be used as oxygen scavenger in conjunction with oxygen.These complex compounds can not form or not be activated (promptly can not or debond oxygen), are exposed to together under water or the water vapor up to amine and metal.
Do not wish to be bound by theory, the contriver believes that common additive (antioxidant and/or oxygen scavenger) can advantageously play a role by following one or more mechanism.At first; additive can be used as classical antioxidant/oxygen scavenger altogether; thereby any preferential additive reaction together of oxygenant (molecular oxygen etc.) that enters in the liquid carrier medium that contains the CrVI reductive agent, thereby protect employed sulfuric acid alkali CrVI reductive agent and any other metal-salt CrVI reductive agent.This had increased its storage life for sulfuric acid alkali CrVI reductive agent and other metal-salt reductive agent effectively before they are added into cement mill or are added in the cement of grinding.
The contriver believes that also aforementioned mechanism also works after sulfuric acid alkali CrVI reduction liquid composition has been added in the cement.When outside moisture and molecular oxygen were penetrated in the cement of processing, oxygen will be before itself and the reaction of sulfuric acid alkali CrVI reductive agent be removed by additive altogether.For this purpose, preferably sulfuric acid alkali CrVI reductive agent is pre-mixed into single fluid additive with optional additional metals salt and/or common additive (antioxidant and/or oxygen scavenger).
The contriver believes that also the common additive that contains antioxidant and/or oxygen scavenger can react, thereby the vitriol of any reduction chromium of regeneration or other metal-salt reductive agent, thereby keep the used sulfate reduction agent or the level of any other reductive agent by having decomposed with the chance reaction of foreign molecules oxygen (or other unwanted oxygenant).This mechanism can be before the fluid additive composition be added to cement, between the shelf lives of finished cement or when finished product cement is used to make mortar or concrete, play a role.
The contriver believes that further the common additive that contains antioxidant and/or oxygen scavenger can form adducts with CrVI reductive agent (sulfuric acid alkali reagent and any other metal-salt) or with its oxidised form such as tin (IV) (itself is active CrVI reductive agent).
Other embodiments comprise is of value to the agent combination that cement is made with sulfate reduction agent and above-mentioned common additive (antioxidant and/or oxygen scavenger) and one or more.These reagent comprise cement auxiliary agent such as glycol, glycerine, amine, alkanolamine and known cement quality modifying agent such as sodium-chlor, nitrocalcite, calcium nitrite, sugar, reach other.Two pure and mild glycerine are considered to improve the stability in storage of tin salt.The mechanism of this benefit is unknown, but its activity that may relate to molecular oxygen in the presence of glycol or glycerine reduces.
Other exemplary common additive comprises the phenol that can be used as oxygen scavenger, as its quinone and OH-form, yet comprises and is not limited to quinhydrones (hydroquinol), pyrocatechol (neighbour-dihydroxy-benzene) and derivative thereof.
Further exemplary oxygen is removed altogether, and additive comprises azanol, hydrazine or its salt or derivative.Exemplary azanol has by structure shown in the following formula,
Figure C20048003444900141
R wherein 1And R 2Comprise hydrogen or C separately 1-C 18Alkyl, thiazolinyl or aryl.
Exemplary hydrazine has by structure shown in the following formula:
Figure C20048003444900142
R wherein 1, R 2, R 4And R 4Comprise hydrogen or C separately 1-C 18Alkyl, thiazolinyl or aryl.Exemplary hydroxylammonium salt comprises oxammonium hydrochloride (NH 2OHHC1) and hydroxylamine sulfate ((NH 2OH) 2H 2SO 4); And exemplary hydrazonium salt comprises hydrazine hydrochloride (N 2H 4HC1 or N 2H 42HC1) and hydrazonium sulfate (N 2H 4H 2SO 4).
Exemplary hydroxyalkyl azanol has formula HO-N-CH 2-[CH (OH)-R] 2Structure, wherein R is selected from H and C 1-C 10Alkyl; Be initial reaction rate about more than 1.5 times between the alkyl azanol of dissolved oxygen and corresponding non-hydroxylated wherein in the initial reaction rate between described hydroxyalkyl azanol and the dissolved oxygen.Another hydroxyalkyl azanol is selected from N, two (2-hydroxyethyl) azanols of N-, N, two (2-hydroxypropyl) azanol and the N of N-, two (2-hydroxybutyl) azanols of N-.
Exemplary oxygen scavenger in addition additive altogether comprises sulfurous acid or its salt, as sulphite, hydrosulphite or thiosulfite.Therefore, for example an alkali metal salt and the sulfuric acid alkali chromium reducing agent of alkali metal salt together can be attached in the fluid additive composition, the form of described an alkali metal salt is for example S-WAT or hydrosulphite or potassium sulfite or hydrosulphite.
In other exemplary of the present invention, sulphite can use with other common additive combination.For example, United States Patent (USP) 4,384,972 disclose use metal-salt, alkaloid substance, sulphite or other deliquescence compound and optional xitix or its salt.
More preferably, illustrative methods of the present invention and fluid additive composition comprise that use sulfuric acid alkali chromium reducing agent and two or more comprise the common additive of antioxidant, oxygen scavenger or its mixture.Therefore, the preferred method of the present invention is included in the mutual process of lapping of cement clinker at least two kinds of antioxidants and/or oxygen scavenger is incorporated in the cement clinker.For example, xitix and sulphite (or its salt and derivative) use capable of being combined.As another example, phenol and azanol (or its salt and derivative) use capable of being combined.Preferably, these combinations can join in the same fluid additive composition with sulfuric acid alkali chromium reducing agent, but it is believed that they also can be before the cement clinker grinding operation, in the process or be added in the cement afterwards.
Provide following examples and embodiment only to be used for illustration purpose, it is not construed as limiting scope of the present invention, and the those of ordinary skill in ability city openly can carry out various changes to it by this paper.
Embodiment 1
The preparation of tin sulphate composition of the present invention: tin sulphate particle (56gm) and outstanding smooth matrix VMA (44gm) are mixed together.Described VMA is available from Grace Construction Products, and commodity are called V-MAR
Figure C20048003444900151
3.Other suitable VMA can comprise xanthan gum, welan gum and ether of cellulose, and the preferred dispersion agent of choosing wantonly that uses is dispersed in the water.
Performance between table 1 expression tin sulphate solid, tin sulphate dispersion and the tin sulphate solution relatively.All additives are ground mutually enter the slag cement for preparing in the ball mill of laboratory.In the cement for preparing in the laboratory, the ratio of various materials is as follows: 70% cement clinker, 25% slag, 2.8% gypsum, 1.9% plaster.Abrasive material prepares in envrionment temperature.
The additive capacity of chromate reduction additive is shown in the table 1.Give the dosage of activared carbon sulfur tin part.Provided the solvable ppm Cr (measuring) of the cold grinding material that is used to prepare with chromic salt, and at the umber of 180 ℃ of heat treated abrasive materials.The purpose of thermal treatment abrasive material is to determine the relevant antagonism of Cr reductive agent to environmental oxidation, and its validity after cement stores thus.
It is suitable with the dose effect of the tin sulphate of dry powder form that observed value with lower soluble chromium, the dose effect of the tin sulphate of dispersion form seem, and surpass the dose effect of the tin sulphate of solution form.
Measuring the cement pore water with the amount of the 1000000/chromium that a (PPM) represents by UV carries out.Dissolubility chromate can be discerned by the UV peak at 277nm and 375nm place.Calibrate by potassium bichromate solution.By preparing the ratio of cement and water wherein is that 2: 1 grout obtains the cement pore water.After mixing 9 minutes, grout is left standstill and aging 30 minutes.Grout is centrifugal, and supernatant decanted liquid also filters, and (BDL in institute's subordinate list is meant ' is lower than limit of detection ' (<0.5ppm)) to obtain pore water.
Table 1
The chromate reduction additive Additive (ppm) Tin sulphate (ppm) Cold grinding material ppm Cr Thermal treatment abrasive material ppm Cr
Do not have -- -- 8 9
The tin sulphate powder 40 40 3 4
56% tin sulphate dispersion 71 40 BDL BDL
20% tin sulphate solution 400 80 2 6
The tin sulphate powder 100 100 BDL BDL
56% tin sulphate dispersion 179 100 BDL BDL
20% tin sulphate solution 1000 200 BDL 6
Example II
The cement that use has following composition percentage ratio carries out similar experiment: 95% cement clinker, 2.8% gypsum, 1.9% plaster.Sample chromate reduction performance separately is shown in the table 2.
Table 2
The chromate reduction additive Additive (ppm) Tin sulphate (ppm) Cold grinding material (ppm) Thermal treatment abrasive material (ppm)
Cr Cr
56% tin sulphate dispersion 179 100 14 18
56% tin sulphate dispersion 357 200 1 5
20% tin sulphate solution 1000 200 9 19
20% tin sulphate solution 2000 400 BDL 1
EXAMPLE III
The cement that use has following composition percentage ratio carries out another test: 65% cement clinker, 7.5% slag, 15.1% Wingdale, 7.5% natural volcanic ash, 2.8% gypsum and 1.9% plaster, percentage ratio is with total weight.In this case, in heat treated cement, the tin sulphate of the 200ppm that sends in dispersion is suitable with the tin sulphate performance of the 300ppm that sends in solution.The result is as shown in table 3.
Table 3
The chromate reduction additive Additive (ppm) Tin sulphate (ppm) Cold grinding material (ppm) Cr Thermal treatment abrasive material (ppm) Cr
Do not have 8 8
56% tin sulphate dispersion 357 200 2 3
20% tin sulphate solution 1500 300 3 3
EXAMPLE IV
The cementing compositions preparation that use has following composition percentage ratio carries out another test: 96% cement clinker, 2.4% gypsum, 1.5% plaster.Compared the tin sulphate of being sent as solid, liquid and dispersion form, the performance of the tin sulphate of sending with the dispersion form equates with the performance of the tin sulphate of sending with solid form undoubtedly, and the 200ppm tin sulphate of sending in solution can not be with chromate reduction to same degree.
Table 4
The chromate reduction additive Additive (ppm) Tin sulphate (ppm) Cold grinding material (ppm) Thermal treatment abrasive material (ppm)
Cr Cr
Do not have 8 9
56% tin sulphate dispersion 357 200 BDL BDL
20% tin sulphate solution 1000 200 5 8
The tin sulphate powder 200 200 BDL BDL
EXAMPLE V
Also tin sulphate can be suspended in the liquid vehicle that comprises at least a alkanolamine as dried particle.Find the efficient of the dose effect of tin sulphate aspect reducing chromate greater than tin sulphate solution, and roughly suitable with the dose effect of the tin sulphate of dry powder form.
Use following component preparation tin sulphate dispersion: water (20g), tin sulphate (34g) and tri-isopropanolamine (46g).Can be by replacing tri-isopropanolamine to prepare another dispersion with the di-alcohol Yi Bingchunan.
Two kinds of alkanolamines all can be used for replacing in the preparation of tin sulphate with ferrous sulfate (II), and discovery is still effective when the required dosage with ferrous sulfate reduces 20-30%, but suspension presents muddy appearance of black.
Below the table 5 expression test-results of using cement to carry out with following ratio: 96% cement clinker, 2.4% gypsum, 1.5% plaster.The preparation of this test material therefor is identical with the serial experiment of the liquid vehicle (water dispersion) of use VMA preparation with evaluation method.Observe in solution, comprise 50ppm tin sulphate and 71ppm tin sulphate sample less than the performance that is dispersed in the tin sulphate in tri-isopropanolamine (" TIPA ") (it is believed that also TIPA oneself does not have the effect of the chromate reducer separately) liquid vehicle.
Table 5
The chromate reduction additive Additive (ppm) Tin sulphate (ppm) Cold grinding material (ppm) Cr Thermal treatment abrasive material (ppm) Cr
Do not have 0 8 ---
Tin sulphate dispersion w/TIPA 76 26 2 4
Tin sulphate dispersion w/TIPA 97 33 1 4
Tin sulphate dispersion w/TIPA 147 50 BDL 1
20% tin sulphate solution 250 50 3 3
20% tin sulphate solution 355 71 3 3
Example VI
Use following component preparation tin sulphate dispersion: water (20g), tin sulphate (26g) and trolamine (54g).Before just adding mixing water, this chromate reduction composition is mixed in the finished cement (making in shredder) with dried adulterant form then.Obtain the cement pore water as previously mentioned, and measure chromic salt by UV as previously mentioned.The result is shown in Figure 1.
The foregoing description and exemplary attempt to be used to illustrate the present invention, model figure of the present invention are not construed as limiting.Those of ordinary skill in the art can carry out various changes and variation to it by this paper is open.

Claims (14)

1. chromium reduction liquid composition comprises:
Contain simultaneously with solubilized form and basically homogeneous dispersive mean particle size be the water liquid carrier of the tin sulphate that exists of the solids form of 0.001-1.0 micron, the described dispersed solids of homogeneous basically particle is dispersed in the described liquid vehicle with the amount that is no more than 70% at least 40% with the dry weight based on described composition;
Described water liquid carrier comprises that the gross weight based on described liquid composition is the water of the amount of 5-50%;
Described water liquid carrier further comprises the biological polymer polysaccharide viscosity modifier that is selected from outstanding smooth glue and xanthan gum, the content of described biological polymer polysaccharide based on the gross weight of described chromium reduction liquid composition at least 0.1% to being no more than 10.0%; With
The effect of described biological polymer polysaccharide viscosity modifier provides the concentration homogeneous of described tin sulphate in described chromium reduction liquid composition, even also is like this in described chromium reduction liquid composition stores after 28 days, and provide and be convenient to the described chromium of pumping reduction liquid to the absolute dilution feature of grinding from grog the cement manufacturing processed that obtains cement, the content of tin sulphate is higher than usually the content that is reached when tin sulphate being dissolved in the independent water in the described water liquid carrier.
2. the composition of claim 1 further comprises at least a alkanolamine.
3. the composition of claim 2, wherein said alkanolamine is selected from the form of trolamine, diethanolamine, tri-isopropanolamine and salt thereof.
4. be used for the method for reduction of hexavalent chromium, comprise: the composition that grinds cement clinker and claim 1 mutually.
5. the composition that comprises the composition of hydratability matrix material and claim 1.
6. the composition of claim 1, wherein said particle is coated by the material that can make particle have more oxidation-resistance.
7. the composition of claim 1 further comprises at least a other hexavalent chrome reduction agent except described sulphate particles.
8. the composition of claim 7, wherein said at least a other hexavalent chrome reduction agent is a metal-salt.
9. the composition of claim 1 further comprises ferrous sulfate.
10. the composition of claim 1 further comprises antioxidant, oxygen scavenger or its mixture.
11. the composition of claim 1, wherein said tin sulphate particle is dispersed in the described liquid vehicle to the amount that is no more than 60% at least 50% with the dry weight based on described composition.
12. the composition of claim 1 further comprises at least a cement additire.
13. chromium reduction liquid composition comprises:
Contain simultaneously with solubilized form and basically homogeneous dispersive median size be the water liquid carrier of the tin sulphate that exists of the solids form of 0.001-1.0 micron, described solid sulphuric acid tin particle is at least 40% to be dispersed in substantially equably in the described liquid vehicle to the amount that is no more than 70% with the dry weight based on described composition;
Described water liquid carrier comprises that the gross weight based on described liquid composition is the water of the amount of 5-50%;
Described water liquid carrier further comprises antioxidant, oxygen scavenger or its mixture;
Described water liquid carrier comprises the biological polymer polysaccharide viscosity modifier that is selected from outstanding smooth glue and xanthan gum, the content of described biological polymer polysaccharide based on the gross weight of described chromium reduction liquid composition at least 0.1% to being no more than 10.0%; With
The effect of described biological polymer polysaccharide viscosity modifier provides the concentration homogeneous of described tin sulphate in described chromium reduction liquid composition, even also is like this in described chromium reduction liquid composition stores after 28 days, and provide and be convenient to the described chromium of pumping reduction liquid to the absolute dilution feature of grinding from grog the cement manufacturing processed that obtains cement, the content of tin sulphate is higher than usually the content that is reached when tin sulphate being dissolved in the independent water in the described water liquid carrier.
14. chromium reduction liquid composition comprises:
Contain simultaneously with solubilized form and basically homogeneous dispersive median size be the water liquid carrier of the tin sulphate that exists of the solids form of 0.001-1.0 micron, the described dispersed solids of homogeneous basically tin sulphate particle is at least 40% to be dispersed in the described liquid vehicle to the amount that is no more than 70% with the dry weight based on described composition;
Described water liquid carrier comprises that the gross weight based on described liquid composition is the water of the amount of 5-50%;
Described water liquid carrier further comprises at least a cement additire that is selected from alkanolamine, glycol, sugar and chloride salt; With
Described water liquid carrier comprises the biological polymer polysaccharide viscosity modifier that is selected from outstanding smooth glue and xanthan gum, the content of described biological polymer polysaccharide based on the gross weight of described chromium reduction liquid composition at least 0.1% to being no more than 10.0%; With
The effect of described biological polymer polysaccharide viscosity modifier provides the concentration homogeneous of described tin sulphate in described chromium reduction liquid composition, even also is like this in described chromium reduction liquid composition stores after 28 days, and provide and be convenient to the described chromium of pumping reduction liquid to the absolute dilution feature of grinding from grog the cement manufacturing processed that obtains cement, the content of tin sulphate is higher than usually the content that is reached when tin sulphate being dissolved in the independent water in the described water liquid carrier.
CNB2004800344494A 2003-11-21 2004-07-13 Sulfate dispersion chromate reducer Expired - Fee Related CN100441531C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US52412503P 2003-11-21 2003-11-21
US60/524,125 2003-11-21
US60/541,842 2004-02-04

Publications (2)

Publication Number Publication Date
CN1882515A CN1882515A (en) 2006-12-20
CN100441531C true CN100441531C (en) 2008-12-10

Family

ID=37520172

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2004800344494A Expired - Fee Related CN100441531C (en) 2003-11-21 2004-07-13 Sulfate dispersion chromate reducer

Country Status (1)

Country Link
CN (1) CN100441531C (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SG190815A1 (en) * 2010-12-08 2013-07-31 Denki Kagaku Kogyo Kk Cement admixture, cement composition, and hexavalent chromium reduction method using same
CN102266650B (en) * 2011-05-05 2012-07-25 中国地质大学(武汉) A Method for Detoxification and Solidification of Cr(Ⅵ) Using Metakaolin-based Mineral Polymer Added FeCl2·6H2O
CN104496251B (en) * 2014-11-25 2017-03-22 中国建筑材料科学研究总院 Liquid hexavalent chromium reducing agent and preparation method thereof, cement and preparation method thereof
CN106830725B (en) * 2017-02-21 2020-12-11 辽宁天宝华瑞建材有限公司 Hexavalent chromium reducing agent for cement
CN113620365A (en) * 2020-05-06 2021-11-09 中国石油化工股份有限公司 Deoxidant and application thereof
CN113060948A (en) * 2021-04-01 2021-07-02 重庆康尼睿能商贸有限公司 Cement raw meal and preparation method of cement
CN114989371B (en) * 2022-06-29 2023-10-03 江苏万邦新材料科技有限公司 High-stability reducing agent for building concrete and preparation method thereof
CN115231847B (en) * 2022-08-15 2023-05-23 辽宁天宝华瑞建材有限公司 Cement chromium remover and preparation method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4209335A (en) * 1977-05-25 1980-06-24 Kabushiki Kaisha Takenaka Komuten Method and composition, including particular additive for hydraulic cement, for fixing waste matter
US4784691A (en) * 1980-12-17 1988-11-15 Aktieselskabet Aalborg Portland - Cement - Fabrik Dry cement composition
EP0960865A1 (en) * 1998-05-25 1999-12-01 Chemische Werke Zell-Wildshausen GMBH Agent for the reduction of chromium (VI) ions in cement
EP0976695A1 (en) * 1998-07-25 2000-02-02 Economic Versicherungs-Vermittlung GmbH Grinding aid for cement

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4209335A (en) * 1977-05-25 1980-06-24 Kabushiki Kaisha Takenaka Komuten Method and composition, including particular additive for hydraulic cement, for fixing waste matter
US4784691A (en) * 1980-12-17 1988-11-15 Aktieselskabet Aalborg Portland - Cement - Fabrik Dry cement composition
EP0960865A1 (en) * 1998-05-25 1999-12-01 Chemische Werke Zell-Wildshausen GMBH Agent for the reduction of chromium (VI) ions in cement
EP0976695A1 (en) * 1998-07-25 2000-02-02 Economic Versicherungs-Vermittlung GmbH Grinding aid for cement

Also Published As

Publication number Publication date
CN1882515A (en) 2006-12-20

Similar Documents

Publication Publication Date Title
KR101135941B1 (en) Sulfate dispersion chromate reducer
KR20060136370A (en) Sulfate dispersion chromate reducer
CN100441533C (en) Liquid additive for intergrinding cement
ES2395423T5 (en) Additives and procedures to reduce hexavalent chromium in cement
EP1752428B1 (en) Method for reducing chromium (VI) in cement
CN100441531C (en) Sulfate dispersion chromate reducer
US20060169177A1 (en) Liquid additive for intergrinding cement
CN114230227B (en) Anti-mud concrete glue reducing agent and preparation method and application thereof
CN112778983A (en) While-drilling plugging agent, preparation method of while-drilling plugging agent and application of while-drilling plugging agent in water-based drilling fluid
CN105948589A (en) Harmless treatment method for electroplating sludge
CN106242333B (en) It is a kind of for tufa stone powder as additive of concrete and preparation method thereof
Özkan et al. Investigation of fly ash effect on rheological and filtration properties of drilling muds
JP2010500281A (en) Coordinated metal compounds for reducing chromium
CN104178095A (en) Drilling fluid and preparation method thereof
CN110551488B (en) Clay inhibitor for drilling fluid and preparation method thereof
JPS6355554B2 (en)
CN112661472A (en) Solidification stabilizing material for water-based drill chip landfill and solidification method of water-based drill chips
MXPA06005235A (en) Sulfate dispersion chromate reducer
EP1661871A1 (en) Additive for the manufacture of cement free of soluble chromates
CN115340352B (en) Micro-expansion in-situ leaching uranium mining well cementation fluid and preparation method thereof
CN115583812B (en) Composite modified bentonite and application thereof in preparing concrete
CN115231847B (en) Cement chromium remover and preparation method thereof
CN112592139B (en) Rapid repairing material for concrete defects at deep water part of sluice in complex operation environment
Song et al. Performance Study of Plant Phenol Modified Tapioca Starch in Drilling Fluid
JPS5915476A (en) Mud water adjustment method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
REG Reference to a national code

Ref country code: HK

Ref legal event code: DE

Ref document number: 1097510

Country of ref document: HK

C14 Grant of patent or utility model
GR01 Patent grant
REG Reference to a national code

Ref country code: HK

Ref legal event code: GR

Ref document number: 1097510

Country of ref document: HK

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20081210

Termination date: 20120713