CA2247205C - Activation of swelling clays and processes of using the activated clays - Google Patents
Activation of swelling clays and processes of using the activated clays Download PDFInfo
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- CA2247205C CA2247205C CA002247205A CA2247205A CA2247205C CA 2247205 C CA2247205 C CA 2247205C CA 002247205 A CA002247205 A CA 002247205A CA 2247205 A CA2247205 A CA 2247205A CA 2247205 C CA2247205 C CA 2247205C
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- bentonite
- carboxylic acids
- sequestering agent
- activated
- sodium
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Classifications
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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
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/13—Compounding ingredients
- C04B33/18—Compounding ingredients for liquefying the batches
-
- 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
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/04—Clay; Kaolin
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
- D21H17/69—Water-insoluble compounds, e.g. fillers, pigments modified, e.g. by association with other compositions prior to incorporation in the pulp or paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/03—Non-macromolecular organic compounds
- D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
- D21H17/14—Carboxylic acids; Derivatives thereof
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/03—Non-macromolecular organic compounds
- D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
- D21H17/14—Carboxylic acids; Derivatives thereof
- D21H17/15—Polycarboxylic acids, e.g. maleic acid
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/66—Salts, e.g. alums
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
- D21H17/68—Water-insoluble compounds, e.g. fillers, pigments siliceous, e.g. clays
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S106/00—Compositions: coating or plastic
- Y10S106/04—Bentonite
Abstract
Alkaline earth bentonite can be activated by the use of sodium citrate or other organic sequestering agent as activator. Dry blends of the activator and the bentonite can be provided.
Description
WO 97!33040 PCT/GB97100648 Activation of swelling Clays and Processes of using the Activated Clays This invention relates to the activation of bentonite i and to the use of the activated bentonite in paper making.
Bentonite is usually obtained initially as an alkali earth compound, for instance a calcium and/or magnesium form of bentonite. In order that it can perform satisfactorily, for instance in paper making, it is necessary to activate the bentonite by subj ecting it to ion exchange whereby calcium and/or magnesium is replaced by sodium or other alkali metal or ammonium ion.
The normal way of doing this is to mix the alkaline earth bentonite clay with an aqueous activating solution containing an alkali metal or ammonium compound. For instance the clay may be provided as a powdered pre-blend of the alkaline earth metal clay and the alkali metal or ammonium compound and this pre-blend may be mixed into water and allowed to stand for sufficient time for ion exchange to occur whereafter it is diluted for use.
Alternatively the quarried alkaline earth bentonite canbe added direct to an aqueous activating solution with mixing.
In practice, the activating compound which is conventionally used is sodium carbonate or sodium bicarbonate, typically in an amount of around 5 to 10% by weight based on the weight of clay. The activation is conducted at the natural pH of the dispersion, around pH
10.
Other electrolytes are described in JP-A-6445754, as being added to promote dispersion. It is also known in U.S. 4,613,542 and 4,624,982 to include sodium polyacrylate. Concentrates of bentonite with various alkali metal compounds are also described in EP 485124 and U.S. 5,266,538 and 5,391,228. The bentonite that is introduced into these concentrated slurries can initially be in the form of sodium bentonite but EP 485,124 and U.S.
5,391,228 also mention making slurries by blending calcium bentonite and sodium carbonate activator with water and sodium chloride. Paper making processes using bentonite with an anionic organic polymer are also described in EP
373306 and U.S. 5,015,334.
One problem with known activated bentonites {for instance the activated bentonite powders which are commercially available) is that the sodium carbonate or other activator which is included in them causes the bentonite {when mixed with water) to give a relatively high pH, for instance above pH 9 and often around pH 10.
Accordingly it is necessary to handle the bentonite with the care associated with materials which do generate a pH
of around pH 10. , Another problem is that the conventional sodium carbonate activator undergoes ion exchange during the activation process to form calcium carbonate, with the result that inorganic scale may be formed and deposited from aqueous compositions of these activated bentonites.
This is a particular problem when the water in which the bentonite is being dispersed is, naturally, relatively hard.
Another difficulty with known activated bentonite powders is that it is sometime found to be rather difficult to make a stable aqueous dispersion of the powders. Again, it has been found that these difficulties of achieving a stable dispersion increase with increasing hardness of the water. Thus, when using relatively hard water, for instance having a hardness of above 10°dH and generally in the range 15° to 50°dH, various problems can arise.
Further, the performance of the bentonite, especially when used in paper making, can be less effective at lower pH values than at higher pH values, and in particular bentonite activated in conventional manner tends to be less effective in acid paper making processes (for instance when t the cellulosic suspension has a pH of below 6.5 and often in the range 4.2 to 5.5) than when the suspension has higher pH values.
WO 97/33040 fCT/GB97/00648 We have now discovered a new range of activators which can give improved performance.
According to a first aspect of the invention, we provide a dry clay composition comprising a blend of an alkaline earth bentonite swelling clay and an activating amount of an alkali metal or ammonium salt of a sequestering agent selected from phosphonates, hydroxy carboxylic acids, amino carboxylic acids and poly carboxylic acids.
According to a second aspect of the invention, we provide a process of activating an alkaline earth bentonite swelling clay to an alkali metal bentonite swelling clay comprising mixing the alkaline earth swelling clay with an aqueous activating solution containing an ammonium or alkali metal salt of a sequestering agent selected from phosphonates, hydroxy carboxylic acids, amino carboxylic acids and di- or tri- (or higher) carboxylic acids.
In both aspects of the invention, the sequestering agent is preferably introduced as a sodium salt.
In both aspects of the invention, the sequestering agent is preferably sodium citrate.
The resultant activated bentonites have several advantages. They are easier to handle since they are less alkaline. They can give better performance than the same bentonite subjected to conventional activation with sodium carbonate at about pH 10. They can perform more effectively in paper making processes where conventional activated bentonites are less effective due to the pH or the presence of hardness salts. Thus conventional bentonites tend to be less effective when the celluiosic suspension has pH below about 6.5, for instance in the range 4.2 to 5.5, but the activated bentonites obtained in the invention can perform very well in such suspensions without any significant loss of activity.
Conventional activated bentonites also may have inferior performance when the cellulosic suspension is made using relatively hard water, for instance having a hardness v a above 10°dH and typically in the range 15°dH to 50~dH
Improved performance is obtained using the activated bentonites obtained in the invention in such hard waters.
This improvement may be manifested by improved drainage rates or by reducing scale deposition or both.
The activation process can be conducted by separately introducing the swelling clay and the sequestering agent activator into the water, for instance by adding the swelling clay to a solution of the activator or by adding the activator to a dispersion of the swelling clay. In each of these alternatives, the swelling clay can be introduced as a powder or as a slurry.
Preferably, however, the process is conducted by mixing a pre-blend of the swelling clay and the activator with an appropriate amount of water. The pre-blend is preferably a powder but it can be a liquid composition containing the bentonite and the activator.
The amount of water present during the activation process is generally such that the swelling clay concentration during the process is from 2 to 8% or even up to 10%. Usually it is at least 3% and frequently it is not more than about 5 or 6%, with 4 or 5% often being preferred. These are the amounts which are typical for sodium carbonate activation processes and it is convenient that the same can be used in the invention.
However a further advantage of the activators used in the invention is that they will also cause good activation at a much wider range of concentrations and so good activation can be achieved at clay concentrations in the range 8 to 14 or 15%-. Despite the clay activating during this process and thus potentially becoming very viscous, an advantage of the activators is that the resultant compositions still have adequately low viscosity and good fluid flow properties that they can be handled easily.
It is also possible to conduct the activation at even higher clay concentrations, for instance in the range 15 to 40%. We describe in our copending PCT application WO 97/33041 concentrates having a clay concentration of 15 to 40% and which contain an activating amount of sodium citrate.
5 The sequestering agent seems to function by exchanging with the alkaline earth ions and fixing the exchanged calcium or magnesium ions in a form such that they cannot exchange back into the bentonite. The sequestering agent is usually in the sodium form as this is the preferred cation which is introduced by ion exchange into the bentonite. However other activating cations can be used if desired, such as potassium or ammonium.
Suitable phosphonates which can be used as the sequestering agent can be selected from any of the phosphonates which are known for seguestering alkaline earth metal ions, such as the materials sold under the trade name bequest.
Suitable hydroxy carboxylic acids that can be used include materials such as sodium tartrate or gluconate but the preferred material is sodium citrate. The free acid form can be used if required in preference to the water soluble salt.
Suitable amino carboxylic acids include materials such as DTPA, NTA and EDDHA and EDTA.
Di- or tri- (or higher) carboxylic acids which can be used include malonic acid, succinic acid, glutaric acid, adipic acid and oxalic acid, usually as sodium salts. The acids (and all the sequestering agents) are preferably low molecular weight materials, for instance having a molecular weight below 500 and are usually monomeric. The use of high molecular weight sodium polyacrylate in slurries is already known in EP 485124 and 4613542 and 4624982 but this does not give the benefits of the invention.
The sequestering agent must be used in an amount sufficient to give activation in the defined system and this will be found by routine experimentation. On a weight basis it is generally in the range 1 to 20% based on the dry weight of bentonite, most preferably in the range 3 to 15~.
All these amounts assume that the sequestering agent is the only significant activating material in the composition. Blends of one or more of the sequestering a agents may be used and blends of one or more of the sequestering agents with other beneficial activators such as sodium carbonate can be used if required. If sodium carbonate is present, then it may reduce the amount of l0 sequestering agent which is required. The amount of sequestering agent may have to be increased significantly if undesirable components such as sodium chloride are present to any significant extent and accordingly it is preferred that no deliberate additions of simple electrolytes such as sodium chloride, sulphate or nitrate are made.
As the bentonite, one can use any of the anionic swelling clays that are conventionally referred to as bentonite-type clays or as bentonites. They are generally smectites or montmorillonites, the latter being preferred.
Suitable smectite or montmorillonite clays include Wyoming bentonite and Fullers Earth and various clays include those known by the chemical terms of hectorite and bentonite.
The clay will be in the alkaline earth form, usually calcium or calcium and magnesium form.
It is very well known to include bentonite in paper making processes for various purposes and the invention is applicable to ail of these. For instance the bentonite may be included as a pitch dispersant.
One paper-making process to which the invention can be applied is a process in which bentonite is added to a cellulosic suspension, typically in an amount of 0.02 to 2~
dry weight and a medium or high molecular weight (e. g., above 500000) polymeric retention aid is added ' subsequently, genera2ly after the last point of high shear (for instance just in front of the head box immediately prior to drainage), The high molecular weight polymer can be non-ionic, anionic or cationic. The cellulosic suspension can be made from relatively pure pulp or froth pulp having a relatively high cationic demand.
Processes of this type that are of particular value are those in which the pulp has a relatively high cationic demand and the polymer is substantially non-ionic or anionic and the paper product is preferably newsprint or fluting medium. Processes of this type in which the total filler content is relatively low are described in U.S.
4305781 and EP-A-17353 to which reference should be made for further details of suitable non-ionic or low ionic polymers and suitable cellulosic suspensions. More highly anionic or cationic polymers may be used. These processes are of particular value when the cellulosic suspension contains de-inked waste. Suitable polymers and fillers (when the pulp is filled) are also described in EP-A-608989 and AU-A-63977/86.
The invention is of particular value when applied to microparticulate retention processes in which a polymeric retention aid is added to the aqueous suspension, the suspension is subjected to shearing and the bentonite is then added after the shearing, and often after the last point of high shear, for instance just prior to the head box prior to drainage. The polymer may be non-ionic or anionic but is often cationic.
The cationic polymer can be a natural material such as cationic starch but is preferably a substantially linear synthetic cationic polymer having molecular weight above 500,000. The amount of cationic polymer that is present in the dispersion at the time of shearing should be sufficient that flocs are formed by the addition of the polymer and the flocs are broken by the shearing to form microflocs that resist further degradation by the shearing but that carry sufficient charge to interact with the bentonite to give better retention and/or formation than is obtainable when adding the polymer alone after the last point of high shear.
The shearing can be due merely to turbulent passage along a duct or can be due to passage through a centriscreen, a pump or other shear-applying device.
Preferred processes include those commercialised by the applicants under the trade mark Hydrocol and preferred processes are described in, for instance, U.S. patents 4753710, 4913775 and 4969976. The optimum amount of polymer for any particular process can be determined by routine experimentation, and will depend inter alia on whether low or medium molecular weight cationic polymer, and/or dry strength resin, had been incorporated in the aqueous suspension at some earlier stage.
The activated bentonite of the invention can be used wherever activated bentonite is useful, for instance in pulp dewatering, paper sludge dewatering, liquid/solids separation processes, effluent clarification, inky waste water clarification and pitch fixing (in paper making processes). The activated bentonite can also be used in other industries which utilise activated bentonite, for instance in the preparation of bentonite for iron ore pelletisation or other mineral processing uses.
The following are some examples.
Example 1 5 parts by weight calcium bentonite was activated in 95 parts by weight of an aqueous solution containing the activator, and the amount of activator, specified below.
In each instance, the amount of activator is expressed as a percentage based on the dry weight of bentonite. The products which were used we as follows.
A - sodium carbonate - 6%
C - sodium citrate - 17%
D - sodium EDTA - 21%.
F~'~amE~~.
a The activated bentonites prepared in Example 1 are used in a laboratory simulation of the paper making process as described in US 4753710. In particular a thinstock of 0.5% bleached Kraft Fibre Furnish has added to it 500 g/t of a high molecular weight (intrinsic viscosity 6 dl/g) cationic polyacrylamide formed from 40% by weight dimethylaminoethyl acrylate quarternised by methyl chloride and 60% by weight acrylamide. The cellulosic suspension is sheared for 60 seconds.1,500 rpm, the activated bentonite is then added in the dose specified, the suspension subjected to gentle mixing in a baffled Britt jar and the Schopper Reigler drainage times recorded for 700 ml to drain from 1,000 ml of the thinkstock. In this test, the lowest possible drainage time gives the best results, and low bentonite amounts are preferred.
In the following tables, the figures in the columns marked "Bentonite" are in g/t dry weight and the figures in the columns marked with a letter are the drainage time in seconds when using the specified amount of the activated bentonite identified in Example 1.
In this table, the column headed Ca represents the results using unactivated calcium bentonite.
Table 1 Bentonite Ca A C D
This data shows that citrate activation (column C) can give results as good as or better than sodium carbonate activation as regards drainage time, and that adequate, but less satisfactory, results can be obtained using EDTA
(column D).
Bentonite is usually obtained initially as an alkali earth compound, for instance a calcium and/or magnesium form of bentonite. In order that it can perform satisfactorily, for instance in paper making, it is necessary to activate the bentonite by subj ecting it to ion exchange whereby calcium and/or magnesium is replaced by sodium or other alkali metal or ammonium ion.
The normal way of doing this is to mix the alkaline earth bentonite clay with an aqueous activating solution containing an alkali metal or ammonium compound. For instance the clay may be provided as a powdered pre-blend of the alkaline earth metal clay and the alkali metal or ammonium compound and this pre-blend may be mixed into water and allowed to stand for sufficient time for ion exchange to occur whereafter it is diluted for use.
Alternatively the quarried alkaline earth bentonite canbe added direct to an aqueous activating solution with mixing.
In practice, the activating compound which is conventionally used is sodium carbonate or sodium bicarbonate, typically in an amount of around 5 to 10% by weight based on the weight of clay. The activation is conducted at the natural pH of the dispersion, around pH
10.
Other electrolytes are described in JP-A-6445754, as being added to promote dispersion. It is also known in U.S. 4,613,542 and 4,624,982 to include sodium polyacrylate. Concentrates of bentonite with various alkali metal compounds are also described in EP 485124 and U.S. 5,266,538 and 5,391,228. The bentonite that is introduced into these concentrated slurries can initially be in the form of sodium bentonite but EP 485,124 and U.S.
5,391,228 also mention making slurries by blending calcium bentonite and sodium carbonate activator with water and sodium chloride. Paper making processes using bentonite with an anionic organic polymer are also described in EP
373306 and U.S. 5,015,334.
One problem with known activated bentonites {for instance the activated bentonite powders which are commercially available) is that the sodium carbonate or other activator which is included in them causes the bentonite {when mixed with water) to give a relatively high pH, for instance above pH 9 and often around pH 10.
Accordingly it is necessary to handle the bentonite with the care associated with materials which do generate a pH
of around pH 10. , Another problem is that the conventional sodium carbonate activator undergoes ion exchange during the activation process to form calcium carbonate, with the result that inorganic scale may be formed and deposited from aqueous compositions of these activated bentonites.
This is a particular problem when the water in which the bentonite is being dispersed is, naturally, relatively hard.
Another difficulty with known activated bentonite powders is that it is sometime found to be rather difficult to make a stable aqueous dispersion of the powders. Again, it has been found that these difficulties of achieving a stable dispersion increase with increasing hardness of the water. Thus, when using relatively hard water, for instance having a hardness of above 10°dH and generally in the range 15° to 50°dH, various problems can arise.
Further, the performance of the bentonite, especially when used in paper making, can be less effective at lower pH values than at higher pH values, and in particular bentonite activated in conventional manner tends to be less effective in acid paper making processes (for instance when t the cellulosic suspension has a pH of below 6.5 and often in the range 4.2 to 5.5) than when the suspension has higher pH values.
WO 97/33040 fCT/GB97/00648 We have now discovered a new range of activators which can give improved performance.
According to a first aspect of the invention, we provide a dry clay composition comprising a blend of an alkaline earth bentonite swelling clay and an activating amount of an alkali metal or ammonium salt of a sequestering agent selected from phosphonates, hydroxy carboxylic acids, amino carboxylic acids and poly carboxylic acids.
According to a second aspect of the invention, we provide a process of activating an alkaline earth bentonite swelling clay to an alkali metal bentonite swelling clay comprising mixing the alkaline earth swelling clay with an aqueous activating solution containing an ammonium or alkali metal salt of a sequestering agent selected from phosphonates, hydroxy carboxylic acids, amino carboxylic acids and di- or tri- (or higher) carboxylic acids.
In both aspects of the invention, the sequestering agent is preferably introduced as a sodium salt.
In both aspects of the invention, the sequestering agent is preferably sodium citrate.
The resultant activated bentonites have several advantages. They are easier to handle since they are less alkaline. They can give better performance than the same bentonite subjected to conventional activation with sodium carbonate at about pH 10. They can perform more effectively in paper making processes where conventional activated bentonites are less effective due to the pH or the presence of hardness salts. Thus conventional bentonites tend to be less effective when the celluiosic suspension has pH below about 6.5, for instance in the range 4.2 to 5.5, but the activated bentonites obtained in the invention can perform very well in such suspensions without any significant loss of activity.
Conventional activated bentonites also may have inferior performance when the cellulosic suspension is made using relatively hard water, for instance having a hardness v a above 10°dH and typically in the range 15°dH to 50~dH
Improved performance is obtained using the activated bentonites obtained in the invention in such hard waters.
This improvement may be manifested by improved drainage rates or by reducing scale deposition or both.
The activation process can be conducted by separately introducing the swelling clay and the sequestering agent activator into the water, for instance by adding the swelling clay to a solution of the activator or by adding the activator to a dispersion of the swelling clay. In each of these alternatives, the swelling clay can be introduced as a powder or as a slurry.
Preferably, however, the process is conducted by mixing a pre-blend of the swelling clay and the activator with an appropriate amount of water. The pre-blend is preferably a powder but it can be a liquid composition containing the bentonite and the activator.
The amount of water present during the activation process is generally such that the swelling clay concentration during the process is from 2 to 8% or even up to 10%. Usually it is at least 3% and frequently it is not more than about 5 or 6%, with 4 or 5% often being preferred. These are the amounts which are typical for sodium carbonate activation processes and it is convenient that the same can be used in the invention.
However a further advantage of the activators used in the invention is that they will also cause good activation at a much wider range of concentrations and so good activation can be achieved at clay concentrations in the range 8 to 14 or 15%-. Despite the clay activating during this process and thus potentially becoming very viscous, an advantage of the activators is that the resultant compositions still have adequately low viscosity and good fluid flow properties that they can be handled easily.
It is also possible to conduct the activation at even higher clay concentrations, for instance in the range 15 to 40%. We describe in our copending PCT application WO 97/33041 concentrates having a clay concentration of 15 to 40% and which contain an activating amount of sodium citrate.
5 The sequestering agent seems to function by exchanging with the alkaline earth ions and fixing the exchanged calcium or magnesium ions in a form such that they cannot exchange back into the bentonite. The sequestering agent is usually in the sodium form as this is the preferred cation which is introduced by ion exchange into the bentonite. However other activating cations can be used if desired, such as potassium or ammonium.
Suitable phosphonates which can be used as the sequestering agent can be selected from any of the phosphonates which are known for seguestering alkaline earth metal ions, such as the materials sold under the trade name bequest.
Suitable hydroxy carboxylic acids that can be used include materials such as sodium tartrate or gluconate but the preferred material is sodium citrate. The free acid form can be used if required in preference to the water soluble salt.
Suitable amino carboxylic acids include materials such as DTPA, NTA and EDDHA and EDTA.
Di- or tri- (or higher) carboxylic acids which can be used include malonic acid, succinic acid, glutaric acid, adipic acid and oxalic acid, usually as sodium salts. The acids (and all the sequestering agents) are preferably low molecular weight materials, for instance having a molecular weight below 500 and are usually monomeric. The use of high molecular weight sodium polyacrylate in slurries is already known in EP 485124 and 4613542 and 4624982 but this does not give the benefits of the invention.
The sequestering agent must be used in an amount sufficient to give activation in the defined system and this will be found by routine experimentation. On a weight basis it is generally in the range 1 to 20% based on the dry weight of bentonite, most preferably in the range 3 to 15~.
All these amounts assume that the sequestering agent is the only significant activating material in the composition. Blends of one or more of the sequestering a agents may be used and blends of one or more of the sequestering agents with other beneficial activators such as sodium carbonate can be used if required. If sodium carbonate is present, then it may reduce the amount of l0 sequestering agent which is required. The amount of sequestering agent may have to be increased significantly if undesirable components such as sodium chloride are present to any significant extent and accordingly it is preferred that no deliberate additions of simple electrolytes such as sodium chloride, sulphate or nitrate are made.
As the bentonite, one can use any of the anionic swelling clays that are conventionally referred to as bentonite-type clays or as bentonites. They are generally smectites or montmorillonites, the latter being preferred.
Suitable smectite or montmorillonite clays include Wyoming bentonite and Fullers Earth and various clays include those known by the chemical terms of hectorite and bentonite.
The clay will be in the alkaline earth form, usually calcium or calcium and magnesium form.
It is very well known to include bentonite in paper making processes for various purposes and the invention is applicable to ail of these. For instance the bentonite may be included as a pitch dispersant.
One paper-making process to which the invention can be applied is a process in which bentonite is added to a cellulosic suspension, typically in an amount of 0.02 to 2~
dry weight and a medium or high molecular weight (e. g., above 500000) polymeric retention aid is added ' subsequently, genera2ly after the last point of high shear (for instance just in front of the head box immediately prior to drainage), The high molecular weight polymer can be non-ionic, anionic or cationic. The cellulosic suspension can be made from relatively pure pulp or froth pulp having a relatively high cationic demand.
Processes of this type that are of particular value are those in which the pulp has a relatively high cationic demand and the polymer is substantially non-ionic or anionic and the paper product is preferably newsprint or fluting medium. Processes of this type in which the total filler content is relatively low are described in U.S.
4305781 and EP-A-17353 to which reference should be made for further details of suitable non-ionic or low ionic polymers and suitable cellulosic suspensions. More highly anionic or cationic polymers may be used. These processes are of particular value when the cellulosic suspension contains de-inked waste. Suitable polymers and fillers (when the pulp is filled) are also described in EP-A-608989 and AU-A-63977/86.
The invention is of particular value when applied to microparticulate retention processes in which a polymeric retention aid is added to the aqueous suspension, the suspension is subjected to shearing and the bentonite is then added after the shearing, and often after the last point of high shear, for instance just prior to the head box prior to drainage. The polymer may be non-ionic or anionic but is often cationic.
The cationic polymer can be a natural material such as cationic starch but is preferably a substantially linear synthetic cationic polymer having molecular weight above 500,000. The amount of cationic polymer that is present in the dispersion at the time of shearing should be sufficient that flocs are formed by the addition of the polymer and the flocs are broken by the shearing to form microflocs that resist further degradation by the shearing but that carry sufficient charge to interact with the bentonite to give better retention and/or formation than is obtainable when adding the polymer alone after the last point of high shear.
The shearing can be due merely to turbulent passage along a duct or can be due to passage through a centriscreen, a pump or other shear-applying device.
Preferred processes include those commercialised by the applicants under the trade mark Hydrocol and preferred processes are described in, for instance, U.S. patents 4753710, 4913775 and 4969976. The optimum amount of polymer for any particular process can be determined by routine experimentation, and will depend inter alia on whether low or medium molecular weight cationic polymer, and/or dry strength resin, had been incorporated in the aqueous suspension at some earlier stage.
The activated bentonite of the invention can be used wherever activated bentonite is useful, for instance in pulp dewatering, paper sludge dewatering, liquid/solids separation processes, effluent clarification, inky waste water clarification and pitch fixing (in paper making processes). The activated bentonite can also be used in other industries which utilise activated bentonite, for instance in the preparation of bentonite for iron ore pelletisation or other mineral processing uses.
The following are some examples.
Example 1 5 parts by weight calcium bentonite was activated in 95 parts by weight of an aqueous solution containing the activator, and the amount of activator, specified below.
In each instance, the amount of activator is expressed as a percentage based on the dry weight of bentonite. The products which were used we as follows.
A - sodium carbonate - 6%
C - sodium citrate - 17%
D - sodium EDTA - 21%.
F~'~amE~~.
a The activated bentonites prepared in Example 1 are used in a laboratory simulation of the paper making process as described in US 4753710. In particular a thinstock of 0.5% bleached Kraft Fibre Furnish has added to it 500 g/t of a high molecular weight (intrinsic viscosity 6 dl/g) cationic polyacrylamide formed from 40% by weight dimethylaminoethyl acrylate quarternised by methyl chloride and 60% by weight acrylamide. The cellulosic suspension is sheared for 60 seconds.1,500 rpm, the activated bentonite is then added in the dose specified, the suspension subjected to gentle mixing in a baffled Britt jar and the Schopper Reigler drainage times recorded for 700 ml to drain from 1,000 ml of the thinkstock. In this test, the lowest possible drainage time gives the best results, and low bentonite amounts are preferred.
In the following tables, the figures in the columns marked "Bentonite" are in g/t dry weight and the figures in the columns marked with a letter are the drainage time in seconds when using the specified amount of the activated bentonite identified in Example 1.
In this table, the column headed Ca represents the results using unactivated calcium bentonite.
Table 1 Bentonite Ca A C D
This data shows that citrate activation (column C) can give results as good as or better than sodium carbonate activation as regards drainage time, and that adequate, but less satisfactory, results can be obtained using EDTA
(column D).
Claims (8)
1. A dry clay composition comprising a blend of alkaline earth bentonite and an activating amount of an alkali metal or ammonium salt of a sequestering agent selected from phosphonates, hydroxy carboxylic acids, amino carboxylic acids and di or tri carboxylic acids.
2. A composition according to claim 1 in which the salt is a sodium salt.
3. A composition according to claim 1 or claim 2 in which the sequestering agent is sodium citrate.
4. A process of activating an alkaline earth bentonite comprising mixing the alkaline earth bentonite with an aqueous activating solution containing an activating amount of an alkali metal or ammonium salt of a sequestering agent selected from phosphonate, hydroxy carboxylic acids, amino carboxylic acids and di or tri carboxylic acids.
5. A process according to claim 4 in which the sequestering agent is in the form of a sodium salt.
6. A process according to claim 4 in which the sequestering agent is sodium citrate.
7. A process according to any one of claims 3 to 6 conducted at a bentonite concentration of 2 to 14%.
8. A process of making paper comprising forming a cellulosic suspension, mixing an activated bentonite dispersion into the suspension, draining water from the suspension to form a wet sheet and drying the sheet, wherein the activated bentonite dispersion has been made by a process according to claim 4, optionally followed by dilution, or by mixing the composition of claim 1 into water.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB9604927.5A GB9604927D0 (en) | 1996-03-08 | 1996-03-08 | Activation of swelling clays and processes of using the activated clays |
| GB9604927.5 | 1996-03-08 | ||
| PCT/GB1997/000648 WO1997033040A1 (en) | 1996-03-08 | 1997-03-10 | Activation of swelling clays and processes of using the activated clays |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2247205A1 CA2247205A1 (en) | 1997-09-12 |
| CA2247205C true CA2247205C (en) | 2005-06-28 |
Family
ID=10790066
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002247205A Expired - Fee Related CA2247205C (en) | 1996-03-08 | 1997-03-10 | Activation of swelling clays and processes of using the activated clays |
Country Status (22)
| Country | Link |
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| US (1) | US6024790A (en) |
| EP (1) | EP0885327B1 (en) |
| JP (1) | JP2000506113A (en) |
| KR (1) | KR100489647B1 (en) |
| CN (1) | CN1088776C (en) |
| AT (1) | ATE211516T1 (en) |
| AU (1) | AU721609B2 (en) |
| BR (1) | BR9707830A (en) |
| CA (1) | CA2247205C (en) |
| CZ (1) | CZ293232B6 (en) |
| DE (1) | DE69709854T2 (en) |
| DK (1) | DK0885327T3 (en) |
| ES (1) | ES2169353T3 (en) |
| GB (1) | GB9604927D0 (en) |
| HU (1) | HU223695B1 (en) |
| NO (1) | NO984108L (en) |
| NZ (1) | NZ331471A (en) |
| PL (1) | PL190372B1 (en) |
| PT (1) | PT885327E (en) |
| RU (1) | RU2144592C1 (en) |
| SK (1) | SK122698A3 (en) |
| WO (1) | WO1997033040A1 (en) |
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| US20030150575A1 (en) * | 1998-06-04 | 2003-08-14 | Snf Sa | Paper and paperboard production process and corresponding novel retention and drainage aids, and papers and paperboards thus obtained |
| TW550325B (en) | 1999-11-08 | 2003-09-01 | Ciba Spec Chem Water Treat Ltd | Manufacture of paper and paperboard |
| KR100408627B1 (en) * | 2000-07-12 | 2003-12-06 | 주식회사 자경케미칼 | Pollution control material for paper |
| MY140287A (en) | 2000-10-16 | 2009-12-31 | Ciba Spec Chem Water Treat Ltd | Manufacture of paper and paperboard |
| MXPA01013126A (en) * | 2001-01-08 | 2004-02-12 | Elementis Specialities Inc | Viscosity stable smectite clay slurries and mixtures of smectite clay and one or more phosphonates useful to make such slurries. |
| US20020144630A1 (en) | 2001-01-08 | 2002-10-10 | Elementis Specialties, Inc. | Viscosity stable smectite clay slurries |
| AU2003245563A1 (en) * | 2002-06-17 | 2003-12-31 | American Clay Enterprises, Llc | Clay plaster |
| US7303654B2 (en) | 2002-11-19 | 2007-12-04 | Akzo Nobel N.V. | Cellulosic product and process for its production |
| US7297668B2 (en) * | 2003-04-03 | 2007-11-20 | Colgate-Palmolive Company | Composition |
| US20050109239A1 (en) * | 2003-11-21 | 2005-05-26 | Elementis Specialties, Inc. | Paint formulations containing hectorite compositions |
| US20050228103A1 (en) * | 2004-04-13 | 2005-10-13 | Eastman Kodak Company | Composition comprising intercalated metal-ion sequestrants |
| US7989402B2 (en) * | 2006-09-14 | 2011-08-02 | Elementis Specialties, Inc. | Functionalized clay compositions for aqueous based drilling fluids |
| DE102008060302A1 (en) * | 2008-12-03 | 2010-06-10 | Süd-Chemie AG | Use of a composition based on phyllosilicate for the production of paper, and phyllosilicate composition and process for their preparation |
| EP2522458B1 (en) | 2011-05-13 | 2016-07-06 | ESSILOR INTERNATIONAL (Compagnie Générale d'Optique) | Process for determining position parameters of a manufactured surface relative to a reference surface |
| CA2862095C (en) | 2012-02-01 | 2017-04-11 | Basf Se | Process for the manufacture of paper and paperboard |
| WO2013127731A1 (en) | 2012-03-01 | 2013-09-06 | Basf Se | Process for the manufacture of paper and paperboard |
| DE102012005454B4 (en) | 2012-03-20 | 2020-06-18 | Outotec Oyj | Method and device for producing hardened granules from iron-containing particles |
| DE102012011240A1 (en) | 2012-06-06 | 2013-12-12 | Outotec Oyj | Process for producing hardened granules from iron-containing particles |
| ES2873105T3 (en) | 2013-01-11 | 2021-11-03 | Solenis Technologies Cayman Lp | Process for the manufacture of paper and cardboard |
| WO2015155110A1 (en) * | 2014-04-07 | 2015-10-15 | Lamberti Spa | Process for making tiles |
| RU2595125C1 (en) * | 2015-08-07 | 2016-08-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Грозненский государственный нефтяной технический университет имени академика М.Д. Миллионщикова" | Method of producing activated bentonite powder |
| KR102442975B1 (en) * | 2020-04-17 | 2022-09-15 | 한국원자력연구원 | Float sorting device for selective separation of non-metallic minerals |
| CN113402904A (en) * | 2021-06-08 | 2021-09-17 | 浙江丰虹新材料股份有限公司 | Preparation method of low-viscosity composite clay thixotropic agent |
| WO2024022984A1 (en) | 2022-07-25 | 2024-02-01 | Byk-Chemie Gmbh | Lithium rich layered silicate and process for producing |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1497280A (en) * | 1974-12-10 | 1978-01-05 | Ass Portland Cement | Agglomerating suspended particulate material in aqueous systems |
| DE3065576D1 (en) * | 1979-03-28 | 1983-12-22 | Allied Colloids Ltd | Production of paper and paper board |
| US4309222A (en) * | 1980-10-09 | 1982-01-05 | Pfizer Inc. | Kaolin clay slurries of reduced viscosity |
| JPS61118499A (en) * | 1984-11-14 | 1986-06-05 | 株式会社 ネオス | Cleaning agent for spray cleaning |
| US4624982A (en) * | 1985-04-05 | 1986-11-25 | American Colloid Company | Method of temporarily inhibiting the swellability of water swellable clays and compositions |
| US4613542A (en) * | 1985-04-05 | 1986-09-23 | American Colloid Company | Method of impregnating a water-penetrable article with a swell-inhibited water swellable clay slurry |
| DE3541163A1 (en) * | 1985-11-21 | 1987-05-27 | Basf Ag | METHOD FOR PRODUCING PAPER AND CARDBOARD |
| GB8602121D0 (en) * | 1986-01-29 | 1986-03-05 | Allied Colloids Ltd | Paper & paper board |
| US4913775A (en) * | 1986-01-29 | 1990-04-03 | Allied Colloids Ltd. | Production of paper and paper board |
| SE8701252D0 (en) * | 1987-03-03 | 1987-03-25 | Eka Nobel Ab | SET FOR PAPER MAKING |
| JP2552128B2 (en) * | 1987-03-18 | 1996-11-06 | 昭治 野上 | High-purity purification method for clay minerals |
| GB8807445D0 (en) * | 1988-03-28 | 1988-05-05 | Allied Colloids Ltd | Pulp dewatering process |
| GB8828899D0 (en) * | 1988-12-10 | 1989-01-18 | Laporte Industries Ltd | Paper & paperboard |
| US5006574A (en) * | 1989-02-10 | 1991-04-09 | Engelhard Corporation | Cationcally dispersed slurries of calcined kaolin clay |
| GB9024016D0 (en) * | 1990-11-05 | 1990-12-19 | Allied Colloids Ltd | Clay compositions,their manufacture and their use in the production of paper |
| US5266538A (en) * | 1990-12-21 | 1993-11-30 | Southern Clay Products, Inc. | Method for preparing high solids bentonite slurries |
| US5391228A (en) * | 1990-12-21 | 1995-02-21 | Southern Clay Products, Inc. | Method for preparing high solids bentonite slurries |
| CA2108027C (en) * | 1991-07-02 | 1997-05-27 | Bruno Carre | A process for the production of paper |
| US5223463A (en) * | 1991-08-01 | 1993-06-29 | Ecc International Inc. | Process for producing a kaolin clay product |
| US5537934A (en) * | 1994-10-19 | 1996-07-23 | Engelhard Corporation | Cationically stabilized slurries of calcined kaolin clay |
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1996
- 1996-03-08 GB GBGB9604927.5A patent/GB9604927D0/en active Pending
-
1997
- 1997-03-10 CA CA002247205A patent/CA2247205C/en not_active Expired - Fee Related
- 1997-03-10 NZ NZ331471A patent/NZ331471A/en unknown
- 1997-03-10 ES ES97906288T patent/ES2169353T3/en not_active Expired - Lifetime
- 1997-03-10 AU AU21028/97A patent/AU721609B2/en not_active Ceased
- 1997-03-10 CN CN97192857A patent/CN1088776C/en not_active Expired - Fee Related
- 1997-03-10 WO PCT/GB1997/000648 patent/WO1997033040A1/en active IP Right Grant
- 1997-03-10 DK DK97906288T patent/DK0885327T3/en active
- 1997-03-10 EP EP97906288A patent/EP0885327B1/en not_active Expired - Lifetime
- 1997-03-10 DE DE69709854T patent/DE69709854T2/en not_active Expired - Fee Related
- 1997-03-10 HU HU9902143A patent/HU223695B1/en not_active IP Right Cessation
- 1997-03-10 CZ CZ19982857A patent/CZ293232B6/en not_active IP Right Cessation
- 1997-03-10 PT PT97906288T patent/PT885327E/en unknown
- 1997-03-10 SK SK1226-98A patent/SK122698A3/en unknown
- 1997-03-10 AT AT97906288T patent/ATE211516T1/en not_active IP Right Cessation
- 1997-03-10 JP JP9531594A patent/JP2000506113A/en not_active Ceased
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- 1997-03-10 US US09/142,220 patent/US6024790A/en not_active Expired - Fee Related
- 1997-03-10 BR BR9707830A patent/BR9707830A/en not_active IP Right Cessation
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1998
- 1998-09-07 NO NO984108A patent/NO984108L/en unknown
Also Published As
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| HUP9902143A2 (en) | 2000-02-28 |
| EP0885327B1 (en) | 2002-01-02 |
| JP2000506113A (en) | 2000-05-23 |
| SK122698A3 (en) | 1999-06-11 |
| CZ285798A3 (en) | 1999-03-17 |
| KR100489647B1 (en) | 2005-08-31 |
| US6024790A (en) | 2000-02-15 |
| WO1997033040A1 (en) | 1997-09-12 |
| HUP9902143A3 (en) | 2003-12-29 |
| CN1213420A (en) | 1999-04-07 |
| PL190372B1 (en) | 2005-12-30 |
| NO984108D0 (en) | 1998-09-07 |
| RU2144592C1 (en) | 2000-01-20 |
| KR19990087616A (en) | 1999-12-27 |
| BR9707830A (en) | 1999-07-27 |
| DK0885327T3 (en) | 2002-04-22 |
| PL329369A1 (en) | 1999-03-29 |
| HU223695B1 (en) | 2004-12-28 |
| NZ331471A (en) | 2000-01-28 |
| CN1088776C (en) | 2002-08-07 |
| NO984108L (en) | 1998-09-07 |
| AU2102897A (en) | 1997-09-22 |
| AU721609B2 (en) | 2000-07-13 |
| CA2247205A1 (en) | 1997-09-12 |
| EP0885327A1 (en) | 1998-12-23 |
| DE69709854T2 (en) | 2002-08-29 |
| GB9604927D0 (en) | 1996-05-08 |
| ES2169353T3 (en) | 2002-07-01 |
| DE69709854D1 (en) | 2002-02-28 |
| PT885327E (en) | 2002-05-31 |
| CZ293232B6 (en) | 2004-03-17 |
| ATE211516T1 (en) | 2002-01-15 |
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