SILICA SOLS, A PROCESS FOR THE PREPARATION OF SILICA SOLS AND USE OF THE SOLS

Abstract: Silica sols with a high content of microgel and particles with a specific surface area within the range 300 to 700 m2/g, preferably 400 to 650 m2/g. The sols can be prepared by acidification of a water glass solution and alkalization at a certain dry content, alternatively to a certain pH. The sols are particularly suitable for use as additives in papermaking in combination with cationic polymers and especially in combination with cationic acrylamide based polymers.

Description: Silica sols, a process for the preparation of silica sols and use of the sols The present invention relates to new silica sols, to a process suitable for preparation of the sols and to the use of the new sols in the production of paper. More particularly the invention relates to new silica sols which have particles of a certain specific surface area and which have a comparatively high amount of so called microgel. The new sols are particu¬ larly suitable for use as additives in combination with poly- mers in the production of paper. Silica sols, which term is used herein for silica hydrosols, are aqueous systems with very small silica par¬ ticles which find use in a variety of fields, among other things dependent on the particle size. In the production of paper silica based sols with very small, colloidal, anionic silica particles have found an increasing utilization during the last few years. Silica sols are hereby used as additives to the stock in combination with cationic or amphoteric polymers, mainly for improving retention and dewatering in the production of paper. In the European patent 41056 the use of colloidal silica sols in combination with cationic starch is for example disclosed. In the PCT applications WO 86/00100 and WO 86/05826 combinations of silica sols, with particles where at least the surface groups contain aluminium, and cationic natural polymers and cationic polyacrylamides, respectively, are disclosed. The silica particles are generally stated to have a specific surface area within the range of from 50 to 1000 m 2 /g. The sols which are used commercially in paper production are of the type which have discrete colloidal particles with a particle size usually of from about 4 to about 7 nm, ie a specific surface area of from about 700 to about 300 m /g, and above all sols with particles having a specific surface area of about 500 m 2 /g have been used commercially. It has generally been considered that sols with particles of the above mentioned size give the best results and they have also been preferred with regard to stability. Quite generally it has been an aim that the silica sols should be as monodisperse as possible, ie that the particles of the sols should be discrete and non-aggregated and have as narrow particle size distribution as possible. At the preparation of sols it has thus been sought to avoid aggregation, ie form¬ ation of microgel. According to the PCT application WO 91/07350 silica sols with a certain degree of microgel formation have been developed. These sols are based on particles with a very high specific surface area and have been found especially useful in combination with polymers in the production of paper. The sols are based on particles with very high specific surface area, from 750 to 1000 m 2 /g, preferably from 800 to 950 m 2 /g, and the particles are surface modified with aluminium for stabilization of the high surface area. According to the present invention it has been found that sols of silica based particles, ie particles based on Si0 2 , which have a specific surface area within the range 300 to 700 m 2 /g and which contain comparatively high amount of microgel give very good effect as concerns retention and dewatering in papermaking. It has especially been found that sols with particles of the given specific surface area and content of microgel according to the invention give sub- stantially improved effect when they are used in combination with cationic acrylamide based polymers in comparison with previously used silica based sols with specific surface area in the same range which substantially contain discrete particles. The content of microgel, or aggregate, can be controlled during the production of the sols. The present invention thus relates to new silica sols, as further defined in claims, and also relates to a process for the production of the sols and to the use of the sols . The new sols are characteristic in that they have a high content of microgel, ie a low S-value, and in that the sol particles have a specific surface area within the range from 300 to 700 m 2 /g. The given specific surface area is measured by means of titration with NaOH according to the method disclosed by Sears in Analytical Chemistry 28(1956) :12, 1981- 1983. The specific surface area is suitably within the range from 400 to 650 m 2 /g. In contrast to known commercial sols with the above mentioned specific surface areas which are used in papermaking the present sols have a comparatively high content of microgel and πhus a low S-value. It is assumed that the microgel, the aggregates, to a substantial extent is present in the form of two- or three-dimensional structures, of more less cloud-like formation, of aggregated primary particles. The S-value for the present sols is within the range from 15 to 40 per cent by weight and preferably the S-value is within the range from 15 to 35%. The given S-value has been measured and calculated in accordance with what is disclosed by Her, R.K. & Dalton R. L. in J. Phys. Chem. 60(1956) , 955-957. The S-value can be considered as a measure of the degree of aggregate or microgel formation and a low S-value indicates a greater part of microgel and can also be considered as a measure of the Si0 2 - content of the dispersed phase in per cent by weight. The particles in the present sols can be unmodified silica particles or be silica particles which are surface modified with aluminium. Sols which contain silica which is not aluminium modified are preferred. For aluminium modified particles these are suitably modified to a degree of from 2 to 25 per cent, suitably from 3 to 20 per cent. With a degree of aluminium modification is meant the part of aluminium atoms which have replaced silicon atoms in the surface of the particles . The degree of aluminium modification is given in per cent and is calculated on basis of 8 silanol groups per nm 2 . This is described by Her, R.K. in Journal of Colloidal and Interface Science , 55(1976) :1, 25-34. The present sols suitably have a dry content, calculated as Si0 2 , of from about 3 to about 40 per cent by weight and the dry content is preferably within the range of from about 5 to about 30 per cent by weight. It has been found that these new sols which contain anionic particles are useful in the production of paper and similar products and that they herein, in combination with cationic polymers give very good improvement of retention and dewatering. It has particularly been found that the new sols according to the invention which contain particles which are not aluminium modified give a substantial improvement when they are used in combination with cationic acrylamide based polymers in comparison with commercially used such sols which have particles of the same size but in which the particles are substantially discrete. In addition to silica sols as. defined in the appended patent claims the present invention also relates to a process for the production of the new silica sols and to the use of the sols as stated in the appended patent claims. The invention also relates to a process for the produc¬ tion of silica sols which have comparatively low S-values and which have a specific surface area within the range of from 300 to 700 m 2 /g. According to the invention silica sols are prepared starting from a conventional alkali water glass, potassium or sodium water glass, preferably sodium water glass. The mole ratio of Si0 2 to Na 2 0 or K 2 0, where Na 2 0 and K 2 0 in the following will be given as M 2 0, in the water glass can, as per se known, be within the range of from 1.5:1 to 4.5:1 and is preferably within the range of from 2.5:1 to 3.9:1. A diluted solution of the water glass is utilized and this suitably has an Si0 2 content of from about 3 to about 12 per cent by weight, preferably from about 5 to about 10 per cent by weight . The water glass solution which usually has a pH around 13, or above 13, is acidified to a pH of from about 1 to about 4. The acidification can be carried out in per se known manner by addition of mineral acids, such as for example sulfuric acid, hydrochloric acid and phosphoric acid or optionally with other known chemicals for acidification of water glass such as ammonium sulphate and carbon dioxide. At addition of mineral acid the acidi ication is carried out in two steps, a first step to a pH of about 8 to 9, whereafter a certain ripening, ie a particle growth, is allowed to occur before further acidification to a pH of from about 1 to about 4. However, it is preferred that the acidification is carried out by means of acid cation exchangers which among other things lead to more stable products and give almost sodium free acid sols. The acidification is preferably carried out by means of strongly acid cation exchange resins, for example of sulfonic acid type. It is preferred that the acidification is carried out to a pH of from about 2.0 to 4.0 and most pre¬ ferably from about 2.2 to about 3.0. The acid sol obtained after acidification is then made alkaline. The alkalization can be carried out with conventional alkali such as sodium, potassium or ammonium hydroxide. It is, however, preferred that alkalization is carried out by addition of water glass. Potassium and sodium water glass, particularly sodium water glass, with a mole ratio of Si0 2 to M 2 0 as above described is used in this alkalization step. The Si0 2 content of the water glass solutions used for alkalization is suitably within the range of from about 3 to about 35 per cent by weight and preferably within the range of from 5 to 30 per cent by weight. The alkalization is suitably carried out to a pH of at the lowest equal to 7 and suitably to a pH within the range of from 7.5 to 9. The alkalization is further suitably carried out to a final mole ratio Si0 2 to M,0 within the range of from about 20:1 to about 75:1, suitably within the range of from about 30:1 to about 60:1. At the preparation of a sol as above the degree of microgel can be influenced in several ways and be controlled to the desired low value. The degree of microgel can be influenced by salt content, by adjustment of the con¬ centration at the preparation of the acid sol and at the alkalization since in this step the degree of microgel is influenced when the stability minimum for the sol is passed, at a pH of about 5. By prolonged times at this passage the degree of microgel can be directed to the desired value. It is particularly suitable to control the degree of microgel by adjustment of the dry content, the Si0 2 content, at the alkalization whereby a higher dry content gives a lower S- value. By keeping the Si0 2 content at the alkalization in the range of from 7.5 to 5 per cent by weight the S-value can be controlled to the given values 15 to 40%. Another suitable way to control the degree of microgel is by adjustment of the alkalization to a certain pH and the above given pH values to which the alkalization is carried out controls the S-values to lower values at a lower pH. To obtain sols with S-values within the range 15 to 40% the pH at the alkalization is suitably controlled to the range 7.5 to 8.5. At alkalization to this pH-range a suitable Si0 2 content is within the range from about 5 to about 6 per cent by weight . The acid sol has particles with a high specific surface area, above 1000 m 2 /g and usually around about 1300 m 2 /g. After the alkalization a particle growth starts and thereby a decrease of the specific surface area. After the alkalization a growth process is thus carried out so that the desired specific surface area is obtained. The desired decrease in surface area to the range 300 to 700 m 2 /g can be obtained by heat treatment. At heat treatment times and temperatures are adjusted so that shorter times are used at higher temperatures. From a practical point of view it is suitable to carry out heat treatment at tempera¬ tures up to about 95°C during about half an hour up to about 24 hours. When the particles have obtained the desired specific surface area an aluminium modification of the surface can be carried out if desired in order to give particles which have a better charge stability in acid environment than unmodified particles. The modification is an aluminium modification and is carried out by means of an aluminate, sodium or potassium aluminate, preferably sodium aluminate. The aluminium modification of the particle surface is carried out in per se known manner and to a degree of surface modifi¬ cation of 2 to 25%, particularly to a degree of 3 to 20%, as mentioned above. According to the present process silica sols with dry contents of from about 3 to about 40 per cent by weight, after optional concentration, can be prepared and the produced sols show very good storage stability, ie they can be stored for several months without substantial decrease of the specific surface area and without gel formation. The new sols according to the invention are particularly suitable for use in papermaking. The present invention relates also to this use of the sols. As mentioned by way of introduc¬ tion it is well known to use silica based sols in combination with cationic polymers in the production of paper, first of all in order to get improved retention and dewatering. The present silica sols are utilized in the same manner as earlier known for silica sols with anionic particles and they give, in combination with cationic polymers and amphoteric polymers, a substantial improvement of the retention and dewatering in the production of paper. Even if arbitrary order of addition can be used it is preferred that the polymer is added before the sol . The sols can with good effect be used within the whole pH range 4 to 10 in papermaking. The improved dewatering also results in that the speed of the papermaking machine can be increased and, further, less water need to be removed in the press and drying sections of the machine and a substantially economically improved papermaking process is thus obtained. The substantially improved effect of the present sols with low S-values in comparison with corresponding sols of higher S- values when they are used in combination with cationic acrylamide based polymers should be especially emphasised. The present invention thus also relates to a process for the production of paper with the characteristic features defined in the claims. The cationic or amphoteric polymers can be natural, ie based on carbohydrates, or be synthetic. As examples of suitable polymers can be mentioned cationic and amphoteric starch, cationic and amphoteric guar gum, cationic and amphoteric acrylamide based polymers, cationic polyethy- leneimines, polyamidoamines and poly(diallyldimethyl ammonium chloride) . The polymers can be used singly or in combination with each other. Cationic acrylamide based polymers are the preferred polymers for use in combination with the present sols. The amount of silica sol and polymer in the production of paper according to the present invention can vary within wide limits depending on, among other things, type of stock, presence of fillers and other conditions. The amount of sol should suitably be at least 0.01 kg/ton, calculated as Si0 2 on dry fibres and optional fillers, and is suitably within the range of from 0.05 to 5 kg/ton and preferably within the range from 0.1 to 2 kg/ton. The sol is suitably added to the stock at dry contents within the range of from 0.1 to 5 per cent by weight. The amount of polymer is to a high degree dependent on the type of this and other effects desired from this. For synthetic polymers at least 0.01 kg polymer per ton, cal¬ culated as dry on dry fibres and optional fillers are usually used. Suitably amounts of from 0.01 to 3 and preferably from 0.03 to 2 kg per ton- are used. For polymers based on carbo- hydrates, such as cationic starch and cationic guar gum, amounts of at least 0.1 kg/ton, calculated as dry on dry fibres and optional fillers, are usually used. Suitably these are used in amounts of from 0.5 to 30 kg/ton and preferably from 1 to 15 kg/ton. The weight ratio of cationic polymer to sol, calculated as Si0 2 , should usually be at least 0.01:1 and suitably at least 0.2:1. The upper limit for the polymer is first of all set by economical considerations and with regard to charges. For polymers of lower cationicity such as cationic starch, alone or in combination with other cationic polymers, very high amounts can thus be utilized, up to a ratio of 100:1 or higher, and the limit is mainly decided by economical reasons. Suitable ratios of cationic or amphoteric polymer to sol, calculated as Si0 2 , for most systems is within the range of from 0.2:1 to 100:1. The present sols can of course be used in papermaking in combination with conventional paper addi¬ tives such as hydrophobing agents, dry strength agents, wet strength agents etc..It is particularly suitable to use aluminium compounds in combination with the present sols and cationic polymers since it has been found that aluminium compounds can give a further improvement of retention and dewatering. Any for use in papermaking known aluminium compound can be used, for example alum, polyaluminium com¬ pounds, aluminates, aluminium chloride and aluminium nitrate. The amount of aluminium compound can also vary within wide limits and it is suitable to use the aluminium compound in a weight ratio to the sol, calculated as Si0 2 , of at least 0.01:1 whereby the aluminium compound has been calculated as A1 2 0 3 . The ratio suitably does not exceed 3 :1 and is preferably within the range from 0.02:1 to 1,5:1. The polyaluminium compounds can for example be polyaluminium chlorides, poly¬ aluminium sulphates and polyaluminium compounds containing both chloride and sulphate ions. The polyaluminium compounds can also contain other anions than chloride ions, for example anions from sulphuric acid, phosphoric acid, organic acids such as citric acid and oxalic acid. The silica sols and the polymers can be utilized in the production of paper from different kinds of stocks of cellu¬ lose containing fibre-s and the stocks should suitably contain at least 50 per cent by weight of such fibres, based on dry material. The components can for example be used for stocks of fibres from chemical pulp, such as sulphate and sulphite pulp, thermomechanical pulp, refiner pulp or groundwood pulp from both hardwood and softwood and can also be used for stocks based on recycled fibres . The stock can also contain mineral fillers of conventional types, such as for example kaolin, titanium dioxide, gypsum, chalk and talcum. The terms paper and papermaking which are used herein do of course not include solely paper and its production but also other cellulose fibre containing products in sheet or web form such as pulp sheets, board and cardboard and their production. The invention is further illustrated in the following examples which, however, are not intended to limit the same. Parts and per cent relate to parts by weight and per cent by weight unless otherwise stated. Example la) - lc) In these examples different sols were prepared: la) Reference. Sol with S-value of about 53 containing non- aluminium modified silica particles having a specific surf ce area of 500 m 2 /g. This sol corresponds to a commercial sol developed on basis of the European patent 41056. The sol was prepared according to the following: 1275 g of water glass with an Si0 2 -content of 24.2% and a weight ratio Si0 2 :Na 2 0 of 3.45 was diluted with 4045 g of water to an Si0 2 -content of 5.8%. The water glass solution was ion exchanged in a column filled with strong cation exchange resin (Amberlite IR 120) and diluted with water to 5.41% Si0 2 . 4000 g of the ion exchanged water glass was charged to a reactor. While stirring well 354.2 g of water glass (5.8% Si0 2 ; Si0 2 :Na 2 0 = 3,45) were added to the ion exchanged water glass. The time of addition was about 15 seconds. The alkaliz¬ ed solution was then heated to 85°C and heat treated at this temperature for 75 minutes. After finished heat treatment the sol was cooled. lb) According to the invention. Sol with an S-value of 31 containing non-aluminium modified silica particles with a specific surface area of 545 m 2 /g. The sol was prepared according to the following: 1625 of water glass with an Si0 2 -content of 24.2% and a ratio Si0 2 :Na 2 0 of 3.45 were diluted with 4075 g of water to an Si0 2 -content of 6.9%. The water glass solution was ion exchanged in an ion exchange column according to Ex. la) and the ion exchanged water glass was diluted to 6.49% Si0 2 . 4600 g of the ion exchanged water glass were charged to a reactor vessel. While stirring well 400 g of water glass (6.9% Si0 2 ; Si0 2 :Na 2 0 = 3,45) were added to the ion exchanged water glass. The alkalized solution was then heated to 85°C and heat treated at this temperature for 60 minutes. After finished heat treatment the sol was cooled. lc) According to the invention. Sol with an S-value of 21 containing aluminium modified silica particles with a specific surface area of 631 m 2 /g. The sol was prepared according to the following. A diluted water glass solution (Si0 2 :Na 2 0 = 3.4) was ion exchanged in a column and an ion exchanged water glass with an Si0 2 content of 5.36% was obtained. To 4000 g of this solution 80.6 g of water glass (22.2% Si0 2 ; Si0 2 :Na 2 0 = 3,41) were added. The addition time was about 15 seconds. The alkalized solution was then heated to 75°C and treated at this tempera¬ ture for 120 minutes. The sol was cooled and then H + -saturated cation exchange resin (Amberlite IR-120) was added in an amount to give a pH value of 7.2. The ion exchange resin was then filtered off. To 3770 g of the pH-adjusted sol 25.4 g of sodium aluminate (Al 2 0 3 -content 25.5%) were added. Before the addition the sodium aluminate had been diluted with 225 g of water. The pH adjusted sol was heated to 45°C before the addition and the addition time for the aluminate was 60 minutes. Example 2 In this example the retention effect, retention of fibres and fillers, of sols la) and lb) in production of paper was investigated. A standard stock, based on pulp with the composition 60% bleached birch sulphate + 40% bleached pine sulphate to which had been added 30% of chalk as filler and 0.3 g/1 of Na 2 S0 4 .10H 2 O, was used. The stock had a concentra¬ tion of about 5 g/1, a fine fraction content of 38% and a pH of 8.1. The retention effect, in this and following examples, was evaluated by means of a Britt Dynamic Drainage Jar at 800 rpm. This is the conventional retention test method used in the paper industry. The sols were used in varying amounts in combination with a cationic acrylamide based polymer (Floerger Fp 4190 PG with 10 mole% cationic charges and a molecular weight of about 10 millions) . The cationic polyacrylamide was in all tests added in an amount of 0.8 kg/t and it was added before the sol. All given dosages, in this and following examples, are calculated as dry on dry fibres and optional fillers. The results are shown in the following table. As evident a considerable improvement of the retention effect was obtained when the cationic polyacrylamide was used in combination with silica sol having high content of micro¬ gel, low S-value, according to the invention in comparison with the effect when it was used in combination with a commercial sol with low content of microgel. Example 3 In this example the retention was evaluated in the same manner as in Ex. 2 using sol c) according to the in¬ vention in comparison with a sol according to the PCT applica- tion WO 91/07350, sol d) , which like sol c) had an S-value of 21 but which had particles with a specific surface area of 897 m 2 /g. The stock was a standard stock with a concentration of 5.2 g/1, a fines fraction content of 34% and a pH of 8.1. The same cationic polyacrylamide as in Ex. 2 was used and was added in an amount of 0.8 kg/t. 0.2 47.5 0.4 71.6 0.8 72.1 As evident as good retention can be obtained with aluminium modified sols with low S-value and a specific surface area of the order 600 m 2 /g as with aluminium modified sols with corresponding low S-value but with particles having substantially larger surface area.

Claims: Claims 1. Silica sol, characterized in that the sol has an S- value within the range of from 15 to 40 per cent and in that it contains silica particles, which can be aluminium modified or non-aluminium modified, having a specific surface area within the range of from 300 to 700 m/g. 2. Silica sol according to claim 1, characterized in that the silica particles have a specific surface area within the range from 400 to 650 m 2 /g. 3. Silica sol according to claim 1 or 2, characterized in that the sol has an S-value within the range of from 15 to 35 per cent. 4. Silica sol according to any of the preceding claims, characterized in that the silica particles are non-aluminium modified. 5. A process for the preparation of a silica sol, characterized in that it comprises acidification of a water glass solution to a pH within the range of from 1 to 4, alkalization of the obtained acid sol at an Si0 2 content within the range of from 7.5 to 5 per cent by weight, alternatively alkalization of the acid sol to a pH value between 7.5 and 9, and particle growth of the sol to a specific surface area within the range of from 300 to 700 m 2 /g, optionally followed by aluminium modification. 6. A process according to claim 5, characterized in that the alkalization is carried out by means of a water glass solution. 7. A process for the production of paper from a suspension of cellulose containing fibres, and optional fillers, whereby a cationic or amphoteric polymer and an anionic silica sol are added to the suspension and the suspension is formed and dewatered on a wire, characterized in that to the suspension are added polymer and a sol which has an S-value within the 'range from 15 to 40 per cent and which contains aluminium modified or non-aluminium modified silica particles having a specific surface area within the range from 300 to 700 m 2 /g. 8. A process according to claim 7, characterized in that the particles of the sol are non-aluminium modified. 9. A process according to claim 7 or 8, characterized in that the silica sol particles have a specific surface area within the range from 400 to 650 m 2 /g. 10. A process according to any of the claims 7, 8 or 9, characterized in that sol and a cationic acrylamide based polymer are added to the suspension.

Inventors: ANDERSSON KJELL, LARSSON BO, LINDGREN ERIK, ANDERSSON, KJELL, LARSSON, BO, LINDGREN, ERIK
Applicants: ANDERSSON KJELL, EKA NOBEL AB, LARSSON BO, LINDGREN ERIK
Application year: 1993
Main classification: C01B33
IPC codes: C01B33, D21F11, D21H17, D21H21