EP0333368B1 - Paper sizing method - Google Patents
Paper sizing method Download PDFInfo
- Publication number
- EP0333368B1 EP0333368B1 EP89302253A EP89302253A EP0333368B1 EP 0333368 B1 EP0333368 B1 EP 0333368B1 EP 89302253 A EP89302253 A EP 89302253A EP 89302253 A EP89302253 A EP 89302253A EP 0333368 B1 EP0333368 B1 EP 0333368B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- rosin
- paper
- sizing
- aluminium compound
- sizing agent
- 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 - Lifetime
Links
Classifications
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/04—Addition to the pulp; After-treatment of added substances in the pulp
- D21H23/06—Controlling the addition
- D21H23/14—Controlling the addition by selecting point of addition or time of contact between components
- D21H23/18—Addition at a location where shear forces are avoided before sheet-forming, e.g. after pulp beating or refining
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/24—Addition to the formed paper during paper manufacture
- D21H23/26—Addition to the formed paper during paper manufacture by selecting point of addition or moisture content of the paper
- D21H23/28—Addition before the dryer section, e.g. at the wet end or press section
Definitions
- the present invention relates to paper sizing methods and is more particularly concerned with the sizing of paper using rosin-based sizing compositions at relatively high pH values.
- the invention also relates to the resultant sized paper products.
- the present invention is based upon the unexpected discovery of a difference in behaviour if a pre-mix of rosin and an aluminium salt is made when or just before it is in fact used, as compared with known methods where it is made a considerable time before its use.
- a paper sizing method in which paper is made from a pulp system containing chalk or otherwise having a neutral or alkaline and therefore high pH, in which a pre-blended composition containing a rosin-based size and an aluminium compound, in the form of an emulsion, is added at an appropriate selected point in the paper machine wet-end.
- the weight ratio of the rosin size to the aluminium compound used in carrying out the method on a dry basis lies in the ratio 1:0.01 to 5.
- the ingredients added to the paper machine wet-end in carrying out the method of the invention, either during operation or as a one-shot pre-mix include at least one urea-based extender.
- a pre-mixed rosin-based sizing composition for use in carrying out the present invention may contain, in addition to the rosin and the aluminium compound, one or more other additives useful in the making of paper, for instance for optimising the sizing function of the rosin-based component per se.
- additional and optional additives include cationic and anionic polyelectrolytes, and also cationic starches.
- the pre-mix can contain one or more of cationic and anionic polyacrylamides, polyethyleneimine, polydialkyl dimethyl ammonium chloride (DADMAC) or polyamide/epichlorohydrin condensates, as well as dicyandiamide/formaldehyde condensation products.
- DADMAC polydialkyl dimethyl ammonium chloride
- dicyandiamide/formaldehyde condensation products can contain one or more of cationic and anionic polyacrylamides, polyethyleneimine, polydialkyl dimethyl ammonium chloride (DADMAC) or polyamide/epichlorohydrin condensates, as well as dicyandiamide/formaldehyde condensation products.
- the mixing device In order to carry out the method of the invention in practical terms, it is necessary to employ some form of mixing device, so as to control the degree of dispersion of the aluminium salt and the rosin size, which in turn affects its distribution amongst the paper fibres, with optimisation of sizing efficiency.
- the mixing device is suitably associated with the wet-end of the paper machine and its proper use ensures that the dispersion serves to control the degree of agglomeration of the fibres in the pulp.
- the rosin-based size component employed by being formulated into a pre-mix with an aluminium compound, can be based on rosin or rosin modifications, prior to conversion into a stable emulsion form.
- gum rosin formaldehyde-treated gum rosin or tall oil rosin, fumaric acid-treated gum rosin or tall oil rosin, disproportionated rosin, maleic anhydride-treated gum rosin or tall oil rosin such as the compounds or any combination of untreated or treated rosin, such as the compounds of the kinds just mentioned.
- esters or part esters of any of the above-mentioned forms of rosin formed with straight chain or polyhydric alcohols, can also be used.
- a third possibility is to use any appropriate mixture of any of the aforementioned untreated or treated forms of rosin, including disproportionated rosin and tall oil rosin, together with any one or more of the esters or part esters just described.
- resinous materials other than rosin per se or chemically-modified rosin compounds.
- hydrocarbon resins both of the aromatic and aliphatic varieties, can be used when suitably formulated, in order to carry out the paper-making methods of the present invention.
- Paraffin waxes and microcrystalline waxes may be used in conjunction with any of the above-mentioned rosin or resin-based types of sizing compositions, the particular use of one or other of the possible waxes depending largely upon the properties which may be required in the eventual paper product.
- any appropriate rosin-based sizing emulsion may incorporate one or more extenders.
- extenders may be employed for this purpose.
- Such extenders are disclosed for example in US-A-4022634, 4093779, 4141750, 4025354, 4437894 and 4605445.
- Any appropriate rosin emulsion may also be extended with emulsions of alkyl ketene dimers, prior to or subsequent to premixing with the aluminium compound.
- the alkyl ketene dimer emulsions may be stabilised with either cationic starch or cationic or anionic polymers.
- the aluminium compound incorporated in the one-shot pre-mix of the invention or otherwise employed in carrying out paper sizing methods according to the present invention is selected from polyaluminium chlorides, aluminium chlorohydrate, aluminium sulphate (paper makers alum) and any mixture of two or more of the foregoing.
- At least one stabilising agent which may take the form of one or more surface active agents or surfactants.
- Mixtures of stabilising agents or surfactants also can be used. A very wide range of possibilities is available as to the nature of such materials, which can be anionic, non-ionic, cationic or amphoteric.
- One particular class of stabilised emulsion comprises essentially a rosin soap and a protective colloid.
- the rosin-based component namely the rosin soap, can be a sodium, potassium or ammonium soap of rosin or of a modified rosin, together with amine salts of rosins or modified rosins, for instance the amine salts formed with mono-, di- or triethanolamine.
- These stabilisers can be added separately or formed in situ when making up the rosin-based emulsion composition.
- Colloids which can be used to stabilise the resultant product include casein, starch, soya protein and cellulose derivatives, the former being the most preferred, as well as certain polymers, such as polyvinyl pyrrolidone or polyvinyl alcohol (PVA).
- a preferred form of stabilised emulsion consists essentially of the potassium or sodium soap of the rosin or rosin derivative and casein as the stabilising colloid.
- surface active agents or surfactants which can be used in formulating the compositions of this invention include:
- a pilot Fourdrinier paper machine was used which was operated to produce paper of 85 gsm at 16 kg per hour from softwood/hardwood Kraft furnish loaded with 10% chalk.
- Pre-mixes of the rosin size and aluminium salt were made using a laboratory mixer and were metered just prior to the flow box.
- sheets were made using Kraft pulp containing 10% of chalk.
- the size and the PAC were added separately to the pulp and held for 30 minutes before sheets were made.
- a commercial paper machine producing envelope paper at the rate of 6.8 tonnes per hour with a chalk content varying from 5.8 to 7.8 per cent was sized by pre-blending free rosin size and alum and adding the pre-mix to the forward side of the thick stock headbox. Throughout the run, the amount of size used (dry basis) was 0.45% and the amount of alum used (dry basis) was 1.93%.
- the invention thus represents a substantial and surprising advance on previous paper sizing methods and compositions.
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- Paper (AREA)
- Polymerisation Methods In General (AREA)
- Basic Packing Technique (AREA)
- Making Paper Articles (AREA)
- Medicinal Preparation (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
Abstract
Description
- The present invention relates to paper sizing methods and is more particularly concerned with the sizing of paper using rosin-based sizing compositions at relatively high pH values. The invention also relates to the resultant sized paper products.
- Conventional paper sizing methods, using rosin in either its emulsified or soaped forms, involve the separate addition to one or more selected points in the paper machine wet-end of the rosin-based sizing composition and of an aluminium salt. This technique operates satisfactorily at pH values lying generally in the range from 4 to 6. When the pH is higher than about 6, to any significant extent, for example in the case where chalk is added to the paper pulp, sizing by this technique becomes erratic and very difficult to control. In view of these difficulties, when attempting to make sized paper or to surface size paper already made, using a pH value above the normal 4 to 6 range, it is common practice to resort to the use of non-rosin sizes, such as those based on alkyl ketene dimers.
- Attempts to size generally at neutral or alkaline pH values or to use specific aluminium salts (e.g. polyaluminium chloride) in the two-shot mode in the presence of chalk have only given very poor results.
- It is also known that if a one-shot mode of operation is used, namely a method involving use of a pre-mix of rosin and aluminium salt, made a considerable time before addition of the pre-mix to the machine, again only spasmodic control of sizing in an alkaline environment is obtainable. Such one-shot systems, operated so as to avoid these difficulties, are disclosed for instance in our pending Application No. 88304405.9 (Publication Number EP-A-0293119) and also in US-A-4333795.
- It has now surprisingly been found that if a pre-mix of a rosin-based size and an aluminium salt is made, on an in-line basis just before its addition to the paper machine, much better and more controlled sizing is obtained with rosin, when the stock contains chalk or otherwise has a neutral or alkaline pH value. Thus, the present invention is based upon the unexpected discovery of a difference in behaviour if a pre-mix of rosin and an aluminium salt is made when or just before it is in fact used, as compared with known methods where it is made a considerable time before its use.
- According to one aspect of the present invention therefore, a paper sizing method is provided, in which paper is made from a pulp system containing chalk or otherwise having a neutral or alkaline and therefore high pH, in which a pre-blended composition containing a rosin-based size and an aluminium compound, in the form of an emulsion, is added at an appropriate selected point in the paper machine wet-end.
- According to a further preferred feature of the method the weight ratio of the rosin size to the aluminium compound used in carrying out the method on a dry basis, lies in the ratio 1:0.01 to 5. According to a further preferred feature of the invention, the ingredients added to the paper machine wet-end in carrying out the method of the invention, either during operation or as a one-shot pre-mix, include at least one urea-based extender.
- In accordance with a preferred embodiment of the invention, a pre-mixed rosin-based sizing composition for use in carrying out the present invention may contain, in addition to the rosin and the aluminium compound, one or more other additives useful in the making of paper, for instance for optimising the sizing function of the rosin-based component per se. Such additional and optional additives include cationic and anionic polyelectrolytes, and also cationic starches. For example, the pre-mix can contain one or more of cationic and anionic polyacrylamides, polyethyleneimine, polydialkyl dimethyl ammonium chloride (DADMAC) or polyamide/epichlorohydrin condensates, as well as dicyandiamide/formaldehyde condensation products.
- In order to carry out the method of the invention in practical terms, it is necessary to employ some form of mixing device, so as to control the degree of dispersion of the aluminium salt and the rosin size, which in turn affects its distribution amongst the paper fibres, with optimisation of sizing efficiency. The mixing device is suitably associated with the wet-end of the paper machine and its proper use ensures that the dispersion serves to control the degree of agglomeration of the fibres in the pulp.
- In carrying out the invention, the rosin-based size component employed, by being formulated into a pre-mix with an aluminium compound, can be based on rosin or rosin modifications, prior to conversion into a stable emulsion form. Thus, use can be made for this purpose of gum rosin, formaldehyde-treated gum rosin or tall oil rosin, fumaric acid-treated gum rosin or tall oil rosin, disproportionated rosin, maleic anhydride-treated gum rosin or tall oil rosin such as the compounds or any combination of untreated or treated rosin, such as the compounds of the kinds just mentioned. In addition, esters or part esters of any of the above-mentioned forms of rosin, formed with straight chain or polyhydric alcohols, can also be used. A third possibility is to use any appropriate mixture of any of the aforementioned untreated or treated forms of rosin, including disproportionated rosin and tall oil rosin, together with any one or more of the esters or part esters just described.
- As a further aspect of the invention, it is possible to use resinous materials other than rosin per se or chemically-modified rosin compounds. For example, hydrocarbon resins, both of the aromatic and aliphatic varieties, can be used when suitably formulated, in order to carry out the paper-making methods of the present invention.
- Paraffin waxes and microcrystalline waxes may be used in conjunction with any of the above-mentioned rosin or resin-based types of sizing compositions, the particular use of one or other of the possible waxes depending largely upon the properties which may be required in the eventual paper product.
- Furthermore, any appropriate rosin-based sizing emulsion, derived from any one or more of the above-mentioned materials, may incorporate one or more extenders. By way of example, urea-based extenders may be employed for this purpose. Such extenders are disclosed for example in US-A-4022634, 4093779, 4141750, 4025354, 4437894 and 4605445. Any appropriate rosin emulsion may also be extended with emulsions of alkyl ketene dimers, prior to or subsequent to premixing with the aluminium compound. The alkyl ketene dimer emulsions may be stabilised with either cationic starch or cationic or anionic polymers.
- According to another aspect of the invention, the aluminium compound incorporated in the one-shot pre-mix of the invention or otherwise employed in carrying out paper sizing methods according to the present invention is selected from polyaluminium chlorides, aluminium chlorohydrate, aluminium sulphate (paper makers alum) and any mixture of two or more of the foregoing.
- In putting the invention into practice, it is desirable to incorporate in the paper sizing composition, when made up in a one-shot form, at least one stabilising agent, which may take the form of one or more surface active agents or surfactants. Mixtures of stabilising agents or surfactants also can be used. A very wide range of possibilities is available as to the nature of such materials, which can be anionic, non-ionic, cationic or amphoteric.
- One particular class of stabilised emulsion comprises essentially a rosin soap and a protective colloid. The rosin-based component, namely the rosin soap, can be a sodium, potassium or ammonium soap of rosin or of a modified rosin, together with amine salts of rosins or modified rosins, for instance the amine salts formed with mono-, di- or triethanolamine. These stabilisers can be added separately or formed in situ when making up the rosin-based emulsion composition. Colloids which can be used to stabilise the resultant product include casein, starch, soya protein and cellulose derivatives, the former being the most preferred, as well as certain polymers, such as polyvinyl pyrrolidone or polyvinyl alcohol (PVA). A preferred form of stabilised emulsion consists essentially of the potassium or sodium soap of the rosin or rosin derivative and casein as the stabilising colloid.
- According to a further feature of the invention, surface active agents or surfactants which can be used in formulating the compositions of this invention include:
- (i) salts of sulphonic acids having the general formula:
- (ii) salts of sulphuric acid half esters having the general formula:
- (iii) alkyl-benzene sulphonates wherein the alkyl substituent comprises from 8 to 24 carbon atoms, including all those compounds described in US-A-4157982.
- (iv) sulphosuccinate half esters of fortified rosin having the formula:
H(3-m). R. [(CH2CH20)n-OC.C2H3SO3Na.-C00Na]m
wherein R is a fortified rosin acid tricarboxylate group, m has an average value of 1.5 to 3 and n has an average value from 4.5 to 25 including all those described in EP-A-159794. - (v) compounds having one or other of the formulae:
- (vi) sulphosuccinate salts of ethylene oxide condensates having the general formula:-
- (vii) organic phosphate esters having one or other of the general formulae:
- In order that the present invention may be fully understood and appreciated, the following examples of use of the paper sizing methods and compositions of the present invention are given, by way of illustration only. In the examples, all amounts are given as percentages by weight, unless otherwise indicated. In example 1, part A represents use of the invention, while part B represents use according to the prior art.
- A pilot Fourdrinier paper machine was used which was operated to produce paper of 85 gsm at 16 kg per hour from softwood/hardwood Kraft furnish loaded with 10% chalk.
- Pre-mixes of the rosin size and aluminium salt were made using a laboratory mixer and were metered just prior to the flow box.
- The following results were obtained: -
Rosin Size Solids/fibre % Polyaluminium chloride (as received) 1 min Cobb gsm pH at Flow Box 1.0 0.5 68 7.8 1.0 1.0 29 7.6 1.0 1.5 29 7.6 - For comparison with the practice exemplified in Part A, sheets were made using Kraft pulp containing 10% of chalk. The size and the PAC were added separately to the pulp and held for 30 minutes before sheets were made.
- The following results were obtained:-
Rosin size Solids/fibre % Polyaluminium chloride (as received) 1 min Cobb gsm pH at Flow Box 1.0 0.5 146 7.4 1.0 1.0 156 7.2 1.0 1.5 154 7.3 2.0 0.5 154 7.4 2.0 1.0 144 7.3 2.0 1.5 137 7.2 - A commercial paper machine producing envelope paper at the rate of 6.8 tonnes per hour with a chalk content varying from 5.8 to 7.8 per cent was sized by pre-blending free rosin size and alum and adding the pre-mix to the forward side of the thick stock headbox. Throughout the run, the amount of size used (dry basis) was 0.45% and the amount of alum used (dry basis) was 1.93%.
Time 1 Min Cobb Flow Box pH 12.30 26 8.0 12.45 20 8.0 13.45 20 8.0 13.50 22 7.5 14.25 21 7.7 14.59 21 7.6 15.34 21 7.7 - Referring to example 1 above, it will be noted that, in part B, the Cobb values indicate that the sheets were close to saturation. Referring to the last three results in part B of example 1, double the amount of rosin size on a percent solid/fibre basis was used, as compared with the first three, but this made very little difference to the Cobb values obtained and none of those obtained in part B came anywhere near the much better results in terms of levels of sizing achieved in carrying out the invention, according to part A of example 1. A very satisfactory range of sizing is given by the last two results of example 1 part A in particular and throughout example 2. In these examples, "as received" in relation to the polyaluminium chloride means that it contained 10 percent Al203.
- The invention thus represents a substantial and surprising advance on previous paper sizing methods and compositions.
Claims (6)
- A method of improving sizing of paper containing chalk as a filler whereby a rosin-based or resin-based sizing agent and an aluminium compound are added to the papermaking stock at a selected point in the paper machine wet-end, characterised in that the sizing agent in the form of an emulsion and the aluminium compound are pre-mixed just prior to the addition and that the papermaking stock contains chalk in an amount sufficient to produce a pH above 6.
- A method according to claim 1, characterised in that the aluminium compound is a polyaluminium chloride or an aluminium chlorohydrate.
- A method according to claim 1 or 2, characterised in that the weight ratio of the sizing agent to the aluminium compound, on a dry basis, lies in the range of from 1:0.01 to 5.
- A method according to claims 1 or 2, characterised in that the pre-mix includes at least one urea-based extender.
- A method according to any of the preceding claims, characterised in that the pre-mix includes an additive selected from cationic starches, cationic and anionic polyacrylamides, polyethyleneimine, polydialkyl dimethyl ammonium chloride, polyamide/epichlorohydrin condensates and dicyandiamide/formaldehyde condensation products.
- A method according to any of the preceding claims, characterised in that the sizing agent is based on rosin or a rosin modification selected from gum rosin, formaldehyde-treated gum rosin or tall oil rosin, fumaric acid-treated gum rosin or tall oil rosin, disproportionated rosin, maleic anhydride treated gum rosin or tall oil rosin, esters or part esters of such rosin or rosin modification with straight chain or polyhydric alcohols.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8806432 | 1988-03-18 | ||
GB888806432A GB8806432D0 (en) | 1988-03-18 | 1988-03-18 | Paper sizing methods & compositions |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0333368A2 EP0333368A2 (en) | 1989-09-20 |
EP0333368A3 EP0333368A3 (en) | 1991-03-27 |
EP0333368B1 true EP0333368B1 (en) | 1996-06-12 |
Family
ID=10633654
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP89302253A Expired - Lifetime EP0333368B1 (en) | 1988-03-18 | 1989-03-07 | Paper sizing method |
Country Status (14)
Country | Link |
---|---|
EP (1) | EP0333368B1 (en) |
JP (1) | JP2656830B2 (en) |
AT (1) | ATE139281T1 (en) |
AU (1) | AU619260B2 (en) |
CA (1) | CA1325500C (en) |
DE (1) | DE68926632T2 (en) |
DK (1) | DK173063B1 (en) |
ES (1) | ES2087862T3 (en) |
FI (1) | FI94974C (en) |
GB (1) | GB8806432D0 (en) |
NO (1) | NO180345C (en) |
NZ (1) | NZ228297A (en) |
PT (1) | PT90040B (en) |
ZA (1) | ZA891925B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016032831A1 (en) * | 2014-08-27 | 2016-03-03 | Ecolab Usa Inc. | Method of increasing paper surface strength by using polyaluminum chloride in a size press formulation containing starch |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2799505B2 (en) * | 1989-07-08 | 1998-09-17 | 荒川化学工業株式会社 | Emulsion size |
JP2913756B2 (en) * | 1990-04-25 | 1999-06-28 | 三菱化学株式会社 | How to size paper |
DE4032660A1 (en) * | 1990-10-15 | 1992-04-16 | Basf Ag | METHOD FOR SIZING PAPER, CARDBOARD AND CARDBOARD |
JP3223649B2 (en) * | 1993-06-25 | 2001-10-29 | 日本ピー・エム・シー株式会社 | Sizing agent for neutral papermaking, production method thereof, sizing method and sizing paper |
JPH07276788A (en) * | 1994-04-02 | 1995-10-24 | Nagoya Pulp Kk | Recording paper |
US5510003A (en) * | 1994-07-20 | 1996-04-23 | Eka Nobel Ab | Method of sizing and aqueous sizing dispersion |
GB2292158B (en) * | 1994-07-26 | 1998-12-09 | Roe Lee Paper Chemicals Compan | Sizing method |
US6033526A (en) * | 1994-12-28 | 2000-03-07 | Hercules Incorporated | Rosin sizing at neutral to alkaline pH |
FI956217A (en) | 1994-12-28 | 1996-06-29 | Hercules Inc | Rosin and hydrocarbon resin for bonding paper |
GB2326170B (en) * | 1997-06-13 | 2001-05-09 | Raisio Chemicals Uk Ltd | Sizing of fibres |
JP6619613B2 (en) * | 2015-10-21 | 2019-12-11 | 大王製紙株式会社 | Manufacturing method of colored paper |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2050453B (en) * | 1979-05-23 | 1983-02-09 | Tenneco Chem | Chemical compositions useful in the manufacture of paper sizing agents |
DE3035634C2 (en) * | 1980-09-20 | 1982-10-21 | Feldmühle AG, 4000 Düsseldorf | Process for the production of a mass-sized paper or cardboard containing calcium carbonate as a filler |
US4522686A (en) * | 1981-09-15 | 1985-06-11 | Hercules Incorporated | Aqueous sizing compositions |
IT1151847B (en) * | 1982-07-14 | 1986-12-24 | Prodeco Spa | PROCEDURE FOR PAPER COLLATION |
GB2159183A (en) * | 1984-03-20 | 1985-11-27 | Roe Lee Paper Chemicals Limite | Paper sizing composition |
SE8405260L (en) * | 1984-10-22 | 1986-04-23 | Eka Ab | HYDROPHOBING AGENTS FOR ORGANIC FIBERS, Separate CELLULOS FIBERS, SET TO MAKE THIS AGENT AND THE USE OF THE MELD HYDROPHOBING AGENT |
IT1188086B (en) * | 1985-01-25 | 1987-12-30 | Antonio Corbellini | METHOD FOR THE PREPARATION OF MIXTURES FOR THE PRODUCTION OF GLUE PAPER BY ADDING A SINGLE GLUE PRODUCT AND RELATED GLUE PRODUCT |
DE3661948D1 (en) * | 1985-04-13 | 1989-03-02 | Chem Fab Bruhl Oppermann Gmbh | Paper-sizing agents and their use |
GB8712370D0 (en) * | 1987-05-26 | 1987-07-01 | Albright & Wilson | Paper sizing compositions |
-
1988
- 1988-03-18 GB GB888806432A patent/GB8806432D0/en active Pending
-
1989
- 1989-03-07 EP EP89302253A patent/EP0333368B1/en not_active Expired - Lifetime
- 1989-03-07 AT AT89302253T patent/ATE139281T1/en not_active IP Right Cessation
- 1989-03-07 ES ES89302253T patent/ES2087862T3/en not_active Expired - Lifetime
- 1989-03-07 DE DE68926632T patent/DE68926632T2/en not_active Expired - Fee Related
- 1989-03-10 NZ NZ228297A patent/NZ228297A/en unknown
- 1989-03-13 FI FI891184A patent/FI94974C/en not_active IP Right Cessation
- 1989-03-14 ZA ZA891925A patent/ZA891925B/en unknown
- 1989-03-15 NO NO891116A patent/NO180345C/en not_active IP Right Cessation
- 1989-03-17 JP JP1063988A patent/JP2656830B2/en not_active Expired - Fee Related
- 1989-03-17 AU AU31429/89A patent/AU619260B2/en not_active Ceased
- 1989-03-17 PT PT90040A patent/PT90040B/en not_active IP Right Cessation
- 1989-03-17 DK DK198901318A patent/DK173063B1/en not_active IP Right Cessation
- 1989-03-17 CA CA000594070A patent/CA1325500C/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016032831A1 (en) * | 2014-08-27 | 2016-03-03 | Ecolab Usa Inc. | Method of increasing paper surface strength by using polyaluminum chloride in a size press formulation containing starch |
US9365979B2 (en) | 2014-08-27 | 2016-06-14 | Ecolab Usa Inc. | Method of increasing paper surface strength by using polyaluminum chloride in a size press formulation containing starch |
Also Published As
Publication number | Publication date |
---|---|
JPH026680A (en) | 1990-01-10 |
CA1325500C (en) | 1993-12-28 |
PT90040A (en) | 1989-11-10 |
AU3142989A (en) | 1989-09-21 |
DK173063B1 (en) | 1999-12-13 |
EP0333368A2 (en) | 1989-09-20 |
NO180345B (en) | 1996-12-23 |
ZA891925B (en) | 1990-05-30 |
PT90040B (en) | 1995-03-01 |
EP0333368A3 (en) | 1991-03-27 |
DK131889A (en) | 1989-09-19 |
AU619260B2 (en) | 1992-01-23 |
ES2087862T3 (en) | 1996-08-01 |
JP2656830B2 (en) | 1997-09-24 |
DK131889D0 (en) | 1989-03-17 |
FI891184A (en) | 1989-09-19 |
GB8806432D0 (en) | 1988-04-20 |
NZ228297A (en) | 1991-07-26 |
ATE139281T1 (en) | 1996-06-15 |
NO891116D0 (en) | 1989-03-15 |
FI94974C (en) | 1995-11-27 |
FI891184A0 (en) | 1989-03-13 |
NO180345C (en) | 1997-04-02 |
DE68926632T2 (en) | 1996-11-21 |
DE68926632D1 (en) | 1996-07-18 |
NO891116L (en) | 1989-09-19 |
FI94974B (en) | 1995-08-15 |
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