CN1035859A - The production method of paper - Google Patents

The production method of paper Download PDF

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Publication number
CN1035859A
CN1035859A CN89101260A CN89101260A CN1035859A CN 1035859 A CN1035859 A CN 1035859A CN 89101260 A CN89101260 A CN 89101260A CN 89101260 A CN89101260 A CN 89101260A CN 1035859 A CN1035859 A CN 1035859A
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China
Prior art keywords
cationic
retention agents
cation
silica
method described
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CN89101260A
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CN1010599B (en
Inventor
斯宛丁·波·约翰
约翰逊·汉斯·埃瑞克
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Nouryon Pulp and Performance Chemicals AB
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Eka Nobel AB
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Publication of CN1035859A publication Critical patent/CN1035859A/en
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    • 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
    • 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
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/06—Paper forming aids
    • D21H21/10—Retention agents or drainage improvers
    • 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
    • D21H17/10—Phosphorus-containing compounds
    • 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
    • D21H17/20—Macromolecular organic compounds
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24—Polysaccharides
    • D21H17/31—Gums
    • D21H17/32—Guar or other polygalactomannan gum
    • 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
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
    • 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

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)

Abstract

A kind of production method of paper, this method are in the presence of silica-based colloidal sol of CATION and cationic polymer retention agents, will contain cellulose fibre and the suspension moulding on the net and the dehydration of the filler selected for use.The retention agents of this cationic polymer is cationic guar gum or a kind of cationic synthetic polymer such as cationic polyacrylamide.Retention and favourable drainage that cationic colloidal silica and CATION retention agents combine and can improve fiber fines and filler.

Description

The production method of paper
The present invention relates to a kind of production method of paper, this method is to use one group of material to improve retention and dehydration property.Especially, this method relates to the bond that uses cationic silica-based colloidal sol and cationic organic polymer retention agents in papermaking.
People know already in papermaking and to adopt the two composition of inorganic silicon colloidal sol and CATION retention agents.Be to make anionic silica sol and cationic polymer retention agents in this class example, for example cationic starch, cationic polyacrylamide etc. are used in combination.Disclose the example of this class usage such as No. 41056, European patent and european patent application book No. 21874.By anionic silica sol and the positive system that constitutes from component, its effect is the interaction between the different material of these two kinds of electric charges, and the particle of imagination colloidal sol is with to a certain degree crosslinked of the retention agents of its reinforcing yin essence electric charge and polymer generation.
Cationic inorganic silicon-based colloid is originally for known, and this class silica gel application in the speciality paper manufacturing technique is also known.The application of CATION inorganic silica gel when for example United States Patent (USP) 4309247 and 4366068 has disclosed and prepared the filter refill with cellulose fibre.Also use cationic colloidal silicon with the WATER RESISTANCE of enhancing water-soluble dye and the light resistance of paper the known inks injection record paper 85-260377 number from the Japanese patent application book.In this Japanese patent application book, there is an example to illustrate that the pulp suspension of cationic starch and cationic colloidal silicon prepares the ink jet record-paper with containing talcum powder.
The combined system that has been surprised to find that silica-based colloidal sol of CATION and cationic organic polymer retention agents according to the present invention can be used for papermaking, and the combination of these two kinds of electric charge same composition can improve retention and improve dehydration.Articulated system according to the present invention can obtain higher retention and make drainage smooth fiber fines and the filler selected for use.Thereby make this papermaking process efficient higher.
Thereby this patent relate to a kind of with cellulose fiber and the suspension of selected filler, the method for the production paper of the dehydration that is shaped on the net.Therefore described shaping and dehydration are carried out having in the presence of silica-based colloidal sol of CATION and the cationic polymer retention agents, and wherein retention agents is selected from CATION guar gum class or cation synthesising copolymer.
Positively charged as previously mentioned silica sol particle is known substantially.Its preparation method discloses in No. 3007878, United States Patent (USP), in No. 2620978 and No. 3719607.The conventional method of preparation cationic colloidal silica is the basic salt reaction with the hydrosol of silica and polyvalent metal, makes the positive surface charge of sol particles band, usually uses stabilizing agent in these methods, such as boric acid, alkali metal class alkali, alkaline-earth metal class alkali, ammonia or the like.The salt of polyvalent metal is aluminium salt normally, because of its price paper and easily acquisition.Although also can use other polyvalent metal basic salt to prepare cationic silica-based colloidal sol certainly, for example chromium, zirconium and other polyvalent metal.The basic salt that any water soluble also can produce desired positively charged surface can both use.Usually the preparation cationic sol is used chloride, nitrate or the acetate of metal.
The particle mean size of the particle of this cationic sol is little, be generally less than 100 nanometers, its size is usually from 2 nanometer to 100 nanometers, be more frequently in 2 nanometers within 80 nanometer range, suitable particle size be from 3 nanometers to 20 nanometers, and 3.5 to 14 nanometers preferably.Positively charged polyvalent metal material to be arranged, preferably aluminium on the surface of cationic silicon dioxide particle.Aluminium can be from 1: 8 to 4: 1 to the molar ratio range of surface silica dioxide, and suitable molar ratio range was from 1: 6 to 4: 1, and preferable scope is between 1: 4 to 4: 1.The most desirable ratio is within 1: 2 to 4: 1 scope.The mol ratio of calculating aluminium and silica is the same with United States Patent (USP) 3,956,171, and by 8 silicon atoms of every square nanometers silica surface, promptly all from the teeth outwards silica partly is 8 * 10 -4* A, A is that the specific area of sol particles is (with rice herein 2The expression of/gram).As previously mentioned, the used cationic colloidal silica of the present invention can be by making the basic salt prepared in reaction of any anionic silica sol and polyvalent metal.Therefore can be with the colloidal silica preparation of commodity, the Ludox preparation of the also available poly-silicic acid that makes by the alkali silicate acidifying (for example mix with waterglass or adopt acid ion exchanger resin) with inorganic acid.Cationic silica is added in the slurry with hydrosol form.The concentration of cationic sol, Yue Keda 50%(weight when making), by commodity anion silica gel as be make by poly-silicic acid can be up to about 10%(weight).A kind of collosol stability in restriction back is so its suitable concentration is about below 5% or 5%.In front in the proportion of being mentioned, if stability is generally higher more for a long time for aluminium.In any case see from the viewpoint of practicality, colloidal sol is added to slurry was diluted to 0.05% to 5.0% concentration in the past earlier and suits, and better to be diluted to 0.1%-2%.
The CATION retention agents that is used in combination with cationic silica is an organic polymer retention agents commonly used in the papermaking, and this class retention agents has clean positive charge, this class retention agents or guar gum or synthetic cationic polymer when the pH value that papermaking is adopted.Some examples of suitable synthetic cationic polymers have cationic polyacrylamide, cationic polyethyleneimine and CATION polyamidoamines amine.Also available above-mentioned two or more mixture of polymers, and can wherein any be used in combination with cationic starch.Synthetic CATION retention agents is preferable, particularly cationic polyacrylamide.
Used cationic silicon dioxide and CATION retention agents amount depend on used paper making pulp, other condition of the filler of existence and papermaking.Usually to fiber of doing and the papermaking filler of selecting for use, the consumption of cationic silicon dioxide (dried) is from 0.005%(weight) to 2%(weight), the result that can draw.Suitable consumption is from 0.005%(weight) to 1%(weight).And consumption is in 0.03%(weight) to 0.3%(weight) the best as a result in the scope.The ratio of CATION retention agents and cationic silicon dioxide can change in very wide scope, and ratio depends on the condition of papermaking, and specific cationic polymer also depends on consequent other effect of requirement.Usually, the CATION retention agents was at least 0.01: 1 the weight ratio of cationic silicon dioxide, and suitable ratio is wanted 0.2: 1 at least.The upper limit of the CATION retention agents (as guar gum) that cationic degree (cationicity) is lower requires not strict, can be very high for this cationic polymer, reach 100: 1 or higher.The limit is decided by economic cause usually.The CATION retention agents is fit to most system the ratio of the cationic silicon dioxide scope at 0.2: 1 to 20: 1.
Second-component system of the present invention is suitable for the slurry papermaking with all kinds paper fibres, is applicable to cellulose fiber 50%(weight at least) slurry papermaking.For example this two component can be used as the additive of following slurry.Fiber derives from the slurry (as sulfate pulp, sulfite pulp) of chemical pulp, gives hot method mechanical pulp, chip groundwood, ground wood pulp.Can be the slurry of leaves moisting material, also can be softwood slurry.The fiber that system of the present invention is used to reclaim also is useful.Mentioned in the slurry and can contain mineral filler commonly used, kaolin for example, titanium dioxide, gypsum (calcium sulfate), chalk (calcium carbonate) and talcum powder.To being commonly referred to be difficult paper pulp and all can obtaining good especially effect to the paper pulp (being various types of mechanical pulps such as ground wood pulp) that contains a large amount of non-cellulose materials (as lignin).This two components system of the present invention is particularly suitable for having 25%(weight at least) the slurry formed of groundwood pulp.Compare with the system that anionic silica sol and CATION retention agents are formed, body series can obtain many improvement effects.Two terms of used here paper and papermaking never only comprise paper and paper production certainly, but also comprise the slabbing of other cellulose fibre or become the product (such as pulpboard, cardboard, mill bristol) of width of cloth shape and the production of these products.
Cationic colloidal silica and cationic polymer retention agents can be added to respectively in the slurry, also can add simultaneously or both add after being pre-mixed again, also can add at twice or repeatedly, preferably add this two components respectively.It seems that the order that adds colloidal sol and retention agents makes some difference to the effect of gained.As if less when sol particles, the CATION retention agents added before cationic silicon dioxide colloidal sol, can obtain effect preferably.When sol particles is big, add cationic silicon dioxide colloidal sol earlier and add the CATION retention agents subsequently again, the effect of gained is better.Compare with independent use CATION retention agents, add cationic silica and CATION retention agents by the present invention, can improve the retention of fiber fines and filler significantly, also significant the improvement dewaters.So available more a spot of cationic polymer retention agents obtains desired effect, thereby just can reduce cost significantly for the cationic polymer (as polyacrylamide) of costliness.Adopt system of the present invention, can make the papermaking process better effects if, and producing strength of paper and other important performance thereof are not had bad effect.There have two components of same electric charge to play the mechanism of effect to be not definite fully as yet, the material composition anion of dissolving but the cationic silicon dioxide of believing colloidal sol has neutralized at least in part; And believe because the penetration capacity of the cationic silicon dioxide opposite end fiber of colloidal sol and the neutralising capacity of electric charge, strengthened the intensity of staple fibre.The CATION retention agents that adds makes solvent components and solid state component in the slurry form staple fibre jointly.
In the production method of paper of the present invention,, can also use conventional additive certainly except two kinds of additives of the present invention.The front had been discussed filler.As what the example of some other additive was mentioned sizing agent arranged, as abietyl sizing agent or synthetic sizing agent, cationic starch, wet strengthening resin.Can use aluminium base compound, as aluminum sulfate, aluminate, the aluminium compound of aluminium chloride or polymerization.Use this composition of matter to improve the papermaking process of retention and dehydration, can in very big pH scope (pH from 4 about to 9 about), carry out.Special advantage is: it is high and contain the paper of lignin to produce fines content with two components system of the present invention under the high situation of retention.And paper sheet formation is not had negative interaction.
Further illustrate the present invention in the example below.Yet do not want to be confined to these examples.Unless add explanation in addition, " several branches several " and " percentage " all calculate according to weight.
Example 1
Used cationic colloidal silica is prepared as follows in example 1 and example 2: be equipped with in the flask of heating jacket, under agitation making aluminum chloride hydrate (Al 2(OH) 5Cl2H 2O) be heated to 47 ℃.After reaching this temperature, add the anion silica gel of having removed sodium ion with time of a fixed length, so that it and aluminium chlorohydrate react, anion silica gel wherein dilutes with deionized water in advance.As follows as preparing scheme more specifically: the Al that makes 408 grams 50% 2(OH) 5Cl2H 2O solution is warmed to 47 ℃.Make and contain 15.21% SiO 2Anionic silica sol 657 gram dilute (particle size of this colloidal sol has 7 nanometers approximately) with 928 gram deionized waters.This anionic silica sol is added to down at 47 ℃ and promptly obtains cationic sol in the aluminum salt solution, then cool to room temperature with 90 minutes.
In the test below according to SCAN-C21: 65 usefulness " Canadian freeness tester " are studied dehydration.This is expression dehydration or drainage capacity feature method commonly used.
Slurry system is by 60% bleached sulphate birch pulp, and 40% bleached sulphate pine slurry is formed, and adds 30% kaolin.With the kilogram number metering of chemical addition agent in dry finish system per ton (fiber+filler), the quantity of colloidal sol and the quantity of cationic polymer are all represented with dry.All chemical addition agents are placed in the electronic water filter of Bu Lite that can clog outlet (Britt Dynamic Drainage Jar), change mixing velocities with per minute 800 and mix for 45 seconds.Then slurry is put into Canadian freeness tester.In all tests, colloidal sol all added before the addition polymerization compound.
The various colloidal sols that use:
A) Ludox of cation aluminium modification, about 7.5 nanometers of particle size, aluminium is 1.30: 1 to the mol ratio of surperficial silicon-dioxide-substrate group (groups).
B) Ludox of cation aluminium modification, about 7 nanometers of particle size, aluminium was to the mol ratio of surperficial silicon-dioxide-substrate group 2.95: 1.
C) Ludox of cation aluminium modification, granularity are about 6 nanometers, and aluminium was to the mol ratio of surperficial silicon-dioxide-substrate group 3.25: 1.
D) Ludox of cation aluminium modification, about 14 nanometers of particle size, aluminium was to the mol ratio of surperficial silicon-dioxide-substrate group 2.40: 1.
Use following several cation polymer:
A) cationic polyacrylamide of medium cationic degree, PAM1, association colloid company (Allied Colloids) sells, and trade name Percol 292.
B) polymine, PEI, bus good fortune company (BASF AG) sells, trade name Polymin.
C) cationic polyacrylamide of low cationic degree, PAM2, association colloid company sells, and trade name Percol 140.
Following form has provided the result of freedom test, shows (ml CSF) with Canadian Standard Freeness milliliter numerical table.Also provided and added the comparison of corresponding cationic polymer separately separately.Also contrast about 5.5 nanometers of this anion silicon particle size with a kind of anion al-modified silica sol.
Colloidal sol/amount cationic polymer/amount slurry pH Canadian Standard Freeness
Kilogram/ton kilogram/ton milliliter
a/1.0 PAM1/0.5 4.5 560
a/1.0 PAM1/1.0 4.5 620
a/1.0 PAM1/2.0 4.5 675
b/1.0 PAM1/0.5 4.5 540
b/1.0 PAM1/1.0 4.5 605
b/1.0 PAM1/2.0 4.5 640
c/1.0 PAM1/0.5 4.5 565
c/1.0 PAM1/1.0 4.5 620
c/1.0 PAM1/2.0 4.5 660
d/1.0 PAM1/0.5 4.5 543
d/1.0 PAM1/1.0 4.5 590
d/1.0 PAM1/2.0 4.5 640
- PAM1/0.5 4.5 430
- PAM1/1.0 4.5 515
- PAM1/2.0 4.5 570
Anionic/1.0 PAM1/0.5 4.5 305
Anionic/1.0 PAM1/1.0 4.5 495
Anionic/1.0 PAM1/2.0 4.5 580
a/1.0 PEI/0.6 7.0 430
a/1.0 PEI/1.0 7.0 470
a/2.0 PEI/2.0 7.0 485
- PEI/0.6 7.0 350
- PEI/1.0 7.0 410
- PEI/2.0 7.0 435
a/1.0 PAM2/0.5 4.5 555
a/1.0 PAM2/1.0 4.5 625
a/1.0 PAM2/2.0 4.5 690
- PAM2/0.5 4.5 410
- PAM2/1.0 4.5 505
- PAM2/2.0 4.5 575
Example 2
In this test, measured the Ludox of the cation aluminium modification of in example 1, pointing out a) and the dehydrating effect of polyacrylamide Percol 292 systems, and compared with the Ludox (about 5.5 nanometers of particle size) of anion aluminium modification and the system of polyacrylamide composition.Slurry is made up of wood mechanical pulp, and beats 130ml CSF, and slurry pH is transferred to 5 with sulfuric acid.In some tests with cationic sol, colloidal sol added in the slurry before polyacrylamide.But the reversed in order that has a test to add.With some tests of anionic sol, colloidal sol is added in the slurry after the addition polymerization compound.Addition is listed with kg/ton, by the dry chemical medicine dry pulp is calculated.
Cationic sol anionic sol polyacrylamide CSF
Kg/ton kg/ton kg/ton milliliter
- - - 130
- - 0.5 210
- - 1.0 230
- - 2.0 250
- - 3.0 245
1.0 - 0.25 290
1.0 - 0.5 325
1.0 - 0.75 340
1.0 - 1.0 355
1.0 - 2.0 360
1.0(addition sequence is put upside down)-1.0 270
3.0 - 0.25 330
3.0 - 0.5 375
3.0 - 1.0 425
3.0 - 2.0 405
- 1.0 0.5 190
- 1.0 0.75 230
- 1.0 1.0 255
- 1.0 2.0 280
- 3.0 0.5 190
- 3.0 1.0 240
- 3.0 2.0 320
- 3.0 3.0 360
- 3.0 4.0 350
Obviously illustrate in the table: with compare with the anionic sol system, add the polyacrylamide of much less with the cationic sol system, and it is the highest to reach the CSF level.
Example 3
Used in this example some different cationic sol [a), b), c) and d)]
By following method prepare colloidal sol a) and c): with 19.49 grams, 50% polyaluminium chloride [Al 2(OH) 5Cl2H 2O] solution dilution to 200 gram of x.At room temperature slowly 1000 grams, 1% poly-silicic acid was injected this solution with 45 minutes.Poly-silicic acid prepares by the following method: water is with waterglass (Na 2O3 SiO 2) be diluted to SiO 2Content is 5%(weight).Spent ion exchange resin Amberlite IR-120 carries out ion-exchange to this aqueous solution, is 2.3 up to pH.The specific area of the poly-silicic acid of resulting acidity press the method that Sears proposes in " analytical chemistry ", use titration measuring, (seeing Sears:Analytical Chemistry 28(1956) 1981) draw its value be 1450 meters/restrain.This polymeric silicicacid is handled coalescent to a great extent chaining and net with the aluminium polychloride that the size of particle is about 1 nanometer scale then.Resulting cationic silica is analyzed as follows: alundum (Al 0.39%, silica 0.84%.Therefore the mol ratio of aluminium and surface silica dioxide is about 1: 2.Colloidal sol a) makes sol c from freshly prepd poly-silicic acid) make from the poly-silicic acid of placing one day.
Colloidal sol b) with d) by being prepared as follows: the polyaluminium chloride [Al of 9.75 grams 50% 2(OH) 5Cl2H 2O] x solution dilution to 200 gram, the poly-silicic acid (preparing with preceding method) of 1000 grams 1% is added so far in the solution, the product analysis of generation is as follows: alundum (Al 0.2%, silica 0.83%.Therefore, aluminium is about 1: 4 to the mol ratio on surface.Colloidal sol b) make by freshly prepd poly-silicic acid, and colloidal sol d) make by placing (wearing out) poly-silicic acid of one day.
Colloidal sol is a) to d) all together use in the slurry with cationic polyacrylamide (PAM).This PAM is by the vending articles title Percol of association colloid company 292.Slurry is made up of 60% sulfate birch pulp and 40% kraft pine slurry, also has 30% calcium carbonate and 1 grams per liter saltcake Na in the slurry 2SO 410H 2O.PH value of slurry is 8.5.Except as otherwise noted, polyacrylamide added in the slurry before cationic colloidal silica.As previously mentioned, the dehydration property with Canadian freeness tester judgement slurry respectively the results are shown in following table.
Polyacrylamide colloidal sol; Amount CSF
Kg/ton kg/ton milliliter
- - 390
0.5 - 475
- b）;1 395
0.5 a）;1 595
0.5 b）;1 605
0.5 c）;1 590
0.5 d）;1 600
0.5 b); 1(puts upside down and adds 505
In proper order)
Also be used for contrasting with the anionic silica sol of aluminium modification, about 5.5 nanometers of this anionic silica sol particle size are share with 1.5 kg/ton and PAM0.5 kg/ton, and drawing CSF is 520.
Example 4
Studied in the example 3 colloidal sol a) and b), also have e in addition) and f), be used for the slurry formed by groundwood pulp with cationic polyacrylamide together.Colloidal sol e) is prepared as follows: 27.84 grams, 50% aluminium polychloride [Al 2(OH) 5Cl2H 2O] x solution dilution to 200 gram.With the same in the example 3,1000 grams, 1% poly-silicic acid is added in the polymeric aluminum chlorides solution.Products therefrom contains 0.56% aluminium and 0.83% silica, so about 1: 1.5 of the mol ratio of aluminium and surface silica dioxide.Colloidal sol f) is prepared as follows: 50% aluminium polychloride [Al 2(OH) 5Cl2H 2O] x solution 34.8 gram is diluted to 200 grams.1000 grams, 1% poly-silicic acid is added in this polymeric aluminum chlorides solution.Product contains 0.70% alundum (Al and 0.83% silica, about 1: 1.2 of the mol ratio of aluminium and surface silicon.
The slurry of this groundwood pulp contains the saltcake Na of 2 grams per liters 2SO 410H 2O, the pH value is 7.0.Study as previously described dehydration to slurry, most test was added to cationic polyacrylamide in the slurry before colloidal sol.As put upside down this order and add colloidal sol earlier and then use (rdo) to indicate.The cationic polyacrylamide that adds is 1.0 kg/ton.This amount (not adding colloidal sol) when using separately is an optimised quantity to above-mentioned slurry.In this test, notice, use the composition of colloidal sol and cationic polyacrylamide, during than independent use polyacrylamide from the clarification of water of freeness tester collection many, this is the former sign fabulous to fines retention.
Polyacrylamide colloidal sol, amount CSF
Kg/ton kg/ton milliliter
- - 120
1.0 - 195
- b）;1.0 120
1.0 a）;1.0 4.00
1.0 a）;1.5 445
1.0 a）;2.0 485
1.0 a）;2.5 510
1.0 a）;1.0（rdo） 330
1.0 a）;1.5（rdo） 345
1.0 a）;2.0（rdo） 355
1.0 a）;2.5（rdo） 360
1.0 b）;1.0 420
1.0 b）;1.5 480
1.0 b）;2.0 505
1.0 b）;2.5 530
1.0 e）;1.5 400
1.0 e）;2.0 440
1.0 e）;2.5 435
1.0 f）;1.5 390
1.0 f）;2.0 425
1.0 f）;2.5 435
Example 5
In this example, the retention of filler and fiber fines is estimated in shop test.Slurry composition 30% chemical pulp, 24% groundwood pulp and 46% pearl filler.Slurry concentration is 0.5%, and pH is 8.3.Filler that records and fiber fines composition are 76.9% altogether.
Estimate retention with the electronic water filter of Bu Lite (Britt).Agitator speed is decided to be per minute 800 to be changeed.The net that uses is 200 orders.
Used cationic silica is identical with example 1.Silica gel added before retention agents.Adopted following CATION retention agents in each test.
A) cationic polyacrylamide (by the Percol 292 of association colloid company manufacturing).
B) CATION guar gum.
Result of the test has been shown in the following table.When each cationic polymer various dose, listed the percentage of filler and fines retention (FF ret.).Dosage calculates slurry and the filler of doing with the polymer of doing.Cationic colloidal silica is 1 kilogram to dry pulp per ton and amount of filler.With only adding cationic polymer has separately done contrast.
The colloidal sol filler fiber fines that the addition that adds adds
Cationic polymer kg/ton kg/ton retention %
A 0.25 1 75
A 0.50 1 97
A 0.75 1 100
A 0.25 - 43
A 0.50 - 61
A 0.75 - 80
B 2 1 95
B 4 1 95
B 6 1 95
B 2 - 45
B 4 - 83
B 6 - 90
Example 6
This routine system be with example 1 in a) identical cationic colloidal silica and polyacrylamide.The test of doing in the factory of production magazine paper.Slurry is by 19% sulfate pulp, 37% ground wood pulp, and 20% gives hot method mechanical pulp and 24% carclazyte is formed, and the slurry of a large amount of non-fibrous materials is promptly arranged.Slurry pH value is 4.45.Retention is measured with the electronic water filter of Bu Lite, and freedom is measured with the free analyzer of Canada.
Addition kg/ton retention freedom
Colloidal sol polyacrylamide % milliliter
- 0.25 26.4 110
- 0.50 44.6 140
- 1.0 57.6 190
2.0 0.25 41.7 150
2.0 0.50 65.0 200
2.0 1.0 85.6 305

Claims (8)

1, a kind of be shaped on the net and dewater with cellulose fiber and the filler suspension selected for use have the production method that the paper of the rate of seeing and dehydration property is stayed in improvement, it is characterized in that being shaped and dehydration is to carry out in the presence of the retention agents of silica-based colloidal sol of CATION and cationic polymer, its retention agents is selected from CATION guar gum class or synthetic cationic polymer.
2, a kind of method described in claim 1 is characterized in that the cationic colloidal silica particle is the silicon dioxide granule of aluminium modification.
3, a kind of method described in claim 1 or 2, the granular size scope that it is characterized in that cationic silicon dioxide granule is to 10 sodium rice from 2 nanometers.
4, a kind of method described in claim 1 is characterized in that the cationic polymer retention agents is the cationic polymer that synthesizes.
5, a kind of method described in claim 4 is characterized in that the cationic polymer retention agents is cationic polyacrylamide.
6, a kind of method described in claim 1 is characterized in that the weight ratio of cationic colloidal silica to fiber and used filler, in 0.005% to 2.0% scope in interior (all with dry weight).
7, a kind of method described in claim 1 or 6 is characterized in that the CATION retention agents was at least 0.01: 1 the weight ratio of cationic silicon dioxide.
8, a kind of method described in claim 7 is characterized in that the weight ratio at least 0.2: 1 of CATION retention agents to cationic silicon dioxide.
CN89101260A 1988-03-08 1989-03-07 Process for production of paper Expired CN1010599B (en)

Applications Claiming Priority (2)

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SE8800816A SE462721B (en) 1988-03-08 1988-03-08 SET FOR PAPER PREPARATION BY FORMING AND DEATHING A SUSPENSION OF CELLULOSAIN HOLDING FIBERS
SE8800816-4 1988-03-08

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CN1035859A true CN1035859A (en) 1989-09-27
CN1010599B CN1010599B (en) 1990-11-28

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KR (1) KR920011032B1 (en)
CN (1) CN1010599B (en)
AU (1) AU3294989A (en)
CA (1) CA1324705C (en)
DK (1) DK215590D0 (en)
ES (1) ES2010430A6 (en)
FI (1) FI93882C (en)
NZ (1) NZ228206A (en)
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WO (1) WO1989008741A1 (en)

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CN1052770C (en) * 1989-11-09 2000-05-24 埃卡·诺贝尔公司 Silica sols, a process for the production of silica sols and use of the sols
CN105542275A (en) * 2015-12-22 2016-05-04 成都新柯力化工科技有限公司 Method for softening inorganic fibers for paper making

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SE9103140L (en) * 1991-10-28 1993-04-29 Eka Nobel Ab HYDROPHOBERATED PAPER
DE4302293A1 (en) * 1993-01-28 1994-08-04 Degussa Filler-containing paper
US7732495B2 (en) 2004-04-07 2010-06-08 Akzo Nobel N.V. Silica-based sols and their production and use
US7629392B2 (en) 2004-04-07 2009-12-08 Akzo Nobel N.V. Silica-based sols and their production and use
US7208429B2 (en) 2004-12-02 2007-04-24 The Procter + Gamble Company Fibrous structures comprising a nonoparticle additive
US7976679B2 (en) 2004-12-02 2011-07-12 The Procter & Gamble Company Fibrous structures comprising a low surface energy additive
US7459179B2 (en) 2004-12-02 2008-12-02 The Procter & Gamble Company Process for making a fibrous structure comprising an additive
FI128012B (en) * 2016-03-22 2019-07-31 Kemira Oyj A system and method for manufacture of paper, board or the like

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SE8403062L (en) * 1984-06-07 1985-12-08 Eka Ab PAPER MANUFACTURING PROCEDURES
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SE451739B (en) * 1985-04-03 1987-10-26 Eka Nobel Ab PAPER MANUFACTURING PROCEDURE AND PAPER PRODUCT WHICH DRAINAGE AND RETENTION-IMPROVING CHEMICALS USED COTTONIC POLYACRYLAMIDE AND SPECIAL INORGANIC COLLOID
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Publication number Priority date Publication date Assignee Title
CN1052770C (en) * 1989-11-09 2000-05-24 埃卡·诺贝尔公司 Silica sols, a process for the production of silica sols and use of the sols
CN105542275A (en) * 2015-12-22 2016-05-04 成都新柯力化工科技有限公司 Method for softening inorganic fibers for paper making
CN105542275B (en) * 2015-12-22 2017-11-14 温州德泰塑业有限公司 A kind of method of paper grade (stock) inorfil flexibility

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JP2607161B2 (en) 1997-05-07
FI93882C (en) 1995-06-12
ES2010430A6 (en) 1989-11-01
CA1324705C (en) 1993-11-30
SE8800816L (en) 1989-09-09
NZ228206A (en) 1990-04-26
AU3294989A (en) 1989-10-05
JPH03503299A (en) 1991-07-25
SE8800816D0 (en) 1988-03-08
DK215590A (en) 1990-09-07
EP0394368B1 (en) 1993-05-12
KR900700690A (en) 1990-08-16
FI904384A0 (en) 1990-09-05
SE462721B (en) 1990-08-20
CN1010599B (en) 1990-11-28
KR920011032B1 (en) 1992-12-26
FI93882B (en) 1995-02-28
DK215590D0 (en) 1990-09-07
EP0394368A1 (en) 1990-10-31
WO1989008741A1 (en) 1989-09-21

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