AU613465B2

AU613465B2 - Production of paper and paper board

Info

Publication number: AU613465B2
Application number: AU31749/89A
Authority: AU
Inventors: John Graham Langley
Original assignee: Allied Colloids Ltd
Current assignee: Ciba Specialty Chemicals Water Treatments Ltd
Priority date: 1988-03-28
Filing date: 1989-03-28
Publication date: 1991-08-01
Anticipated expiration: 2009-03-28
Also published as: FI97307C; DE68905208T3; EP0335575A2; JPH0529719B2; EP0335575A3; AU3174989A; KR960002733B1; EP0335575B1; NO174724B; FI891465A; KR890014836A; DE68905208T2; JPH05239800A; ES2053980T3; FI891465A0; JPH026683A; CA1322435C; NO891301L; EP0335575B2; DE68905208D1

Description

V. t- 0 6 13465 COMMONWEALTH OFASTAA PATENTS AC I 1952 NAME ADDRESS OF APPLICANT: Allied Colloids Limited P0 Box 38, Low Moor Bradford West Yorkshire BD12 0Th United Kingdom NAME(S) OF INVENTOR(S): o John Graham LANGLEY ADDRESS FOR SERVICE: DAVIES COLLISON Patent Attorneys 1 Little Collins Street, Melbourne, 3000.

4 )MPLETE SPECIFICATION FOR THE INVENTION ENTITLD: Production of paper and paper board The following statement is a full, description of this invention, including the best method of performing it known to me/us:-

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la Paper or paper board is made by providing a thick stock, diluting the thick stock to form a thin stock, draining the thin stock to form a sheet and drying the sheet. The thick stock can be made either by mixing water into dried pulp or, in an integrated mill, by diluting a drained pulp.

It is standard practice to improve the process 10 performance, or the product quality, by including various additives at one or more of these stages.

o000 For instance, if the pulp from the which the thick 00 0 0 oo, stock is made is impure, the normal way of preparing it for drainage is by adding inorganic material, such as 0 0 0o 0o 15 alum, talc or bentonite, at the pulping or thick stock 0 0 stages. These treatments can have the effect of minimising problems due to pitch and other sticky 0000 o0 materials.

If it is necessary to improve the strength of the Q 00 final sheet it is common to include a dry strength resin, 00 ao a. for instance a cationic starch, in the stock that is to be drained.

It is standard practice to include cationic polymers 0 00 °000, in the stock that is to be drained in order to improve O 0 25 drainage and/or retention.

Processes for improving retention are described in i U.S. 4,388,150 -and involve the addition of cationic starch and colloidal silicic acid to the stock before drainage. Such processes have been commercialised under the trade name "Composil" (trade mark).

Processes that give improved drainage, retention, drying and formation are described in EP 235893 and involve adding a first synthetic cationic polymer before a shear stage and bentonite after that shear stage.

_II I Such processes have been commercialised under the t-ade name "Hydrocol" (trade mark).

Although this process gives very good results in most instances, there is room for improvement with some stocks, especially impure stocks, and for some end products, for instance newsprint and board.

In the invention, paper or paper board is made by a process comprising providing a cellulosic suspension, subjecting this to one or more shear stages selected from cleaning, mixing and pumping stages, adding a main o° polymer, selected from substantially linear synthetic cationic polymer having molecular weight above 500,000 "o and cationic starch, before one of the shear stages and adding inorganic material selected from bentonite and 15 colloidal silicic acid after that shear stage, draining the suspension to form a sheet and drying the sheet, and in this process there is a preliminary polymer inclusion stage selected from the inclusion in the suspension before the main polymer of a low molecular weight water soluble synthetic cationic polymer having molecular weight lower than the molecular weight of the main polymer, and the inclusion of a water soluble synthetic cationic polymer as a drainage aid for tle drainage of cellulosic pulp when the suspension is m, 3e by draining a cellulosic pulp (in the presence of the drainage aid) and diluting the drained pulp.

The preferred aspect of the invention comprises the incorporation of the said low molecular weight water soluble synthetic cationic polymer.

The inclusion of the low molecular weight cationic polymer in the thin stock before addition of the main polymer can lead to improvement in the processing and performance properties obtained by the addition of the main polymer before a shear stage and bentonite or colloidal silicic acid after that shear stage. For

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instance, depending upon the other conditions, it can lead to reduced problems due to pitch and other sticky materials and can lead to improved wet and/or dry strengths, runability, drainage, linting, opacity and other paper qualities.

In this first aspect of the invention, the aqueous cellulosic suspension can be made either from dried pulp or, in an integrated mill, by diluting a drained pulp, all in conventional manner.

000. 10 In the second aspect of the invention, the 0 O cellulosic suspension is made by diluting a drained pulp *Do* in an integrated mill and the drainage of the pulp is l oo,, promoted by including a pulp drainage aid in the pulp oa that is to be drained, this draining aid comprising a 0 0 15 water soluble cationic polymer. The cationic polymer for this purpose can be any of the synthetic polymers discussed below for use as the main cationic polymer.

000 Ooo When draining a pulp, in an integrated mill, to form :o0: a wet pulp that can then be diluted to make the thick stock and the thin stock, it is common to include no S 00 drainage aid in the pulp since drainage often occurs adequately without incurring the expense of a drainage aid. However in this aspect of the invention it is .at desirable to include a drainage aid since it promotes 0 25 drainage and/or retention and provides a drained pulp that already contains cationic polymer and the inclusion i; of this cationic polymer has beneficial effects on the subsequent treatment with the described main polymer and the inorganic additive. For instance it can reduce the amount of main polymer that is required for optimum performance and the combined amount of drainage aid and main polymer may then be appro::imately the same as the optimum amount of main polymer if the pulp had not been treated with drainage aid. Thus by applying drainage aid the process can be improved both at the pulp drainage ~00 0 0 06 a 0 0 on00 0* *0 O *0 0 0 ar 00 o o 0 0 Q0 0000 0 0 stage and the sheet formation stage but the total amount of polymer that is used is substantially unchanged and the final performance quality can be substantially unchanged.

The amount of drainage aid polymer is usually at least 0.005 or 0.01%, often at least 0.03 or 0.05%, but it is generally unnecessary for it to be more than 0.3% or, at the most, Amounts of 0.1 to 0.2% are often preferred. These percentages are based on the dry 10 weight of the pulp.

The sunthetic polymeric drainage aid can be a drainage-promoting, relatively low molecular weight polymer, for instance any of those discussed below as the polymer having lower molecular weight than the main 15 polymer, but is generally a relatively high molecular weight polymer for instance having a molecular weight conventional for dewatering aids and retention aids.

For instance the polymer typically is a substantially linear synthetic cationic polymer having molecular weight above 500,000, and preferably having intrinsic viscosity above 4dl/g. Thus it may be any of the polymers described in EP 0235893.

Intrinsic viscosities herein are derived in standard manner from determination of solution visccsities by 25 suspended level viscometer of solutions at 253C in 1 Molar NaCI buffered to pH about 7 using sodium phosphate.

Irrespective of whether or not the thick stock is made by dilution of a wet pulp that has been draitted in the presence of a drainage aid, it is preferred in the invention to incorporate the described low molecular weight weight soluble synthetic cationiic polymer before the main polymer.

It is preferred that the remainder of the process should be similar to the "Hydrocol" process and, thus, should be otherwise conducted as in EP 235893, using a T- synthetic cationic polymer having molecular weight at least 500,000 before one of the shear stages and bentonite after. The materials and processing conditions described in EP 235893 can be used in the invention, subject to the modification that the suspension includes the low molecular weight polymer before addition of the main polymer. Alternatively, and less preferably, the bentonite can be replaced by colloidal silicic acid or other suitable fine particulate o 1 0 material or the synthetic polymer can be replaced by cationic starch.

a000 moo< Sometimes lower amounts of the main polymer than are 0o o, recommended in EP235893 can give good results in the a0oooo present invention, for instance amounts of less than o 15 300g/t e.g. 50g/t (0.005%) to 250g/t, especially above 100g/t based on the dry weight of the stock.

The process can alternatively be similar to that S0 described in US4388150 with the addition of cationic o0°o starch into the suspension prior to the colloidal silicic Q 00 acid (which can be modified as W086/5826).

o The low molecular weight polymer can be present in the thick stock that is diluted to form the thin stock or it may be added to the thin stock. For instance 0,.0 generally the thick stock is diluted to form the thin 0 25 stock by use of white water. It is desirable to add the low molecular weight polymer before, or immediately after or during, the dilution with white water and to add the main polymer to the thin stock, after the addition of the low molecular weight polymer.

The low molecular weight polymer should have a molecular weight sufficiently lower than the molecular weight of the main polymer that it will provide different process or performance benefits. For instance this aspect of the invention does not include a process in which both the low molecular weight and high molecular 2 0 0 I 0 00 000 0 00 1 0 0 0 00 0 00 0 0 000 0o0 00 0 i 0 0" 0 0 o 00 1 00 00 ,i 0 0 0 00 B 0 0 00 weight polymers are primarily cationic retention aids.

Instead, it is restricted to processes in which the low molecular weight polymer does provide a different performance benefit. Generally the low molecular weight polymer has intrinsic viscosity below 2dl/g and usually has molecular weight below 500,000. The molecular weight is usually above 50,000 and often above 100,000.

A preferred relatively low molecular weight polymer is polyethylene imine. A suitable grade of this type of polymer is the material sold under the trade name Polymin SK. Other suitable materials are polymers and copolymers of diallyl dimethyl ammonium chloride, of dialkyl amino alkyl (meth) acrylates and of dialkylaminoalkyl (meth) acrylamides (both generally as 15 acid addition or quaternary ammonium salts), as well as polyamines and polydicyandiamides-formaldehyde polymers.

Amphoteric synthetic polymers may be used.

One preferred process according to the invention utilises a relatively crude stock containing significant amounts of pitch and/or having high cationic demand.

For instance it may require at least 0.1% Polymin SK to give improved retention when the Polymin SK is used in conventional manner as retention aid. Polymin is a trade mark. Such stocks are, for instance, those 25 containing more than 25% by weight, usually more than by weight, of mechanically derived pulps and/or deinked pulps. By mechanically derived pulps we mean groundwood, pressure refined groundwood, thermo-mechanical, chemi-thermo mechanical or any other high yield mechanically derived fibres.

In these instances, the low molecular weight polymer can be selected primarily to reduce cationic demand and/or avoid pitch problems and/or linting.

When using these relatively crude pulps, the process is of particular value when the stock is to be used for.

f- 7 the manufacture of newsprint, and for this purpose stock is generally substantially unfilled or only contains small amounts of filler, for instance 0 to 15% and often O to 10% based on the dry weight of the stock. Benefits are however also achieved if the stock contains filler in amounts to give up to 30% filler in the final paper produced.

The process is also of value in the manufacture of board, again often from similar crude pulps containing little or no filler. In these instances an alternative Sor additional property of the low molecular weight o.o polymer may be to improve the strength of the board and 00 ooo for this purpose a low molecular weight water soluble oo. synthetic cationic dry strength resin may be used as the Soo 15 polymer. Amphoteric polymers are particularly suitable f-r this purpose.

The amount of low molecular weight polymer is up to oo 0.5% generally in the range 0.01 or 0.05 to based o ~e on the dry weight of the stock, and the optimum can be 0 00 found by routine experimentation. Often the pulp, 0o 00 o o0 before treatment with the low molecular weight polymer, has a cationic demand (as measured by titration with the main cationic polymer) of above 400g/t and the low "ot' molecular weight polymer is included in the stock, or 00 o° 25 ahead of the stock, in an amount to reduce the cationic demand of the thin stock to below 300g/t before adding the main polymer.

The process of the invention is found to give an improvement in the performance since it can give improved pitch and/or stickies removal, improved paper quality such as opacity and linting characteristics improved wet strength or runnability during manufacture. Furthermore the performance of the process when assessed in terms of the drainage characteristics is improved by the incorporation of the second polymer, as compared to a ~YI_ ijl I_ I I 8 process without that polymer, for instance a process as described in EP235893 or US4388150.

In the following examples, Polymer A is a polymer of IV 7dl/g formed from 75% acrylamide and dimethylaminoethyl acrylate, MeC1 quaternised, and Polymer B is a modified polyethyleneimine as sold under the trade name Polymin SK.

Example 1 A 100% mixed waste stock having a consistency of o 10 0.5% was prepared. Drainage tests were conducted on the stock using a modified Shopper Riegler freeness tester, noi the time for 600mls of backwater to drain from the stock 00 so sample being measured. The stock was subjected to shear oe.-o and the drainage was measured. In one test no additions 0 0 o oo 15 were made before or after the shear. In other tests o 0 bentonite was added after the shear and polymer A and/or polymer B was added before the shear. When both 00 o' g polymers A and B were added, B was added considerably 0 00O ahead of polymer A.

0 00 The results are as follows.

0o o Table 1 oo o 00 0 0000 25 0 00 Polymer B Polymer A Bentonite Drainage 0 0 0 74 0 0.04% 0.2% 32 0.02% 0.04% 0.2% 18 0.04% 0.04% 0.2% 13 0.04% 0 0.2% 51 Example 2 A process similar to the preceding example was conducted using a stock having a high mechanical fibre content, and in particular being a 50:50 groundwood:bleached kraft pulp having a consistency of In addition to measuring the drainage time as in the previous example, a pitch count was made (in particles/ml by the Allen method) The following results were obtained.

Table 2 Poly ner B Polymer A Bentonite Drainage Pitch Percentage Count Pitch Reduction 0 O 0O 0 0 0 0 0 ac a0 00 O 0 0 80 5.8 x 10 6 0 0.025% 0.2% 49 1.7 x 106 0.025% 0.025% 0.2% 35 1.2 x 106 79% 0.05% 0.025% 0.2% 31 5.1 x 105 91% These examples clearly demonstrate the value of adding, for instance 0.01 to generally around 0.02 to 0.07%, polyethylene imine so as to reduce the amount of high molecular weight (for instance IV above 4) 20 cationic retention aid that is required for good drainage and retention and so as to counteract the effect of stock having high cationic demand and, especially, high pitch count.

Example 3 Newsprint is made using a stock based on 3% kraft, 17, magnefite, 38% thermomechanical pulp and 42% groundwocd, and to which 20% broke has been added. High molecular weight polymer is added, in some tests, just before the last shear stage and bentonite is added, in some tests, after the last shear stage. Low molecular weight polymer is added to the thin stock soon after it is diluted from the thick stock.

In these tests the low molecular weight polymer is polymer K which is a solution polymer of about IV I dl/g and formed from about 20% acrylamide and 80% by weight diallyl dimethyl ammonium chloride. The high molecular weight polymers are L, which is 70% acrylamide, methyl chloride quaternised dimethylaminoethyl acrylate IV 8, and polymer M which is 95% acrylamide and 5% methyl chloride quaternised dimethylaminoethyl acrylate IV 11.

The drainage rate for each of the treated suspensions is measured, with the best results being those that have the highest drainage figure. The results are as follows.

Table 3 Clio a 00 00 a O 0 00 00 C DOO 0 0 *r 00 00 00 00 *O 0 0 O 0 0 Qo 0P 0: 15 Polymer K High MW Bentonite Drainage Polymer 0 0 0 205 0.2% 0 0 195 0.2% 0 0.2% 300 0.2% 0.05%L 0.2% 335 0.2% 0.05%M 0.2% 340 0 0.05%M 0.2% 325 These results clearly demonstrate the benefit in the manufacture of newsprint from adding high molecular weight cationic polymer immediately before shear and bentonite after shear even when the high molecular weight 25 polymer only has a relatively low cationic charge, and they also show that a useful result can be obtained when the high molecular weight polymer is replaced by a lower molecular weight polymer having molecular weight above 500,000, but that best results are obtained using a combination of both.

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Claims

1. A process in which paper or paper board is made by forming an aqueous callulosic suspension, passing the suspension tchrough one or more shear stages selected from cleaning, mixing and pumping stages, adding a main polymer selected from cationic starch and high molecular weight water soluble cationic polymer having a molecular weight above 500,000 to the suspens ion bef ore one of the shear stages and adding inorganic material selected from bentorilte and colloidal silica after that, shear stage, draining the suspension to form a sheet and drying the sheet, characterised in that the process includes a preliminary polymer inclusion stage selected from (a) adding to the suspensioni, before the addition of the main polymer, a low molecular weight water soluble synthetic *0cationic polymer having molecular weight lower than the molecular weight of the main polymer and adding a water soluble, cationic, polymeric drainage aid to a cellulosic pulp and then draining the pulp and diluting the drained S 20 pulp to form the aqueous cellulosic suspension.

2. A process according to claim 1 in which the inorganic material is bentonite.

3. A process according to any preceding claim in which at least 25% by weight of the cellulosic suspension is formed from mechanically derived pulp and/or deinked pulp. 0,4. A process according to any preceding claim in which the product is newsprint or board. A process according to any preceding claim in which the main polymer is a synthetic polymer having intrinsic viscosity at least 4d1/g or is cationic starch and a low molecular weight water soluble synthetic cationic polymer 12 having lower molecular weight is incorporated in the suspension before the main polymer. A process according to claim- -4in which the low molecular weight polymer has intrinsic viscosity below 2dl/g. A process according to claim kin which the low molecular weight polymer has molecular weight 100,000 to 500,000. A process according to any of claims 6\to I\in which the low molecular weight polymer is selected from o polyethylene imine, polyamines, polycyandiamide a formaldehyde polymers, amphoteric polymers, and polymers of. monomers selected from diallyl dimethyl ammonium aoo chloruide, diallylarminoalkyl (meth) acrylates and o 15 dialkylaminoalkyl (meth) acrylamides. A process according to any of claims 4\to .9\in which the low molecular weight polymer is an amphoteric cationic dry strength resin and the product is board. A process according to any of claims \to in which the suspenr.on to which the low molecular weight o polymer is added has a cationic demand, as measured on the main cationic polymer, of at least 400g/t and the amount of low molecular weight polymer that is added reduces the said cationic demand to below 300g/t. SS 25 4.t.1. A process according to any of claims 4\to 10 in which the suspension that is drained to form the paper or paper board is a thin stock formed by dilution of a thick stock and the main polymer is added to the thin stock and the low molecular weight polymer is present in the thick stock. ?a3 ,A process according to claim in whI h the suspension that is drained to form the paper or paper board is a thin stock formed by dilution of a thick stock and the main polymer i added to the thin stock and the low molecular weight polymer is added to the thin stock T- Y 13 or to the thick stock in an amount of from 0.01 to based on the dry weight of suspension. -4I3,.A process according to any preceding claim in which the suspension that is drained to form the paper or paper board is made by diluting a drained pulp that has been made by draining a cellulosic pulp containing a pulp drainage aid and in which the drainage aid comprises a water soluble, cationic, synthetic, polymeric drainage aid having intrinsic viscosity above 4dl/g. 3 00 1 0 Soo 020 O0 rX 14 1S.WkN. A paper or paper board making process substantially as hereinbefore described with reference to the Examples. :b CA COIL~ m oucTptrUILs disclosed herein or referred to or L atedi the spenCification and/or ci Ia-m of this application, individually o ectively, and any and all combinations of -a -wao r mrs nf lq;iA~ nq-Pp r fei-iires 0 0c 0 0 DATED this TWENTY EIGHTH day of MARCH 1989 Allied Colloids Limited by DAVIES COLLISON Patent Attorneys for the applicant(s)