Paper making and fiber liberation – Processes and products – Non-fiber additive
Reexamination Certificate
2002-04-30
2004-04-06
Griffin, Steven P. (Department: 1731)
Paper making and fiber liberation
Processes and products
Non-fiber additive
C162S149000, C162S185000
Reexamination Certificate
active
06716313
ABSTRACT:
TECHNICAL FIELD
The present invention concerns an additive for paper making, which is added to the fiber pulp prior to the web formation step in a paper making process. By means of the additive it is possible to impart to the paper i.a. a reduced tendency for dusting. In addition, the additive has been shown to facilitate water removal in the web formation stage, to improve filler retention, and to affect advantageously the removal of harmful substances, which have accumulated in the water circulation system of the paper machine. The additive also increases the strength of the finished paper, both dry strength and wet strength. By using the additive for paper making according to the invention improvements have been seen also in the printability of the paper, i.a. as regards its applicability for ink-jet printing. The term paper as used in this application also includes the term paperboard.
BACKGROUND OF INVENTION
A problem that is encountered in finished paper is its high tendency for dust formation, the reason for which are fiber particles and filler particles released from the paper surface. The dust gives rise to problems already at the drying stage in paper making, but above all in the machines and equipments handling paper, such as in printing equipment. The printing methods as such are developed which means high machine speeds and long printing series. High speeds aggravate dust formation, and long printing series reduce standing times, during which it would be possible to carry out a cleaning of the equipments.
In order to solve the dusting problem it is known to use methods, which rule are based on chemical compounds to be added to the fiber pulp, prior to the paper web formation. The use of mineral and micro waxes, of sizing agents, such as AKD and ASA dispersions, of wet strength resins and of pulp sizing starch is known. Irrespective of these known measures, paper dusting is still a significant problem.
Low strength between long fibres, short fibres and fines and fillers give rise to increased dust formation. The number of contact points between fibres, fines, fillers and dry strength aid e.g. wet end starch impact on strength properties. A large number of the contact points, into which starch or other dry strength aid is adsorbed in between, leads to good strength properties. In cases where the quantity of short fibres, fines and fillers is high and the amount of long fibres is thus correspondingly low, conventional non-degraded cationic starches do not increase strength in a satisfactory way. One possible explanation is that the molecular weight of starch is too big to reach in a sufficient quantity to the contact points or the quantity of the molecules is just too little and the result is thus poor strength.
Fiber lengths of fibrous material, which is used on paper making are typically between 0.05-4 mm. The fractionation of fibrous material can be done by several means e.g. by Bauer-McNett or by Clark classifier. The classification of fibres in pulp is described e.g. in Tappi Test Method T 233 cm-95. The term long fibres mean in this application those fibres with the fiber length 1.68 mm or greater. Fibres longer than 1.68 mm mean those fibres, which retain on Tyler screen 10 according to Tappi Test Method T 233 cm-95, in the case that the length of the fibres can't be determined otherwise. The term fibres means in this application long fibres, short fibres and fine material, which is based on fibrous material, Fillers are thus excluded in the term fibres.
SUMMARY OF INVENTION
Now it has surprisingly been discovered that i.a. the dusting of paper can be reduced significantly by means of the additive according to the invention to be added to the fiber pulp prior to web formation. The said additive functions well, when it is used in the pulp, in which the long fiber content is 60% or below calculated from the total fiber content, more preferably if the long fiber content is 50% or below and most preferably if the long fiber content is 45% or below.
The additive is based on starch, which has been modified to be applicable in the invention by reducing its molecular size and reacted with an appropriate nitrogen compound in order to provide a suitable cationic charge level to the starch.
BEST AND VARIOUS MODES FOR CARRYING OUT INVENTION
The reduction of the molecular size has been carried out advantageously by oxidizing, such as by peroxide oxidation. But also other oxidants such as hypochlorites and persulfates can be used as well as degradation method. Also other commonly known degradation methods e.g. degradation by acids can be used as a degradation method. The reduction of the molecular size is appropriately carried out so that the viscosity of a 5% starch suspension at 60° C. is in the range 10-500 mPas (Brookfield). The viscosity is advantageously 40-300 mPas, and especially advantageously in the range 100-200 mPas. Oxidation to viscosity level of 10-500 mPas can be achieved for example using a hydrogen peroxide dose of 0.02-2% from the starch dry matter in slightly alkaline reaction conditions. The desired degree of degradation is also bound to the desired cationic charge of the end product, since an increase in the cationic charge decreases the viscosity of the end product. There is also interdependence between the molecular size and the cationic charge which affects the behaviour of the starch in the paper machine i.e. the retention of highly degraded molecules is improved by increased cationic charge level of the molecules.
Starch which has been processed to have the desired viscosity level is thereafter processed with a quaternary nitrogen compound according to the present invention so that its cationic charge level will be in the range <1.5 meq/g (mq/g means in this application milliequivalent of charges per gramme of dry, nonaqueous polymer), preferably in the range 0.36-1.46 meq/g, advantageously 0.72-1.46 meq/g and especially advantageously in the range 0.72-1.10 meq/g, whereby the nitrogen contents when using the quaternary cationizing chemical, will be correspondingly in the range 0.50-2.04%, 1.01-2.04% and 1.01-1.54%. The product is advantageously prepared using solution cationization, in which the starch is fed into the cationization process in granular form, the process conditions are chosen so that the starch dissolves completely during the process. Essential process quantities in this respect are the concentration of the starch to be cationized, suitable alkalinity and increased temperature. The alkali dose (NaOH) is suitably in the range of approximately 1.5-3% of the starch dry matter, and the temperature suitably in the range of approximately 60-80° C. The dry matter content of the reaction mixture should advantageously be over 50%, which gives i.a. a good yield for the end product. A suitable quaternary cationizing chemical is 2,3-epoxypropyltrimethylammonium chloride, which should be used in an amount of approxixmately 10-40% of the amount of starch.
The spirit of the invention also comprises the use of other suitable cationization methods e.g. dry cationization method, in which the moisture content is typically below 30% and in which starch remains powder like. Also cationization can be alternatively done prior to the oxidation step.
The applicability of the invention is illustrated with the following examples, in which i.a. paper properties, which have an effect on the dusting of the paper in different paper handling conditions, have been monitored. Measuring the dusting tendency from a paper is as such problematic without a prolonged run of the paper in an application process, such as a printing operation. It is, however, generally known that the tendency for dust formation correlates to strength parameters which can be measured from the paper, such as Dennison, IGT and Scott Bond.
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patent: 3770472 (1973-11-01), Jarowenko
patent: 3875054 (1975-04-01), Hunt et al.
patent: 4122253 (1978-10-01), Watts et al.
patent: 4146515 (1979-03-01), Buikema et al.
patent: 4373099 (1983-02-01), Hubbard et al.
patent: 5858174 (1999-
Luukkonen Kari
Niinivaara Veikko
Vihervaara Tapio
Connolly Bove & Lodge & Hutz LLP
Griffin Steven P.
Hug Eric
Raisio Chemicals Ltd.
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