Hydrophobic sizing refers to the making of paper or board more or less water repellant. This property may be measu¬ red e.g. by the so-called Cobb test, in which the penetration of water into paper or board is measured as a function of time. The result is indicated as an absorp¬ tion g/m ² . In a properly hydrophobically sized product, the value is generally < 25 g/m ² , whereas in a product, which has not been treated with sizing agents increasing the hydrophobicity, the value may be > 100 g/m ² .

Conventional compounds used as a hydrophobic sizing agent include wood-based resin acids and their derivatives.

Nowadays, the paper and board industry has increasingly transferred to using for hydrophobic sizing so-called neutral sizing agents, which generally are compounds based on alkyl-ketene-dimer (AKD) or alkenyl-succinic- acid-anhydride (ASA) .

Hydrophobic sizing agents are generally delivered to the paper and board mills as a water dispersion, in which the share of the active agent (AKD, ASA, resin) of the prod¬ uct is within the range of 5-50%. When a sizing agent of the ASA type is concerned, the sizing agent dispersion is primarily prepared at a paper or board mill.

Hydrophobic sizing agents are added to a pulp at the pa¬ per or board machine at the starting step of the manufac¬ turing process. In certain cases, these sizing agents may be added also at a later step of the manufacturing pro¬ cess, e.g. at the size press. The quantities of the hydrophobic sizing agents to be used generally amount to 0.05-2.0% of the dry weight of the paper or board.

In addition to the active agent (AKD, ASA or wood resin) ,

a hydrophobic sizing agent dispersion contains stabil¬ izers, surfactants and other additional chemicals. As a stabilizer e.g. cationic starch, cationic polyethylene i ines, cationic polyacryl amides, gelatin or casein are used.

As surfactants e.g. sodium lignosulphonate or alkyl sul- phonates are used.

Typical additional chemicals include biocides, alum and pH adjusting chemicals.

A conventional way of preparing a hydrophobic sizing agent dispersion from these components is to prepare, by mixing and heating in a reactor, a homogenous premixture containing in a suitable ratio water, an active agent, a stabilizer, surfactants and other potential additional chemicals.

After obtaining the homogenous premixture, it is circu¬ lated via a high-pressure homogenizer, a colloid mill or a high-revolution centrifugal pump generally several times, until a sufficiently small particle size has been obtained (generally 0.1 - 10 μm) . The pressure varies within the range of 50 - 500 bar and the temperature within 50 - 100°C. The dispersion obtained is thereafter run via a heat exchanger into a product container. In the heat exchanger, the temperature of the dispersion is decreased to < 30°C.

Surprisingly, it has now been found that a high-pressure digester, a steam jet digester, primarily designed for cooking starch acts as an extremely good dispersing de¬ vice in the preparation of a hydrophobic sizing agent dispersion.

The invention will be explained more detailed with refer-

ence to the enclosed drawing. A steam jet digester pro¬ cess acts as follows:

A premixture is prepared in a reactor 1 according to the same principle as in the afore-mentioned conventional process. After this, the mixture is pumped into a digest¬ er portion 2 itself, wherein the mixture contacts a high- pressure steam flow 3 and the temperature and the pres¬ sure increase (the pressure generally to 2 - 15 bar and the temperature to 100 - 200°C) . The dispersion formed is thereafter run into a tubular reactor 4, after which the pressure and the temperature are decreased in an expander device 5 and the excess of steam may be separated by means of a steam condenser 6. The homogenous product formed is then run via a heat exchanger into a product container.

This process deviates from a conventional process as fol¬ lows:

Conventional process:

Pressure 50 - 500 bar Temperature 50 - 100°C

Steam jet digester process

Pressure 2 - 15 bar Temperature 100 - 200°C

The preparation of a hydrophobic sizing agent dispersion in a process of a steam jet digester type makes it poss¬ ible to use high solids contents during the processing, and since the delay in the digester and reactor tubes is extremely short, usually < 2 minutes, this makes it poss¬ ible to use very small units having a large production capacity.

Example 1

In a laboratory scale a stearine/palmitine alkyl ketene dimer (AKD) premixture was prepared having the following composition:

water 800 g

AKD 200 g

Orotan SN* 3.0 g Raisamyl 150E** 22 g

* Naphthalene formaldehyde sulphonate condensate, sodium salt

** Cationic potato starch (DS = 0.05). The starch was cooked before adding.

This premixture was divided into two portions, one of which was run 3 times through the laboratory high-pres¬ sure homogenizer (Rannie) . The pressure was 200 bar, the temperature 70°C. The other portion was run once through a laboratory-scale steam-jet digester, the temperature being 120°C and the pressure 3 bar. Both emulsions were diluted into a solids content of 12,5% and cooled into room temperature.

The following characteristics were measured from each of the dispersions: viscosity (Brookfield) and average particle size.

High-pressure homocrenizer/Steam-iet digester

Viscosity 10 cP 8 cP

Average particle size 0.56 μm 0.60 μ

The results show that the dispersions are by their char¬ acteristics nearly identical.

The dispersions were kept at room temperature for one month, and the same measurements were performed again, whereby the result was as follows:

High-pressure homogenizer/Steam-jet digester

Viscosity 15 cP 16 cP

Average particle size 0.86 μm 0.95 μm

The results show that the storage stabilities of the two dispersions are of the same order.

Example 2

In a laboratory scale an alkenyl succinic-acid anhydride* (ASA) premixture was prepared having the following compo¬ sition:

* As an alkenyl succinic-acid anhydride anhydrides de¬ rived from straight-chain C ₁₃ - C ₂₀ α-olefines were used.

This premixture was divided into two portions as well, one of which was run through a high-pressure homogenizer (pressure 200 bar, temperature 50°C) and the other por¬ tion was run through a steam-jet digester, the tempera¬ ture being 110°C and the pressure 1.5 bar.

The dispersions produced were diluted into a solids con¬ tent of 7.5%, and their viscosity and average particle size were measured.

High-pressure homogenizer/Steam-iet digester

Viscosity 600 cP 520 cP

Average particle size 0.50 μm 0.65 μm

The results show that the dispersions are nearly ident¬ ical.

A value < 1 μm is regarded as a generally accepted par¬ ticle size in products of this type.