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Saiccor - The First 50 Years 5.8 MB - Sappi

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<strong>The</strong> <strong>First</strong> Fifty <strong>Years</strong><br />

Design work for chlorine dioxide bleaching (including No 8 filter)<br />

started in November 1962, orders were placed from December 1962,<br />

plant erection started in May 1963 and the plant was commissioned<br />

in December 1963� No 1 filter in bleaching was replaced with a Kamyr<br />

M57 unit almost twice the size in May 1965, after first installing a<br />

temporary filter to enable No 1 to be taken out� In November 1965<br />

No 4A filter was commissioned, which effectively doubled the<br />

washing capacity after the chlorine dioxide stage�<br />

A second Rauma pressure washer was ordered in June 1964 and<br />

commissioned in August 1965� In December 1964 a fourth thickener<br />

was ordered for second screening, which was started up in June 1965�<br />

With all the new plant and equipment being installed, power<br />

consumption increased significantly, making it prudent to increase<br />

<strong>Saiccor</strong>’s power generation capacity� <strong>The</strong> foundations for No 3<br />

turbogenerator started in April 1964� This was a 6,5 MW Allen<br />

machine that doubled the total generating capacity� <strong>The</strong> machine<br />

was started in March 1965�<br />

Sheet pulp quality did not change over the period 1960-1965�<br />

Blockage constants (KWs) averaged around 15, although often ranging<br />

above the Courtaulds limit of 20� Calciums were high, with monthly<br />

averages from 4<strong>50</strong> to 6<strong>50</strong> ppm summer to winter, while silicas<br />

averaged around <strong>50</strong> ppm� Until flock pulp went through second<br />

screening (June 1962) KW values averaged 30 and silica 270 ppm�<br />

After June 1962 these values dropped to 19 and 60 respectively�<br />

Courtaulds were not entirely happy with <strong>Saiccor</strong>’s pulp quality,<br />

particularly the high calcium levels� Fred Aldred, John More, and<br />

Malcolm Simpson from Courtaulds paid a number of visits to <strong>Saiccor</strong><br />

to investigate what could be done to improve calciums, but nothing<br />

proved successful� Copper numbers (about 1,6) and resin (about 0,35<br />

per cent) were considerably higher than today’s levels of about 1,2<br />

and 0,1 per cent�<br />

Various timbers were tried� Wattle was first used in 1957, but the<br />

KW was 100� Wattle usage continued over the years up to 20 per cent<br />

of the furnish, but its pulp had high KW values until it was cooked<br />

separately in high pressure digesters (from 1970), then the percentage<br />

wattle was increased reaching a peak of 40 per cent in the late 1970s�<br />

<strong>The</strong> first trial using pine was done in November 1959, and was<br />

successful� For a period in 1962 pine was blended up to 5 per cent<br />

with saligna, producing satisfactory pulp� Casuarina was tried but<br />

proved unsuitable�<br />

<strong>The</strong> first 2 <strong>50</strong>0 t of high alpha pulp for the American market<br />

(Mobile) was made in November 1961� A second lot was made in<br />

January 1962� Mobile received 94 alpha for a few years but then it<br />

was decided 94 alpha was not an economic proposition for Courtaulds<br />

and <strong>Saiccor</strong> combined� A further 94 alpha trial was conducted in the<br />

late 1970s, but was only made commercially from 1996�<br />

48

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