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Home Group One - Starch Dewatering
We found that each 100 tons of potatoes processed produced approximately 2-3 tons of starch, and a cake of 60% dry solids could be recovered, with a value around $180. This proved to be a significant advance in comparison with the traditional system, which involved hydro cyclones and trucking away the slurry at 25 - 30 % dry solids. The reduction in process area and transport costs is also a factor, which must be attractive. Whether or not the purchaser of the starch re-slurries the material for further treatment is irrelevant, but it is important to move the starch within a few days of production especially in hot weather (alternatively cold storage) to prevent deterioration of the product. As a result of the success of these first machines, we approached the French-fry manufacturers.
Wear Characteristics: No signs of wear to the bowl or screw conveyor Process Problems: Gelatinized starch produced by the blanching process or by steam peeling, caused us some concern. During trials carried out at one customer factory, we identified two products discharging from the centrifuge solids outlet.
We exhausted all possible machine design changes and still we were seeing two different products. However, our client modified the potato fiber screen and the gelatinized starch was removed before it reached the decanter. Conclusion: The Centriquip centrifuge is admirably suited for starch dewatering. Where some manufacturers accept the starch as part of the effluent, there are several incentives to remove the starch before wastewater treatment.
Group Two - Effluent Treatment
The centrifuge was installed to replace the thickener and cakes of up to 40 % were easily achieved without flocculent addition. The product was saleable to farmers as an animal feed additive. Suspended solids in the water discharged to the city was reduced from 1200 ppm to less than 300 ppm. When steam peeling is used instead of abrasive peelers, gelatinized starch affects the cake and the dry solids content will not be as high. Nevertheless the resultant cake at 20 - 25 % is still stackable and a saleable product.
Conclusion: The low speed decanter centrifuge is ideally suited for effluent derived from the potato process. Clients who have used belt presses have complained of high maintenance costs in comparison with our centrifuges. It is to be noted that one case our centrifuge has replaced
a rotary vacuum filter for similar reasons. Group Three - Potato Meal Potato peel, reject potatoes, and substandard products can be pulverized into slurry. At this point water is added and the slurry can be centrifuged to produce a cake of approximately 40 % dry solids. This commands a higher price than the waste in its original form. The proportion of cooked potato in the feed largely influences the dryness of the cake. Group Four- Potato Wash Water Cleaning Use of the decanter centrifuge on a closed loop to the potato pre-washer or potato flume/transport water leads to the continuous removal of earth, mud, soil, potato debris etc. from the washing water. The solids are discharged as a stackable cake at up to 50% ds. The cleaned liquid discharge is returned to the washer for reuse thus reducing the amount of water used at plant and allowing the washer to be run for extended periods before emptying. The addition of a flocculent is not normally required but may be used to improve the superfine capture if needed, and achieve a centrate of < 100 ppm suspended solids. Wear Characteristics: In order to minimize wear, the bowl speed is kept low. The welded wear protection on the conveyors operates for 15,000 to 20,000 hours before attention. Tiled conveyors can be used to extend conveyor run times. No significant wear is found on any of the other parts. Potato Processing Industry Reference List of Installations
![]() Centrifuged Potato Starch at 62% DS ![]() Cake and Centrate Produced by Centrifuging Potato Effluent ![]() 500 ppm DS |
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US Centrifuge · 4011
Championship Drive · Indianapolis, Indiana |
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