Corn starch production plant
International Starch has a process for the extraction and refining of starch even from corn flour or mill by-products.
A proper steeping is essential for high yields and high starch quality. The steeping is carried out in a continuous counter-current process. The cleaned corn is filled into a battery of large steeping tanks (steeps), where the corn is soaked in hot water 30 to 48 hours to begin breaking the starch and protein bonds . The gluten bonds within the corn begin to loosen and release the starch. The steeping is actually a controlled fermentation. Sulphur dioxide improves the fermentation by enhancing growth of favourable micro-organisms, preferably lactobacillus, while suppressing detrimental bacteria, moulds, fungi and yeast. Solubles are extracted and the kernel softens. The kernel swells to more than double size and increases its moisture content from about 15% to 45%.
The steepwater containing approximately 10% dry substance is drained from the kernels and condensed on a multi-stage evaporator. Most organic acids formed during the fermentation are volatile and evaporate with the water. The condensate from the first evaporator stage will therefore be discharged after the heat is recovered by preheating the entering steepwater.
The steepwater is condensed to an auto-sterile product - a valuable nutrient in the fermentation industry - or concentrated to approximate 48% dry matter and mixed and dried with the fibre fraction.
The sulphur dioxide may be prepared by burning sulphur and absorbing the gas in water. Because modern processes call for more strict and narrow dosage, a supply of sulphur dioxide gas under pressure is preferred or SO2 is replaced by sodium hydrogen bisulphite where no local gas supply is available.
The soften kernels are broken up in attrition mills to loosen the hull and break the bonds between germ and endosperm. Water is added to assist the wet milling. A good steeping ensures that the germ will be freely released intact from the kernel by a gentle milling operation with no free oil.
Oil constitutes half the weight of the germ at this stage, and the germ is easy to separate by centrifugal force. The lightweight germs are separated from the ground slurry by hydrocyclones in a two step separation with regrinding in between.
The germs are washed repeatedly counter-currently on a three-stage screen to remove starch. Process wash water is added at the last stage.
Surface water is removed from the germs by a tapered screw press. The dewatered and clean germs are fed to a rotary steam tube bundle dryer and dried to approximate 4% moisture. Low moisture content improves shelf life. The germs are cooled and pneumatically transported to a germ silo ready for bagging or oil extraction.
Mechanical presses and/or solvent extraction are used to extract the crude oil from the germ. The crude oil is refined and filtered. A typical yield per ton corn is 27 kg corn oil. During refining free fatty acids and phospholipids are removed. The finished corn oil finds uses as food and cooking oil or as raw material for margarine. Refined corn oil has a pleasant taste and does not develop off-flavours in cooking and frying. The high content of polyunsaturated fats is a nutritional advantage.
The residual extracted corn germ meal is used in animal feeds or combined with the gluten feed.
FINE GRINDING AND SCREENING
After germ separation the mill flow is finely ground in impact or attrition mills to release starch and gluten from the endosperm cell walls (fibres).
The degerminated mill starch leaving the fine mill is pumped to the first stage of a fibre washing system, where starch and gluten is screened off. The overs, hull and larger fibres, are washed free from adhering starch and gluten (insoluble protein) on screens in counter-current with process wash water added at the last stage. The last fibre washing stage has a slightly courser screen for re-dewatering the fibre prior to a tapered screw press.
The dewatered fibres from the dewatering press may be mixed with concentrated steepwater and cakes from the oil press and dried to approximate 12% moisture. The dried fibre are pelletized to reduce bulkiness and pneumatically transported to a silo ready for shipping.
The fibre fraction is a valuable constituent of animal feeds.
img/HPHC240.jpg (4903 bytes) New High Pressure Hydrocyclone Technology (HP HC) is efficently applied in primary separation. Crude starch milk from the dewatering screen ahead of the fine mill and from the first stage fibre washing are combined. The crude starch milk contains starch, gluten and solubles.
A primary HP HC separator splits by centrifugal force the mill stream in two fractions:
• Gluten Overflow
• Starch Underflow
A mill stream thickener may be applied on the separator feed.
The gluten fraction from the primary separator is traditionally concentrated on a nozzle type continuous centrifugal separator - a gluten thickener.
The gluten separator splits the gluten fraction in two streams:
• Process water Overflow
• Gluten Underflow
Multi-Stage Hydrocyclone Unit.
The underflow, which is mainly protein and a small amount of starch, is discharged to the gluten dewatering section.
GLUTEN DEWATERING AND DRYING
The gluten slurry is dewatered on a vacuum belt filter or decanter. The decanter removes more water, but require strict pH-adjustment to the iso-electrical point of the gluten.
Dewatering splits the gluten stream in:
• Process water
• Gluten (moist)
The dewatered gluten is dried in a rotary steam tube bundle dryer to approximately 10% moisture and disintegrated in a hammer mill. Drying is facilitated by powder recycling.
The dried gluten is sold as corn gluten meal with 60% protein. It is a valuable source of methionine. The high xanthophyll content - typically 500 ppm - makes it an efficient pigmenting ingredient in poultry feeds.
Washing with fresh clean water refines the crude starch milk. With hydrocyclones it is feasible to reduce fibre and solubles including soluble protein to low levels with a minimum of fresh water. To save water the wash is done counter currently, i.e. the incoming fresh water is used on the very last step and the overflow is reused for dilution on the previous step, and so on.
By using multi stage hydrocyclones all soluble materials and fine cell residues are removed in a water saving process. The refined starch milk contains an almost 100% pure starch slurred in pure water.
With a middling separator the overflow from the starch refining hydrocyclones may be refined into:
• Process water Overflow
• Starch Underflow
In the strong gravitational fields of a hydrocyclones and a centrifuge, the starch settles quickly. Refining is based on the differences in weight density between water, fibres and starch:
Although some impurities go with the starch in the underflow, there is - by means of a sieve - a last chance to remove the larger particles. Impurities not removed this way are not removable by any known technique.
CENTRIFUGES AND HYDROCYCLONES.
The centrifuge obtains its gravitational force by spinning the bowl. The hydrocyclone has no moving parts and the separation is totally dependent on the pressure difference over the cyclone.
The technological development and quality demands have forced centrifuges to give way for hydrocyclones in corn starch refining, but centrifuges still hold a defensive position in gluten concentration.
Starch is among the most pure of all agricultural products. Actually, purity is the most important parameter in being competitive.
The purified starch milk is discharged to a peeler centrifuge for dewatering. The peeler filtrate is recycled to starch refining. The dewatered starch is batch-wise peeled of and discharged by gravity to the moist starch hopper.
From the moist starch hopper the starch is fed by a metering screw conveyor into a flash dryer and dried in hot air. The inlet air temperature is moderate. The dried starch is pneumatically transported to a starch silo ready for screening and bagging. The moisture of cornstarch after drying is normally 12-13 %.