Removal of insolubles from aqueous streams used in food processing
A food processing system includes at least one receptacle containing a composition of water and insoluble solids, a centripetal force-based solid/liquid separator having an inlet, a solids outlet, and a liquid outlet, and a pump able to direct the composition from the receptacle to the inlet of the separator. The separator is configured to separate the composition into a solids stream including the insoluble solids and a liquid stream including water and to direct the solids stream through the solids outlet and the liquid stream through the liquid outlet.
1. A method of scalding poultry workpieces, comprising
immersing the workpieces in a first scalder tank containing water, wherein, during the immersing step, insoluble solids are dislodged from the workpieces and deposited in the scalder tank to create an aqueous composition comprising the water, the insoluble solids and insoluble liquids;
using a centrifugal pump to direct the aqueous composition from the first scalder tank to an inlet of a centripetal force-based solid/liquid separator at a sufficient pressure and velocity to induce centrifugal separation of heavier-than-water insoluble solids from the aqueous composition in the separator;
using the separator to separate the heavier-than-water insoluble solids from the aqueous composition to create a solids stream comprising the heavier-than-water insoluble solids and a liquid stream comprising the water, the insoluble liquids and lighter-than-water insoluble solids, wherein the solids stream is directed through a solids outlet of the separator and the liquid stream is directed through a liquid outlet of the separator to a liquid/liquid decanter;
using the liquid/liquid decanter to separate the insoluble liquids and the lighter-than-water insoluble solids from the water; and
returning the water from the liquid/liquid decanter to the first scalder tank.
2. The method of claim 1 , further comprising:
immersing the workpieces in a second scalder tank; and
overfilling the second scalder tank with fresh water such that it overflows into the first scalder tank.
3. The method of claim 1 , wherein the water in the scalder tank is heated to a temperature of from 100 to 150° F.
4. The method of claim 1 , wherein the water in the scalder tank is heated to a temperature of from 110 to 140° F.
5. The method of claim 1 , wherein the water in the scalder tank is heated to a temperature of from 125 to 135° F.
6. The method of claim 1 , wherein the centrifugal pump directs the water and insoluble solids from the scalder to the separator at a velocity of from 50 to 100 gallons per minute and at a pressure of from 25 to 50 psig.