Edible Oil PROCESSING

Absorption solutions offer opportunities for energy savings and sustainability in process cooling in the edible oil refining industry

EDIBLE OIL

Edible oil undergoes intensive refining phases before the final product is synthesized. The line includes cleaning of the seeds, preheating, flaking, conditioning, pre-pressing, solvent extraction, and storage. Modern extraction utilities yield 95% of oil with majority of the solvent recovered as well.

Edible oil undergoes intensive refining phases before the final product is synthesized. The line includes cleaning of the seeds, preheating, flaking, conditioning, pre-pressing, solvent extraction, and storage. Modern extraction utilities yield 95% of oil with majority of the solvent recovered as well.

SOLVENT EXTRACTION

Solvent extraction is the process of separating the residual oil from oil seeds. The process begins with grinding the seed, followed by purging the seed cake with hexane. The process results in releasing the oil in the seed. The solvent is then “flashed off” by heating the oil in a sealed chamber. The oil/solvent blend is next heated to 100º C, the vapour of which is passed through a condenser. The condenser in the solvent removal unit requires chilled water at a temperature lesser than the cooling water from the cooling tower.

Absorption chillers utilise steam from one of the plant’s utilities and offer chilled water at the desired temperature for the condensers. The condensate (water) from the chiller is used to cool the oil cakes, which serves as animal food.

BENEFITS
  • Uses low-grade heat from the plant saving significant operational costs.
  • Can be operated at designed COP
  • Low payback period
  • Low maintenance cost
  • No emissions of ozone-depleting CFS

To know more about the application and benefits of our solutions, contact our experts now

OUR OFFERINGS

SINGLE EFFECT STEAM DRIVEN VAPOUR ABSORPTION CHILLER

Heat Source: Steam 
Pressure:  0 bar.g – 3.5 bar.g  
COP: 0.8
Capacity: 100 – 3500 TR

Heat energy available in the form of (LP- low pressure)

  • LP vapour (0.1 bar.g, 103OC) coming from continuous polymerisation process in textile industry
  • LP steam generated from potato fryer, instant noodle plant etc.
  • LP Steam extraction from steam turbine in power plants
  • Flash steam recovery

DOUBLE EFFECT STEAM FIRED VAPOUR ABSORPTION CHILLER

Heat Source: Steam 
Pressure:  3 bar.g – 10.5 bar.g 
COP: 1.5
Capacity: 50 – 3500 TR
Heat energy available in the form of

  • Steam from boiler
  • Steam from processes
  • Steam from cogeneration plants
  • Extraction from steam turbine

DOUBLE EFFECT STEAM FIRED VAPOUR ABSORPTION CHILLER

Heat Source: Steam 
Pressure:  3 bar.g – 10.5 bar.g 
COP: 1.5
Capacity: 50 – 3500 TR
Heat energy available in the form of

  • Steam from boiler
  • Steam from processes
  • Steam from cogeneration plants
  • Extraction from steam turbine

REFERENCES

Ghana Speciality Fats Industries Ltd
Edible Oil
Location: Ghana
Type: Double effect steam fired absorption chiller
Capacity: 300 TR

Asia Pacific Oil Manufacturing Corp
Edible Oil
Location: Philippines
Type: Double effect steam fired absorption chiller
Capacity: 40 TR

Mgm Edible Oils Pvt Ltd
Edible Oil
Location: Philippines
Type: Double effect steam fired absorption chiller
Capacity: 400 TR

Emami Agrotech Limited
Edible Oil
Location: India
Type: Double effect steam fired absorption chiller
Capacity: 450 TR

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