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Evaporators & Dryers

We are leaders in the market for providing best range of Evaporators/Vapour Cells and RISING FILM EVAPORATORS

Evaporators/Vapour Cells

We have successfully Supplied, Erected, And commissioned about 75 Nos. of various type of Rising film evaporator (Semi Kestner), Falling film evaporator & Robert type evaporators (Vapour cell) in India.

We offer following types of evaporators:
  1. Robert Type Evaporator (with central down take OR multi down take)
  2. Rising Film Evaporator ( Semi Kestner ),
  3. Falling Film Evaporator
Robert type Evaporator body with multi down take:

The juice coming out from clarifier is known as clear juice & This juice is concentrated for the formation of crystal sugar in the form of syrup and for this set of evaporator is used. The biggest evaporator of 6000M have supplied by us to M/s Krishna S.S.K. Ltd. Rethare Bk. In year 1993-94.

Design feature:
  1. Less tube height & less vapour pressure
  2. Multi down take for bigger diameter of Calendria for large capacity
  3. Better condensate removal
  4. Better steam economy & distribution
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RISING FILM EVAPORATORS

We offer semi Kestner of tube length 4 Mtrs. To 6 Mtrs. we have handled Design, Manufacturing, erection & commissioning of largest Semi Kestner of capacity 5500 M H.S. to well known sugar industry in India. ( i.e. The Ugar Sugar Works Ltd. in year 2014 15 )

Advantages:
  1. Less space required due to long tube length
  2. Capacity increases by 15 20% Higher heat transfer & High velocity Of Juice
  3. Cost Reduction.
  4. Less inversion losses because of less Retention time of juice at high Temperature.
  5. High bricks of syrup.
  6. Less steam quantity is required and Gives high vapour pressure, hence Vapour can bleed to pan, juice Heaters & Evaporator set
Design Features:

Calendria can be designed with min. 4.0 Mtrs. Long tubes up to 6.0 Mtrs. Long tube as per clients requirement & availability of exhaust back pressure of power house turbine. Calendria is designed by keeping sufficient annular space & to give the tangential steam entry of exhaust and non condensate gasses are taken out from centre as well as peripheral vents. Umbrella above top tube plate is given to avoid carry over juice particles through vapour. Polly- baffle catcher also provided to avoid juice entrainment.

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