Production of soda ash

  1. Workshop production of soda ash.
  2. Calcination and heavy soda furnaces.
  3. Unique to the domestic chemical industry complex project of heat recovery system implementation on all installed furnace units.
  4. Year of realization: 2012. - 2016
  5. Scope of supply: the heat exchanger Manufacturing, delivery, installation and commissioning.
  6. Result: Under these operating parameters in specification were achieved.
  7. Payback Period: Confirmed.

Performance parameters:Heat transfer areaHeated air
Flue gas inlet, С°4500
Flue gas outlet, С°по факту300
Volumetric size, Nm3/h12 1008 000
The pressure loss in the heat exchanger channels, mmWg111
Heat power, kWt7 364
Recuperation degree, %63,0



Production of catalysts.

  1. Calcination spherical alumina catalyst in the reactor.
  2. The baking furnace.
  3. The heat recovery system implementation project.
  4. Year of realization: 2013.
  5. Scope of supply: the heat exchanger Manufacturing, delivery, installation and commissioning.
  6. Result: Under these operating parameters in specification were achieved.
  7. Payback Period: Confirmed.

Performance parameters:Heat transfer areaHeated air
Flue gas inlet, С°90020
Flue gas outlet, С°458520
Volumetric size, Nm3/h2 5001 600
The pressure loss in the heat exchanger channels, mmWg10120

Manufacturing of synthetic rubber.

  1. Synthetic Rubber Plant.
  2. The dryer.
  3. The investment project on modernization of / implementation of heat recovery systems for use of heat removed from the dryers.
  4. at the present time - the stage of implementation.

Performance parameters:Heat transfer areaHeated air
Flue gas inlet, С°7816
Flue gas outlet, С°5860
Volumetric size, Nm3/h13 6006 500
The pressure loss in the heat exchanger channels, mmWg19107
Heat power, kWt102
Recuperation degree, %71,1

Sulfuric acid production

  1. Sulfuric acid redistribution of the chemical plant.
  2. The intermediate absorption.
  3. Replacement project of the failed tube type heat exchanger for cooling the sulfur dioxide in the ribbed plate-type OPT, with the same performance and full preservation of backsight sizes.
  4. Approval of the terms of reference.

Performance parameters:Heat transfer areaHeated air
Flue gas inlet, С°485185
Flue gas outlet, С°376320
Volumetric size, Nm3/h149 127131 356
The pressure loss in the heat exchanger channels, mmWg7381
Heat power, kWt6 618
Recuperation degree, %44,9




Our equipment is used by: