Atmospheric and vacuumа distillation of crude oil

  1. Atmospheric and vacuum distillation of crude oil AVD-5.
  2. Tube furnace 201A.
  3. Replacement of broken tubular air preheater with full backsight all sizes within the energy efficiency programs and import substitution.
  4. Year of realization: 2015.
  5. Scope of supply: the heat exchanger Manufacturing, delivery, installation and commissioning.
  6. Result: Replacement of air preheater has been carried out in prof.break by modular air preheater «OPT». In the operation indicated in the specification and performance claimed efficiency were achieved.
  7. Payback period: Confirmed

Performance parameters :Heat transfer areaHeated air
Flue gas inlet, С°35015
Flue gas outlet, С°157218
Volumetric size, Nm3/h57 80058 900
Pressure loss, mmWg14557
Heat power,kWt4 367
Recuperation degree, %60,7



Atmospheric distillation of crude oil

  1. Installation of Atmospheric distillation shop number 8.
  2. Furnace #1, installation number 1
  3. The project to replace the failed air heater with full retention of all tie-in sizes in the framework of energy efficiency programs.
  4. Year of implementation: 2017.
  5. Scope of delivery: Manufacturing of air heater, delivery, installation supervision and commissioning.
  6. Result: The replacement of the air heater was carried out in the course of the profitable operation due to the modular execution of the air heater of the OPT. During the operation, the indicators specified in the specification and the declared effectiveness were achieved.

Performance parameters :Heat transfer areaHeated air
Flue gas inlet, С°43050
Flue gas outlet, С°198315
Volumetric size, Nm3/h85 42479 526
Pressure loss, mmWg5160
Heat power,kWt7 900

Economizer

  1. Heat recovery of flue gas regeneration shop RB-2/3 unit #1
  2. Design of an economizer for heating high-pressure steam condensate.
  3. Year of implementation: 2017.
  4. Scope of supply: Designing and manufacturing of economizer, delivery, installation supervision and participation in commissioning.
  5. Result: The economizer was installed in a break for major repairs due to modular execution. In the process of operation, the indicators specified in the specification are exceeded, and greater efficiency has been achieved.

Operating parameters :Heat transfer areaHeated side (steam condensate)
Flue gas inlet, С°26090
Flue gas outlet, С°190150
Volumetric size, kg/h500 000110 864
Heat power,kWt14 005

Installation of reheating fuel before distillation

  1. Installation of reheating fuel before distillation.
  2. Tubular tent furnace P-1 and P-2.
  3. The replacement of the failed project of the tubular air preheater.
  4. Year of realization: 2015.
  5. Scope of supply: the heat exchanger Manufacturing, testing and delivery.
  6. Result: Under these operating parameters in specification were achieved.
  7. Payback Period: Confirmed

Performance parameters :Heat transfer areaHeated air
Flue gas inlet, С°700-25
Flue gas outlet, С°528220
Volumetric size, Nm3/h30 00027 300
Pressure loss, mmWg560
Heat power,kWt2 473

Installation of vacuum distillation

  1. Installation of vacuum distillation.
  2. Tube furnace H-10001A/B.
  3. Section by section replacement of the failed tube type air preheater with full backsight all sizes.
  4. Year of realization: 2016 - 2017.

Performance parameters :Heat transfer areaHeated air
Flue gas inlet, С°31368
Flue gas outlet, С°181225
Volumetric size, Nm3/h57 92652 143
Pressure loss, mmWg3328
Heat power,kWt3 014

Oil line heaters PTB-10/64

  1. Oil and Gas Management.
  2. The line heaters oil PTB-10/64.
  3. The draft of heat recovery system implementation for preheating the oil.
  4. It is alleged to be implemented in 2017 - 2018.

Performance parameters :Heat transfer area (Дымовые газы)Heated air (Гликоль)
Flue gas inlet, С°55030
Flue gas outlet, С°293110
Volumetric size, Nm3/h6 3007
Pressure loss, mmWg2295
Heat power,kWt659


PT-16/150 Oil line heaters

  1. Oil and Gas Management.
  2. The line heaters oil PTB-10/64
  3. The draft of recovery system implementation in order to save fuel ( associated gas processed at a nearby factory).
  4. It is alleged to be implemented in 2017 - 2018.

Performance parameters :Heat transfer areaHeated air
Flue gas inlet, С°3364
Flue gas outlet, С°234127
Volumetric size, Nm3/h2 7002 450
Pressure loss, mmWg614
Heat power,kWt109




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