Description

Flow measurement of crude oil going to distillation

Requisitos para el punto de medición

  • Contamination of the crude oil could block mechanical meters
  • Process Control

Description

Flow measurement of off gas

Requisitos para el punto de medición

  • Ensure optimised burner control
  • Fluctuating operating conditions

Description

Level measurement in distillation columns

Requisitos para el punto de medición

  • Improve efficiency of separation process
  • Prevent overfill of distillation column

Description

Flow measurement of atmospheric bottoms

Requisitos para el punto de medición

  • High temperature
  • High viscosity
  • Risk of blockage

Description

Flow measurement of distilled gas

Requisitos para el punto de medición

  • Agressive media
  • Process control

Description

Flow measurement of products from atmospheric distillation

Requisitos para el punto de medición

  • Help to maintain mass balance
  • Process control

Description

Flow measurement of products from vacuum distillation

Requisitos para el punto de medición

  • High temperature
  • Help to maintain mass balance
  • Process control

Description

Flow measurement of vacuum reisduum and asphalt

Requisitos para el punto de medición

  • High temperature
  • High viscosity
  • Risk of blockage

Description

Supervisory and validation software

Requisitos para el punto de medición

  • Visualisation and monitoring of critical processes
  • Control of reporting, trends and alarm handling
  • Statistical evaluation of measurement data

Overview

Distillation in the chemical industry

Atmospheric and vacuum distillation measuring

After desalting, the crude oil is further heated to around 375oC in a furnace. From here it flows into the bottom of an atmospheric distillation column, actually at slightly above atmospheric pressure. As the oil vapours rise up the column and cool, various fractions with different boiling temperatures condense into liquids, and are removed from the side of the column. These liquid fractions are known as sidecuts, and include naphtha, kerosene, light gas oil etc, as shown on the diagram. The liquids are cooled and process efficiency improved by exchanging their heat with the incoming oil feedstock. The gas remaining at the top of the column comprises the lightest fractions of the crude oil, those with the lowest boiling points. Typically the distillation column will be run in a continuous steady state, controlled by crude oil distillation instrumentation: here flow measurement and the consequent balancing of the fractions is important for control.

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