Description

Bleached oil high level monitoring

Requisitos para el punto de medición

  • Overfilling prevention
  • SIL 2/3 certified for safety-related applications

Description

Oil feed to polishing stage

Requisitos para el punto de medición

  • High accuracy mass flow and density measurement
  • Device commissioning, verification, diagnostics and monitoring via a secure wireless Bluetooth

Description

Boiler temperature and pressure

Requisitos para el punto de medición

  • Thermowell material: 1.4404 / 316L or 1.4571 / 316Ti
  • High pressure overload resistance

Description

Differential pressure over the filter

Requisitos para el punto de medición

  • Filter DP monitoring

Description

Steam distribution and load control

Requisitos para el punto de medición

  • Integrated gross and net heat calculation
  • Integral pressure and temperature compensation (option)

Description

Polished oil to deaerator monitoring

Requisitos para el punto de medición

  • Thermowell material: 1.4404 / 316L or 1.4571 / 316Ti
  • Different connection heads available (IP54…IP68)

Description

Extracted oil from deodoriser

Requisitos para el punto de medición

  • High accuracy mass flow control for deodoriser
  • Integrated temperature measurement

Description

Temperature balance over stripping column

Requisitos para el punto de medición

  • Thermowell material: 1.4404 / 316L or 1.4571 / 316Ti
  • Applications with low to medium pressures and flow velocities

Description

Temperature balance over stripping column

Requisitos para el punto de medición

  • Thermowell material: 1.4404 / 316L or 1.4571 / 316Ti
  • Applications with low to medium pressures and flow velocities

Description

Stripper packet DP monitoring

Requisitos para el punto de medición

  • Monitoring of packet condition

Description

Stripper head vacuum measurement

Requisitos para el punto de medición

  • Process control

Description

Steam supply for deodoriser

Requisitos para el punto de medición

  • Optimized deodorization
  • Full compensation of temperature and pressure

Description

Circulation flow pressure measurement

Requisitos para el punto de medición

  • Process control

Description

Disatillate cooling

Requisitos para el punto de medición

  • Bi-directional flow measurement over a wide dynamic range
  • Cost-saving installation without grounding rings

Description

Fatty acid recirculation to stripper

Requisitos para el punto de medición

  • Optional heating jacket available
  • For extended process temperature ranges

Description

Final distillate

Requisitos para el punto de medición

  • High accuracy mass, density and volume flow measurement
  • Cost-effective twin straight tube Coriolis mass flowmeter

Description

Recirculate temperature

Requisitos para el punto de medición

  • Compression fitting connection
  • Ex works with optional temperature transmitter

Description

Refined bleached deodorized product

Requisitos para el punto de medición

  • High accuracy mass, density and volume flow measurement
  • Cost-effective twin straight tube Coriolis mass flowmeter

Overview

Fatty acid separation in the palm oil production

Instrumentation Enabling Heat Recovery Processes for Improved Energy Efficiency in Fatty Acid Separation

Fatty acid separation is basically achieved in a combined stripper/distiller, where odours are removed at the same time: the fatty acids can be separated according to their different boiling points. Preheated fatty acid feed is made to flow through a series of reaction chambers.
Each reaction chamber is heated at the bottom, typically by superheated steam, which is injected into the feed in each chamber through a sparger. The low pressure imposed in the reaction chamber and the high temperature of the feed and the superheated steam flow all agitate and evaporate the fatty acids, in a form of distillation.

The vapours are led to a pipe header and condensed in a water-cooled condenser. The steam passes through, travelling on to the barometric condenser: the non-condensable gases are removed by a vacuum pump. The residue leaving the base of the last reaction chamber is cooled. In all these process steps measurements of pressure and temperature are crucial. One disadvantage of steam distillation of fatty acids is the formation of emulsions in the last stage of condensation, where a water spray is used. The calcium and magnesium salts typically present in the water spray react with the fatty acids forming soaps.
To recover the fatty acids, the soap is acidified and redistilled if desired.

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