Description

Level measurement of pretreated oil

Besoins pour ce point de mesure

  • Protective connection systems for corrosive media
  • SIL 2/3 certified for safety-related applications

Description

Feed temperature monitoring

Besoins pour ce point de mesure

  • Thermowell material: 1.4404 / 316L or 1.4571 / 316Ti
  • With optional temperature transmitter

Description

Low level monitoring in water reservoir

Besoins pour ce point de mesure

  • Typical for small tanks
  • Maintenance-free, can be installed in any position

Description

Water and glycerol feed temperature

Besoins pour ce point de mesure

  • Customised or standard lengths
  • Applications with low to medium pressures and flow velocities

Description

Heat exchanger differential pressure monitoring

Besoins pour ce point de mesure

  • Heat exchanger monitoring

Description

Overfilling prevention

Besoins pour ce point de mesure

  • Tank internal reflections can be eliminated
  • SIL 2/3 certified

Description

Pressure measurement main reactor

Besoins pour ce point de mesure

  • Overhead methanol pressure measurement

Description

Main reactor and methanol feed

Besoins pour ce point de mesure

  • Available intrinsically safe: ATEX, IECEx
  • Thermowell material: 1.4404 / 316L or 1.4571 / 316Ti

Description

Recirculation temperatures

Besoins pour ce point de mesure

  • Applications with low to medium pressures and flow velocities
  • Assemblies with DIN standards required

Description

Recirc-pump pressure measurement

Besoins pour ce point de mesure

  • Process control

Description

Methanol tank hydrostatic level measurement

Besoins pour ce point de mesure

  • Level control

Description

Flow and density monitoring of recyclate

Besoins pour ce point de mesure

  • High accuracy mass flow and density measurement
  • Maintains operation with air or gas entrainments in the medium

Description

Methanol feed to reactor

Besoins pour ce point de mesure

  • Compact or field-mounted version (incl. cable length up to 30 m / 90 ft)
  • Large dynamic range, no pressure loss

Description

Mass balance of separator 1

Besoins pour ce point de mesure

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

Description

FAME flash dryer vacuum measurement

Besoins pour ce point de mesure

  • Vacuum pump control

Description

FAME storage overfilling prevention

Besoins pour ce point de mesure

  • Tank internal reflections can be eliminated
  • SIL 2/3 certified

Overview

Fatty acid methyl ester in the palm oil production

Precision Instrumentation Ensuring High Purity Levels in FAME Outputs

Fatty acid methyl esters (FAME) are produced by transesterification of fats or oils (triglycerides) with methanol. Palm oil methyl esters (PME) are similar to FAME.
This reaction can be catalyzed acidic or alkaline, depending on the feedstock properties. The trivalent alcohol glycerine is exchanged for methanol. Glycerine and FAME are formed as reaction products, whereby, when using natural fats, a mixture of different fatty acid methyl esters with an even number of carbon atoms is obtained, since natural triglycerides generally contain several different fatty acid residues.
More generally expressed, Biodiesel production is the process of producing the biofuel, biodiesel, through the chemical reactions of transesterification and esterification. This involves vegetable (or animal fats) and oils being reacted with short-chain alcohols (typically methanol or ethanol). The alcohols used should be of low molecular weight. Ethanol is frequently used because of its low cost, however, greater conversions into biodiesel can be reached using methanol.
Although the transesterification reaction can be catalyzed by either acids or bases, the base-catalyzed reaction is more common. This path has lower reaction times and catalyst cost than those using acid catalysis. However, alkaline catalysis has the disadvantage of high sensitivity to both water and free fatty acids present in the oils.

In order to shift the equilibrium of the transesterification reaction to the side of the products, i.e. to the side of the fatty acid methyl esters, glycerine can be removed or alcohol (methanol) can be added in excess.

Another variant in the food industry, is specific enzymatic transesterification using special 1,3-lipases. This specificity is not possible chemically and so this enzymatic route can be used for the production of cocoa butter substitute, margarine, butter and baking fats.

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