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Refining of Vegetable
Oils for Biofuels
The Advantages
Introduction
The Process
The Problem
The Solution
HIGH SHEAR MIXERS/EMULSIFIERS
CHEMICALS
Solutions for Your TOUGHEST
MIXING Applications in
APPLICATION REPORT
There are therefore 4 processes carried out on oil used for this application. Although
there are variations, and some processes may combine or eliminate certain stages (e.g.
Bleaching), they can be summarized as follows:
There is considerable growth in the use of vegetable oils such as palm, rape seed,
soybean, sunflower etc. as an alternative to petroleum based diesels. Currently there
are two options for this; Straight Vegetable Oil (SVO) and Biodiesel.
In either case the untreated or “crude” oil has to be refined prior to use, in a series of
stages; Degumming, Neutralizing and Bleaching. The resultant SVO can be used in diesel
engines but it must first be heated to around 150˚F (65˚C) to reduce the viscosity.
Separate fuel tanks and/or pre-heating systems are used to achieve this.
Biodiesel offers the advantage that it can be used as a direct replacement for ordinary
diesel without requiring preheating. It is produced by subjecting SVO to a further
refining process called Transesterification. The properties of biodiesel are covered by
legislation such as American ASTM standards and European Standard EN14214.
CHEMICALS
The Process
Refining of Vegetable Oils for Biofuels
untreated
oil
heat to
120 -
160˚F
(50-70˚C)
In-Line
Mixer
acid addition, typically phosphoric
or citric acid at 0.1 - 1 %
acid reacts with
phosphatides (gums)
in the oil, making them
hydratable
oil may pass straight to neutralizing
or bleaching without removal of
gums (“acid conditioning”)
water may be added to hydrate the
phosphatides before removal in the
separator
water
separator
gums
degummed oil
untreated,
degummed
or acid
conditioned
oil
sodium hydroxide solution
(caustic soda) a washing stage
may be carried
out to remove
residual soap
water
separator
neutralized
oil
soap stock spent water
degummed and/or
neutralized oil
water
removal oil/clay suspension
formed
impurities are
adsorbed by
the clay
Straight Vegetable
Oil (SVO)
bleaching
clay
filter
clay and adsorbed
impurities
separator
SVO heat
premixed to
form
“methoxide”
methanol
methoxide mixed
with oil and reacts
to form methyl ester
(“biodiesel”),
glycerine and
residual soaps
filter aid powder
(e.g. magnesium silicate)
filter aid powder
(e.g. kieselguhr)
biodiesel
caustic soda
(catalyst)
1. Degumming
2. Neutralizing
3. Bleaching
4.Transesterification
In-Line
Mixer
sodium hydroxide
neutralizes excess
acid and saponifies
fatty acids in the oil
washing stage
removes
residual soaps
water
separator
glycerine
filter
soap stock
heat to
around
200˚F
(95˚C)
CHEMICALS
A Silverson High Shear Mixer can overcome these problems and dramatically improve
the process This is achieved by the 3 stage mixing/shearing action of the rotor/stator
workhead as follows:
The Solution
The reagent additions were typically carried out using low shear static mixers or inline
agitators in a high volume, continuous operation. The transesterification process is
more varied in volume and the methanol premix may be prepared in a separate vessel
prior to addition to the oil in a “reactor vessel.” Again, conventional agitators were
often used. These processes are subject to a number of problems:
• The acid and sodium hydroxide solutions make up only a small fraction of the total
product, and must be reduced to the smallest possible droplet size to ensure intimate
contact with the oil. Low shear devices with a relatively short dwell time cannot
easily achieve this.
• Where an emulsion is formed it must be easy to break during separation.
• Conventional agitation cannot rapidly produce the agglomerate-free, homogeneous
suspension required for the clays and filter aid powders.
• Poor dispersion of reagents reduces process efficiency, leading to increased chemical
consumption and waste.
The Problem
Further reduction in particle size follows
as the mixture is forced out through the
stator, increasing the surface area of
reagent exposed to the oil. This
accelerates the reaction, and maximizes
the yield.
Centrifugal force drives the materials to
the periphery of the workhead where
they are reduced to a fine droplet/
particle size in the gap between the rotor
blades and the inner wall of the stator.
The reagent is introduced to the oil just
prior to the intake of the Silverson mixer.
The ingredients are drawn into the
rotor/stator workhead and vigorously
mixed.
Silverson Machines,Inc. 355 Chestnut Street, East Longmeadow, MA 01028
Ph: (413) 525-4825 • Fax:(413) 525-5804 • www.silverson.com
Information contained in this report is believed to be correct and
is included as a guide only. No warranty is expressed or implied
as to fitness for use or freedom from patents. Silverson Machines
reserve the right to change product specification without notice.
Issue No. 63CA1
• Improved dispersion of reagents into the oil maximizes the surface area exposed to
the oil, accelerating the reaction
• Reduced chemical and energy consumption and less environmental impact
• Rapid processing times
• Easily interchangeable workheads and screens allow the Silverson mixer to be
adapted to optimize performance for processing a range of oils, including those with
a tendency to emulsify
Silverson offers a range of machines suitable for the acid and sodium hydroxide
additions, and the Silverson Flashblend for the clay and filter aid dispersions:
The Advantages
High Shear In-Line Mixers
• Aeration free
• Easily retro-fitted to existing
plant
• Ideal for continuous processes
• Explosionproof units available.
• Multistage units available offering
greater degree of shear, resulting
in finer particle size and faster
processing times.
Silverson Flashblend
• Designed for high speed
dispersion of powders into liquids
• Minimized cleaning requirements
• Minimum operator input
required
• Easily automated
• Silverson should be consulted
regarding systems involving
flammable solvents
Centrifugal
Pump
Venturi
Assembly
In-Line
Mixer
Powder Feed
Hopper
Liquid in
Product out
Reagent/water
fed into line just
prior to intake
of In-Line mixer.
untreated
oil in
Clay/filter aid powder
feed hopper
Feedstock oil in
reagent/oil
blend passes
to next
processing
stage

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Biofuel Industry Case Study: Refining of Vegetable Oils for Biofuels

  • 1. Refining of Vegetable Oils for Biofuels The Advantages Introduction The Process The Problem The Solution HIGH SHEAR MIXERS/EMULSIFIERS CHEMICALS Solutions for Your TOUGHEST MIXING Applications in APPLICATION REPORT
  • 2. There are therefore 4 processes carried out on oil used for this application. Although there are variations, and some processes may combine or eliminate certain stages (e.g. Bleaching), they can be summarized as follows: There is considerable growth in the use of vegetable oils such as palm, rape seed, soybean, sunflower etc. as an alternative to petroleum based diesels. Currently there are two options for this; Straight Vegetable Oil (SVO) and Biodiesel. In either case the untreated or “crude” oil has to be refined prior to use, in a series of stages; Degumming, Neutralizing and Bleaching. The resultant SVO can be used in diesel engines but it must first be heated to around 150˚F (65˚C) to reduce the viscosity. Separate fuel tanks and/or pre-heating systems are used to achieve this. Biodiesel offers the advantage that it can be used as a direct replacement for ordinary diesel without requiring preheating. It is produced by subjecting SVO to a further refining process called Transesterification. The properties of biodiesel are covered by legislation such as American ASTM standards and European Standard EN14214. CHEMICALS The Process Refining of Vegetable Oils for Biofuels untreated oil heat to 120 - 160˚F (50-70˚C) In-Line Mixer acid addition, typically phosphoric or citric acid at 0.1 - 1 % acid reacts with phosphatides (gums) in the oil, making them hydratable oil may pass straight to neutralizing or bleaching without removal of gums (“acid conditioning”) water may be added to hydrate the phosphatides before removal in the separator water separator gums degummed oil untreated, degummed or acid conditioned oil sodium hydroxide solution (caustic soda) a washing stage may be carried out to remove residual soap water separator neutralized oil soap stock spent water degummed and/or neutralized oil water removal oil/clay suspension formed impurities are adsorbed by the clay Straight Vegetable Oil (SVO) bleaching clay filter clay and adsorbed impurities separator SVO heat premixed to form “methoxide” methanol methoxide mixed with oil and reacts to form methyl ester (“biodiesel”), glycerine and residual soaps filter aid powder (e.g. magnesium silicate) filter aid powder (e.g. kieselguhr) biodiesel caustic soda (catalyst) 1. Degumming 2. Neutralizing 3. Bleaching 4.Transesterification In-Line Mixer sodium hydroxide neutralizes excess acid and saponifies fatty acids in the oil washing stage removes residual soaps water separator glycerine filter soap stock heat to around 200˚F (95˚C)
  • 3. CHEMICALS A Silverson High Shear Mixer can overcome these problems and dramatically improve the process This is achieved by the 3 stage mixing/shearing action of the rotor/stator workhead as follows: The Solution The reagent additions were typically carried out using low shear static mixers or inline agitators in a high volume, continuous operation. The transesterification process is more varied in volume and the methanol premix may be prepared in a separate vessel prior to addition to the oil in a “reactor vessel.” Again, conventional agitators were often used. These processes are subject to a number of problems: • The acid and sodium hydroxide solutions make up only a small fraction of the total product, and must be reduced to the smallest possible droplet size to ensure intimate contact with the oil. Low shear devices with a relatively short dwell time cannot easily achieve this. • Where an emulsion is formed it must be easy to break during separation. • Conventional agitation cannot rapidly produce the agglomerate-free, homogeneous suspension required for the clays and filter aid powders. • Poor dispersion of reagents reduces process efficiency, leading to increased chemical consumption and waste. The Problem Further reduction in particle size follows as the mixture is forced out through the stator, increasing the surface area of reagent exposed to the oil. This accelerates the reaction, and maximizes the yield. Centrifugal force drives the materials to the periphery of the workhead where they are reduced to a fine droplet/ particle size in the gap between the rotor blades and the inner wall of the stator. The reagent is introduced to the oil just prior to the intake of the Silverson mixer. The ingredients are drawn into the rotor/stator workhead and vigorously mixed.
  • 4. Silverson Machines,Inc. 355 Chestnut Street, East Longmeadow, MA 01028 Ph: (413) 525-4825 • Fax:(413) 525-5804 • www.silverson.com Information contained in this report is believed to be correct and is included as a guide only. No warranty is expressed or implied as to fitness for use or freedom from patents. Silverson Machines reserve the right to change product specification without notice. Issue No. 63CA1 • Improved dispersion of reagents into the oil maximizes the surface area exposed to the oil, accelerating the reaction • Reduced chemical and energy consumption and less environmental impact • Rapid processing times • Easily interchangeable workheads and screens allow the Silverson mixer to be adapted to optimize performance for processing a range of oils, including those with a tendency to emulsify Silverson offers a range of machines suitable for the acid and sodium hydroxide additions, and the Silverson Flashblend for the clay and filter aid dispersions: The Advantages High Shear In-Line Mixers • Aeration free • Easily retro-fitted to existing plant • Ideal for continuous processes • Explosionproof units available. • Multistage units available offering greater degree of shear, resulting in finer particle size and faster processing times. Silverson Flashblend • Designed for high speed dispersion of powders into liquids • Minimized cleaning requirements • Minimum operator input required • Easily automated • Silverson should be consulted regarding systems involving flammable solvents Centrifugal Pump Venturi Assembly In-Line Mixer Powder Feed Hopper Liquid in Product out Reagent/water fed into line just prior to intake of In-Line mixer. untreated oil in Clay/filter aid powder feed hopper Feedstock oil in reagent/oil blend passes to next processing stage