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Mayonnaise Manufacture
The Advantages
Introduction
The Process
The Problem
The Solution
HIGH SHEAR MIXERS/EMULSIFIERS
FOOD
Solutions for Your TOUGHEST
MIXING Applications in
APPLICATION REPORT
The manufacturing process is subject to a number of difficulties, many of which can be
exacerbated by operator error:
• Continuous phase ingredients are only a small proportion of the total formulation,
but they perform vital functions. The mixing equipment must be capable of dispersing
and hydrating these properly in a relatively low liquid volume. If the egg and other
emulsifying agents are not properly dispersed and hydrated the emulsion can break
during the oil addition stage.
• Hydration of stabilisers and thickeners is one of the most difficult mixing operations.
In some cases the solution has to be agitated for a long period to complete hydration.
Agglomerates can easily form; these cannot be broken down by agitation alone.
• Due to the high proportion of oil in the recipe the emulsion can break if the oil is not
added to the continuous phase correctly. This is very difficult to control when
the oil addition is carried out manually.
• Oil phase droplets must be reduced to the smallest size possible to maximise the
surface area of oil within the continuous phase to ensure a stable emulsion. This is
not readily achieved without specialised equipment.
• Aeration must be minimised or eliminated to ensure maximum product shelf life.
The Problem
A typical method for manufacture of mayonnaise would be as follows:
• In the first stage of production, the egg, which may be used in either liquid or powder
form is dispersed into the water. This acts as the emulsifying agent.
• Remaining continuous phase ingredients are then added and mixed until dispersed and
hydrated.
• The oil is added as rapidly as the continuous phase will take it up. This results in a
dramatic rise in product viscosity as the emulsion is formed.
Mayonnaise is an oil-in-water emulsion which can contain up to 80% oil. Some typical
recipes would be as follows:
Gums and thickeners such as starches are used in low fat products to replace the
viscosity and bulking effect of the oil, to enhance mouthfeel, and to ensure that a stable
emulsion is formed.
Large scale production is normally carried out using plant specifically designed for
mayonnaise manufacture. This process is often semi-automated. For R&D, pilot scale
and small scale production typical of the “ready to use” market - sandwich producers,
caterers and other low-volume applications - mayonnaise needs to be produced in a
manner which allows much more flexibility, especially when changing formulae.
The Process
Mayonnaise Manufacture
80% Oil Formula
Vegetable oil 80%
Egg yolk 6%
Vinegar 4%
Sugar 1%
Salt 1%
Spices (e.g. mustard) 0.5%
Water 7.5%
Low Fat Formula
Vegetable oil 50%
Egg yolk 4%
Other thickeners 4%
Vinegar 3%
Sugar 1.5%
Salt 0.7%
Spices 1.5%
Water 35.3%
FOOD
FOOD
Silverson has developed a unit for manufacture of mayonnaise for the ready to use
market, R&D and pilot scale production. The unit is capable of carrying out the entire
process, including rapid preparation of premixes, hydration of thickening and stabilising
agents and preparation of the final oil-in-water emulsion. Operation is as follows:
The Solution
hopper for
oil addition
modified high
shear In-Line
mixer
aqueous phase
powder/liquid
feed hopper
process
vessel
Water is recirculated from the vessel through the system by the specially designed In-
Line mixer. The egg (either powder or liquid) is added to the vessel and in the case of
powder, is rapidly wetted out and dispersed into the high velocity liquid stream.
The remaining aqueous phase ingredients are then added to the vessel or via the
powder feed hopper depending on batch size and powder characteristics. Mixing
continues until the ingredients are fully dispersed and hydrated.
The oil is added to the second hopper. When the valve is opened it is drawn into the
aqueous phase at a controlled rate. The aqueous and oil phase ingredients then pass
directly into the workhead of the In-Line mixer where they are subjected to intense
high shear. This finely disperses the oil into the aqueous phase, immediately forming an
emulsion. The vinegar (and lemon juice) is added together with the last of the oil.
Recirculation of the product continues to ensure a uniform consistency as the viscosity
rises. After a short recirculation period the process is completed and the finished
product is discharged.
discharge
Stage 1
Stage 2
Stage 3
Stage 4
Silverson Machines Ltd. Waterside, Chesham, Buckinghamshire England HP5 1PQ
Tel: +44 (0) 1494 786331 • Fax: +44 (0) 1494 791452 • 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. 52FA1
• Ideal for small batches that are intended for immediate use.
• Aeration is minimised.
• The system practically eliminates operator error.
• Offers the batch-to-batch consistency and stability of mayonnaise manufactured in
turnkey plant without the high capital expenditure.
• Yield of raw materials is maximised, as thickening agents are fully hydrated and other
ingredients are correctly dispersed.
• The system is designed for handling high viscosity products without the need for
additional pumps or auxiliary equipment.
• Easily adapted to variations in product type and recipe.
The Advantages
Two In-Line mixers can
be used installed in
series, the first mixing
the aqueous phase with
part of the oil. The
remainder of the oil is
added before the
second In-Line. All
liquids are fed by
metering pumps. High
production levels (>5
Tonnes/hour) can easily
be achieved.
Large Scale Manufacture
Aqueous Phase
20% oil 80% oil
2nd
In-Line
1st
In-Line
Packing
Egg
Sugar
Salt
Spices
Thickeners etc.
Water
Silverson High Shear In-Line mixers can also be used for large scale manufacture of
mayonnaise. A typical process would be as follows:

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Food Industry Case Study: Manufacturing Mayonnaise

  • 1. Mayonnaise Manufacture The Advantages Introduction The Process The Problem The Solution HIGH SHEAR MIXERS/EMULSIFIERS FOOD Solutions for Your TOUGHEST MIXING Applications in APPLICATION REPORT
  • 2. The manufacturing process is subject to a number of difficulties, many of which can be exacerbated by operator error: • Continuous phase ingredients are only a small proportion of the total formulation, but they perform vital functions. The mixing equipment must be capable of dispersing and hydrating these properly in a relatively low liquid volume. If the egg and other emulsifying agents are not properly dispersed and hydrated the emulsion can break during the oil addition stage. • Hydration of stabilisers and thickeners is one of the most difficult mixing operations. In some cases the solution has to be agitated for a long period to complete hydration. Agglomerates can easily form; these cannot be broken down by agitation alone. • Due to the high proportion of oil in the recipe the emulsion can break if the oil is not added to the continuous phase correctly. This is very difficult to control when the oil addition is carried out manually. • Oil phase droplets must be reduced to the smallest size possible to maximise the surface area of oil within the continuous phase to ensure a stable emulsion. This is not readily achieved without specialised equipment. • Aeration must be minimised or eliminated to ensure maximum product shelf life. The Problem A typical method for manufacture of mayonnaise would be as follows: • In the first stage of production, the egg, which may be used in either liquid or powder form is dispersed into the water. This acts as the emulsifying agent. • Remaining continuous phase ingredients are then added and mixed until dispersed and hydrated. • The oil is added as rapidly as the continuous phase will take it up. This results in a dramatic rise in product viscosity as the emulsion is formed. Mayonnaise is an oil-in-water emulsion which can contain up to 80% oil. Some typical recipes would be as follows: Gums and thickeners such as starches are used in low fat products to replace the viscosity and bulking effect of the oil, to enhance mouthfeel, and to ensure that a stable emulsion is formed. Large scale production is normally carried out using plant specifically designed for mayonnaise manufacture. This process is often semi-automated. For R&D, pilot scale and small scale production typical of the “ready to use” market - sandwich producers, caterers and other low-volume applications - mayonnaise needs to be produced in a manner which allows much more flexibility, especially when changing formulae. The Process Mayonnaise Manufacture 80% Oil Formula Vegetable oil 80% Egg yolk 6% Vinegar 4% Sugar 1% Salt 1% Spices (e.g. mustard) 0.5% Water 7.5% Low Fat Formula Vegetable oil 50% Egg yolk 4% Other thickeners 4% Vinegar 3% Sugar 1.5% Salt 0.7% Spices 1.5% Water 35.3% FOOD
  • 3. FOOD Silverson has developed a unit for manufacture of mayonnaise for the ready to use market, R&D and pilot scale production. The unit is capable of carrying out the entire process, including rapid preparation of premixes, hydration of thickening and stabilising agents and preparation of the final oil-in-water emulsion. Operation is as follows: The Solution hopper for oil addition modified high shear In-Line mixer aqueous phase powder/liquid feed hopper process vessel Water is recirculated from the vessel through the system by the specially designed In- Line mixer. The egg (either powder or liquid) is added to the vessel and in the case of powder, is rapidly wetted out and dispersed into the high velocity liquid stream. The remaining aqueous phase ingredients are then added to the vessel or via the powder feed hopper depending on batch size and powder characteristics. Mixing continues until the ingredients are fully dispersed and hydrated. The oil is added to the second hopper. When the valve is opened it is drawn into the aqueous phase at a controlled rate. The aqueous and oil phase ingredients then pass directly into the workhead of the In-Line mixer where they are subjected to intense high shear. This finely disperses the oil into the aqueous phase, immediately forming an emulsion. The vinegar (and lemon juice) is added together with the last of the oil. Recirculation of the product continues to ensure a uniform consistency as the viscosity rises. After a short recirculation period the process is completed and the finished product is discharged. discharge Stage 1 Stage 2 Stage 3 Stage 4
  • 4. Silverson Machines Ltd. Waterside, Chesham, Buckinghamshire England HP5 1PQ Tel: +44 (0) 1494 786331 • Fax: +44 (0) 1494 791452 • 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. 52FA1 • Ideal for small batches that are intended for immediate use. • Aeration is minimised. • The system practically eliminates operator error. • Offers the batch-to-batch consistency and stability of mayonnaise manufactured in turnkey plant without the high capital expenditure. • Yield of raw materials is maximised, as thickening agents are fully hydrated and other ingredients are correctly dispersed. • The system is designed for handling high viscosity products without the need for additional pumps or auxiliary equipment. • Easily adapted to variations in product type and recipe. The Advantages Two In-Line mixers can be used installed in series, the first mixing the aqueous phase with part of the oil. The remainder of the oil is added before the second In-Line. All liquids are fed by metering pumps. High production levels (>5 Tonnes/hour) can easily be achieved. Large Scale Manufacture Aqueous Phase 20% oil 80% oil 2nd In-Line 1st In-Line Packing Egg Sugar Salt Spices Thickeners etc. Water Silverson High Shear In-Line mixers can also be used for large scale manufacture of mayonnaise. A typical process would be as follows: