Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung Integrierte Vermeidung und Verminderung der Umweltverschmutzung

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Chapter 2 2.2.4.3 Crystallisation of edible oils and fats Crystallisation of edible oils and fats, also called fractionation, is based on the principle that the solubility of the higher melting components in the liquid phase change at different temperatures. This difference can be extended by using an organic solvent which has the effect of decreasing the viscosity and leading to better washing of the crystals. The equipment includes tanks for preheating; stirred and cooled tanks for crystallisation; band or membrane filters for the separation of the crystals from the liquor and distillation vessels for solvent recovery. The oil is heated to 10 ºC above the melting point of the highest triacylglycerol present, to give a fully liquid starting material, e.g. the heating point is typically 75 ºC for palm oil. The molten oil is then cooled and stirred to form crystal nuclei, and the temperature is maintained at a lower temperature to induce crystal growth, typically for 12 hours at 28 – 30 ºC for palm oil. If a solvent is used, it is added to the molten oil prior to cooling. The mixtures containing the crystallised solids and the dissolved liquids are separated by filters. If a solvent is used, it is removed from the fractions by distillation. 2.2.4.4 Further processing of edible oils and fats – margarine The main products manufactured from edible oils and fats are margarine, edible fats, edible oils and mayonnaise. In view of its major outstanding importance, only margarine production is described here. Most installations carry out hydrogenation to produce fats with superior retention qualities and higher melting points. Hydrogenation is usually carried out by dispersing hydrogen gas in the oil, in the presence of a finely divided nickel catalyst supported on diatomaceous earth. The resultant hydrogenated fats are filtered to remove the hydrogenation catalyst, subjected to a light earth bleach and deodorised before they can be used for edible purposes. After hardening, the oil is mixed with an aqueous solution to produce an emulsion. The emulsified mixture is then pasteurised, cooled and crystallised to obtain the final product. 2.2.4.5 Olive oil The words “olive oil” mean the product obtained from Olea europea. It is composed of about 98 % glycerides with the remaining 2 % being various components naturally present in olives, some of which play a fundamental role in the olfactory and taste characteristics and which are also important for the stability and quality of the product. Olive oils and husk oils are classified on the basis of denominations and definitions from Regulation 136/66/EEC of 22 September 1966 on the establishment of a common organisation of the market in oils and fats [215, EC, 1996]. Extra virgin oils, virgin oils and ordinary virgin oils are edible; yet only extra virgin oils and virgin oils can be commercialised as they are for direct consumption. Ordinary virgin oils are commonly used mixed with refined olive oils and refined husk oils. Acid oils with an acidity higher than 3.3 degrees must be refined. The quality of the olive oil depends on the ripeness of the olives, the type of harvesting, e.g. picking or shaking, the type of intermediate storage, and the type of processing carried out. Olives contain 38 to 58 % oil and up to 60 % water. Ripe olives should be processed as quickly as possible since lipases in the pulp cause rapid hydrolysis of the oil, impairing its quality for edible purposes. Top-grade oils are made from fresh, handpicked olives by size reduction, pasting, and cold pressing. In the production of olive oil, there are three systems currently in use for the extraction of the oil; traditional, by pressing; three-phase separation or two-phase separation. 78 January 2006 RHC/EIPPCB/FDM_BREF_FINAL

Chapter 2 In traditional production of olive oil, olives are ground into a paste with stone mills, however these days modern milling equipment is also used. Milling is followed by mashing, possibly with the addition of salt. The pulp is then pressed and the press oil is clarified by sedimentation or centrifugation. Traditional open-cage presses are now being replaced by continuous screw expellers. The mashed pulp can also be separated in a horizontal decanter, in which case the crude oil is re-centrifuged after the addition of wash-water. Alternatively, machines can be used to remove the kernels from the pulp and the residue is then separated using self-discharging centrifuges. Cold pressing, which yields virgin grades, is generally followed by a warm pressing at approximately 40 ºC. Cold-pressed olive oil is a valuable edible oil. In Spain, most installations use the two-phase type centrifuges, while in most other Mediterranean countries larger installations use the three-phase technique, and smaller installations typically still use traditional pressing. While the two-phases generate a paste-like waste, both the traditional and the three-phase systems produce a liquid phase, i.e. olive mill waste water, or alpechin and a press cake known as pomace, husk, or orujo. This latter product may be further treated as husk or pomace oil. The remaining solid husk is dried to 3 – 6 % of humidity and used as fuel. Olive kernel oil is obtained by pressing and solvent extraction of cleaned kernels. It is similar to olive oil but lacks its typical flavour. Trade specifications are based primarily on the content of ffa and flavour assessment. In some countries, warm-pressed olive oil with a high acidity is refined by neutralisation, bleaching, and deodorisation, and flavoured by blending with cold-pressed oil. The press cake contains 8 to 15 % of a relatively dark oil, called sanza or orujo, which can be extracted with hexane and is used for technical purposes. After refining, it is also fit for edible consumption. 2.2.4.6 Olive-pomace oil Olive-pomace installations process the olive-pomace remaining after the extraction of oil from the olives. Oil is extracted with solvents resulting in crude pomace oil and exhausted husks. Oil is sent to refineries and later used in the food industry, while exhausted pomace is mainly used as fuel. Refined olive-pomace oils are mixed with virgin oils different from the lampante oils. It is also classified on the basis of denominations and definitions from Regulation 136/66/EEC [215, EC, 1996]. 2.2.5 Dairy products Milk is approximately 87 % water, with the remainder being protein, fat, lactose, calcium, phosphorus, iron and vitamins. Cows milk is primarily consumed, but goats and sheep milk are also consumed in significant quantities. A number of dairy products such as cream, cheese and butter are produced from milk. 2.2.5.1 Milk and cream Raw chilled milk is received at the dairy and transferred to bulk storage. The milk may be centrifugally separated to produce skimmed or semi-skimmed milk and a cream stream. The milk is then heat treated by a variety of methods such as pasteurisation or sterilisation, also known as UHT. Heat processing may be a batch or continuous operation depending upon the quantity of the milk to be processed and the method employed. The milk is first homogenised. Homogenisation disperses fat globules and prevents separation of the cream component. To achieve a sufficient creaming stability for pasteurised milks with a relatively short shelf-life, reduction of the fat globules size to a mean diameter of 1 to 2 μ is required, while the long shelf-life UHT milks require a much greater reduction in fat globule size,

Chapter 2<br />

2.2.4.3 Crystallisation of edible oils and fats<br />

Crystallisation of edible oils and fats, also called fractionation, is based on the principle that the<br />

solubility of the higher melting components in the liquid phase change at different temperatures.<br />

This difference can be extended by using an organic solvent which has the effect of decreasing<br />

the viscosity and leading to better washing of the crystals.<br />

The equipment includes tanks for preheating; stirred and cooled tanks for crystallisation; band<br />

or membrane filters for the separation of the crystals from the liquor and distillation vessels for<br />

solvent recovery. The oil is heated to 10 ºC above the melting point of the highest<br />

triacylglycerol present, to give a fully liquid starting material, e.g. the heating point is typically<br />

75 ºC for palm oil. The molten oil is then cooled and stirred to form crystal nuclei, and the<br />

temperature is maintained at a lower temperature to induce crystal growth, typically for<br />

12 hours at 28 – 30 ºC for palm oil. If a solvent is used, it is added to the molten oil prior to<br />

cooling. The mixtures containing the crystallised solids and the dissolved liquids are separated<br />

by filters. If a solvent is used, it is removed from the fractions by distillation.<br />

2.2.4.4 Further processing of edible oils and fats – margarine<br />

The main products manufactured from edible oils and fats are margarine, edible fats, edible oils<br />

and mayonnaise. In view of its major outstanding importance, only margarine production is<br />

described here.<br />

Most installations carry out hydrogenation to produce fats with superior retention qualities and<br />

higher melting points. Hydrogenation is usually carried out by dispersing hydrogen gas in the<br />

oil, in the presence of a finely divided nickel catalyst supported on diatomaceous earth. The<br />

resultant hydrogenated fats are filtered to remove the hydrogenation catalyst, subjected to a light<br />

earth bleach and deodorised before they can be used for edible purposes. After hardening, the<br />

oil is mixed with an aqueous solution to produce an emulsion. The emulsified mixture is then<br />

pasteurised, cooled and crystallised to obtain the final product.<br />

2.2.4.5 Olive oil<br />

The words “olive oil” mean the product obtained from Olea europea. It is composed of<br />

about 98 % glycerides with the remaining 2 % being various components naturally present in<br />

olives, some of which play a f<strong>und</strong>amental role in the olfactory and taste characteristics and<br />

which are also important for the stability and quality of the product. Olive oils and husk oils are<br />

classified on the basis of denominations and definitions from Regulation 136/66/EEC of<br />

22 September 1966 on the establishment of a common organisation of the market in oils and<br />

fats [215, EC, 1996].<br />

Extra virgin oils, virgin oils and ordinary virgin oils are edible; yet only extra virgin oils and<br />

virgin oils can be commercialised as they are for direct consumption. Ordinary virgin oils are<br />

commonly used mixed with refined olive oils and refined husk oils. Acid oils with an acidity<br />

higher than 3.3 degrees must be refined.<br />

The quality of the olive oil depends on the ripeness of the olives, the type of harvesting, e.g.<br />

picking or shaking, the type of intermediate storage, and the type of processing carried out.<br />

Olives contain 38 to 58 % oil and up to 60 % water. Ripe olives should be processed as quickly<br />

as possible since lipases in the pulp cause rapid hydrolysis of the oil, impairing its quality for<br />

edible purposes. Top-grade oils are made from fresh, handpicked olives by size reduction,<br />

pasting, and cold pressing. In the production of olive oil, there are three systems currently in use<br />

for the extraction of the oil; traditional, by pressing; three-phase separation or two-phase<br />

separation.<br />

78 January 2006 RHC/EIPPCB/FDM_BREF_FINAL

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