Integrierte Vermeidung und Verminderung der Umweltverschmutzung
Integrierte Vermeidung und Verminderung der Umweltverschmutzung Integrierte Vermeidung und Verminderung der Umweltverschmutzung
Chapter 2 2.1.4.9.2 Field of application Hardening is applied in the processing of edible oils for the production of margarine and other edible fats. 2.1.4.9.3 Description of techniques, methods and equipment Hardening, or hydrogenation of oils, is the process of saturating mono or poly-unsaturated fatty acids by adding hydrogen gas (H2) for the hydrogenation and nickel as a catalyst. Hydrogen molecules, in the presence of nickel and under special process conditions, saturate the unsaturated bonds of the fatty acids of edible oils. Neutral or bleached oil is heated to a temperature of 150 to 205 °C in the presence of a nickel catalyst, maximum 10 kg catalyst/tonne product. H2 is then added to the mixing reactor to achieve the hardening, i.e. the transformation from oil to fat. Hydrogenation is an exothermic process. After the reaction, the fats are separated from the nickel, using filter presses or other filter systems. In a minority of cases, the nickel catalyst can be re-used several times until it is deactivated. Specialised companies recycle the spent nickel. The residual nickel concentration in the fats is removed by bleaching, which produces bleaching earth contaminated with nickel. The equipment used for hardening consists of mixing vessels, reaction tanks, autoclaves and filters. 2.1.4.10 Sulphitation (D.10) 2.1.4.10.1 Objective The aim of sulphitation is to prevent either microbiological degradation, unwanted colour formation or to adjust pH. 2.1.4.10.2 Field of application Sulphitation is applied in winemaking, potato processing and shellfish processing. It is also sometimes applied in sugar production to adjust the pH. 2.1.4.10.3 Description of techniques, methods and equipment Sulphitation is the introduction of sulphur dioxide (SO2) into liquids; the quantity of SO2 which can be added is regulated. It can be introduced in various forms. First, in gaseous form, generated either by burning sulphur or from liquefied gas and direct expansion. The SO2 is drawn by a fan into an absorption column in which the liquid flows. Second, in liquid form, from liquefied gas or in sodium or potassium bisulphite solution. The SO2 may also be stored as a liquid, under approximately 5 bar, in horizontal cylindrical tanks of 25 to 50 m 3 capacity, from which it can then be introduced into the desired process stream. Third, in solid form, as sodium or potassium metabisulphite dissolved in the liquid to be treated. An alternative sulphite source is ammonium bisulphite. Sodium bisulphite can also be used. 2.1.4.11 Carbonatation (D.11) 2.1.4.11.1 Objective The aim of carbonatation is to remove impurities from a solution. 2.1.4.11.2 Field of application Applied in the sugar industry. 32 January 2006 RHC/EIPPCB/FDM_BREF_FINAL
2.1.4.11.3 Description of techniques, methods and equipment Chapter 2 Carbonatation is the introduction of the milk of lime, calcium hydroxide, and carbon dioxide gas (CO2) into a liquid to form calcium carbonate and to precipitate and remove impurities. The effect of lime and CO2 is the precipitation of insoluble calcium salts, the flocculation of colloidal components, the chemical degradation of other molecules such as invert sugar and amides, and the absorption of non-sugars on precipitated calcium carbonate. Lime and CO2 are normally produced in lime kilns by the thermal dissociation of limestone. Any non-sugar components contained in the raw sugar juice after extraction from the beet, make the subsequent stages in the sugar process impossible to perform. Therefore, the raw juice must be purified to allow further processing. This is achieved by continuously adding milk of lime and carbon dioxide from the lime kiln to precipitate most of the non-sugars. The product after filtration contains the calcium carbonate and the non-sugars and is used in agriculture as a liming material to improve the structure of arable soil and to regulate soil acidity. Sugar factory lime may also be used for site recovery, e.g. filling quarry ditches, and for producing bricks or cement. For aspects relating to lime kilns, see the “Cement and lime BREF” [219, EC, 2001]. 2.1.4.12 Carbonation (D.12) 2.1.4.12.1 Objective The aim of this process is to dissolve a quantity of carbonic gas into different products to obtain a gasified or carbonated final product. When dissolved in water, carbon dioxide (CO2), is sparingly soluble and thus, slowly released, forming bubbles that provide a characteristic mouthfeel and a unique taste when consumed. In addition to an organoleptic property, under suitable conditions, CO2 has a preserving property by the inhibition of the development of harmful aerobic micro-organisms. This, however, is not a substitute for other methods used to ensure microbiological safety. 2.1.4.12.2 Field of application Carbonation is an important process step in the preparation of many soft drinks and certain types of mineral waters. It is also applied in the wine and brewing industries. In the manufacture of still wines, carbonation is used to protect the colour and increase the aroma. 2.1.4.12.3 Description of techniques, methods and equipment Carbonation results from the impregnation of a liquid with CO2 to form carbonic acid. The CO2 was traditionally obtained from lime kilns, by heating calcium carbonate, but this has now been universally replaced in the soft drinks sector by the storage of bulk liquefied gas externally delivered by a CO2 supplier. The gas is stored within pressurised insulated tanks kept at a very low temperature. In common practice, the gas tends to be generated as a by-product of fermentation or chemical processes from companies outside of the soft drinks sector. A carbonator combines CO2 gas with the liquid to be carbonated. Current carbonators can be classified into two main categories; those that carbonate water only and those that carbonate the finished product mixture of syrup and water. These are sometimes coupled with coolers, often referred to as carbo-coolers. The principal designs available are carbonators with integral coolers, draining wall heat-exchangers and carbon dioxide injectors. In combination with this process, de-aeration, i.e. the removal of air, is vital and is usually applied to the water component in a first stage. The presence of air can create spoilage problems. CO2 is sometimes used to flush out air, however, the use of mechanically de-aerated water has become more popular in recent years. RHC/EIPPCB/FDM_BREF_FINAL January 2006 33
- Seite 42 und 43: 4.5.6.1 Waste water sludge treatmen
- Seite 44 und 45: 4.7.3.2 Dry cleaning...............
- Seite 46 und 47: 4.7.5.14.3 Minimise the production
- Seite 48 und 49: 4.7.9.8.2 Gradual discharge of clea
- Seite 50 und 51: List of figures Figure 2.1: Flow di
- Seite 52 und 53: Abbildung 4.66: Zweistufiges Trockn
- Seite 54 und 55: Table 3.39: Energy carrier and orde
- Seite 56 und 57: Tabelle 4.63: Wirksamkeit verschied
- Seite 59: GELTUNGSBEREICH RHC/EIPPCB/FDM_BREF
- Seite 62 und 63: Chapter 1 More detailed figures for
- Seite 64 und 65: Chapter 1 The top individual export
- Seite 66 und 67: Chapter 1 Traditionally, in many Eu
- Seite 69 und 70: 2 APPLIED PROCESSES AND TECHNIQUES
- Seite 71 und 72: 2.1.1.1.3 Description of techniques
- Seite 73 und 74: 2.1.1.4.2 Field of application Chap
- Seite 75 und 76: 2.1.2.2 Mixing/blending, homogenisa
- Seite 77 und 78: 2.1.2.4.3 Description of techniques
- Seite 79 und 80: 2.1.3.4 Centrifugation and sediment
- Seite 81 und 82: Chapter 2 The plate and frame filte
- Seite 83 und 84: 2.1.3.8.2 Field of application Chap
- Seite 85 und 86: Chapter 2 The process can also be c
- Seite 87 und 88: 2.1.4.2 Dissolving (D.2) 2.1.4.2.1
- Seite 89 und 90: Chapter 2 To start the process, bac
- Seite 91: Chapter 2 Dry brining/curing is app
- Seite 95 und 96: 2.1.5 Heat processing (E) 2.1.5.1 M
- Seite 97 und 98: Chapter 2 There are four types of o
- Seite 99 und 100: 2.1.5.7.3 Description of techniques
- Seite 101 und 102: 2.1.6 Concentration by heat (F) 2.1
- Seite 103 und 104: Chapter 2 Generally, as an integral
- Seite 105 und 106: 2.1.7 Processing by the removal of
- Seite 107 und 108: Chapter 2 The operating principle o
- Seite 109 und 110: 2.1.8.1.3 Description of techniques
- Seite 111 und 112: 2.1.8.2.2 Field of application Chap
- Seite 113 und 114: 2.1.9.2.2 Field of application Requ
- Seite 115 und 116: 2.1.9.3.3 Process water Chapter 2 I
- Seite 117 und 118: Chapter 2 The reciprocating pump, w
- Seite 119 und 120: Meat Fish Meat Potat o Fruit and ve
- Seite 121 und 122: 2.2.1 Meat and poultry Chapter 2 Be
- Seite 123 und 124: 2.2.1.1.2 Cutting (B.1) Chapter 2 F
- Seite 125 und 126: 2.2.1.2.3 Pickling (D.7) Chapter 2
- Seite 127 und 128: 2.2.1.3.2 Ageing (D.14) Chapter 2 H
- Seite 129 und 130: 2.2.2.3 Crustaceans Chapter 2 Once
- Seite 131 und 132: 2.2.3.2 Fruit juice Chapter 2 Fruit
- Seite 133 und 134: 2.2.3.6 Dried fruit Chapter 2 Dried
- Seite 135 und 136: 2.2.3.10 Heat treated and frozen ve
- Seite 137 und 138: Chapter 2 The neutralised oil is bl
- Seite 139 und 140: Chapter 2 In traditional production
- Seite 141 und 142: Chapter 2 UHT or sterilisation is u
2.1.4.11.3 Description of techniques, methods and equipment<br />
Chapter 2<br />
Carbonatation is the introduction of the milk of lime, calcium hydroxide, and carbon dioxide<br />
gas (CO2) into a liquid to form calcium carbonate and to precipitate and remove impurities. The<br />
effect of lime and CO2 is the precipitation of insoluble calcium salts, the flocculation of<br />
colloidal components, the chemical degradation of other molecules such as invert sugar and<br />
amides, and the absorption of non-sugars on precipitated calcium carbonate. Lime and CO2 are<br />
normally produced in lime kilns by the thermal dissociation of limestone.<br />
Any non-sugar components contained in the raw sugar juice after extraction from the beet, make<br />
the subsequent stages in the sugar process impossible to perform. Therefore, the raw juice must<br />
be purified to allow further processing. This is achieved by continuously adding milk of lime<br />
and carbon dioxide from the lime kiln to precipitate most of the non-sugars. The product after<br />
filtration contains the calcium carbonate and the non-sugars and is used in agriculture as a<br />
liming material to improve the structure of arable soil and to regulate soil acidity. Sugar factory<br />
lime may also be used for site recovery, e.g. filling quarry ditches, and for producing bricks or<br />
cement. For aspects relating to lime kilns, see the “Cement and lime BREF” [219, EC, 2001].<br />
2.1.4.12 Carbonation (D.12)<br />
2.1.4.12.1 Objective<br />
The aim of this process is to dissolve a quantity of carbonic gas into different products to obtain<br />
a gasified or carbonated final product. When dissolved in water, carbon dioxide (CO2), is<br />
sparingly soluble and thus, slowly released, forming bubbles that provide a characteristic<br />
mouthfeel and a unique taste when consumed. In addition to an organoleptic property, <strong>und</strong>er<br />
suitable conditions, CO2 has a preserving property by the inhibition of the development of<br />
harmful aerobic micro-organisms. This, however, is not a substitute for other methods used to<br />
ensure microbiological safety.<br />
2.1.4.12.2 Field of application<br />
Carbonation is an important process step in the preparation of many soft drinks and certain<br />
types of mineral waters. It is also applied in the wine and brewing industries. In the manufacture<br />
of still wines, carbonation is used to protect the colour and increase the aroma.<br />
2.1.4.12.3 Description of techniques, methods and equipment<br />
Carbonation results from the impregnation of a liquid with CO2 to form carbonic acid. The CO2<br />
was traditionally obtained from lime kilns, by heating calcium carbonate, but this has now been<br />
universally replaced in the soft drinks sector by the storage of bulk liquefied gas externally<br />
delivered by a CO2 supplier. The gas is stored within pressurised insulated tanks kept at a very<br />
low temperature. In common practice, the gas tends to be generated as a by-product of<br />
fermentation or chemical processes from companies outside of the soft drinks sector.<br />
A carbonator combines CO2 gas with the liquid to be carbonated. Current carbonators can be<br />
classified into two main categories; those that carbonate water only and those that carbonate the<br />
finished product mixture of syrup and water. These are sometimes coupled with coolers, often<br />
referred to as carbo-coolers. The principal designs available are carbonators with integral<br />
coolers, draining wall heat-exchangers and carbon dioxide injectors.<br />
In combination with this process, de-aeration, i.e. the removal of air, is vital and is usually<br />
applied to the water component in a first stage. The presence of air can create spoilage<br />
problems. CO2 is sometimes used to flush out air, however, the use of mechanically de-aerated<br />
water has become more popular in recent years.<br />
RHC/EIPPCB/FDM_BREF_FINAL January 2006 33