Integrierte Vermeidung und Verminderung der Umweltverschmutzung
Integrierte Vermeidung und Verminderung der Umweltverschmutzung Integrierte Vermeidung und Verminderung der Umweltverschmutzung
Chapter 3 3.2.36.2 Air emissions Steam/water vapour may be discharged to the air. Depending on the raw material being blanched, the exhaust air may contain low levels of VOCs, which may generate a low level of odour. 3.2.36.3 Solid output Some solid organic material may accumulate in the bottom of the blanchers. This needs to be removed periodically. 3.2.36.4 Energy Energy is used for heating the blanching water. 3.2.37 Cooking and boiling (E.3) 3.2.37.1 Water Waste water is generated during processing and cleaning and contains product residues. The waste water produced also contains dissolved organic material, SS, FOG, dissolved solids and possibly nitrate, nitrite, ammonia and phosphate. 3.2.37.2 Air emissions Emissions to air include odour and VOCs. 3.2.37.3 Solid output Solid output containing organic material and FOG may result from the cleaning of cooking equipment. 3.2.37.4 Energy Cooking and boiling uses energy to provide heat, e.g. for steam production. 3.2.38 Baking (E.4) 3.2.38.1 Water Waste water is produced which contains soluble organic material, SS and FOG. 3.2.38.2 Air emissions During baking, VOCs, odour and CO2 are emitted to the air together with water vapour. An example bakery with a production capacity of 340 tonnes per day has an air emission from the ovens containing ethanol, at a concentration of approximately 1 g/Nm 3 . The proposed UK environmental benchmark for the annual average release of ethanol is 0.0192 g/Nm 3 and the hourly mean benchmark is 0.576 g/Nm 3 [102, UK, 2002]. 3.2.38.3 Solid output Solid output is produced which contains organic material. Some residues may result from dry cleaning. 138 January 2006 RHC/EIPPCB/FDM_BREF_FINAL
3.2.38.4 Energy Chapter 3 Ovens are heated using either electrical energy or fuel in the form of natural gas or oil. For infrared ovens, special types of burners are applied. The energy usage for baking normally ranges from 0.125 – 0.167 kWh/kg of product (450 – 600 kJ/kg). 3.2.39 Roasting (E.5) 3.2.39.1 Water Small amounts of water are used for quenching, e.g. roasted coffee, cereals and chicory. This water is partly evaporated and emitted into the air and partly absorbed by the product, e.g. coffee. 3.2.39.2 Air emissions The outlet of both the roaster and the cooler contain odour components, CO2, NO2 and VOCs. The concentration of VOCs causing this odour is higher for the roaster outlet than for the cooler outlet. VOC levels are higher when the product is roasted to a higher degree, e.g. when the product temperature at the end of the roasting process is higher. The difference in emissions between a low roasted and a very high, i.e. very dark, roasted product can be as much as a factor 10. For batch roasters, the highest concentrations are emitted just before the end of the roasting process. In continuous roasters, the emissions are also continuous. The absolute level of VOCs depends on the product temperature at the end of the roasting; the amount of air used for roasting, which has a diluting effect; the product itself and the roasting time. The emissions of organic substances and the organic roasting losses result from the decomposition or chemical reaction of, e.g. chlorogenic acid, citric acid, oxalic acid, crude proteins and trigonellin. Nitrogen-based compounds, e.g. amines and sulphur-based compounds, e.g. mercaptans contribute considerably to the odours emitted by coffee roasting installations. In the raw gas, odorant contents of up to 300000 OU/Nm 3 have been measured. TOC mass concentrations of up to 10000 mg/Nm³ are produced. Ammonia, nitrogen oxides, carbon dioxide and carbon monoxide are also produced. Dust emissions may also be a problem. 3.2.39.3 Solid output Solid outputs include, e.g. the skins of coffee beans. For coffee, the solid output can be between 0.1 to 1.5 % of the amount of green coffee. 3.2.39.4 Energy The actual energy consumption depends on the type of roaster being used and also on the layout of the flue-gas system. 3.2.40 Frying (E.6) 3.2.40.1 Water Waste water arises from the cleaning of equipment and contains FOG, in the form of free fat and emulsified fat as well as other product residues. The waste water also contains SS, dissolved organic material and acid/alkali solutions. 3.2.40.2 Air emissions The air above a fryer is extracted to prevent emissions into the working environment. This exhaust air may contain VOCs, such as the breakdown products of the edible oil. Odour may also be an issue associated with the exhaust. RHC/EIPPCB/FDM_BREF_FINAL January 2006 139
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Chapter 3<br />
3.2.36.2 Air emissions<br />
Steam/water vapour may be discharged to the air. Depending on the raw material being<br />
blanched, the exhaust air may contain low levels of VOCs, which may generate a low level of<br />
odour.<br />
3.2.36.3 Solid output<br />
Some solid organic material may accumulate in the bottom of the blanchers. This needs to be<br />
removed periodically.<br />
3.2.36.4 Energy<br />
Energy is used for heating the blanching water.<br />
3.2.37 Cooking and boiling (E.3)<br />
3.2.37.1 Water<br />
Waste water is generated during processing and cleaning and contains product residues. The<br />
waste water produced also contains dissolved organic material, SS, FOG, dissolved solids and<br />
possibly nitrate, nitrite, ammonia and phosphate.<br />
3.2.37.2 Air emissions<br />
Emissions to air include odour and VOCs.<br />
3.2.37.3 Solid output<br />
Solid output containing organic material and FOG may result from the cleaning of cooking<br />
equipment.<br />
3.2.37.4 Energy<br />
Cooking and boiling uses energy to provide heat, e.g. for steam production.<br />
3.2.38 Baking (E.4)<br />
3.2.38.1 Water<br />
Waste water is produced which contains soluble organic material, SS and FOG.<br />
3.2.38.2 Air emissions<br />
During baking, VOCs, odour and CO2 are emitted to the air together with water vapour. An<br />
example bakery with a production capacity of 340 tonnes per day has an air emission from the<br />
ovens containing ethanol, at a concentration of approximately 1 g/Nm 3 . The proposed UK<br />
environmental benchmark for the annual average release of ethanol is 0.0192 g/Nm 3 and the<br />
hourly mean benchmark is 0.576 g/Nm 3 [102, UK, 2002].<br />
3.2.38.3 Solid output<br />
Solid output is produced which contains organic material. Some residues may result from dry<br />
cleaning.<br />
138 January 2006 RHC/EIPPCB/FDM_BREF_FINAL