Integrierte Vermeidung und Verminderung der Umweltverschmutzung
Integrierte Vermeidung und Verminderung der Umweltverschmutzung Integrierte Vermeidung und Verminderung der Umweltverschmutzung
Chapter 3 3.2.29.4 Energy Energy is supplied as steam and electricity. Total energy consumption is between 110 to 280 kWh/t product (400 and 1000 MJ/t). 3.2.29.5 Noise Noise issues may arise from cooling towers, compressors or vacuum systems. 3.2.30 Sulphitation (D.10) 3.2.30.1 Air emissions A substance of environmental concern is SO2, however, it is readily absorbed by the liquid to be treated, e.g. wine, and actual residual emissions are extremely low. 3.2.31 Carbonatation (D.11) 3.2.31.1 Air emissions Excess CO2 is vented to the air. If a limekiln is used, then there is CO emitted due to the inevitable incomplete combustion within the kiln. SO2 and NOx combustion products also occur and are vented to the air accompanied by small amounts of dust. Lime hydrators, used in conjunction with kilns, will also emit small quantities of dust. There is usually an over-pressure vent on the kiln. The normal kiln exhaust gases are washed before being introduced in the process. Exhaust gases and vapours from the carbonatation vessels contain NH3, CO and other malodorous compounds. 3.2.31.2 Solid output Any precipitate formed during the carbonatation is separated out from the sugar juice and is sometimes sent for landspreading. Residues from lime production and hydrating are sent to landfill or, e.g. used for road paving or road foundations. 3.2.31.3 Noise If a limekiln is used, then the charging of limestone and coke may produce noise off site. 3.2.32 Carbonation (D.12) 3.2.32.1 Air emisssions There is risk of accidental releases of CO2. 3.2.32.2 Energy Energy is required to operate heat-exchangers and coolers. 3.2.33 Coating/spraying/enrobing/agglomeration/encapsulation (D.13) 3.2.33.1 Water Waste water is produced from the cleaning of the equipment. This will contain product residues consisting of dissolved organic material, SS and FOG. 136 January 2006 RHC/EIPPCB/FDM_BREF_FINAL
3.2.33.2 Air emissions Odour is produced. 3.2.33.3 Solid output Solid output is produced which contains organic and inorganic material. 3.2.34 Ageing (D.14) 3.2.34.1 Water Chapter 3 Water is used for cleaning and this generates waste water which contains soluble organic material and SS. 3.2.34.2 Air emissions Emissions to air include odour and VOCs. 3.2.34.3 Solid output Solid output is produced which contains organic material. Waste from packaging may also be produced. 3.2.35 Melting (E.1) 3.2.35.1 Water Waste water is generated during cleaning. This waste water generally has a high BOD level and may contain SS and FOG. 3.2.35.2 Air emissions Odour emissions may occur in the dry melting process of meat residues, for example. 3.2.35.3 Solid output In some melting processes, a solid phase remains. This is considered to be a by-product. 3.2.35.4 Energy In the melting process, the use of steam is the main energy component. 3.2.36 Blanching (E.2) 3.2.36.1 Water The leaching of sugars, starches and other soluble organic compounds from the raw fruit or vegetables into the blanching water results in high BOD, SS and dissolved solids levels. As blanching water is normally re-used/recycled, the volume of waste water from blanching is normally relatively small. However, this tends to concentrate pollutants in the waste water. RHC/EIPPCB/FDM_BREF_FINAL January 2006 137
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Chapter 3<br />
3.2.29.4 Energy<br />
Energy is supplied as steam and electricity. Total energy consumption is between<br />
110 to 280 kWh/t product (400 and 1000 MJ/t).<br />
3.2.29.5 Noise<br />
Noise issues may arise from cooling towers, compressors or vacuum systems.<br />
3.2.30 Sulphitation (D.10)<br />
3.2.30.1 Air emissions<br />
A substance of environmental concern is SO2, however, it is readily absorbed by the liquid to be<br />
treated, e.g. wine, and actual residual emissions are extremely low.<br />
3.2.31 Carbonatation (D.11)<br />
3.2.31.1 Air emissions<br />
Excess CO2 is vented to the air. If a limekiln is used, then there is CO emitted due to the<br />
inevitable incomplete combustion within the kiln. SO2 and NOx combustion products also occur<br />
and are vented to the air accompanied by small amounts of dust. Lime hydrators, used in<br />
conjunction with kilns, will also emit small quantities of dust. There is usually an over-pressure<br />
vent on the kiln. The normal kiln exhaust gases are washed before being introduced in the<br />
process. Exhaust gases and vapours from the carbonatation vessels contain NH3, CO and other<br />
malodorous compo<strong>und</strong>s.<br />
3.2.31.2 Solid output<br />
Any precipitate formed during the carbonatation is separated out from the sugar juice and is<br />
sometimes sent for landspreading. Residues from lime production and hydrating are sent to<br />
landfill or, e.g. used for road paving or road fo<strong>und</strong>ations.<br />
3.2.31.3 Noise<br />
If a limekiln is used, then the charging of limestone and coke may produce noise off site.<br />
3.2.32 Carbonation (D.12)<br />
3.2.32.1 Air emisssions<br />
There is risk of accidental releases of CO2.<br />
3.2.32.2 Energy<br />
Energy is required to operate heat-exchangers and coolers.<br />
3.2.33 Coating/spraying/enrobing/agglomeration/encapsulation (D.13)<br />
3.2.33.1 Water<br />
Waste water is produced from the cleaning of the equipment. This will contain product residues<br />
consisting of dissolved organic material, SS and FOG.<br />
136 January 2006 RHC/EIPPCB/FDM_BREF_FINAL