Method for operating a surface treatment plant
A method for operating a surface treatment plant, resulting overspray in a coating booth is taken up by an air flow. The air flow loaded with overspray is conveyed as exhaust air flow to at least one separation unit in which overspray is separated out. In a supply region upstream of the at least one separation unit and/or in an internal space of the at least one separation unit, a filter aid having a separation aggregate state is added to the exhaust air flow and forms, with the overspray, a separation mixture which is separated in or at the at least one separation unit. The filter aid used is solid or liquid in the separation aggregate state. In the at least one separation unit, conditions are established in which the filter aid transitions from the separation aggregate state into a gaseous aggregate state such that the gaseous filter air can separate from the separation mixture.
1. A method for operating a surface treatment plant comprising the steps of:
a) absorbing overspray, which occurs in a coating booth, in an airflow;
b) conducting the overspray-laden airflow as exhaust airflow to at least one separation unit in which the overspray is separated out;
c) feeding a filtration aid material, which features a separation aggregate state, to the exhaust airflow in a feed region upstream of the at least one separation unit and/or in an interior of the at least one separation unit, which filtration aid material forms with the overspray a separation mixture which is deposited in or on the at least one separation unit,
wherein
d) the filtration aid material is solid or liquid in the separation aggregate state; and
e) conditions are created in the at least one separation unit in which the filtration aid material undergoes a phase change and changes from the separation aggregate state into a gaseous aggregate state so that the gaseous filtration aid material can be separated from the separation mixture and reduce the amount of filtration aid material deposited on the at least one separation unit.
2. The method as claimed in claim 1 , wherein the at least one separation unit is designed as a disposable separation unit and after reaching a limit loading is exchanged as a laden disposable separation unit for an empty disposable separation unit.
3. The method as claimed in claim 1 , wherein use is made of a filtration aid material which can be atomized or nebulized.
4. The method as claimed in claim 1 , wherein a powder material is used as filtration aid material.
5. The method as claimed in claim 1 , wherein the filtration aid material comprises one or more of the following materials: liquefiable gases, especially carbon dioxide, nitrogen, air, oxygen, hydrogen, natural gases and also hydrocarbons; compounds which during normal conditions have an increased saturated water vapor pressure of over 10 hPa, especially alcohols, propellants or refrigerants; compounds which at temperatures of up to 150° C. have a saturated water vapor pressure of over 10 hPa, especially water or glycols.
6. The method as claimed in claim 1 , wherein a material which can be statically charged is used as filtration aid material.
7. The method as claimed in claim 5 , wherein the compounds during normal conditions have an increased saturated water vapor pressure over 100 hPa; and the compounds which at temperatures of up to 150° C. have a saturated water vapor pressure over 100 hPa.