Method for the removal and disposal of paint solvent

Claim 2

In an industrial painting system including a spray booth and a bake oven, a method for the removal and disposal of the paint solvent contained in the spray booth exhaust gas discharged from the spray booth comprising, (a) passing solvent laden exhaust gas from said spray booth through a filter capable of adsorbing said solvent from said spray booth exhaust to remove said solvent from said exhaust; (b) degassing said filter by passing through said filter a gas such that the pressure drop across said filter is less than about six inches of water, said gas having a velocity and temperature sufficient to remove said solvent from said filter such that the solvent concentration in the gas exhausted from the filter does not exceed the lower explosive limit for the solvent; (c) introducing said filter exhaust to said bake oven to increase the solvent concentration in the bake oven atmosphere; said degassing gas velocity and temperature being so selected that upon introduction of said filter exhaust to said bake oven, the solvent concentration in the bake oven does not exceed the lower explosive limit of the designed theoretical level of operation of the brake oven; (d) removing a portion of the atmosphere of the bake oven from the bake oven and incinerating said bake oven atmosphere so as to oxidize said solvent to non-polluting combustion products and thereby dispose of said solvent.

Claim 3

The method of claim 1 wherein said bake oven atmosphere is incinerated in a washer having a burner, and whereby the solvent provides a supplement to the fuel requirement of the burner.

Claim 4

The method of claim 1 wherein said industrial painting system includes a drying oven suitable for drying a wet work piece and the gas for degassing the filter is provided by the exhaust from said drying oven.

Claim 5

The method of claim 1 wherein said degassing gas temperature is in the range of from about 100° F. to about 280° F.

Claim 6

The method of claim 1 wherein said filter is activated carbon.

Claim 7

The method of claim 1 wherein the flow of said degassing gas is co-current with said adsorption flow.

Claim 8

The method of claim 1 wherein the flow of said degassing gas is counter-current to said adsorption flow.

Claim 9

In an industrial painting system comprising a washer having a burner, a dry-off oven, a spray booth and a bake oven, a method for the removal and disposal of the paint solvent contained in the spray booth exhaust gas discharged from the spray booth, comprising passing solvent laden exhaust from said spray booth through a solvent concentrating means to remove solvent from said exhaust and to concentrate said solvent, removing the solvent from said concentrating means by passing through said concentrating means a gas such that the pressure drop across said concentrating means is less than about six inches of water, said gas having a velocity and a temperature sufficient to remove said solvent to form a solvent laden gas such that the solvent concentration in said solvent laden gas does not exceed the lower explosive limit for the solvent, introducing said solvent laden gas to the bake oven to increase the solvent concentration in the bake oven atmosphere said gas velocity and temperature being so selected that upon introduction of said solvent laden gas to said bake oven the solvent concentration in the bake oven does not exceed the lower explosive limit of the designed theoretical level of operation of the bake oven, introducing a portion of the solvent laden atmosphere of the bake oven to the burner of the washer to incinerate the solvent, and passing the gasses produced by the incineration of the solvent to the dry-off oven to form the atmosphere of the dry-off oven.

Claim 10

In an industrial painting system comprising a washer having a burner, a dry-off oven, a spray booth and a bake oven, a method for the removal and disposal of the paint solvent contained in the spray booth exhaust gas discharged from the spray booth, comprising passing solvent laden exhaust from said spray booth through a solvent concentrating means to remove solvent from said exhaust and to concentrate said solvent, removing the solvent from said concentrating means by passing through said concentrating means a gas such that the pressure drop across said concentrating means is less than about six inches of water, said gas having a velocity and a temperature sufficient to remove said solvent to form a solvent laden gas such that the solvent concentration in said solvent laden gas does not exceed the lower explosive limit for the solvent, introducing said solvent laden gas to the bake oven to increase the solvent concentration in the bake oven atmosphere said gas velocity and temperature being so selected that upon introduction of said solvent laden gas to said bake oven the solvent concentration in the bake oven does not exceed the lower explosive limit of the designed theoretical level of operation of the bake oven, introducing a portion of the solvent laden atmosphere of the bake oven to the burner of the washer to incinerate the solvent, and passing the gasses produced by the incineration of the solvent to the dry-off oven to form the atmosphere of the dry-off oven.

Claim 11

The method of claim 8 wherein the solvent concentrating means is an activated carbon filter.

Claim 12

The method of claim 9 wherein the gas passing through said filter has a temperature of from about 100° F. to about 280° F.

Claim 13

The method of claim 9 wherein the gas passing through said filter to remove solvent is co-current with the solvent concentrating flow.

Claim 14

The method of claim 9 wherein the gas passing through said filter to remove solvent is countercurrent to said solvent concentrating flow.

Claim 15

The method of claim 8 wherein at least a portion of the dry-off oven atmosphere is passed to said solvent concentrating means to remove solvent therefrom.