Method and regenerative separating apparatus for separating contaminants from process exhaust air

Patent metadata

Field	Value
Publication number	US-10286354-B2
Application number	US-201515510452-A
Country	US
Kind code	B2
Filing date	Sep 8, 2015
Priority date	Sep 12, 2014
Publication date	May 14, 2019
Grant date	May 14, 2019

Abstract

A method for separating organic solvents from solvent-containing process exhaust air, where the process exhaust air is directed through a separation zone of a separating device, and the separating device is regenerated by passing a regeneration stream through a regeneration zone of the separating device. The regeneration stream passing through the separating device is divided into a first partial stream having an impurity concentration less than a first predetermined limit, and a second partial stream having an impurity concentration equal or greater than a second predetermined limit, by a divider, where the second predetermined limit is equal to or greater than the first predetermined limit, to return the first partial stream generated during regeneration to the separating device and direct the second partial stream generated during regeneration to a cleaning device.

First claim

The invention claimed is:

1. A method for separating impurities from process exhaust air, comprising the steps of:
passing a process exhaust air through a separating device;
regenerating said separating device by passing a regeneration stream therethrough;
dividing said regeneration stream passing through said separating device during regeneration into a first partial stream having an impurity concentration less than a first predetermined limit, and a second partial stream having an impurity concentration equal to or greater than a second pre-determined limit, said second predetermined limit being equal to or greater than said first predetermined limit;
returning said first partial stream generated during regeneration to said separating device; and
directing said second partial stream generated during regeneration to a cleaning device,
wherein at least one of a flow amount of said first partial stream generated during regeneration, and a ratio of the flow amount of said first partial stream generated during regeneration to the flow amount of said second partial stream generated during regeneration, are controlled variably.

2. The method according to claim 1 , wherein said first partial stream generated during regeneration is fed into said process exhaust air upstream of said separating device.

3. The method according to claim 1 , wherein said separating device is cooled between the regeneration and the next cleaning of the process exhaust air by a cooling air flow, and said first partial stream generated during regeneration is fed into said cooling air flow upstream of said separating device.

4. The method according to claim 1 , further comprising a further partial stream branched off from said second partial stream generated during regeneration and returned to said separating device.

5. The method according to claim 4 , wherein the branched-off further partial stream flow is fed into at least one of said first partial stream, said process exhaust air and said regeneration stream.

6. The method according to claim 1 , wherein said separating device is operated continuously.

7. A regenerative separating device for separating impurities from process exhaust air, comprising:
a port for introducing a process exhaust air;
a separation unit for receiving the impurities from said process exhaust air introduced into said separating device;
a port for discharging clean air;
a port for introducing a regeneration stream;
a divider configured for dividing said regeneration stream passed through said separation unit into a first partial stream having an impurity concentration less than a first predetermined limit, and a second partial stream having an impurity concentration equal to or greater than a second pre-determined limit, wherein said second predetermined limit is equal to or greater than said first predetermined limit;
a port for discharging said first partial stream; and
a port for discharging said second partial stream,
wherein said divider is configured to variably control a flow amount of said first partial stream.

8. The separation device according to claim 7 , wherein said separation unit is designed as a rotor whose end faces are continuously loaded by said process exhaust air and said regeneration stream.

9. The separating device according to claim 8 , further comprising a sector-shaped separation zone and a sector-shaped regeneration zone, wherein said separation zone and said regeneration zone do not overlap each other, and said divider divides said regeneration zone into a first subzone and a second subzone in a direction of rotation of said separation unit.

10. The separating device according to claim 7 , further comprising a port for introducing a cooling air flow and a port for discharging said cooling air flow after passing through said separation unit.

11. A system for separating impurities from process exhaust air, comprising:
a regenerative separating device according to claim 7 ; and
a cleaning device for extracting the impurities from said second partial stream generated during a regeneration process of said separating device.

12. The system according to claim 11 , further comprising a flow line for returning said first partial stream generated during a regeneration process to said separating device.

13. The system according to claim 11 , further comprising a flow controller for branching off a further partial stream from said second partial stream generated during a regeneration process, and at least one flow line for returning said further partial stream to said separating device.

14. The system according to claim 11 , wherein said cleaning device is configured for regenerative thermal oxidation (RTO), direct thermal oxidation (TO), recuperative catalytic oxidation (CO), regenerative catalytic oxidation (RCO), condensation or comprises a gas turbine aggregate having a combustion apparatus for combusting the combustible components of said second partial stream.

Assignees

• Duerr Systems Ag

Inventors

• Herm Enrico
• Rieder Erhard
• Eichhorn Christian

Classifications

• B01D2257/708

  Volatile organic compounds V.O.C.'s · CPC title

• B01D2257/704

  Solvents not covered by groups B01D2257/702 - B01D2257/7027 · CPC title

• B01D2253/102

  Carbon · CPC title

• B01D53/0446 Primary

  Means for feeding or distributing gases · CPC title

• B01D2253/108

  Zeolites · CPC title