Apparatus and method for thermal exhaust gas purification

Patent metadata

Field	Value
Publication number	US-10429066-B2
Application number	US-201715622333-A
Country	US
Kind code	B2
Filing date	Jun 14, 2017
Priority date	Dec 22, 2014
Publication date	Oct 1, 2019
Grant date	Oct 1, 2019

Abstract

An apparatus for thermal exhaust gas purification includes at least one thermal reactor to which a raw gas to be purified is supplied and in which the supplied raw gas is thermally purified, and an energy recovery apparatus to which a gas purified in the thermal reactor is supplied via at least one outlet line. For improving the balance of energy, it is proposed that the energy recovery apparatus includes at least one condensation heat exchanger in which the purified gas is cooled down such that condensable substances contained in the purified gas condense, and enthalpies released thereby are transmitted to a heat exchange medium and/or the raw gas upstream of the thermal reactor.

First claim

The invention claimed is:

1. An apparatus for thermal exhaust gas purification, comprising:
a thermal reactor connected to a raw gas supply line for supplying a raw gas to the thermal reactor and comprising a combustion chamber for thermally purifying the supplied raw gas; and
an energy recovery means connected to said combustion chamber of said thermal reactor via an outlet line for supplying a purified gas resulting from the thermal purification process in said combustion chamber to said energy recovery means,
wherein said energy recovery means comprises:
a first heat exchanger for cooling down the purified gas to a first temperature level and transmitting an enthalpy released thereby to a heat exchange medium; and
at least one condensation heat exchanger arranged downstream of said first heat exchanger for further cooling down the purified gas to a second temperature level lower than the first temperature level such that condensable substances contained in the purified gas condense and enthalpies released thereby are transmitted to a heat exchange medium and/or the raw gas upstream of said thermal reactor.

2. The apparatus according to claim 1 , wherein said further heat exchanger and said condensation heat exchanger are in heat exchange with a common heat exchange medium circuit, wherein said condensation heat exchanger is arranged upstream of said further heat exchanger in said common heat exchange medium circuit.

3. The apparatus according to claim 1 , wherein said further heat exchanger is in heat exchange with a first heat exchange medium circuit, and said condensation heat exchanger is in heat exchange to a second heat exchange medium circuit being separate from said first heat exchange medium circuit.

4. The apparatus according to claim 1 , wherein said further heat exchanger is in heat exchange with a first heat exchange medium circuit, and said condensation heat exchanger is in heat exchange with a raw gas supply line upstream of said thermal reactor.

5. The apparatus according to claim 1 , wherein a further condensation heat exchanger being in heat exchange with a raw gas supply line upstream of said thermal reactor is provided downstream of said further heat exchanger in said common heat exchange medium circuit.

6. The apparatus according to claim 1 , wherein there is provided a first heat exchange medium circuit being in heat exchange with said further heat exchanger or a common heat exchange medium circuit being in heat exchange both with said further heat exchanger and said condensation heat exchanger, and a power generating device is arranged downstream of said further heat exchanger in said common heat exchange medium circuit or said first heat exchange medium circuit.

7. The apparatus according to claim 3 , wherein at least one device selected from a hot water consumer, a district heating terminal and an RC or ORC system is arranged downstream of said condensation heat exchanger in said second heat exchange medium circuit.

8. The apparatus according to claim 1 , wherein a condensate generated in said condensation heat exchanger is recycled to the process via a condensate drain.

9. The apparatus according to claim 1 , wherein said thermal reactor is a thermal oxidation reactor, preferably a regenerative thermal oxidation reactor.

10. The apparatus according to claim 1 , wherein said raw gas is one of a mine exhaust gas, in particular a Ventilation Air Methane or a mixture of Ventilation Air Methane and Coal Mine Methane, and an exhaust gas containing combustible constituents, in particular containing VOC.

11. The apparatus according to claim 1 , wherein said raw gas is a raw gas containing liquid drops.

12. A method for thermal exhaust gas purification, comprising the steps of:
thermally purifying a raw gas to be purified in a combustion chamber of a thermal reactor;
cooling down a purified gas produced during the thermal purification process in said combustion chamber to a first temperature level in a first heat exchanger, wherein an enthalpy released thereby is transmitted to a heat exchange medium; and
further cooling down the purified gas in a condensation heat exchanger downstream of said first heat exchanger to a second temperature level lower than the first temperature level such that condensable substances contained in the purified gas condense and enthalpies released thereby are transmitted to a heat exchange medium and/or the raw gas upstream of said thermal reactor.

13. The method according to claim 12 , wherein said further heat exchanger and said condensation heat exchanger are in heat exchange with a common heat exchange medium circuit, and the heat exchange medium of said common heat exchange medium circuit is preheated in said condensation heat exchanger.

14. The method according to claim 12 , wherein said further heat exchanger is in heat exchange with a first heat exchange medium circuit, and said condensation heat exchanger is in heat exchange with a second heat exchange medium circuit being separate from said first heat exchange medium circuit.

15. The method according to claim 12 , wherein said further heat exchanger is in heat exchange with a first heat exchange medium circuit, and said condensation heat exchanger is in heat exchange with a raw gas supply line upstream of said thermal reactor.

16. The method according to claim 12 , wherein a further condensation heat exchanger being in heat exchange with a raw gas supply line upstream of said thermal reactor is provided downstream of said further heat exchanger in said common heat exchange medium circuit.

17. The method according to claim 12 , wherein the heat exchange medium heated in said further heat exchanger is used for generating electricity.

18. The method according to claim 14 , wherein the heat exchange medium of said second heat exchange medium circuit is a process water or a heating medium.

19. The method according to claim 12 , wherein a condensate generated in said condensation heat exchanger is recycled to the process via a condensate drain.

20. The method according to claim 12 , wherein said raw gas is one of a mine exhaust gas, in particular a Ventilation Air Methane or a mixture of Ventilation Air Methane and Coal Mine Methane, and an exhaust gas containing combustible constituents, in particular containing VOC.

21. The method according to claim 12 , wherein said raw gas is a raw gas containing liquid drops.

Assignees

• Duerr Systems Ag

Inventors

• Schröter Martin
• Rieder Erhard

Classifications

• F23G7/068

  using regenerative heat recovery means · CPC title

• Y02E20/12

  Heat utilisation in combustion or incineration of waste · CPC title

• F25J2260/02

  Integration in an installation for exchanging heat, e.g. for waste heat recovery · CPC title

• F01K11/02

  the engines being turbines · CPC title

• F23G7/066 Primary

  preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator · CPC title