Method and installation for the purification of exhaust gases, having a regenerative post-combustion installation

Patent metadata

Field	Value
Publication number	US-2016199779-A1
Application number	US-201414917227-A
Country	US
Kind code	A1
Filing date	Aug 5, 2014
Priority date	Sep 11, 2013
Publication date	Jul 14, 2016
Grant date	—

Abstract

Improved methods and systems for purifying exhaust gases using regenerative post-combustion systems help reduce operating problems and increase service life of such regenerative post-combustion systems. One such method may involve preheating an exhaust gas to be purified before feeding the exhaust gas into a regenerative post-combustion system. The exhaust gas may be preheated in at least one preheating stage to temperatures between 100° C. and 250° C., for instance, preferably between 100° C. and 200° C., and most preferably between 120° C. and 150° C. Moreover, one regenerative post-combustion system may include a preheating stage, two heat stores, and an oxidation zone disposed between the heat stores for oxidizing harmful constituents present in the exhaust gas.

First claim

1 .- 15 . (canceled)

16 . A method for purifying exhaust gas using a regenerative post-combustion system, the method comprising:
preheating the exhaust gas that is to be purified at least in part in a preheating stage to temperatures between 100 degrees Celsius and 250 degrees Celsius; and feeding the preheated exhaust gas into the regenerative post-combustion system.

17 . The method of claim 16 further comprising:
heating the exhaust gas alternately in at least one of a first heat store and a second heat store of the post-combustion system;
oxidizing harmful constituents in the exhaust gas in an oxidation zone of the post-combustion system; and
removing a resultant purified exhaust gas via one of the first and second heat stores.

18 . The method of claim 16 wherein the preheating of the exhaust gas comprises preheating the exhaust gas to be purified with a heat exchanger.

19 . The method of claim 18 further comprising transferring heat of a hot gas stream using a heat transfer medium in the heat exchanger at least in part to the exhaust gas to be purified, wherein a temperature of the hot gas stream is greater than a temperature of the exhaust gas to be purified before preheating.

20 . The method of claim 18 further comprising transferring heat of a hot gas stream in the heat exchanger to the exhaust gas to be purified, wherein a temperature of the hot gas stream is greater than a temperature of the exhaust gas to be purified before preheating.

21 . The method of claim 20 wherein the hot gas stream comprises at least in part a resultant purified exhaust gas from the regenerative post-combustion system.

22 . The method of claim 16 wherein the exhaust gas to be purified is at least in part an exhaust gas from at least one of a cement industry or a mineral industry.

23 . The method of claim 16 wherein the preheating of the exhaust gas comprises preheating the exhaust gas to be purified with a burner in the preheating stage.

24 . The method of claim 23 further comprising inputting an amount of fuel fed by way of the burner such that no further fuel or a corresponding reduced amount of fuel need be inputted in the regenerative post-combustion system.

25 . The method of claim 16 wherein the preheating stage is configured as a combustion chamber.

26 . The method of claim 25 further comprising inputting an amount of fuel fed by way of the combustion chamber such that no further fuel or a corresponding reduced amount of fuel need be inputted in the regenerative post-combustion system.

27 . The method of claim 16 further comprising reducing at least one of carbon monoxide, hydrocarbons, or nitrogen oxides in the regenerative post-combustion system.

28 . A system for purifying exhaust gas according to the method of claim 16 , the system comprising a regenerative post-combustion system and a preheating stage upstream of the regenerative post-combustion system.

29 . A system for purifying exhaust gas, the system comprising:
a preheating stage in which the exhaust gas that is to be purified is preheated at least in part to temperatures between 100 degrees Celsius and 250 degrees Celsius; and a regenerative post-combustion system downstream of the preheating stage, the regenerative post-combustion system comprising:
a first heat store,
a second heat store, and
an oxidation zone disposed between the first and second heat stores.

30 . The system of claim 29 wherein the first and second heat stores are configured to at least one of reduce nitrogen oxides or oxidize hydrocarbons at least in part with catalytically active material.

31 . The system of claim 29 wherein the upstream preheating stage comprises at least one of a heat exchanger, a burner, or a combustion chamber.

32 . The system of claim 29 wherein the preheating stage consists of a combination of at least one heat exchanger and at least one combustion chamber.

Assignees

• Thyssenkrupp Ind Solutions Ag

Inventors

• Rohloff Kathrin
• Flasspöhler Melanie
• Stender Timo

Classifications

• B01D53/8646

  Simultaneous elimination of the components (B01D53/8656 takes precedence) · CPC title

• B01D2258/0233

  from cement factories · CPC title

• B01D53/72

  Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons · CPC title

• F27B7/20

  Details, accessories or equipment specially adapted for rotary-drum furnaces · CPC title

• B01D53/56

  Nitrogen oxides (B01D53/60 takes precedence) · CPC title