MORELLO BRADLEY DOUGLAS (US)
SHELL OIL CO (US)
| WO2001051182A1 | 2001-07-19 | |||
| WO2005110582A1 | 2005-11-24 | |||
| WO2015014863A1 | 2015-02-05 |
| US8420036B1 | 2013-04-16 | |||
| JP2007154819A | 2007-06-21 | |||
| US7824636B1 | 2010-11-02 | |||
| DE102010022775A1 | 2011-12-08 | |||
| US20050137082A1 | 2005-06-23 | |||
| US7294321B2 | 2007-11-13 | |||
| US5171553A | 1992-12-15 | |||
| US5705136A | 1998-01-06 | |||
| US6419889B1 | 2002-07-16 |
CATALYSIS COMMUNICATIONS, vol. 4, 2003, pages 505 - 509
| C L A I M S 1. A process for the treatment of a NOx-containing gas stream, said NOx-containing gas stream containing N02 and NO in a molar ratio of N02:NO of at least 1:1, to remove at least a portion of the NOx contained therein, said process comprising: i) providing an additional gas stream comprising NO to the ΝΟχ-containing gas stream, such that the molar ratio of N02:NO in the ΝΟχ-containing gas stream is reduced to be less than 1:1; and ii) then passing the ΝΟχ-containing gas stream through a catalyst bed comprising a deNOx catalyst under suitable conditions to reduce the level of NOx in the gas stream and thus produce a deNOx treated gas stream, said deNOx treated gas stream containing a reduced amount of NOx. 2. A process as claimed in Claim 1 wherein the NOx- containing gas stream is derived from the exhaust gas stream from a process for the production of nitric acid. 3. A process for the treatment of a N20- and NOx- containing gas stream to remove at least a portion of each of the NOx and the N20 contained therein, said process comprising: i) passing the N20- and ΝΟχ-containing gas stream through a catalyst bed comprising a deN20 catalyst under suitable conditions to reduce the level of N20 in said N20- and ΝΟχ-containing gas stream and thus produce a deN20-treated gas stream, said deN20-treated gas stream containing a reduced amount of N20; ii) taking at least a portion of said deN20-treated gas stream to provide a ΝΟχ-containing gas stream; and iii) passing at least a portion of said ΝΟχ-containing iv) gas stream through a catalyst bed comprising a deNOx catalyst under suitable conditions to reduce the level of ΝΟχ in the deN20-treated gas stream and thus produce a deNOx-treated gas stream, said deNOx-treated gas stream containing a reduced amount of NOx; v) wherein an additional gas stream comprising NO is provided to either or both of the N20- and NOx-containing gas stream and the NOx-containing gas stream, such that the ratio of N02:NO in the NOx-containing gas stream is less than 1:1. 4. A process as claimed in Claim 3, wherein the molar ratio of N02:NO in the N20- and NOx-containing gas stream, before any introduction of the additional gas stream comprising NO is at least 1:1. 5. A process as claimed in Claim 3 or Claim 4, wherein the N20- and NOx-containing gas stream is derived from the exhaust gas stream from a process for the production of nitric acid 6. A process as claimed in any one of Claims 1 to 5, wherein the N02 content of the NOx-containing gas stream is in the range of from 500 to lOOOOppmv. 7. A process as claimed in any one of Claims 1 to 6, wherein the NO content of the NOx-containing gas stream is in the range of from 500 to lOOOOppmv. 8. A process as claimed in any one of Claims 3 to 7, wherein the N20 content of the N20- and NOx-containing gas stream is in the range of from 500 to lOOOOppmv. 9. A process as claimed in any one of Claims 1 to 8, wherein the deNOx catalyst comprises a titania carrier and one or more metal compounds which metals are selected from the group consisting of vanadium, molybdenum and tungsten . 10. A process as claimed in any one of Claims 2 to 9, wherein the NOx-containing gas stream is derived from the exhaust gas stream from a nitric acid plant and the additional gas stream is formed from at least a portion of an outlet stream from the ammonia burner in such a process . 11. A process as claimed in any one of Claims 5 to 9, wherein the N20 and NOx-containing gas stream is derived from the exhaust gas stream from a nitric acid plant and the additional gas stream is formed from at least a portion of an outlet stream from the ammonia burner in such a process . |
Field of the Invention
The invention relates to an improved process for the removal of NO x from exhaust gases.
Background of the Invention
Oxides of nitrogen are common by-products and/or desirable intermediates in a number of industrial processes, including the manufacture of chemicals, such as nitric acid, or combustion processes in air. Nitrogen oxides of the formula NO and N0 2 are typically referred to together as NO x . NO x is a large scale pollutant and significant efforts have been made for the reduction of ΝΟχ in exhaust gas streams from processes in which they are produced. Processes for removal of NO x from gas streams are generally referred to in the art as DeNO x processes and the catalysts used therein as DeNO x catalysts .
One process used for the removal of NO x from gas streams is the selective catalytic reduction (SCR) process. One version of this process is disclosed in US7294321. In this selective catalytic reduction process, a combustion gas that contains a concentration of NO x and ammonia (NH 3 ) , which is typically added to the combustion gas as a reactant, is contacted with a catalyst that promotes the reduction reaction in which the NO x reacts with ammonia and oxygen to yield nitrogen and water.
Nitrous oxide (N 2 0) is a greenhouse gas and is considered to be a greater contributor to climate change by weight than carbon dioxide. In many countries limits on nitrous oxide emissions have been set and efforts have been focussed on developing methods to remove nitrous oxide from exhaust gases. Many of these efforts have focussed on identifying catalysts suitable for use in the catalytic decomposition of nitrous oxides. Processes for removal of N 2 0 from gas streams are generally referred to in the art as DeN 2 0 processes and the catalysts used therein as DeN 2 0 catalysts.
Zeolite-supported iron catalysts, optionally also containing a noble metal such as Pt or Ru, have been described, for example in US5171553, WO2005110582 and
Journal of Catalysis 243 (2006), 340-349. Other known nitrous oxide decomposition catalysts include those based on base metal oxides such as Co 3 0 4 , as described in
US5705136 and Catalysis Communications 4 (2003) 505-509. A bulk metal oxide catalyst for the removal of nitrous oxide from waste gas is described in WO2015014863.
It is considered advantageous to be able to treat a gas stream containing both NO x and N 2 0 in order to reduce the amounts of both NO x and minimise N 2 0 in the treated gas stream. This may be carried out by subjecting said gas stream to a DeN 2 0 process in the presence of a DeN 2 0 catalyst and then subjecting the resultant stream to a DeNOx process in the presence of a DeNO x catalyst.
However, competing reactions occur in these
processes which may reduce their efficiency in producing a treated stream low in both NO x and N 2 0. For example, treatment of a NO x -containing stream which is N0 2 -rich (containing more N0 2 than NO on a molar basis) over a DeNOx catalyst may result in the formation of N 2 0.
It would be desirable to provide a robust process for the reduction of NO x from NO x -containing streams, in which the level of N 2 0 in the treated stream is also minimised . Summary of the Invention
Accordingly, the present invention provides a process for the treatment of a NO x -containing gas stream, said ΝΟχ-containing gas stream containing N0 2 and NO in a molar ratio of N0 2 :NO of at least 1:1, to remove at least a portion of the NO x contained therein, said process comprising :
i) providing an additional gas stream comprising NO to the ΝΟχ-containing gas stream, such that the molar ratio of N0 2 :NO in the NO x -containing gas stream is reduced to be less than 1:1; and
ii) then passing the ΝΟχ-containing gas stream through a catalyst bed comprising a deNO x catalyst under suitable conditions to reduce the level of NO x in the gas stream and thus produce a deNO x treated gas stream, said deNO x treated gas stream containing a reduced amount of NO x .
The present invention also provides a process for the treatment of a N 2 0- and NO x -containing gas stream to remove at least a portion of each of the NO x and the N 2 0 contained therein, said process comprising:
i) passing the N 2 0- and NO x -containing gas stream through a catalyst bed comprising a deN 2 0 catalyst under suitable conditions to reduce the level of N 2 0 in said N 2 0- and NO x -containing gas stream and thus produce a deN 2 0- treated gas stream, said deN 2 0-treated gas stream
containing a reduced amount of N 2 0;
ii) taking at least a portion of said deN 2 0-treated gas stream to provide a NO x -containing gas stream; and iii) passing at least a portion of said NO x -containing gas stream through a catalyst bed comprising a deNO x catalyst under suitable conditions to reduce the level of NO x in the deN 2 0-treated gas stream and thus produce a deNO x -treated gas stream, said deNO x -treated gas stream containing a reduced amount of NO x ;
wherein an additional gas stream comprising NO is provided to either or both of the N 2 0- and NO x -containing gas stream and the NO x -containing gas stream, such that the ratio of N0 2 :NO in the ΝΟχ-containing gas stream is less than 1:1.
Brief Description of the Drawings
Figures 1 and 2 are representations of exemplary, but non-limiting embodiments of the invention.
Detailed Description of the Invention
The present inventors have surprisingly found that by decreasing the ratio of N0 2 :NO in a ΝΟχ-containing gas stream before subjecting it to treatment with a deNO x catalyst, the overall level of pollutants in the
resultant deNO x treated gas stream, in the form of oxides of nitrogen, can be decreased.
The ΝΟχ-containing gas stream in the process of the invention may be any gas stream containing NO x .
Preferably, the ΝΟχ-containing gas stream is derived from an exhaust gas stream, typically from an industrial process. Exhaust gas streams particularly suitable for use as the NO x -containing gas stream in the process of the present invention include exhaust gas streams from a process for the production of nitric acid.
Typically the N0 2 content of the ΝΟχ-containing gas stream is in the range of from 500 to lOOOOppmv.
Typically the NO content of the ΝΟχ-containing gas stream is in the range of from 500 to lOOOOppmv.
When using the process of the invention, the ratio of N0 2 : NO in the ΝΟχ-containing gas stream, before the introduction of the additional gas stream comprising NO is at least 1:1, preferably greater than 1:1.
The ΝΟχ-containing gas stream is contacted with a catalyst bed comprising a deNO x catalyst under suitable conditions to reduce the level of NO x in said NO x - containing gas stream and thus produce a deNO x treated gas stream.
Any deNO x catalysts may suitably be used in the process of the present invention, for example those described in US 6419889. An exemplary catalyst from US 6419889 comprises a titania carrier and one or more metal compounds which metals are selected from the group consisting of vanadium, molybdenum and tungsten. Said catalyst typically has a surface area measured by nitrogen adsorption of between about 70 m 2 /g and about 99 m 2 /g. Said catalyst suitably has a bimodal pore
distribution with more than 90% of the pore volume present in pores having a diameter of at most about 100 nm, which pore volume is considered to be the pore volume present in pores having a diameter between about 1 nm and about 10 4 nm. Further, said catalyst is obtainable by impregnating or deposition of the carrier with the metal compound (s) after extruding, drying and calcining the carrier .
Suitable conditions to reduce the level of NO x in the gas stream include a pressure in the range of from 0 kPa (gauge) to 1200 kPa (gauge) and a temperature in the range of from 140°C to 400°C.
The deNO x treated gas stream will contain a reduced level of NO x (considering both NO and N0 2 on a molar basis) compared to the NO x -containing gas stream.
Preferably, the deNO x treated gas stream contains no more than 10% of the amount of NO x in the NO x -containing gas stream. More preferably, the deNO x treated gas stream contains no more than 5% of the amount of NO x in the NOx- containing gas stream. Even more preferably, the deNO x treated gas stream contains no more than 2% of the amount of ΝΟχ in the NO x -containing gas stream. Most
preferably, the deNO x treated gas stream contains no more than 1% of the amount of NO x in the NO x -containing gas stream.
In a preferred embodiment of the invention, the NOx- containing gas stream is derived from a N 2 0- and NOx- containing gas stream. In said embodiment, the N 2 0- and ΝΟχ-containing gas stream in the process of the invention may be any gas stream containing N 2 0 and NO x .
Preferably, the N 2 0- and ΝΟχ-containing gas stream is an exhaust gas stream, typically from an industrial process. Exhaust gas streams particularly suitable for use as the N 2 0- and ΝΟχ-containing gas stream in the process of the present invention include exhaust gas streams from a process for the production of nitric acid.
In this embodiment, depending on the exhaust stream, the amount of N 2 0 present will vary. For the exhaust stream from a nitric acid plant, typically the N 2 0 content of the N 2 0- and ΝΟχ-containing gas stream is in the range of from 500 to lOOOOppmv, preferably in the range of from 500 to 2000ppmv.
Further, in this embodiment, prior to the NOx- containing gas stream being passed through a catalyst bed comprising a deNO x catalyst under suitable conditions to reduce the level of NO x in the gas stream, the N 2 0- and ΝΟχ-containing gas stream is passed through a catalyst bed comprising a deN 2 0 catalyst under suitable conditions to reduce the level of N 2 0 in said N 2 0- and ΝΟχ-containing gas stream and, thus, produce a deN 2 0-treated gas stream, said deN 2 0-treated stream containing a reduced amount of N 2 0. At least of portion of said deN 2 0-treated gas stream is then used as the ΝΟχ-containing gas stream. When using the process of the invention, the molar ratio of N02:NO in the N 2 0- and NO x -containing gas stream, before any introduction of the additional gas stream comprising NO is typically at least 1:1,
preferably greater than 1:1. However, in some
embodiments in which the deN 2 0 catalyst converts some NO to N0 2 , the ratio of N0 2 :NO in the N 2 0- and NO x -containing gas stream, before any introduction of the additional gas stream may be lower than this.
Other gases present in the ΝΟχ-containing and/or
N 2 0- and ΝΟχ-containing gas stream, wherein the said gas stream or streams are derived from the exhaust stream from a nitric acid plant include, but are not limited to, nitrogen, H 2 0, oxygen and argon.
In the process of the present invention, a N 2 0- and
ΝΟχ-containing gas stream may initially be passed through a catalyst bed comprising a deN 2 0 catalyst under suitable conditions to reduce the level of N 2 0 in the gas stream and thus produce a deN 2 0-treated gas stream, said deN 2 0- treated gas stream containing a reduced amount of N 2 0.
Any deN 2 0 catalysts may suitably be used in the process of the present invention, including base metal catalyst and zeolite-supported iron catalysts, optionally also containing a noble metal such as Pt or Ru . Such zeolite-supported iron catalysts include those described in US5171553, WO2005110582 and Journal of Catalysis 243 (2006), 340-349. Suitable base metal catalyst have been described in in US5705136, Catalysis Communications 4 (2003) 505-509 and WO2015014863.
Suitable conditions to reduce the level of N 2 0 in the gas stream include a pressure in the range of from 0 kPa (gauge) to 1200 kPa (gauge) and a temperature in the range of from 350°C to 650°C. The deN 2 0-treated gas stream contains a reduced amount of N 2 0. Preferably, the deN 2 0-treated gas stream contains no more than 10% of the amount of N 2 0 in the N 2 0- and ΝΟχ-containing gas stream. More preferably the deN 2 0-treated gas stream contains no more than 5% of the amount of N 2 0 in the N 2 0- and NO x -containing gas stream. Even more preferably, the deN 2 0-treated gas stream contains no more than 2% of the amount of N 2 0 in the N 2 0- and ΝΟχ-containing gas stream. Most preferably, the deN 2 0-treated gas stream contains no more than 1% of the amount of N 2 0 in the N 2 0- and NO x -containing gas stream.
In the process of the present invention, an
additional gas stream comprising NO is provided to either or both of (i) the ΝΟχ-containing gas stream before it is contacted with the deNO x catalyst and (ii) the N 2 0- and
ΝΟχ-containing gas stream before it is contacted with the deN 2 0 catalyst in the embodiment wherein a N 2 0- and NOx- containing gas stream is treated with a deN 2 0 catalyst in order to form a deN 2 0-treated gas stream, at least a portion of which is used as the ΝΟχ-containing gas stream. This additional gas stream contains NO in such an amount and concentration that the resultant ratio of N0 2 :NO in the ΝΟχ-containing gas stream is less than 1:1, preferably no more than 0.8:1.
Preferably the additional gas stream comprising NO is another process gas stream produced in the process which produces either the ΝΟχ-containing or the N 2 0- and ΝΟχ-containing gas streams. In one particularly
preferred embodiment, the ΝΟχ-containing or the N 2 0- and ΝΟχ-containing gas stream is an exhaust gas stream from an industrial process and the additional gas stream is another gas stream within that process. Most preferably, the ΝΟχ-containing or the N 2 0- and ΝΟχ-containing gas stream is an exhaust gas stream from a nitric acid plant and the additional gas stream is formed from at least a portion of an outlet stream from the ammonia burner in such a process .
Detailed Description of the Drawings
The present invention is further illustrated in the preferred, but non-limiting, embodiments of the invention illustrated in Figures 1 and 2. In these Figures, the first digit of each reference number refers to the Figure number (i.e. 1XX for Figure 1 and 2XX for Figure 2) . The remaining digits refer to the individual features and the same features are provided with the same number in each Figure. Therefore, the same feature is numbered 104 in Figure 1 and 204 in Figure 2.
In Figure 1, a NO x -containing gas stream 101 is passed through a catalyst bed 102 comprising a deNO x catalyst under suitable conditions to reduce the level of ΝΟχ in the gas stream and thus produce a deNO x treated gas stream 103, said deNO x treated gas stream containing a reduced amount of NO x . An additional gas stream 104 comprising NO is provided to the NO x -containing gas stream, such that the ratio of N0 2 :NO in the NOx- containing gas stream is no more than 1:1.
Figure 2 illustrates a preferred embodiment in which a N 2 0- and ΝΟχ-containing gas stream 205 through a catalyst bed 206 comprising a deN 2 0 catalyst under suitable conditions to reduce the level of N 2 0 in the gas stream and thus produce a deN 2 0-treated gas stream, which is then used as the ΝΟχ-containing gas stream 201, said deN 2 0-treated gas stream containing a reduced amount of
N 2 0. In this embodiment, the additional gas stream 204 comprising NO is provided to either or both of the N 2 0- and ΝΟχ-containing gas stream 205 and the ΝΟχ-containing gas stream 201, such that the ratio of N0 2 :NO in the NO x - containing gas stream 201 is no more than 1:1
The invention will now be illustrated by means of the following Examples, which are not intended to limit the invention.
Examples
The examples were carried out by passing a gas stream containing Ox, N 2 0, NH 3 , N 2 , 0 2 and H 2 0 over a DeNOx catalyst at 250°C and at different NO/N0 2 ratios. The composition of the gas streams and the results of the tests are shown in Table 1. For the Examples of the invention (2, 4, 6 and 7), extra NO was added to the gas stream in order to correspond to an additional gas stream comprising NO being added to the NO x -containing gas stream in these examples.
The DeNOx catalyst used in the test runs was S-096 catalyst (a vanadium on titania catalyst commercially available from CRI Catalyst Company) . A nominal catalyst diameter of 3.2mm was used in runs 1 to 4 and a nominal catalyst diameter of 1.0mm was used in runs 5 to 8.
The tests showed that, in the examples of the invention (2, 4, 6 and 7), ratios of NO/N02 above 1:1
(corresponding to an additional gas stream comprising NO being added to the NO x -containing gas stream) result in no increase of the concentration of N 2 0 over the catalyst being detected. However, for the comparative examples (1, 3, 5 and 8) with lower ratios (corresponding to no additional gas stream comprising NO being added to the ΝΟχ-containing gas stream) N 2 0 concentration was
increased over the deNOx catalyst. Table 1
*Ammonia to NOx ratio
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