IMPROVED PROCESS FOR REMOVING NOX FROM EXHAUST GAS

Abstract

The present invention provides a process for the treatment of a NO.sub.X-containing gas stream, said NO.sub.X-containing gas stream containing NO2 and NO in a molar ratio of NO.sub.2:NO of at least 1:1, to remove at least a portion of the NO.sub.X contained therein, said process comprising: i) providing an additional gas stream comprising NO to the NO.sub.X-containing gas stream, such that the molar ratio of NO.sub.2:NO in the NO.sub.X-containing gas stream is reduced to be less than 1:1; and ii) then passing the NO.sub.X-containing gas stream through a catalyst bed comprising a deNO.sub.X catalyst under suitable conditions to reduce the level of NO.sub.X in the gas stream and thus produce a deNO.sub.X treated gas stream, said deNO.sub.X treated gas stream containing a reduced amount of NO.sub.X.

Claims

1. A process for the treatment of a NO.sub.X-containing gas stream, said NO.sub.X-containing gas stream containing NO.sub.2 and NO in a molar ratio of NO.sub.2:NO of at least 1:1, to remove at least a portion of the NO.sub.X contained therein, said process comprising: i) providing an additional gas stream comprising NO to the NO.sub.X-containing gas stream, such that the molar ratio of NO.sub.2:NO in the NO.sub.X-containing gas stream is reduced to be less than 1:1; and ii) then passing the NO.sub.X-containing gas stream through a catalyst bed comprising a deNO.sub.X catalyst under suitable conditions to reduce the level of NO.sub.X in the gas stream and thus produce a deNO.sub.X treated gas stream, said deNO.sub.X treated gas stream containing a reduced amount of NO.sub.X.

2. The process as claimed in claim 1 wherein the NO.sub.X-containing gas stream is derived from the exhaust gas stream from a process for the production of nitric acid.

3. The process for the treatment of a N.sub.2O- and NO.sub.X-containing gas stream to remove at least a portion of each of the NO.sub.X and the N.sub.2O contained therein, said process comprising: i) passing the N.sub.2O- and NO.sub.X-containing gas stream through a catalyst bed comprising a deN.sub.2O catalyst under suitable conditions to reduce the level of N.sub.2O in said N.sub.2O- and NO.sub.X-containing gas stream and thus produce a deN.sub.2O-treated gas stream, said deN.sub.2O-treated gas stream containing a reduced amount of N.sub.2O; ii) taking at least a portion of said deN.sub.2O-treated gas stream to provide a NO.sub.X-containing gas stream; iii) passing at least a portion of said NO.sub.X-containing; iv) gas stream through a catalyst bed comprising a deNO.sub.X catalyst under suitable conditions to reduce the level of NO.sub.X in the deN.sub.2O-treated gas stream and thus produce a deNO.sub.X-treated gas stream, said deNO.sub.X-treated gas stream containing a reduced amount of NO.sub.X; and v) wherein an additional gas stream comprising NO is provided to either or both of the N.sub.2O- and NO.sub.X-containing gas stream and the NO.sub.X-containing gas stream, such that the ratio of NO.sub.2:NO in the NO.sub.X-containing gas stream is less than 1:1.

4. The process as claimed in claim 3, wherein the molar ratio of NO.sub.2:NO in the N.sub.2O- and NO.sub.X-containing gas stream, before any introduction of the additional gas stream comprising NO is at least 1:1.

5. The process as claimed in claim 3, wherein the N.sub.2O- and NO.sub.X-containing gas stream is derived from the exhaust gas stream from a process for the production of nitric acid.

6. The process as claimed in claim 1, wherein the NO.sub.2 content of the NO.sub.X-containing gas stream is in the range of from 500 to 10000 ppmv.

7. The process as claimed in claim 1, wherein the NO content of the NO.sub.X-containing gas stream is in the range of from 500 to 10000 ppmv.

8. The process as claimed in claim 3, wherein the N.sub.2O content of the N.sub.2O- and NO.sub.X-containing gas stream is in the range of from 500 to 10000 ppmv.

9. The process as claimed in claim 1, wherein the deNO.sub.X 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. The process as claimed in claim 2, wherein the NO.sub.X-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. The process as claimed in claim, wherein the N.sub.2O and NO.sub.X-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.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0011] FIGS. 1 and 2 are representations of exemplary, but non-limiting embodiments of the invention.

DETAILED DESCRIPTION OF THE INVENTION

[0012] The present inventors have surprisingly found that by decreasing the ratio of NO.sub.2:NO in a NO.sub.X-containing gas stream before subjecting it to treatment with a deNO.sub.X catalyst, the overall level of pollutants in the resultant deNO.sub.X treated gas stream, in the form of oxides of nitrogen, can be decreased.

[0013] The NO.sub.X-containing gas stream in the process of the invention may be any gas stream containing NO.sub.X. Preferably, the NO.sub.X-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.sub.X-containing gas stream in the process of the present invention include exhaust gas streams from a process for the production of nitric acid.

[0014] Typically the NO.sub.2 content of the NO.sub.X-containing gas stream is in the range of from 500 to 10000 ppmv.

[0015] Typically the NO content of the NO.sub.X-containing gas stream is in the range of from 500 to 10000 ppmv.

[0016] When using the process of the invention, the ratio of NO.sub.2:NO in the NO.sub.X-containing gas stream, before the introduction of the additional gas stream comprising NO is at least 1:1, preferably greater than 1:1.

[0017] The NO.sub.X-containing gas stream is contacted with a catalyst bed comprising a deNO.sub.X catalyst under suitable conditions to reduce the level of NO.sub.X in said NO.sub.X-containing gas stream and thus produce a deNO.sub.X treated gas stream.

[0018] Any deNO.sub.X catalysts may suitably be used in the process of the present invention, for example those described in U.S. Pat. No. 6,419,889. An exemplary catalyst from U.S. Pat. No. 6,419,889 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.sup.2/g and about 99 m.sup.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.sup.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.

[0019] Suitable conditions to reduce the level of NO.sub.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.

[0020] The deNO.sub.X treated gas stream will contain a reduced level of NO.sub.X (considering both NO and NO.sub.2 on a molar basis) compared to the NO.sub.X-containing gas stream. Preferably, the deNO.sub.X treated gas stream contains no more than 10% of the amount of NO.sub.X in the NO.sub.X-containing gas stream. More preferably, the deNO.sub.X treated gas stream contains no more than 5% of the amount of NO.sub.X in the NO.sub.X-containing gas stream. Even more preferably, the deNO.sub.X treated gas stream contains no more than 2% of the amount of NO.sub.X in the NO.sub.X-containing gas stream. Most preferably, the deNO.sub.X treated gas stream contains no more than 1% of the amount of NO.sub.X in the NO.sub.X-containing gas stream.

[0021] In a preferred embodiment of the invention, the NO.sub.X-containing gas stream is derived from a N.sub.2O- and NO.sub.X-containing gas stream. In said embodiment, the N.sub.2O- and NO.sub.X-containing gas stream in the process of the invention may be any gas stream containing N.sub.2O and NO.sub.X. Preferably, the N.sub.2O- and NO.sub.X-containing gas stream is an exhaust gas stream, typically from an industrial process. Exhaust gas streams particularly suitable for use as the N.sub.2O- and NO.sub.X-containing gas stream in the process of the present invention include exhaust gas streams from a process for the production of nitric acid.

[0022] In this embodiment, depending on the exhaust stream, the amount of N.sub.2O present will vary. For the exhaust stream from a nitric acid plant, typically the N.sub.2O content of the N.sub.2O- and NO.sub.X-containing gas stream is in the range of from 500 to 10000 ppmv, preferably in the range of from 500 to 2000 ppmv.

[0023] Further, in this embodiment, prior to the NO.sub.X-containing gas stream being passed through a catalyst bed comprising a deNO.sub.X catalyst under suitable conditions to reduce the level of NO.sub.X in the gas stream, the N.sub.2O- and NO.sub.X-containing gas stream is passed through a catalyst bed comprising a deN.sub.2O catalyst under suitable conditions to reduce the level of N.sub.2O in said N.sub.2O- and NO.sub.X-containing gas stream and, thus, produce a deN.sub.2O-treated gas stream, said deN.sub.2O-treated stream containing a reduced amount of N.sub.2O. At least of portion of said deN.sub.2O-treated gas stream is then used as the NO.sub.X-containing gas stream.

[0024] When using the process of the invention, the molar ratio of NO2:NO in the N.sub.2O- and NO.sub.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.sub.2O catalyst converts some NO to NO.sub.2, the ratio of NO.sub.2:NO in the N.sub.2O- and NO.sub.X-containing gas stream, before any introduction of the additional gas stream may be lower than this.

[0025] Other gases present in the NO.sub.X-containing and/or N.sub.2O- and NO.sub.X-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.sub.2O, oxygen and argon.

[0026] In the process of the present invention, a N.sub.2O- and NO.sub.X-containing gas stream may initially be passed through a catalyst bed comprising a deN.sub.2O catalyst under suitable conditions to reduce the level of N.sub.2O in the gas stream and thus produce a deN.sub.2O-treated gas stream, said deN.sub.2O-treated gas stream containing a reduced amount of N.sub.2O.

[0027] Any deN.sub.2O 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 U.S. Pat. No. 5,171,553, WO2005110582 and Journal of Catalysis 243 (2006), 340-349. Suitable base metal catalyst have been described in U.S. Pat. No. 5,705,136, Catalysis Communications 4 (2003) 505-509 and WO2015014863.

[0028] Suitable conditions to reduce the level of N.sub.2O 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.

[0029] The deN.sub.2O-treated gas stream contains a reduced amount of N.sub.2O. Preferably, the deN.sub.2O-treated gas stream contains no more than 10% of the amount of N.sub.2O in the N.sub.2O- and NO.sub.X-containing gas stream. More preferably the deN.sub.2O-treated gas stream contains no more than 5% of the amount of N.sub.2O in the N.sub.2O- and NO.sub.X-containing gas stream. Even more preferably, the deN.sub.2O-treated gas stream contains no more than 2% of the amount of N.sub.2O in the N.sub.2O- and NO.sub.X-containing gas stream. Most preferably, the deN.sub.2O-treated gas stream contains no more than 1% of the amount of N.sub.2O in the N.sub.2O- and NO.sub.X-containing gas stream.

[0030] In the process of the present invention, an additional gas stream comprising NO is provided to either or both of (i) the NO.sub.X-containing gas stream before it is contacted with the deNO.sub.X catalyst and (ii) the N.sub.2O- and NO.sub.X-containing gas stream before it is contacted with the deN.sub.2O catalyst in the embodiment wherein a N.sub.2O- and NO.sub.X-containing gas stream is treated with a deN.sub.2O catalyst in order to form a deN.sub.2O-treated gas stream, at least a portion of which is used as the NO.sub.X-containing gas stream. This additional gas stream contains NO in such an amount and concentration that the resultant ratio of NO.sub.2:NO in the NO.sub.X-containing gas stream is less than 1:1, preferably no more than 0.8:1.

[0031] Preferably the additional gas stream comprising NO is another process gas stream produced in the process which produces either the NO.sub.X-containing or the N.sub.2O- and NO.sub.X-containing gas streams. In one particularly preferred embodiment, the NO.sub.X-containing or the N.sub.2O- and NO.sub.X-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 NO.sub.X-containing or the N.sub.2O- and NO.sub.X-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

[0032] The present invention is further illustrated in the preferred, but non-limiting, embodiments of the invention illustrated in FIGS. 1 and 2. In these Figures, the first digit of each reference number refers to the Figure number (i.e. 1XX for FIGS. 1 and 2XX for FIG. 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 FIGS. 1 and 204 in FIG. 2.

[0033] In FIG. 1, a NO.sub.X-containing gas stream 101 is passed through a catalyst bed 102 comprising a deNO.sub.X catalyst under suitable conditions to reduce the level of NO.sub.X in the gas stream and thus produce a deNO.sub.X treated gas stream 103, said deNO.sub.X treated gas stream containing a reduced amount of NO.sub.X. An additional gas stream 104 comprising NO is provided to the NO.sub.X-containing gas stream, such that the ratio of NO.sub.2:NO in the NO.sub.X-containing gas stream is no more than 1:1.

[0034] FIG. 2 illustrates a preferred embodiment in which a N.sub.2O- and NO.sub.X-containing gas stream 205 through a catalyst bed 206 comprising a deN.sub.2O catalyst under suitable conditions to reduce the level of N.sub.2O in the gas stream and thus produce a deN.sub.2O-treated gas stream, which is then used as the NO.sub.X-containing gas stream 201, said deN.sub.2O-treated gas stream containing a reduced amount of N.sub.2O. In this embodiment, the additional gas stream 204 comprising NO is provided to either or both of the N.sub.2O- and NO.sub.X-containing gas stream 205 and the NO.sub.X-containing gas stream 201, such that the ratio of NO.sub.2:NO in the NO.sub.X-containing gas stream 201 is no more than 1:1

[0035] The invention will now be illustrated by means of the following Examples, which are not intended to limit the invention.

Examples

[0036] The examples were carried out by passing a gas stream containing NOx, N.sub.2O, NH.sub.3, N.sub.2, O.sub.2 and H.sub.2O over a DeNOx catalyst at 250 C. and at different NO/NO.sub.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.sub.X-containing gas stream in these examples.

[0037] 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 3.2 mm was used in runs 1 to 4 and a nominal catalyst diameter of 1.0 mm 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/NO2 above 1:1 (corresponding to an additional gas stream comprising NO being added to the NO.sub.X-containing gas stream) result in no increase of the concentration of N.sub.2O 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 NO.sub.X-containing gas stream) N.sub.2O concentration was increased over the deNOx catalyst.

TABLE-US-00001 TABLE 1 Outlet data Inlet data N.sub.2O NOx NO NO.sub.2 NO:NO.sub.2 N.sub.2O % NOx Make ppmv ppmv ppmv ratio O.sub.2 % H.sub.2O % ppmv ANR* Conversion ppmv 1 2000 400 1600 0.25:1 3 2 20 0.95 82.61 282.3 2 2000 1200 800 1.5:1 3 2 1000 1.05 95.69 0.0 3 300 60 240 0.25:1 10.5 2 1000 0.95 60.24 30.2 4 300 180 120 1.5:1 10.5 2 20 1.05 98.54 0.0 5 300 60 240 0.25:1 3 2 1000 1.05 95.43 79.0 6 300 180 120 1.5:1 3 2 20 0.95 93.17 0.0 7 2000 1200 800 1.5:1 8.5 2 1000 0.95 86.08 0.0 8 2000 400 1600 0.25:1 8.5 2 20 1.05 94.12 493.4 *Ammonia to NOx ratio