from the nitric acid production process, and an installation suitable for same
Number of patents in Portfolio can not be more than 2000
United States of America Patent
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Aug 22, 2017
Issued Date -
N/A
app pub date -
Feb 14, 2012
filing date -
Feb 21, 2011
priority date (Note) -
In Force
status (Latency Note)
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Abstract
The invention relates to a process and apparatus for preparing nitric acid by catalytic oxidation of NH3 by means of oxygen and subsequent reaction of the NOx formed with an absorption medium in an absorption tower, which comprises a catalyst bed for N2O decomposition arranged in the process gas downstream of the catalytic NH3 oxidation and upstream of the absorption tower in the flow direction and a catalyst bed for NOx reduction and effecting a further decrease in the amount of N2O arranged in the tailgas downstream of the absorption tower in the flow direction,
- wherein the amount of N2O removed in the catalyst bed for N2O removal arranged in the process gas is not more than that which results in an N2O content of >100 ppmv and a molar N2O/NOx ratio of >0.25 before entry of the tailgas into the catalyst bed for NOx reduction andthe catalyst bed for NOx reduction and effecting a further decrease in the amount of N2O arranged in the tailgas contains at least one iron-loaded zeolite catalyst andNH3 is added to the tailgas before entry into the catalyst bed in such an amount that an NOx concentration of <40 ppmv results at the outlet from the catalyst bed andthe operating parameters are selected in such a way that an N2O concentration of <200 ppmv results.
First Claim
all claims..Other Claims data not available
Family

- 15 United States
- 10 France
- 8 Japan
- 7 China
- 5 Korea
- 2 Other
Patent Owner(s)
Patent Owner | Address | |
---|---|---|
THYSSENKRUPP INDUSTRIAL SOLUTIONS AG | THYSSENKRUPP ALLEE 1 ESSEN 45143 |
International Classification(s)
Inventor(s)
Inventor Name | Address | # of filed Patents | Total Citations |
---|---|---|---|
Fuchs, Jürgen | Dortmund, DE | 15 | 54 |
# of filed Patents : 15 Total Citations : 54 | |||
Groves, Michael | Gevelsberg, DE | 14 | 129 |
# of filed Patents : 14 Total Citations : 129 | |||
Ruthardt, Klaus | Dortmund, DE | 7 | 15 |
# of filed Patents : 7 Total Citations : 15 | |||
Schwefer, Meinhard | Meschede, DE | 22 | 190 |
# of filed Patents : 22 Total Citations : 190 | |||
Siefert, Rolf | Rheda-Wiedenbrück, DE | 15 | 123 |
# of filed Patents : 15 Total Citations : 123 |
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Patent Citation Ranking
- 2 Citation Count
- C01B Class
- 27.23 % this patent is cited more than
- 8 Age
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Maintenance Fees
Fee | Large entity fee | small entity fee | micro entity fee | due date |
---|---|---|---|---|
7.5 Year Payment | $3600.00 | $1800.00 | $900.00 | Feb 22, 2025 |
11.5 Year Payment | $7400.00 | $3700.00 | $1850.00 | Feb 22, 2029 |
Fee | Large entity fee | small entity fee | micro entity fee |
---|---|---|---|
Surcharge - 7.5 year - Late payment within 6 months | $160.00 | $80.00 | $40.00 |
Surcharge - 11.5 year - Late payment within 6 months | $160.00 | $80.00 | $40.00 |
Surcharge after expiration - Late payment is unavoidable | $700.00 | $350.00 | $175.00 |
Surcharge after expiration - Late payment is unintentional | $1,640.00 | $820.00 | $410.00 |
Full Text
- wherein the amount of N2O removed in the catalyst bed for N2O removal arranged in the process gas is not more than that which results in an N2O content of >100 ppmv and a molar N2O/NOx ratio of >0.25 before entry of the tailgas into the catalyst bed for NOx reduction andthe catalyst bed for NOx reduction and effecting a further decrease in the amount of N2O arranged in the tailgas contains at least one iron-loaded zeolite catalyst andNH3 is added to the tailgas before entry into the catalyst bed in such an amount that an NOx concentration of <40 ppmv results at the outlet from the catalyst bed andthe operating parameters are selected in such a way that an N2O concentration of <200 ppmv results.

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