Process for the removal of acid forming gases from exhaust gases and production of phosphoric acid
Patent
·
OSTI ID:868251
- El Cerrito, CA
- San Pablo, CA
Exhaust gases are treated to remove NO or NO.sub.x and SO.sub.2 by contacting the gases with an aqueous emulsion or suspension of yellow phosphorous preferably in a wet scrubber. The addition of yellow phosphorous in the system induces the production of O.sub.3 which subsequently oxidizes NO to NO.sub.2. The resulting NO.sub.2 dissolves readily and can be reduced to form ammonium ions by dissolved SO.sub.2 under appropriate conditions. In a 20 acfm system, yellow phosphorous is oxidized to yield P.sub.2 O.sub.5 which picks up water to form H.sub.3 PO.sub.4 mists and can be collected as a valuable product. The pressure is not critical, and ambient pressures are used. Hot water temperatures are best, but economics suggest about 50.degree. C. The amount of yellow phosphorus used will vary with the composition of the exhaust gas, less than 3% for small concentrations of NO, and 10% or higher for concentrations above say 1000 ppm. Similarly, the pH will vary with the composition being treated, and it is adjusted with a suitable alkali. For mixtures of NO.sub.x and SO.sub.2, alkalis that are used for flue gas desulfurization are preferred. With this process, better than 90% of SO.sub.2 and NO in simulated flue gas can be removed. Stoichiometric ratios (P/NO) ranging between 0.6 and 1.5 were obtained.
- Research Organization:
- Lawrence Berkeley National Laboratory (LBNL), Berkeley, CA
- DOE Contract Number:
- AC03-76SF00098
- Assignee:
- Regents of University of California (Alameda, CA)
- Patent Number(s):
- US 5106601
- OSTI ID:
- 868251
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
/423/
10
1000
20
50
90
acfm
acid
acid form
acid forming
addition
adjusted
alkali
alkalis
ambient
ambient pressure
ambient pressures
ammonium
amount
appropriate
appropriate conditions
aqueous
aqueous emulsion
collected
composition
concentrations
conditions
contacting
critical
degree
desulfurization
dissolved
dissolves
economics
emulsion
exhaust
exhaust gas
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flue
flue gas
form
forming
forming gas
forming gases
gas
gas desulfurization
gases
hot
hot water
induces
mists
mixtures
obtained
oxidized
oxidizes
ph
phosphoric
phosphoric acid
phosphorous
phosphorus
picks
ppm
preferably
preferred
pressure
pressures
process
product
production
ranging
ratios
readily
reduced
removal
remove
removed
resulting
scrubber
similarly
simulated
stoichiometric
stoichiometric ratio
subsequently
suggest
suitable
suitable alkali
suspension
temperatures
treated
valuable
vary
water
water temperature
wet
wet scrubber
yellow
yellow phosphorus
yield
10
1000
20
50
90
acfm
acid
acid form
acid forming
addition
adjusted
alkali
alkalis
ambient
ambient pressure
ambient pressures
ammonium
amount
appropriate
appropriate conditions
aqueous
aqueous emulsion
collected
composition
concentrations
conditions
contacting
critical
degree
desulfurization
dissolved
dissolves
economics
emulsion
exhaust
exhaust gas
exhaust gases
flue
flue gas
form
forming
forming gas
forming gases
gas
gas desulfurization
gases
hot
hot water
induces
mists
mixtures
obtained
oxidized
oxidizes
ph
phosphoric
phosphoric acid
phosphorous
phosphorus
picks
ppm
preferably
preferred
pressure
pressures
process
product
production
ranging
ratios
readily
reduced
removal
remove
removed
resulting
scrubber
similarly
simulated
stoichiometric
stoichiometric ratio
subsequently
suggest
suitable
suitable alkali
suspension
temperatures
treated
valuable
vary
water
water temperature
wet
wet scrubber
yellow
yellow phosphorus
yield