Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
287 words
A process for treating an exhaust stream which includes one or more noxious compounds containing chemically bound nitrogen, to produce an effluent stream that is reduced in oxides of nitrogen for discharge into the atmosphere; said process comprising: adding to said exhaust stream a source of oxygen and sufficient fuel to create a fuel-rich mixture, the quantity of fuel being sufficient to react with the available oxygen; providing said fuel-enriched stream to a thermal reactor and reacting therein said fuel, noxious compounds, and available oxygen, to provide a heated oxygen-depleted stream which includes by-product chemically bound nitrogen compounds; cooling said oxygen-depleted stream to 800° to 1000° F. by passing same through a first heat exchanger; adding conversion oxygen to said cooled stream from said first heat exchanger, and passing the cooled oxygen-augmented stream over a first catalyst bed under overall reducing conditions, the quantity of conversion oxygen added being in stoichiometric excess of the amount of chemically bound nitrogen in said stream, but less than the amount of combustibles; whereby the bound nitrogen is first dissociated and oxidized to NO 2 , and then the NO 2 is reduced by the excess combustibles; cooling said stream from said first catalyst bed to a temperature of about 450° to 550° F. by passing said stream through a second heat exchanger; adding air to the resulting cooled stream to produce a further cooled stream at a temperature of about 400° to 500° F., and having a stoichiometric excess of oxygen; and passing said stream having said stoichiometric excess of oxygen over an oxidizing catalyst bed at said temperature of 400° to 500° F. to oxidize any unreacted chemically bound nitrogen compounds, to thereby provide an effluent stream for discharge.
Claim 2
Dependent Claim
287 words
A process for treating an exhaust stream which includes one or more noxious compounds containing chemically bound nitrogen, to produce an effluent stream that is reduced in oxides of nitrogen for discharge into the atmosphere; said process comprising: adding to said exhaust stream a source of oxygen and sufficient fuel to create a fuel-rich mixture, the quantity of fuel being sufficient to react with the available oxygen; providing said fuel-enriched stream to a thermal reactor and reacting therein said fuel, noxious compounds, and available oxygen, to provide a heated oxygen-depleted stream which includes by-product chemically bound nitrogen compounds; cooling said oxygen-depleted stream to 800° to 1000° F. by passing same through a first heat exchanger; adding conversion oxygen to said cooled stream from said first heat exchanger, and passing the cooled oxygen-augmented stream over a first catalyst bed under overall reducing conditions, the quantity of conversion oxygen added being in stoichiometric excess of the amount of chemically bound nitrogen in said stream, but less than the amount of combustibles; whereby the bound nitrogen is first dissociated and oxidized to NO 2 , and then the NO 2 is reduced by the excess combustibles; cooling said stream from said first catalyst bed to a temperature of about 450° to 550° F. by passing said stream through a second heat exchanger; adding air to the resulting cooled stream to produce a further cooled stream at a temperature of about 400° to 500° F., and having a stoichiometric excess of oxygen; and passing said stream having said stoichiometric excess of oxygen over an oxidizing catalyst bed at said temperature of 400° to 500° F. to oxidize any unreacted chemically bound nitrogen compounds, to thereby provide an effluent stream for discharge.
Claim 3
Dependent Claim
18 words
A method in accordance with claim 1, wherein said noxious compounds include one or more oxides of nitrogen.
Claim 4
Dependent Claim
23 words
A method in accordance with claim 2, including NO x in the range of up to 100% by volume of said exhaust stream.
Claim 5
Dependent Claim
13 words
A method in accordance with claim 1, wherein said noxious compounds include HCN.
Claim 6
Dependent Claim
15 words
A method in accordance with claim 1, wherein said noxious compounds include NH 3 .
Claim 7
Dependent Claim
17 words
A method in accordance with claim 1, wherein said noxious compounds include organic compounds with bound nitrogen.
Claim 8
Dependent Claim
17 words
A method in accordance with claim 1, wherein said exhaust stream further includes one or more VOC's.
Claim 9
Dependent Claim
13 words
A method in accordance with claim 1, wherein said exhaust stream is gaseous.
Claim 10
Dependent Claim
13 words
A method in accordance with claim 1, wherein said exhaust stream is liquid.
Claim 11
Dependent Claim
20 words
A method in accordance with claim 1, wherein the resultant stream from said oxidizing catalyst bed is provided for venting.
Claim 12
Dependent Claim
22 words
A method in accordance with claim 10, further including recovering heat from the effluent from the oxidizing catalyst prior to said venting.
Claim 13
Dependent Claim
27 words
A method in accordance with claim 1, wherein the reaction in said thermal reactor is conducted at a temperature range of from about 1400° to 2000° F.
Claim 14
Dependent Claim
31 words
A method in accordance with claim 1, wherein the amount of fuel added to said stream provides a stoichiometric excess of fuel of up to 150% with respect to available oxygen.
Claim 15
Dependent Claim
19 words
A method in accordance with claim 13, wherein the excess fuel is in the range of 105 to 110%.
Claim 16
Dependent Claim
22 words
A method in accordance with claim 11, wherein the residence time in said thermal reactor is from about 0.25 to 0.5 seconds.
Claim 17
Dependent Claim
48 words
A method in accordance with claim 1, wherein said first heat exchanger is a steam boiler, and further including converting a portion of the heat energy of the stream from said first catalyst bed into steam at said second heat exchanger, for supplementing the steam from said boiler.
Claim 18
Dependent Claim
28 words
A process in accordance with claim 1, wherein the space velocity of said resultant stream passing over said oxidizing catalyst is about 60,000 to 80,000 hr. -1 .