Monolithic gas trap adsorber for high efficiency, cost effective, low-emission condensing furnace
An improved method and system for treating flue gases from a natural gas furnace are provided. The method and system include an acidic gas trap (AGT) adsorber which enables the continuous adsorption and storage of SOx, NOx redox, and formic acid/CO/HC/CH 4 oxidation, with a negligible pressure drop. The AGT adsorber includes a catalyst coating having a nanotube structure (e.g., a uniform nanostructure forest coating) or a uniform porous nanostructure of various low-cost oxides through scalable low temperature solution processes, including oxides of Ti, Cu, Ba, Mn, Zr, Zn, Sr, Ca, Li, K, Na, Al, or Ce.
1. A method for treating flue gases from a natural gas furnace, the method comprising:
positioning an acidic gas trap adsorber in an exhaust gas flow path between a primary heat exchanger and a secondary heat exchanger; and
contacting a combustion waste gas from a natural gas furnace with the acidic gas trap adsorber, the combustion waste gas including gaseous sulfur compounds and gaseous nitrogen compounds, wherein the acidic gas trap adsorber comprises:
a shell canister,
a divergent cone coupled to an upstream side of the shell canister,
a convergent cone coupled to a downstream side of the shell canister,
a flow-through monolithic substrate within the shell canister, the flow-monolithic substrate including plurality of channels extending in a longitudinal direction between the divergent cone and the convergent cone, the plurality of channels each defining channel surfaces that are orthogonal to the longitudinal direction, and
a catalyst coating on the channel surfaces of the flow-through monolithic substrate, the catalyst coating including a plurality of nanotubes that are oriented in a non-parallel direction with respect each other, the plurality of nanotubes comprising a metal oxide sorber component for trapping the gaseous sulfur compounds, trapping the gaseous nitrogen compounds, or trapping gaseous nitrogen redox from the combustion waste gas, the metal oxide sorber component comprising an oxide of Ti, Cu, Ba, Mn, Zr, Zn, Sr, Ca, Li, K, Na, Al, Ce or mixtures thereof.
2. The method of claim 1 , wherein the flow-through monolithic substrate comprises a cordierite or stainless steel honeycomb structure.
3. The method of claim 1 , further including positioning a mat comprising silica between the flow-through monolithic substrate and the shell canister.
4. The method of claim 1 , wherein the flow-through monolithic substrate is wash coated with titanium dioxide followed by the application of platinum nanoparticles and cupric oxide.
5. The method of claim 1 , wherein the primary heat exchanger is a tubular heat exchanger, and wherein the secondary heat exchanger is a tube and fin heat exchanger.
6. A method for treating flue gases from a natural gas furnace, the method comprising:
positioning an acidic gas trap adsorber in an exhaust gas flow path between a primary heat exchanger and a secondary heat exchanger; and
contacting a combustion waste gas from a natural gas furnace with the acidic gas trap adsorber, the combustion waste gas including gaseous sulfur compounds and gaseous nitrogen compounds, wherein the acidic gas trap adsorber comprises:
a catalyst coating on a flow-through monolithic substrate, the catalyst coating including a metal oxide sorber component for trapping the gaseous sulfur compounds, trapping the gaseous nitrogen compounds, or trapping gaseous nitrogen redox from the combustion waste gas, the metal oxide sorber component comprising an oxide of Ti, Cu, Ba, Mn, Zr, Zn, Sr, Ca, Li, K, Na, Al, Ce or mixtures thereof, wherein the flow-through monolithic substrate comprises a zinc oxide that is wash coated with BaCO 3 nanoparticles.
7. A system for treating flue gases from a natural gas furnace, the system comprising:
an acidic gas trap adsorber in an exhaust gas flow path between a primary heat exchanger and a secondary heat exchanger, wherein the acidic gas trap adsorber comprises:
a shell canister,
a divergent cone coupled to an upstream side of the shell canister,
a convergent cone coupled to a downstream side of the shell canister,
a flow-through monolithic substrate within the shell canister, the flow-monolithic substrate including plurality of channels extending in a longitudinal direction between the divergent cone and the convergent cone, the plurality of channels each defining channel surfaces that are orthogonal to the longitudinal direction, and
a catalyst coating on the channel surfaces of the flow-through monolithic substrate, the catalyst coating including a plurality of nanotubes that are oriented in a non-parallel direction with respect each other, the plurality of nanotubes comprising a metal oxide sorber component for trapping gaseous sulfur compounds, trapping gaseous nitrogen compounds, or trapping gaseous nitrogen redox from the combustion waste gas, the metal oxide sorber component comprising an oxide of Ti, Cu, Ba, Mn, Zr, Zn, Sr, Ca, Li, K, Na, Al, Ce or mixtures thereof.
8. The system of claim 7 , wherein the flow-through monolithic substrate comprises a cordierite or stainless-steel honeycomb structure.
9. The system of claim 7 , further comprising a mat comprising silica disposed between the flow-through monolithic substrate and the shell canister.
10. The system of claim 7 , wherein the flow-through monolithic substrate is wash coated with titanium dioxide followed by the application of platinum nanoparticles and cupric oxide.