# US 9,433,898 B2 · Toxic gas condensation and retreatment system > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 9,433,898 B2 - Document ID: US9433898B2 - Status: Granted - Kind: B2 - Application number: 14/475,108 - Filed: 2014-09-02 - Published: 2014-12-25 - Granted: 2016-09-06 - Earliest claimed: 2014-06-19 - Applicants: Saeed J. Almalowi - Inventors: Saeed J. Almalowi - Web page: https://patentgrep.com/patent/US9433898B2 ## CPC - B01D 53/92: of engine exhaust gases (exhaust {or silencing} apparatus {for internal combustion engines, machines or engines in general}, having means for purifying, {rendering innocuous} or otherwise treating exhaust gases F01N3/00) - B01D 53/002: {by condensation} - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) ## Abstract Apparatuses and systems for reduction and elimination of toxic gases emitted from a motor vehicle or industrial exhaust system. The systems may be single-tier or two-tier, and include at least one direct contact heat exchanger wherein exhaust gas is condensed or dissolved in cold moist air vapor. Uncondensed and undissolved gases may be recirculated into the direct contact heat exchanger to be treated again. The systems also include at least one post-treatment tank wherein condensate liquids and gas solutions are subject to agglomeration and are finally discharged into the environment as a clean liquid. The systems provided herein may complement the existing catalytic converters used in motor vehicles. ## Claims ### Claim 1 An exhaust system for eliminating toxic gases from a gaseous exhaust stream comprising: an exhaust line; a direct contact heat exchanger having a mixing chamber containing a plurality of nozzles spraying cold moist air vapor and at least two horizontal strips positioned at different vertical levels inside the chamber; a first inlet connected to the direct contact heat exchanger above the horizontal strips and configured to receive the gaseous exhaust stream via the exhaust line and transfer the gaseous exhaust stream to the chamber; a second inlet connected to the direct contact heat exchanger on an opposite side of the first inlet and having the plurality of nozzles attached thereto, the second inlet receiving cooled air external to the exhaust system; a recirculation line connected with the second inlet and the direct contact heat exchanger at an upper portion of the chamber above the second inlet; and a post-treatment tank that is in fluid connection to the direct contact heat exchanger containing a holding reservoir and at least one injection device; wherein the nozzles are configured to spray cold moist air vapor in a sufficient amount to at least partially condense and dissolve the toxic gases, wherein the recirculation line is configured to recirculate remaining toxic gases from an upper portion of the chamber into the second inlet to condense or dissolve in the cold moist air vapor, and wherein the post-treatment tank is configured to agglomerate condensed and dissolved toxic gases. ### Claim 2 (depends on 1) The exhaust system of claim 1, further comprising a catalytic converter. ### Claim 3 (depends on 2) The exhaust system of claim 2, wherein the catalytic converter treats the remaining toxic gases before the remaining toxic gases are recirculated into the direct contact heat exchanger. ### Claim 4 (depends on 1) The system of claim 1, wherein the recirculation line is configured to recirculate remaining toxic gases into the direct contact heat exchanger in a forward stream. ### Claim 5 (depends on 1) The system of claim 1, wherein the recirculation line is configured to recirculate remaining toxic gases into the direct contact heat exchanger in a backward stream. ### Claim 6 (depends on 1) The system of claim 1, wherein the recirculation line is configured to recirculate remaining toxic gases into the direct contact heat exchanger in a forward stream and a backward stream. ### Claim 7 (depends on 1) The exhaust system of claim 1, wherein the second inlet is located above both the horizontal strips and the first inlet. ### Claim 8 (depends on 1) The exhaust system of claim 1, wherein the post-treatment tank performs an agglomeration process by adding a chemical material to the dissolved gases to solidify the gases. ### Claim 9 An exhaust system for eliminating toxic gases from a gaseous exhaust stream comprising: an exhaust line in fluid connection with a first direct contact heat exchanger and a second direct contact heat exchanger downstream of the first direct contact heat exchanger, each direct contact heat exchanger having a mixing chamber containing a plurality of nozzles spraying cold moist air vapor and at least two horizontal strips positioned at different vertical levels inside the chamber; and a catalytic converter connected to the first direct contact heat exchanger and the second direct contact heat exchanger; wherein the first direct contact heat exchanger includes a connection line located at a top of the mixing chamber to transfer toxic gases to the catalytic converter, and a first post-treatment tank that is in fluid connection with at least the second direct contact heat exchanger containing a holding reservoir and at least one injection device, and wherein the second direct contact heater exchanger includes a recirculation line in fluid connection with a second inlet of the second direct contact heater exchanger at a location above the horizontal strips, and a first inlet disposed directly opposite and below the second inlet and connected to an output of the catalytic convert, wherein the nozzles are configured to spray cold moist air vapor in a sufficient amount to at least partially condense and dissolve the toxic gases; wherein the connection line is configured to transport remaining toxic gases from the first direct contact heat exchanger to the second direct contact heat exchanger wherein the recirculation line is configured to recirculate remaining toxic gases into the second direct contact heat exchanger to condense or dissolve in the cold moist air vapor; and wherein the first post-treatment tank is configured to agglomerate condensed and dissolved toxic gases. ### Claim 10 (depends on 9) The exhaust system of claim 9, wherein the catalytic converter is disposed downstream of the first direct contact heat exchanger and upstream of the second direct contact heat exchanger and treats the remaining toxic gases before the remaining toxic gases are injected into the second direct contact heat exchanger. ### Claim 11 (depends on 9) The system of claim 9, wherein the recirculation line is configured to recirculate remaining toxic gases into the second direct contact heat exchanger in a forward stream. ### Claim 12 (depends on 9) The system of claim 9, wherein the recirculation line is configured to recirculate remaining toxic gases into the second direct contact heat exchanger in a backward stream. ### Claim 13 (depends on 9) The system of claim 9, wherein the recirculation line is configured to recirculate remaining toxic gases into the second direct contact heat exchanger in a forward stream and a backward stream. ### Claim 14 (depends on 9) The system of claim 9, further comprising a second post-treatment tank. ### Claim 15 (depends on 14) The system of claim 14, wherein the first post-treatment tank is in fluid connection with the second direct contact heat exchanger and the second post-treatment tank is in fluid connection with the first direct contact heat exchanger. ### Claim 16 A gas- and liquid-phase direct contact heat exchanger comprising: a housing of a generally cuboidal shape; a mixing chamber; a second inlet on a second side surface directly opposite the first side surface having an extended portion inside the mixing chamber, the second inlet receiving cooled air external to the exhaust system; a plurality of nozzles on the extended portion of the second inlet; a plurality of horizontal strips positioned at different vertical levels below the plurality of nozzles; a first inlet connected above the horizontal strips and configured to receive an gaseous exhaust stream via an exhaust line and transfer the gaseous exhaust stream to the mixing chamber; a first outlet; a recirculation line connected with the second inlet at an upper portion of the mixing chamber above the second inlet; and a second outlet; wherein the first inlet is configured to inject hot gases into the mixing chamber; wherein the second inlet is configured to inject cold moist air; wherein the nozzles are configured to spray cold moist air vapor in a sufficient amount to at least partially condense and dissolve the hot gases; wherein the recirculation line is configured to recirculate remaining hot gases vented by the second outlet into the mixing chamber via the second inlet to condense and dissolve in the cold moist air vapor; and wherein the second outlet is configured to release condensed and dissolved gases. ### Claim 17 (depends on 16) The heat exchanger of claim 16, wherein the heat exchanger is in fluid communication with an exhaust line. ### Claim 18 (depends on 16) The heat exchanger of claim 16, wherein the horizontal strips are made of metal selected from the group consisting of copper, iron, nickel, aluminum, titanium, chromium, combinations and alloys thereof.