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    CONDENSATION PLUME MITIGATION SYSTEM FOR EXHAUST STACKS
    1.
    发明申请
    CONDENSATION PLUME MITIGATION SYSTEM FOR EXHAUST STACKS 审中-公开

    公开(公告)号：WO2012100074A3

    公开(公告)日：2012-07-26

    申请号：PCT/US2012/021897

    申请日：2012-01-19

    Applicant: HEARTLAND TECHNOLOGY PARTNERS LLC ,  DUESEL, Bernard, F., Jr. ,  RUTSCH, Michael, J. ,  CLERKIN, Craig

    Inventor： DUESEL, Bernard, F., Jr. ,  RUTSCH, Michael, J. ,  CLERKIN, Craig

    IPC: B01D53/78 ,  B01D5/00 ,  F25J5/00

    Abstract: An exhaust gas plume mitigation process and system includes either mixing secondary heat into a moisture rich exhaust gas stream, or diverting a moisture rich exhaust gas stream into a primary exhaust stack having hot exhaust gases flowing therethrough. Moisture rich exhaust gas from a liquid concentrator may be diverted into a high temperature exhaust stack of an engine, a generator, or a flare. The high temperature exhaust gases from the engine, the generator, or the flare raise the temperature of the moisture rich exhaust gas from the concentrator. The high temperature exhaust gases from the engine, the generator, or the flare are also lower in moisture content, so that the moisture rich exhaust gas from the concentrator is diluted by the drier high temperature exhaust gas. As a result, the mixed gas is less likely to develop a moisture plume upon exit to the atmosphere.

    COMPACT WASTEWATER CONCENTRATOR UTILIZING A LOW TEMPERATURE THERMAL ENERGY SOURCE
    3.
    发明申请
    COMPACT WASTEWATER CONCENTRATOR UTILIZING A LOW TEMPERATURE THERMAL ENERGY SOURCE 审中-公开
    使用低温热能源的紧凑型废水浓缩器

    公开(公告)号：WO2017011704A1

    公开(公告)日：2017-01-19

    申请号：PCT/US2016/042360

    申请日：2016-07-14

    Applicant: HEARTLAND TECHNOLOGY PARTNERS LLC

    Inventor： DUESEL, Bernard, F., Jr. ,  CLERKIN, Craig ,  RUTSCH, Michael, J.

    IPC: C02F1/04 ,  C02F1/16 ,  C02F1/12 ,  B01D1/00 ,  B01D1/16

    CPC classification number: B01D1/14 ,  B01D1/0058 ,  B01D1/16 ,  B01D1/305 ,  C02F1/12 ,  C02F1/16

    Abstract: A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. A source of low energy gas, such as low pressure steam from a power plant, is connected to the liquid to be concentrated to heat the liquid to be concentrated before or during the concentration process.

    Abstract translation: 紧凑便携的液体浓缩器包括气体入口，气体出口和连接气体入口和气体出口的流动走廊，其中流动走廊包括通过流动走廊加速气体的变窄部分。 液体入口在变窄部分之前的某一点将液体注入到气流中，使得气液混合物在流动走廊内充分混合，导致部分液体蒸发。 在变窄部分下游的除雾器或流体洗涤器从气流中除去夹带的液滴，并通过再循环回路将去除的液体再循环到液体入口。 将来自发电厂的低能量气体的来源，例如来自发电厂的低压蒸汽连接到待浓缩的液体，以在浓缩过程之前或期间加热待浓缩的液体。

    WASTEWATER PROCESSING SYSTEMS FOR POWER PLANTS AND OTHER INDUSTRIAL SOURCES
    4.
    发明申请
    WASTEWATER PROCESSING SYSTEMS FOR POWER PLANTS AND OTHER INDUSTRIAL SOURCES 审中-公开
    电厂和其他工业源的废水处理系统

    公开(公告)号：WO2014124080A2

    公开(公告)日：2014-08-14

    申请号：PCT/US2014/015007

    申请日：2014-02-06

    Applicant: HEARTLAND TECHNOLOGY PARTNERS LLC

    Inventor： DUESEL, Bernard, F., Jr. ,  CLERKIN, Craig

    CPC classification number: C02F1/048 ,  B01D1/0058 ,  B01D1/14 ,  C02F1/10 ,  C02F1/16 ,  C02F1/38 ,  C02F1/74 ,  C02F9/00 ,  C02F2101/101 ,  C02F2103/023 ,  C02F2201/008

    Abstract: Methods, systems, and/or apparatuses for treating wastewater produced at a thermoelectric power plant, other industrial plants, and/or other industrial sources are disclosed. The wastewater is directed through a wastewater concentrator including a direct contact adiabatic concentration system. A stream of hot feed gases is directed through the wastewater concentrator. The wastewater concentrator mixes the hot feed gases directly with the wastewater and evaporates water vapor from the wastewater. The wastewater concentrator separates the water vapor from remaining concentrated wastewater. A contained air-water interface liquid evaporator may be arranged to pre-process the wastewater before being treated by the wastewater concentrator.

    Abstract translation: 公开了用于处理在热电厂，其它工厂和/或其他工业源处产生的废水的方法，系统和/或设备。 废水通过包括直接接触绝热浓缩系统的废水浓缩器。 热进料气流被引导通过废水浓缩器。 废水浓缩器将热源气体直接与废水混合，并从废水中蒸发出水汽。 废水浓缩器将水蒸气与剩余的浓缩废水分开。 包含的空气 - 水界面液体蒸发器可以被布置成在废水浓缩器处理之前预处理废水。

    MULTI-STAGE WASTEWATER TREATMENT SYSTEM AND METHOD
    6.
    发明申请
    MULTI-STAGE WASTEWATER TREATMENT SYSTEM AND METHOD 审中-公开
    多级废水处理系统及方法

    公开(公告)号：WO2014124078A2

    公开(公告)日：2014-08-14

    申请号：PCT/US2014/015002

    申请日：2014-02-06

    Applicant: HEARTLAND TECHNOLOGY PARTNERS LLC

    Inventor： DUESEL, Bernard, F., Jr. ,  CLERKIN, Craig

    CPC classification number: B01D1/14 ,  B01D1/305 ,  C02F1/048 ,  C02F1/16 ,  C02F2103/365 ,  C02F2303/10 ,  Y02W10/30

    Abstract: Methods, systems, and/or apparatuses for treating wastewater produced at a thermoelectric power plant, other industrial plants, and/or other industrial sources are disclosed. The wastewater is directed through a wastewater concentrator including a direct contact adiabatic concentration system. A stream of hot feed gases is directed through the wastewater concentrator. The wastewater concentrator mixes the hot feed gases directly with the wastewater and evaporates water vapor from the wastewater. The wastewater concentrator separates the water vapor from remaining concentrated wastewater. A contained air-water interface liquid evaporator may be arranged to pre-process the wastewater before being treated by the wastewater concentrator.

    Abstract translation: 公开了用于处理在热电厂，其它工厂和/或其他工业源处产生的废水的方法，系统和/或设备。 废水通过包括直接接触绝热浓缩系统的废水浓缩器。 热进料气流被引导通过废水浓缩器。 废水浓缩器将热源气体直接与废水混合，并从废水中蒸发出水汽。 废水浓缩器将水蒸气与剩余的浓缩废水分开。 包含的空气 - 水界面液体蒸发器可以被布置成在废水浓缩器处理之前预处理废水。

    COMPACT WASTEWATER CONCENTRATOR AND POLLUTANT SCRUBBER
    8.
    发明申请
    COMPACT WASTEWATER CONCENTRATOR AND POLLUTANT SCRUBBER 审中-公开
    小型废水浓缩器和污染物洗涤器

    公开(公告)号：WO2011014617A2

    公开(公告)日：2011-02-03

    申请号：PCT/US2010/043648

    申请日：2010-07-29

    Applicant: HEARTLAND TECHNOLOGY PARTNERS LLC ,  DUESEL, Bernard, F., Jr. ,  RUTSCH, Michael, J. ,  CLERKIN, Craig

    Inventor： DUESEL, Bernard, F., Jr. ,  RUTSCH, Michael, J. ,  CLERKIN, Craig

    IPC: C02F1/04 ,  C02F1/70 ,  C02F1/66

    CPC classification number: C02F1/048 ,  B01D1/14 ,  B01D1/16 ,  B01D1/20 ,  B01D53/77 ,  C02F1/16 ,  C02F1/66 ,  C02F11/12 ,  C02F2101/101 ,  C02F2101/16 ,  C02F2103/001 ,  C02F2103/06 ,  C02F2103/10 ,  C02F2201/008 ,  C02F2209/005 ,  Y02E50/346 ,  Y02T50/678

    Abstract: A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor.

    Abstract translation: 紧凑和便携式液体浓缩器包括气体入口，气体出口和连接气体入口和气体出口的流动通道，其中流动通道包括加速气体通过流动的变窄部分 走廊。 液体入口在狭窄部分之前的一点处将液体注入气流中，使得气液混合物在流动通道内充分混合，导致一部分液体蒸发。 狭窄部分下游的除雾器或流体洗涤器从气流中除去夹带的液滴并通过再循环回路将除去的液体再循环至液体入口。 待浓缩的新鲜液体也以足以抵消流动走廊中蒸发的液体量的速率引入再循环回路。

    COMPACT WASTEWATER CONCENTRATOR USING WASTE HEAT
    9.
    发明申请
    COMPACT WASTEWATER CONCENTRATOR USING WASTE HEAT 审中-公开
    使用废热的紧凑型废水浓缩器

    公开(公告)号：WO2011014616A2

    公开(公告)日：2011-02-03

    申请号：PCT/US2010/043647

    申请日：2010-07-29

    Applicant: HEARTLAND TECHNOLOGY PARTNERS LLC ,  DUESEL, Bernard, F., Jr. ,  RUTSCH, Michael, J. ,  CLERKIN, Craig

    Inventor： DUESEL, Bernard, F., Jr. ,  RUTSCH, Michael, J. ,  CLERKIN, Craig

    IPC: C02F1/02 ,  C02F11/12 ,  C02F11/16

    CPC classification number: C02F1/048 ,  B01D1/14 ,  B01D1/16 ,  B01D1/20 ,  B01D53/77 ,  C02F1/16 ,  C02F1/66 ,  C02F11/12 ,  C02F2101/101 ,  C02F2101/16 ,  C02F2103/001 ,  C02F2103/06 ,  C02F2103/10 ,  C02F2201/008 ,  C02F2209/005 ,  Y02E50/346 ,  Y02T50/678

    Abstract: A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor.

    Abstract translation: 紧凑和便携式液体浓缩器包括气体入口，气体出口和连接气体入口和气体出口的流动通道，其中流动通道包括加速气体通过流动的变窄部分 走廊。 液体入口在狭窄部分之前的一点处将液体注入气流中，使得气液混合物在流动通道内充分混合，导致一部分液体蒸发。 狭窄部分下游的除雾器或流体洗涤器从气流中除去夹带的液滴并通过再循环回路将除去的液体再循环至液体入口。 待浓缩的新鲜液体也以足以抵消流动走廊中蒸发的液体量的速率引入再循环回路。

    HARMFUL SUBSTANCE REMOVAL SYSTEM AND METHOD
    10.
    发明申请
    HARMFUL SUBSTANCE REMOVAL SYSTEM AND METHOD 审中-公开

    公开(公告)号：WO2020243510A1

    公开(公告)日：2020-12-03

    申请号：PCT/US2020/035240

    申请日：2020-05-29

    Applicant: HEARTLAND TECHNOLOGY PARTNERS LLC

    Inventor： CLERKIN, Craig ,  LAURENT, Benjamin, N.

    IPC: C02F1/04 ,  C02F1/58 ,  B01D1/14 ,  B01D1/30 ,  B01D46/12 ,  B01D53/86

    Abstract: A harmful substance removal system and method include a direct contact liquid concentrator having a gas inlet, a gas outlet, a mixing chamber disposed between the gas inlet and the gas outlet, and a liquid inlet for importing liquid into the mixing chamber. Gas and liquid mixing in the are mixed chamber and a portion of the liquid is vaporized. A demister is disposed downstream of the mixing chamber. The demister includes at least one stage of mist elimination having a first filter that removes particles greater than 9 microns. A fan is coupled to the demister to assist gas flow through the mixing chamber.

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