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公开(公告)号：US08425664B2
公开(公告)日：2013-04-23
申请号：US12687746
申请日：2010-01-14
申请人： J. Clair Batty , David A. Bell , Craig E. Cox
发明人： J. Clair Batty , David A. Bell , Craig E. Cox
IPC分类号： B01D47/00
CPC分类号： F28D7/103 , B01D1/0058 , B01D1/14 , B01D1/16 , B01D1/20 , B01D1/30 , B01D5/0012 , B01D5/0039 , B01D5/006 , B01D47/06 , C02F1/12 , C02F2103/18 , C02F2103/365 , F23J15/022 , F23J2217/50 , F28D21/0003 , F28F1/105 , Y02W10/37
摘要： Petroleous production is associated with effluents well known to foul lines, nozzles, and containers while consuming substantial energy to assist in both production and remediation. A heat exchanger and manifold system maximizes flows, minimizes changes in flow cross-section, and maximizes heat transfer area, while recycling both water and heat between processes. Dirty regions and clean regions result from scrubbing horizontal exhaust stacks and evaporation of production water in concert to remediate one another, while recycling a significant portion of the energy consumed by each. The heat exchanger relies on a manifold having many layered conduits, each connected to a single layer level of one or more cylindrical conduits in the exchanger. The cylinders of the exchanger themselves are arranged in multiple layers, each layer of a heat exchanger element being connected to a single layer of the manifold. Any shape of cylinder may work, but a right circular cylinder having corrugated sheets spacing the layers may be simple to construct.
摘要翻译： 石油生产与污染线，喷嘴和容器众所周知的流出物相关联，同时消耗大量能量以帮助生产和修复。 热交换器和歧管系统使流量最大化，最大限度地减少流动横截面的变化，并最大限度地提高传热面积，同时在工艺间循环水和热。 污染区域和清洁区域是通过洗涤水平排气管和蒸发生产水来协调一致地进行补救，同时回收大量消耗的能量。 热交换器依赖于具有多个分层管道的歧管，每个管道连接到交换器中的一个或多个圆柱形管道的单层级。 交换器本身的气缸以多层布置，热交换器元件的每一层连接到歧管的单层。 圆柱体的任何形状可以起作用，但是具有间隔层的波纹片的右圆柱体可能很简单。
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公开(公告)号：US20100257781A1
公开(公告)日：2010-10-14
申请号：US12759207
申请日：2010-04-13
申请人： J. Clair Batty , Craig E. Cox , David A. Bell
发明人： J. Clair Batty , Craig E. Cox , David A. Bell
CPC分类号： B01D53/1456 , B01D53/1487 , B01D53/77 , B01D53/84 , B01D2257/302 , B01D2257/404 , B01D2257/504 , B01D2257/708 , Y02A50/235 , Y02A50/2358 , Y02C10/02 , Y02P60/24
摘要： Stack gases of a burner, such as a power plant or other combustion source, may be remediated by a captive algae farm cycling some portion of the stack gases through a scrubber, and ultimately out into a manifold feeding a farm composed of tubes hosting the growth of algae. Liquids from the scrubber, including water capturing volatile organic compounds, solid particulates, nitrogen compounds, sulfur compounds, carbon dioxide, and the like, remediate the water and feed the algae farm. Meanwhile, the vapors and other gases provide an environment rich in water vapor, nitrogen compounds acting as fertilizer, and carbon dioxide to feed the algae to promote increased rates of growth. The algae may be recycled as a fuel itself, or may be harvested for use as a soil amendment to enrich the organic content of soils.
摘要翻译： 诸如发电厂或其他燃烧源的燃烧器的堆积气体可以通过捕获的藻类养殖场来修复，所述养殖场将堆积气体的一部分通过洗涤器循环，并且最终进入进料由主管生长的管组成的农场 的藻类。 来自洗涤器的液体，包括水捕获挥发性有机化合物，固体颗粒，氮化合物，硫化合物，二氧化碳等，补救水并进食藻类。 同时，蒸汽和其他气体提供了富含水蒸气的环境，作为肥料的氮化合物，以及二氧化碳来供应藻类以促进增长的生长速率。 藻类可以作为燃料本身被回收，或者可以收获用作土壤修饰物以富集土壤的有机物含量。
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3.发明授权Back pressure-matched, integrated, environmental-remediation apparatus and method 有权背压配套，综合，环保整治设备和方法公开(公告)号：US08425666B2
公开(公告)日：2013-04-23
申请号：US12687753
申请日：2010-01-14
申请人： J. Clair Batty , Craig E. Cox , David A. Bell
发明人： J. Clair Batty , Craig E. Cox , David A. Bell
IPC分类号： B01D47/00
CPC分类号： F28D7/103 , B01D1/0058 , B01D1/14 , B01D1/16 , B01D1/20 , B01D1/30 , B01D5/0012 , B01D5/0039 , B01D5/006 , B01D47/06 , C02F1/12 , C02F2103/18 , C02F2103/365 , F23J15/022 , F23J2217/50 , F28D21/0003 , F28F1/105 , Y02W10/37
摘要： Production brines are used to scrub a horizontal stack receiving exhaust from an energy source, controlling, reducing, or both noxious chemicals. Mutual remediation of flows from petroleous production cool and scrub exhausts from flares burning waste hydrocarbons, heaters lowering viscosity of crude oil, engines driving oil pumps or natural gas compressors, and the like. Resulting evaporation of production brines results in distilled water, more concentrated brines to reduce hauling, or, optionally, dehydrated dry waste minerals from the brines. Year-round operation of brine evaporation ponds is facilitated, and may be another source of process pre-heating.
摘要翻译： 生产盐水用于擦洗从能量源接收废气的水平堆垛，控制，减少或两种有害化学物质。 来自石油气生产的冷却和清洗废气相互补救来自燃烧废碳氢化合物的燃料废气，降低原油粘度的加热器，驱动油泵或天然气压缩机的发动机等。 生产盐水的蒸发导致蒸馏水，更浓缩的盐水，以减少拖运，或任选地从盐水中脱水的干废物矿物质。 盐水蒸发池的全年运行便利，可能是过程预热的另一个来源。
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公开(公告)号：US20100175983A1
公开(公告)日：2010-07-15
申请号：US12687746
申请日：2010-01-14
申请人： J. Clair Batty , David A. Bell , Craig E. Cox
发明人： J. Clair Batty , David A. Bell , Craig E. Cox
CPC分类号： F28D7/103 , B01D1/0058 , B01D1/14 , B01D1/16 , B01D1/20 , B01D1/30 , B01D5/0012 , B01D5/0039 , B01D5/006 , B01D47/06 , C02F1/12 , C02F2103/18 , C02F2103/365 , F23J15/022 , F23J2217/50 , F28D21/0003 , F28F1/105 , Y02W10/37
摘要： Petroleous production is associated with effluents well known to foul lines, nozzles, and containers while consuming substantial energy to assist in both production and remediation. A heat exchanger and manifold system maximizes flows, minimizes changes in flow cross-section, and maximizes heat transfer area, while recycling both water and heat between processes. Dirty regions and clean regions result from scrubbing horizontal exhaust stacks and evaporation of production water in concert to remediate one another, while recycling a significant portion of the energy consumed by each. The heat exchanger relies on a manifold having many layered conduits, each connected to a single layer level of one or more cylindrical conduits in the exchanger. The cylinders of the exchanger themselves are arranged in multiple layers, each layer of a heat exchanger element being connected to a single layer of the manifold. Any shape of cylinder may work, but a right circular cylinder having corrugated sheets spacing the layers may be simple to construct.
摘要翻译： 石油生产与污染线，喷嘴和容器众所周知的流出物相关联，同时消耗大量能量以帮助生产和修复。 热交换器和歧管系统使流量最大化，最大限度地减少流动横截面的变化，并最大限度地提高传热面积，同时在工艺间循环水和热。 污染区域和清洁区域是通过洗涤水平排气管和蒸发生产水来协调一致地进行补救，同时回收大量消耗的能量。 热交换器依赖于具有多个分层管道的歧管，每个管道连接到交换器中的一个或多个圆柱形管道的单层级。 交换器本身的气缸以多层布置，热交换器元件的每一层连接到歧管的单层。 圆柱体的任何形状可以起作用，但是具有间隔层的波纹片的右圆柱体可能很简单。
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5.发明申请Back Pressure-Matched, Integrated, Environmental-Remediation Apparatus and Method 有权背压匹配，综合，环境修复设备和方法公开(公告)号：US20100176064A1
公开(公告)日：2010-07-15
申请号：US12687753
申请日：2010-01-14
申请人： J. Clair Batty , Craig E. Cox , David A. Bell
发明人： J. Clair Batty , Craig E. Cox , David A. Bell
CPC分类号： F28D7/103 , B01D1/0058 , B01D1/14 , B01D1/16 , B01D1/20 , B01D1/30 , B01D5/0012 , B01D5/0039 , B01D5/006 , B01D47/06 , C02F1/12 , C02F2103/18 , C02F2103/365 , F23J15/022 , F23J2217/50 , F28D21/0003 , F28F1/105 , Y02W10/37
摘要： Production brines are used to scrub a horizontal stack receiving exhaust from an energy source, controlling, reducing, or both noxious chemicals. Mutual remediation of flows from petroleous production cool and scrub exhausts from flares burning waste hydrocarbons, heaters lowering viscosity of crude oil, engines driving oil pumps or natural gas compressors, and the like. Resulting evaporation of production brines results in distilled water, more concentrated brines to reduce hauling, or, optionally, dehydrated dry waste minerals from the brines. Year-round operation of brine evaporation ponds is facilitated, and may be another source of process pre-heating.
摘要翻译： 生产盐水用于擦洗从能量源接收废气的水平堆垛，控制，减少或两种有害化学物质。 来自石油气生产的冷却和清洗废气相互补救来自燃烧废碳氢化合物的燃料废气，降低原油粘度的加热器，驱动油泵或天然气压缩机的发动机等。 生产盐水的蒸发导致蒸馏水，更浓缩的盐水，以减少拖运，或任选地从盐水中脱水的干废物矿物质。 盐水蒸发池的全年运行便利，可能是过程预热的另一个来源。
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公开(公告)号：US20120205235A1
公开(公告)日：2012-08-16
申请号：US13372232
申请日：2012-02-13
CPC分类号： B01D1/2856 , B01D1/0082 , B01D1/28 , B01D1/30 , B01D3/007 , B01D3/02 , B01D3/42 , B01D5/0039 , B01D5/006 , F28D21/0001
摘要： An accelerated vapor recompression apparatus 10 converts incoming flow 35a to a concentrate 35c by developing a concentration profile 146 within a tank 30 holding a liquid 23 containing dissolved solids. The resulting curve 160 of saturation temperature of the stratified liquid 23 (such as a brine 23 or other material 23) moves away from the curve 162 corresponding to fully mixed conditions. The shift 174, 180 in saturation temperature results in increased boiling without increased energy from a heater 70 or compressor 50. A method 90, 200 of control of the system provides interventions 203, 204, 205, 206 at different levels 92, 94, 96, 98 of control, ranging from mass flows 35 to work of a compressor 50, heat from a heater 70, and a predictive processing 215 of feedback 217 for controlling commands 216 algorithmically.
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7.发明授权公开(公告)号：US08986509B2
公开(公告)日：2015-03-24
申请号：US13372232
申请日：2012-02-13
CPC分类号： B01D1/2856 , B01D1/0082 , B01D1/28 , B01D1/30 , B01D3/007 , B01D3/02 , B01D3/42 , B01D5/0039 , B01D5/006 , F28D21/0001
摘要： An accelerated vapor recompression apparatus 10 converts incoming flow 35a to a concentrate 35c by developing a concentration profile 146 within a tank 30 holding a liquid 23 containing dissolved solids. The resulting curve 160 of saturation temperature of the stratified liquid 23 (such as a brine 23 or other material 23) moves away from the curve 162 corresponding to fully mixed conditions. The shift 174, 180 in saturation temperature results in increased boiling without increased energy from a heater 70 or compressor 50. A method 90, 200 of control of the system provides interventions 203, 204, 205, 206 at different levels 92, 94, 96, 98 of control, ranging from mass flows 35 to work of a compressor 50, heat from a heater 70, and a predictive processing 215 of feedback 217 for controlling commands 216 algorithmically.
摘要翻译： 加速蒸汽再压缩装置10通过在容纳溶解的固体的液体23的罐30内形成浓度分布146来将进入流35a转化为浓缩物35c。 分层液体23（例如盐水23或其他材料23）的饱和温度的所得曲线160远离对应于完全混合条件的曲线162。 在饱和温度下的位移174,180导致沸腾增加而不增加来自加热器70或压缩机50的能量。系统控制的方法90,200提供不同等级92,94,96的干预203,204,205,206 控制的98，范围从质量流35到压缩机50的工作，加热器70的加热，以及用于在算法上控制命令216的反馈217的预测处理215。
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公开(公告)号：US20120205232A1
公开(公告)日：2012-08-16
申请号：US13372182
申请日：2012-02-13
CPC分类号： B01D1/2856 , B01D1/0082 , B01D1/28 , B01D1/30 , B01D3/007 , B01D3/02 , B01D3/42 , B01D5/0039 , B01D5/006 , F28D21/0001
摘要： An accelerated vapor recompression apparatus 10 converts incoming flow 35a to a concentrate 35c by developing a concentration profile 146 within a tank 30 holding a liquid 23 containing dissolved solids. The resulting curve 160 of saturation temperature of the stratified liquid 23 (such as a brine 23 or other material 23) moves away from the curve 162 corresponding to fully mixed conditions. The shift 174, 180 in saturation temperature results in increased boiling without increased energy from a heater 70 or compressor 50. A method 90, 200 of control of the system provides interventions 203, 204, 205, 206 at different levels 92, 94, 96, 98 of control, ranging from mass flows 35 to work of a compressor 50, heat from a heater 70, and a predictive processing 215 of feedback 217 for controlling commands 216 algorithmically.
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9.发明申请公开(公告)号：US20120205231A1
公开(公告)日：2012-08-16
申请号：US13372276
申请日：2012-02-13
CPC分类号： B01D1/2856 , B01D1/0082 , B01D1/28 , B01D1/30 , B01D3/007 , B01D3/02 , B01D3/42 , B01D5/0039 , B01D5/006 , F28D21/0001
摘要： An accelerated vapor recompression apparatus 10 converts incoming flow 35a to a concentrate 35c by developing a concentration profile 146 within a tank 30 holding a liquid 23 containing dissolved solids. The resulting curve 160 of saturation temperature of the stratified liquid 23 (such as a brine 23 or other material 23) moves away from the curve 162 corresponding to fully mixed conditions. The shift 174, 180 in saturation temperature results in increased boiling without increased energy from a heater 70 or compressor 50. A method 90, 200 of control of the system provides interventions 203, 204, 205, 206 at different levels 92, 94, 96, 98 of control, ranging from mass flows 35 to work of a compressor 50, heat from a heater 70, and a predictive processing 215 of feedback 217 for controlling commands 216 algorithmically.
摘要翻译： 加速蒸汽再压缩装置10通过在容纳溶解的固体的液体23的罐30内形成浓度分布146来将进入流35a转化为浓缩物35c。 分层液体23（例如盐水23或其他材料23）的饱和温度的所得曲线160远离对应于完全混合条件的曲线162。 在饱和温度下的位移174,180导致沸腾增加而不增加来自加热器70或压缩机50的能量。系统控制的方法90,200提供不同等级92,94,96的干预203,204,205,206 控制的98，范围从质量流35到压缩机50的工作，加热器70的加热，以及用于在算法上控制命令216的反馈217的预测处理215。
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公开(公告)号：US09044693B2
公开(公告)日：2015-06-02
申请号：US13372276
申请日：2012-02-13
CPC分类号： B01D1/2856 , B01D1/0082 , B01D1/28 , B01D1/30 , B01D3/007 , B01D3/02 , B01D3/42 , B01D5/0039 , B01D5/006 , F28D21/0001
摘要： An accelerated vapor recompression apparatus 10 converts incoming flow 35a to a concentrate 35c by developing a concentration profile 146 within a tank 30 holding a liquid 23 containing dissolved solids. The resulting curve 160 of saturation temperature of the stratified liquid 23 (such as a brine 23 or other material 23) moves away from the curve 162 corresponding to fully mixed conditions. The shift 174, 180 in saturation temperature results in increased boiling without increased energy from a heater 70 or compressor 50. A method 90, 200 of control of the system provides interventions 203, 204, 205, 206 at different levels 92, 94, 96, 98 of control, ranging from mass flows 35 to work of a compressor 50, heat from a heater 70, and a predictive processing 215 of feedback 217 for controlling commands 216 algorithmically.
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