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公开(公告)号：EP3170541B1
公开(公告)日：2018-09-26
申请号：EP16199234.2
申请日：2016-11-17
Applicant: Bosal Emission Control Systems NV
Inventor： Van Bockryck, Yvo , Luyck, Martijn , Janssens, Jean-Paul Hubert
CPC classification number: F22B1/1807 , B01B1/005 , B01D1/0058 , B01D1/065 , B01D1/14 , B01F5/0421 , B01F5/043 , B01F15/065 , C02F1/16 , F01N5/02
Abstract: A Combined evaporator and mixer (1) for evaporating a liquid, particularly water, and mixing with a gas, particularly natural gas, comprises a housing (2) for receiving individual mixing-evaporation modules (3) and having heating gas openings (21) at two of its ends for allowing hot gas to pass through the mixing-evaporation modules (3), at least one individual mixing-evaporation module (3) having exhaust gas openings (31) at two of its ends, the mixing-evaporation module (3) comprising at least one mixing-evaporation stack (4), the mixing-evaporation stack (4) having at least two individual heat transfer cells (5), wherein the at least two individual heat transfer cells (5) comprise a plurality of heat transfer tubes (51), each heat transfer tube (51) having a tube inlet (511) and a tube outlet (512), the tube inlets (511) being connected to an inlet manifold (52) and the tube outlets (512) being connected to an outlet manifold (53), and wherein the heat transfer tubes (51) are laterally adjacently arranged in at least one row, wherein the at least two heat transfer cells (5) are arranged one beneath the other, and the manifolds (52, 53) of adjacently arranged heat transfer cells (5) are connected to one another through at least one connecting channel piece (54) in a manner so as to form a series arrangement of heat transfer cells (5) forming a mixing-evaporation stack (4), wherein the mixing-evaporation stack (4) further comprises a liquid inlet (41) to the first heat transfer cell (5), for the liquid to be evaporated, as well as a mixing gas inlet (42) for introducing a gas to be mixed with the evaporated liquid into the mixing-evaporation stack (4), and an mixed gas outlet (43) for the gaseous fluid mixture to leave the mixing-evaporation stack (4), the mixing gas inlet (41) being arranged between the heat transfer tube outlets (512) of the first heat transfer cell (5) and the heat transfer tube inlets (511) of the last heat transfer cell (5) of each mixing-evaporation stack (4).
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公开(公告)号：EP3137192A4
公开(公告)日：2018-03-14
申请号：EP15786441
申请日：2015-05-04
Applicant: JOHNSON DAN A , WILSON TOM
Inventor： JOHNSON DAN A , WILSON TOM
CPC classification number: B01D19/0005 , B01D1/14 , B01D1/16 , B01D53/1431 , B01D53/1468 , B01D53/185 , B01D53/52 , C07C7/005 , C10G31/00 , C10G2300/202
Abstract: An apparatus for removing sulfur from a hydrocarbon liquid may comprise a tank with a chamber, a barrier in the chamber forming at least a partial barrier to liquid flow with a gap defined therein, a gas distribution manifold for introducing the gas into the liquid, and a gas conversion structure defining an interior in fluid communication with the chamber. The gas conversion structure may include a conversion tube defining a tube interior in fluid communication with the chamber, an air injection device configured to inject air into the tube interior and draw gas from the chamber, a water injection device configured to inject water into the tube interior to create a mist of water in the tube interior to contact the gas from the chamber of the tank, and a fluid drain configured to drain fluid from the tube interior.
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公开(公告)号：EP3201140A1
公开(公告)日：2017-08-09
申请号：EP15820833.0
申请日：2015-12-18
Applicant: Siemens Aktiengesellschaft
Inventor： ZIEGMANN, Markus
CPC classification number: B01D61/005 , B01D1/14 , B01D5/0027 , B01D5/006 , B01D61/002 , C02F1/445 , F03G7/005
Abstract: The invention relates to a method for operating an osmotic power plant. A first solution (3) with a first concentration of at least one substance (20), which can be dissolved in a solvent of the first solution (3), and a second solution (4) are provided. The second solution (4) has a second lower concentration of the at least one substance (20). At least the first solution (3) is provided by means of at least one thermal separating device (12). In the at least one thermal separating device (12), a starting solution (18) which contains the at least one substance (20) is introduced into an evaporator (17), through which a gaseous medium flows. The at least one substance (20) is discharged out of the evaporator (17) by means of the gaseous medium. The at least one substance (20) which is discharged in the gaseous medium is converted into a liquid phase in a condenser (22) of the at least one thermal separating device (12) in order to provide the first solution (3). In the starting solution (18), a substance which can be more easily converted into the gas phase than the solvent of the starting solution (18) is used as the at least one substance (20). The invention further relates to an osmotic power plant.
Abstract translation: 本发明涉及一种用于操作渗透发电设备的方法。 提供具有第一浓度的至少一种可溶于第一溶液（3）的溶剂中的物质（20）的第一溶液（3）和第二溶液（4）。 第二溶液（4）具有第二较低浓度的至少一种物质（20）。 至少第一解决方案（3）借助于至少一个热分离装置（12）来提供。 在所述至少一个热分离装置（12）中，将包含所述至少一种物质（20）的起始溶液（18）引入蒸发器（17）中，气态介质流过所述蒸发器。 借助气体介质将至少一种物质（20）排出蒸发器（17）。 在气态介质中排出的至少一种物质（20）在至少一个热分离装置（12）的冷凝器（22）中转化为液相以提供第一溶液（3）。 在起始溶液（18）中，使用比起始溶液（18）的溶剂更容易转化为气相的物质作为至少一种物质（20）。 本发明还涉及一种渗透动力装置。
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4.发明公开WASTEWATER PROCESSING SYSTEMS FOR EVAPORATING WATER WITH IMMERGED FLUE GAS INLET 审中-公开用于烟气进入的废水处理系统
公开(公告)号：EP3200888A1
公开(公告)日：2017-08-09
申请号：EP15784192.5
申请日：2015-10-01
Applicant: Heartland Technology Partners LLC
Inventor： RUTSCH, Michael J. , DUESEL, Bernard F. , CLERKIN, Craig
CPC classification number: C02F1/048 , B01D1/0058 , B01D1/14 , B01D19/0057 , C02F2103/34 , F01K7/16 , F01K11/02 , F01K15/00
Abstract: Methods, systems, and/or apparatuses (5) for treating wastewater produced at a thermoelectric power plant, other industrial plants, and/or other industrial sources are disclosed. The wastewater (16) is directed through a wastewater concentrator (5) including a direct contact adiabatic concentration system. A stream of hot feed gases is directed (104) 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 (A) 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，其他工厂和/或其他工业来源处产生的废水的方法，系统和/或装置。 废水直接通过包括直接接触绝热浓缩系统的废水浓缩器。 热原料气流通过废水浓缩器。 废水浓缩器将热的原料气直接与废水混合并蒸发废水中的水蒸气。 废水浓缩器将剩余的浓缩废水中的水蒸气分离出来。 可以布置容纳的空气 - 水界面液体蒸发器，以在废水浓缩器处理之前对废水进行预处理。
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5.发明公开METHOD AND APPARATUS FOR EXTRACTING BOTANICAL OILS 审中-公开VERFAHREN UND VORRICHTUNG ZUR EXTRAKTION PFLANZLICHERÖLE
公开(公告)号：EP3052602A4
公开(公告)日：2017-06-14
申请号：EP14850389
申请日：2014-10-06
Applicant: NATURAL EXTRACTION SERVICES LLC
Inventor： THOMAS C RUSSELL
CPC classification number: B01D11/02 , B01D1/14 , B01D3/343 , B01D11/023 , B01D11/028 , B01D11/0288 , B01D11/0296 , B01D2011/007 , C11B1/10 , C11B9/027
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Patent Agency Ranking
公开(公告)号：EP3170541A1
公开(公告)日：2017-05-24
申请号：EP16199234.2
申请日：2016-11-17
Applicant: Bosal Emission Control Systems NV
Inventor： Van Bockryck, Yvo , Luyck, Martijn , Janssens, Jean-Paul Hubert
CPC classification number: F22B1/1807 , B01B1/005 , B01D1/0058 , B01D1/065 , B01D1/14 , B01F5/0421 , B01F5/043 , B01F15/065 , C02F1/16 , F01N5/02
Abstract: A Combined evaporator and mixer (1) for evaporating a liquid, particularly water, and mixing with a gas, particularly natural gas, comprises
a housing (2) for receiving individual mixing-evaporation modules (3) and having heating gas openings (21) at two of its ends for allowing hot gas to pass through the mixing-evaporation modules (3),
at least one individual mixing-evaporation module (3) having exhaust gas openings (31) at two of its ends, the mixing-evaporation module (3) comprising at least one mixing-evaporation stack (4), the mixing-evaporation stack (4) having at least two individual heat transfer cells (5),
wherein the at least two individual heat transfer cells (5) comprise a plurality of heat transfer tubes (51), each heat transfer tube (51) having a tube inlet (511) and a tube outlet (512), the tube inlets (511) being connected to an inlet manifold (52) and the tube outlets (512) being connected to an outlet manifold (53), and wherein the heat transfer tubes (51) are laterally adjacently arranged in at least one row,
wherein the at least two heat transfer cells (5) are arranged one beneath the other, and the manifolds (52, 53) of adjacently arranged heat transfer cells (5) are connected to one another through at least one connecting channel piece (54) in a manner so as to form a series arrangement of heat transfer cells (5) forming a mixing-evaporation stack (4),
wherein the mixing-evaporation stack (4) further comprises a liquid inlet (41) to the first heat transfer cell (5), for the liquid to be evaporated, as well as a mixing gas inlet (42) for introducing a gas to be mixed with the evaporated liquid into the mixing-evaporation stack (4), and an mixed gas outlet (43) for the gaseous fluid mixture to leave the mixing-evaporation stack (4), the mixing gas inlet (41) being arranged between the heat transfer tube outlets (512) of the first heat transfer cell (5) and the heat transfer tube inlets (511) of the last heat transfer cell (5) of each mixing-evaporation stack (4).Abstract translation: 用于蒸发液体特别是水并与气体特别是天然气混合的组合式蒸发器和混合器（1）包括用于接收单独的混合蒸发模块（3）并具有加热气体开口（21）的壳体（2） 在其两端用于允许热气体穿过混合 - 蒸发模块（3），至少一个单独的混合 - 蒸发模块（3）在其两端具有排气口（31），混合 - 蒸发模块 （3）包括至少一个混合蒸发堆叠（4），所述混合蒸发堆叠（4）具有至少两个单独的传热单元（5），其中所述至少两个单独的传热单元（5）包括多个 （51），每个传热管（51）具有管入口（511）和管出口（512），管入口（511）连接到入口歧管（52）并且管出口 512）连接到出口歧管（53），并且其中传热管（51）是晚期的 至少两个传热单元（5）彼此相邻布置，并且相邻布置的传热单元（5）的歧管（52,53）通过至少一个传热单元 至少一个连接通道件（54），以形成形成混合 - 蒸发堆叠（4）的传热单元（5）的串联布置，其中所述混合 - 蒸发堆叠（4）还包括液体入口 （41）供应给第一传热单元（5）以供蒸发的液体以及用于将待与蒸发的液体混合的气体引入混合蒸发堆叠（4）的混合气体入口（42） ，以及用于气态流体混合物离开混合蒸发堆叠（4）的混合气体出口（43），混合气体入口（41）布置在第一传热单元的传热管出口（512） 5）和每个混合蒸发器的最后一个传热单元（5）的传热管入口（511） （4）。
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7.发明授权Delivery device, methods of manufacture thereof and articles comprising the same 有权输出装置，用于其生产和制品的方法，从而
公开(公告)号：EP2896719B1
公开(公告)日：2016-09-14
申请号：EP15151100.3
申请日：2015-01-14
Applicant: Rohm and Haas Electronic Materials LLC
IPC: C23C16/448 , B01B1/00 , B01B1/06 , B01J4/00
CPC classification number: C23C16/4482 , B01B1/005 , B01B1/06 , B01D1/14 , B01J4/002 , B01J4/004 , B01J4/02 , C23C16/4407 , C23C16/45561 , Y10T137/0391 , Y10T137/2076
Abstract: Disclosed herein is a delivery device comprising a chamber; a gas inlet; a gas outlet; and a dip tube contained within the chamber and having an upper portion and a lower portion, the upper portion of the dip tube being in fluid communication with the gas inlet and being operative to permit the entry of a carrier gas; the lower portion of the dip tube extending into the chamber, the lower portion of the dip tube terminating in an outlet end; and a sleeve; where the sleeve has a first end and a second end; the first end being in an interference fit with the lower portion of the dip tube; and where the sleeve vibrates upon being subjected to a disturbance.
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公开(公告)号：EP3037148A1
公开(公告)日：2016-06-29
申请号：EP15202678.7
申请日：2015-12-24
Applicant: Nanomist Technologies Co., Ltd.
Inventor： MATSUURA, Kazuo
CPC classification number: B01D17/00 , B01D1/14 , B01D1/16 , B01D3/007 , B01D3/346 , B01D5/0039 , B01D46/02 , B04C9/00 , B04C2009/005 , Y02B30/52 , Y02P70/34
Abstract: The method includes an atomization step, and a separation step. A solution L is atomized into mist in air whereby producing mist-mixed air in the atomization step. Droplets of the mist included in the mist-mixed air are classified according to their particle diameter sizes, and exhaust air that contains air as carrier gas is exhausted in the separation step. In the atomizing separation method, the heat energy of both of the latent heat and sensible heat that are included in the exhaust air exhausted in the separation step are collected, and one or both of the solution L to be atomized in the atomization step and air to be blown toward the solution L are heated by the collected heat.
Abstract translation: 该方法包括雾化步骤和分离步骤。 溶液L在空气中雾化成雾状，由此在雾化步骤中产生雾化混合空气。 包含在雾混空气中的雾滴根据其粒径分类，并且在分离步骤中排出含有空气作为载气的排气。 在雾化分离方法中，收集在分离步骤中排出的排气中包含的潜热和显热两者的热能，并且雾化步骤中要雾化的溶液L中的一个或两个和空气 被吹向溶液L的热量被收集的热量加热。
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公开(公告)号：EP3007789A1
公开(公告)日：2016-04-20
申请号：EP14734357.8
申请日：2014-06-06
Inventor： GOVINDAN, Prakash , ELSHARQAWY, Mostafa , LAM, Steven , ST. JOHN, Maximus , LIENHARD, John
CPC classification number: C02F1/048 , B01D1/14 , B01D3/065 , B01D3/146 , B01D3/32 , B01D19/0015 , C02F1/06 , C02F2103/08 , C02F2103/10
Abstract: A feed liquid flows into a second-stage humidifier chamber to form a second-stage humidifier bath. A first remnant of the feed liquid from the second-stage humidifier chamber then flows into a first-stage humidifier chamber to form a first-stage humidifier bath having a temperature lower than that of the second-stage bath. A second remnant of the feed liquid is then removed from the first-stage humidifier. Meanwhile, a carrier gas is injected into and bubbled through the first-stage humidifier bath, collecting a vaporizable component in vapor form from the first remnant of the feed liquid to partially humidify the carrier gas. The partially humidified carrier gas is then bubbled through the second-stage humidifier bath, where the carrier gas collects more of the vaporizable component in vapor form from the feed liquid to further humidify the carrier gas before the humidified carrier gas is removed from the second-stage humidifier chamber.
Abstract translation: 进料液体流入第二级加湿器室以形成第二级加湿器池。 来自第二级增湿器室的进料液体的第一残余物然后流入第一级增湿器室以形成温度低于第二级浴的第一级增湿器浴。 然后从第一级加湿器中除去第二种补料液。 同时，将载气注入并鼓泡通过第一级加湿器槽，从供料液体的第一残余物收集蒸汽形式的可蒸发组分，以部分加湿载气。 然后将部分加湿的载气鼓泡通过第二级加湿器槽，其中载气从进料液体中收集更多汽化组分以在从第二级加湿器室移除之前进一步加湿载气。
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公开(公告)号：EP2922604A1
公开(公告)日：2015-09-30
申请号：EP13811804.7
申请日：2013-11-22
Applicant: Perlemax Ltd
Inventor： ZIMMERMAN, William, Bauer, Jay
CPC classification number: B01D3/16 , B01D1/14 , B01D17/0205 , B01D19/0005 , B01D53/14 , B01D53/18
Abstract: A process of mass transfer is described which utilises latent heat transfer with little or sensible heat transfer. In a preferred process microbubbles are used under certain conditions of contact with a liquid phase to ensure highly effective mass transfer between a gaseous and liquid phase with significantly less than expected or little or no sensible heat transfer. The present invention in part provides a means by which the known state of a cold liquid of varying depths can be changed using a hot gas injected via a micro bubble inducing internal mixing without allowing the resultant mixture to reach equilibrium thereby ensuring the transfer process becomes continuous. Thus a process is described wherein at least one gaseous phase is contacted with at least one liquid phase such that the heat ratio of the system (AA) is maintained at an a value of greater than 0.5, and the mass transfer is effected by passing a gaseous phase comprising microbubbles through a liquid phase of thickness no more than 10 cm.
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