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公开(公告)号：US20210057455A1
公开(公告)日：2021-02-25
申请号：US16998267
申请日：2020-08-20
IPC分类号： H01L27/12 , H01L27/11502 , H01L21/02
摘要： Various examples are provided related to hydrogen plasma treatment of hafnium oxide. In one example, a method includes depositing a monolayer of a precursor on a first oxide monolayer; forming a second oxide monolayer by applying an oxygen (O2) plasma to the monolayer of the precursor; and creating oxygen vacancies in the second oxide monolayer by applying a hydrogen (H2) plasma to the second oxide monolayer. In another example, a device includes a hafnium oxide (HfO2) based ferroelectric thin film on a first side of a substrate and an electrode layer disposed on the HfO2 based ferroelectric thin film opposite the substrate. The HfO2 film includes a plurality of oxide monolayers including at least one HfO2 monolayer, each of the plurality of oxide monolayers having oxygen vacancies distributed throughout that oxide monolayer.
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2.发明申请公开(公告)号：US20190314769A1
公开(公告)日：2019-10-17
申请号：US16382851
申请日：2019-04-12
发明人： Saeed Moghaddam
摘要： Various examples are provided for highly selective and ultra-high throughput filtration using bilayer two-dimensional (2D) material laminates and highly absorptive medium of 2D material laminates or solution dispersions. In one example, a 2D material bilayer membrane includes a first membrane layer; an interlinking layer of interlinking molecules disposed on the first membrane layer; and a second membrane layer disposed on the interlinking layer. The interlinking molecules electrostatically or covalently interlink the second membrane layer and first membrane layer.
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公开(公告)号：US09488392B2
公开(公告)日：2016-11-08
申请号：US14353391
申请日：2012-10-25
发明人： Saeed Moghaddam
CPC分类号： F25B15/00 , F25B17/02 , F25B37/00 , F25B2315/00 , F28D3/02 , F28D21/0015 , Y02A30/277 , Y02B30/62
摘要： An exchanger for absorption or desorption of a refrigerant employs an ultra thin film (UTF) of a refrigerant solution constrained to a channel by a permeable membrane. The UTF has a thickness of about 250 μm or less. The permeable membrane can be a nanostructured membrane, such as a membrane of nanofibers. The exchangers can be employed in an absorption refrigeration system (ARS) that use waste heat or solar heaters permitting the ARS to be less than one tenth the volume and mass of a conventional ARS.
摘要翻译： 用于制冷剂吸收或解吸的交换器采用通过渗透膜限制在通道上的制冷剂溶液的超薄膜（UTF）。 UTF具有约250μm或更小的厚度。 渗透膜可以是纳米结构膜，例如纳米纤维膜。 这些交换器可用于使用废热或太阳能加热器的吸收式制冷系统（ARS），其允许ARS小于常规ARS的体积和质量的十分之一。
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4.发明申请Hierarchical Hydrophilic/Hydrophobic Micro/Nanostructures for Pushing the Limits of Critical Heat Flux 审中-公开用于推动临界热通量极限的分层亲水/疏水微/纳米结构公开(公告)号：US20160295742A1
公开(公告)日：2016-10-06
申请号：US15185766
申请日：2016-06-17
发明人： Saeed Moghaddam , Seyyed A. Fazeli
IPC分类号： H05K7/20 , H01L23/427 , H01L23/367 , F28D15/02
CPC分类号： H05K7/20309 , F28D15/025 , F28D15/046 , F28F3/02 , F28F13/187 , F28F2245/04 , F28F2255/20 , H01L23/3675 , H01L23/427 , H01L2924/0002 , H05K7/20318 , H05K7/20327 , H01L2924/00
摘要： A high efficiency heat sink for the cooling of microelectronic devices involves a phase change from liquid fluid to fluid vapor with a vapor quality of 100%. The liquid fluid is provided to an active area that contains fins having micrometer dimension that support a membrane that is nanoporous. The membrane is effectively impermeable to liquid fluid but permeable to fluid vapor. The heat sink provides very high heat flux and coefficient of heat transfer at low mass flux over a broad range of surface superheat temperatures. The heat sink can be constructed of equi-spaced posts that separate liquid microchannels from vapor microchannels that are connected through capillary forced valves formed between adjacent equi-spaced posts.
摘要翻译： 用于微电子器件冷却的高效率散热器涉及从液体流体到具有100％蒸气质量的流体蒸气的相变。 液体流体被提供到活动区域，该活动区域包含支撑纳米多孔膜的微米尺寸的翅片。 该膜对液体流体是有效的不可渗透的，但是可以渗透流体蒸气。 在宽范围的表面过热温度下，散热器在低质量通量下提供非常高的热通量和传热系数。 散热器可以由等间隔的柱构成，其将液体微通道与通过形成在相邻等间隔柱之间的毛细管强制阀连接的蒸气微通道分开。
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公开(公告)号：US20170103988A1
公开(公告)日：2017-04-13
申请号：US15286946
申请日：2016-10-06
IPC分类号： H01L27/115 , H01L29/51 , H01L21/02 , H01L29/66 , H01L21/28 , H01L29/423 , H01L29/78 , H01L29/49
CPC分类号： H01L21/0228 , G11C11/22 , G11C11/221 , H01L21/02148 , H01L21/02181 , H01L21/02189 , H01L21/02194 , H01L21/022 , H01L21/02321 , H01L21/02356 , H01L21/28291 , H01L28/40 , H01L28/56 , H01L29/42364 , H01L29/516 , H01L29/517 , H01L29/6684
摘要： Techniques for forming an electronic device having a ferroelectric film are described. The electronic device comprises a ferroelectric material having one or more crystalline structures. The one or more crystalline structures may comprise hafnium, oxygen, and one or more dopants. The one or more dopants are distributed in the ferroelectric material to form a first layer, a second layer, and a third layer. The second layer is positioned between the first layer and the third layer. Distribution of one or more dopants within the first layer, the second layer, and the third layer may promote a crystalline structure to have an orthorhombic phase.
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6.发明申请Open Absorption Cycle for Combined Dehumidification, Water Heating, and Evaporative Cooling 审中-公开组合除湿，热水和蒸发冷却的开放吸收循环公开(公告)号：US20160320079A1
公开(公告)日：2016-11-03
申请号：US15206920
申请日：2016-07-11
发明人： Saeed Moghaddam , Devesh Chugh , Rasool Nasrisfahani , Sajjad Bigham , Seyyed A. Fazeli , Dazhi Yu , Mehdi Mortazavi , Omar Abdelaziz
CPC分类号： F24F5/0014 , F24F3/1411 , F24F3/1417 , F24F5/0035 , F24F2003/1435 , F24F2013/225 , F24F2221/54 , F24H4/00 , F25B15/06 , F25B25/005 , F25B31/00 , F25B35/02 , Y02A30/277 , Y02B30/12 , Y02B30/62
摘要： An absorption cycle system, which permits water heating, dehumidifying, and/or evaporative cooling, includes a desorber, absorber, heat exchanger, and, optionally, an evaporator, is constructed to heat a process water that is plumbed through the absorber, heat exchanger, and condenser. In the absence or isolation of the evaporator, the system can dehumidify ambient air to the absorber. The water vapor released by evaporative cooling at the evaporator can be provided to the absorber in a controlled manner to simultaneously maintain a desired humidity while cooling the air ambient by the evaporator. The absorption cycle system can be housed within a single unit or can be compartmentalized.
摘要翻译： 允许水加热，除湿和/或蒸发冷却的吸收循环系统包括解吸器，吸收器，热交换器和任选的蒸发器，以加热通过吸收器，热交换器 ，和冷凝器。 在不存在或隔离蒸发器的情况下，系统可以将环境空气除湿到吸收器。 在蒸发器中通过蒸发冷却释放的水蒸汽可以以受控的方式提供给吸收器，以同时保持所需的湿度，同时通过蒸发器冷却空气环境。 吸收循环系统可以容纳在单个单元中，或者可以被分隔。
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公开(公告)号：US10677501B2
公开(公告)日：2020-06-09
申请号：US15762333
申请日：2016-09-26
发明人： Saeed Moghaddam , Mehdi Mortazavi , Sajjad Bigham
摘要： An absorber for an absorption refrigeration system for a vertically mounted plate absorber has fins positioned over the plate to promote distribution of a fluid under flow as a nearly continuous thin film. The absorber has rows of fins that are evenly spaced with the fins occupying a portion of the active width of the plate with adjacent rows offset by the width of the plate. A combined evaporator-absorber module is constructed with the absorbing face of the absorber parallel with an evaporating surface of an evaporator where absorber solution and refrigerant fall as parallel falling sheets of liquid. The absorber is covered with a porous hydrophobic membrane to isolate the falling absorber solution from the falling liquid refrigerant.
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公开(公告)号：US09951976B2
公开(公告)日：2018-04-24
申请号：US15316246
申请日：2015-06-02
发明人： Saeed Moghaddam , Devesh Chugh
CPC分类号： F25B15/16 , F25B15/00 , F25B15/06 , Y02A30/277 , Y02B30/62
摘要： An absorption based heater is constructed on a fluid barrier heat exchanging plate such that it requires little space in a structure. The absorption based heater has a desorber, heat exchanger, and absorber sequentially placed on the fluid barrier heat exchanging plate. The vapor exchange faces of the desorber and the absorber are covered by a vapor permeable membrane that is permeable to a refrigerant vapor but impermeable to an absorbent. A process fluid flows on the side of the fluid barrier heat exchanging plate opposite the vapor exchange face through the absorber and subsequently through the heat exchanger. The absorption based heater can include a second plate with a condenser situated parallel to the fluid barrier heat exchanging plate and opposing the desorber for condensation of the refrigerant for additional heating of the process fluid.
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公开(公告)号：US20210113753A1
公开(公告)日：2021-04-22
申请号：US17072983
申请日：2020-10-16
发明人： Saeed Moghaddam
摘要： Various examples are provided related to dialysate-free renal replacement. In one example, a dialysate-free continuous renal replacement system includes a blood filtration stage (e.g., in a microfluidic membrane module). The blood filtration stage can include a blood filtration membrane configured to that can provide a filtered fluid by renal filtration of blood passing through the blood filtration stage at arterial pressure. The continuous renal replacement system can also include a salt recovery stage and a water recovery stage. The salt recovery stage can recover ions through separation from the blood filtration stage. The water recovery stage can separate water from the desalted fluid from the salt recovery stage, where the water is combined with the separated ions and reinfused into the blood after passing through the blood filtration stage.
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公开(公告)号：US10315165B2
公开(公告)日：2019-06-11
申请号：US15516989
申请日：2015-10-05
发明人： Mark E. Orazem , Rui Kong , Saeed Moghaddam , Yuelong Huang , Dazhi Yu , Han Lai , David A. Horner , David Bloomquist
IPC分类号： B01D61/56 , C02F11/00 , C02F11/12 , C02F101/10
摘要： Various methods and systems are provided for electrokinetic dewatering of suspensions such as, e.g., phosphatic clay. In one example, among others, a system for continuous dewatering includes a cake formation zone including a first anode and a first cathode each extending across a first portion of a separation chamber; a cake dewatering zone including a second anode and a second cathode; an inlet configured to supply a dilute feed suspension comprising solids suspended in water to the cake formation zone; and a conveying belt extending between the first anode and the first cathode and between the second anode and the second cathode. A first electric field between the first anode and the first cathode forms a cake on the conveying belt by consolidating the solids, and a second electric field between the second anode and the second cathode dewaters the cake on the conveying belt.
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