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公开(公告)号:US20240084720A1
公开(公告)日:2024-03-14
申请号:US18263469
申请日:2022-01-28
Applicant: NUOVO PIGNONE TECNOLOGIE - SRL
Inventor: Andrea RONCHIERI , Alessandro SZORENYI
CPC classification number: F01K11/02 , F01D25/32 , F01K9/003 , F05D2220/31
Abstract: The disclosure concerns a gland condenser skid system comprising a direct contact heat exchanger as gland condenser, configured to collect and condensate steam coming from a steam turbine sealing system, wherein the steam turbine sealing system is provided with an air buffering seal device, separating steam turbine shaft lubricating oil system from the steam turbine sealing system.
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公开(公告)号:US11821682B2
公开(公告)日:2023-11-21
申请号:US17586081
申请日:2022-01-27
Applicant: Southwest Research Institute
Inventor: Griffin C. Beck , David L. Ransom , Kevin M. Hoopes
CPC classification number: F25J1/0095 , E21B43/34 , F01K9/003 , F01K11/00 , F01K19/00 , F01K27/02 , F25J1/0022 , F25J1/0055 , F25J2210/60 , F25J2260/60 , F25J2260/80 , F25J2270/18 , F25J2290/60
Abstract: The systems and methods described herein integrate a supercritical fluid power generation system with a LNG production/NGL separation system. A heat exchanger thermally couples the supercritical fluid power generation system with the LNG production/NGL separation system. A relatively cool heat transfer medium, such as carbon dioxide, passes through the heat exchanger and cools a first portion of extracted natural gas. The relatively warm heat transfer medium returns to the supercritical fluid power generation system where a compressor and a thermal input device, such as a combustor, are used to increase the pressure and temperature of the heat transfer medium above its critical point to provide a supercritical heat transfer medium. A second portion of the extracted natural gas may be used as fuel for the thermal input device.
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公开(公告)号:US20180252120A1
公开(公告)日:2018-09-06
申请号:US15757350
申请日:2016-08-18
Applicant: ATLAS COPCO AIRPOWER, NAAMLOZE VENNOOTSCHAP
Inventor: Henrik OHMAN
Abstract: An Organic Rankine Cycle (ORC) device and method for transforming heat from a heat source into mechanical energy. The ORC includes a closed circuit containing a two phase working fluid. The circuit comprises a liquid pump for circulating the working fluid consecutively through an evaporator which is configured to be placed in thermal contact with the heat source; through an expander for transforming the thermal energy of the working fluid into mechanical energy; and through a condenser which is in thermal contact with a cooling element. The expander is situated above the evaporator. The fluid outlet of the evaporator is connected to the fluid inlet of the expander by a raiser column which is filled with a mixture of liquid working fluid and of gaseous bubbles of the working fluid, which mixture is supplied to the expander.
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公开(公告)号:US20180224224A1
公开(公告)日:2018-08-09
申请号:US15749115
申请日:2016-07-28
Applicant: Mahle International GmbH
Inventor: Richard Bruemmer , Eberhard Pantow
CPC classification number: F28F19/002 , E03B11/00 , E03B2011/005 , F01K9/00 , F01K9/003 , F01K25/00 , F28D21/0001 , F28D21/0003 , F28D2021/004 , F28D2021/0063 , F28F2250/08 , F28F2255/02
Abstract: A container for a waste heat utilization circuit may include a housing that defines a housing interior such that the housing interior can be flowed through by a working medium. A sheath may be arranged in the housing interior for accommodating an auxiliary medium. The sheath may be fluid-tight and heat-conductive at least in certain areas. The sheath may define a sheath interior of variable volume.
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公开(公告)号:US20180223696A1
公开(公告)日:2018-08-09
申请号:US15504531
申请日:2015-09-08
Applicant: MITSUBISHI HITACHI POWER SYSTEMS, LTD.
Inventor: Kazunori FUJITA
Abstract: This cooling equipment comprises: a refrigerant supply line (81) supplying, to a condenser (6), a condenser refrigerant which cools steam (Sb) that has driven a steam turbine (5), to return the steam (Sb) to water (W); and a cooling part (80) which is disposed on the refrigerant supply line (81), and performs heat exchange between liquefied gas used as fuel for a gas turbine (2) and the condenser refrigerant to heat and vaporize the liquefied gas and to cool the condenser refrigerant at the same time.
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公开(公告)号:US20180202671A1
公开(公告)日:2018-07-19
申请号:US15918916
申请日:2018-03-12
Applicant: Christopher Lee Martin
Inventor: Christopher Lee Martin
CPC classification number: F24F3/1417 , F01K9/003 , F24F5/0035 , F24F2003/144 , F28B9/06 , F28C1/02 , F28C1/04 , F28C1/16 , F28C2001/006 , F28F23/02 , F28F25/02 , F28F25/087 , F28F25/12
Abstract: In various embodiments, the present invention relates to heat dissipation systems including a hygroscopic working fluid integrating waste water as makeup water. The present invention also relates to methods of using the same. The present invention also relates to hygroscopic cooling systems adapted to dispose of waste water by combining the waste water with a hygroscopic working fluid, precipitating impurities and evaporating the remaining water.
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公开(公告)号:US09988946B2
公开(公告)日:2018-06-05
申请号:US14401173
申请日:2013-05-17
Applicant: Naji Amin Atalla
Inventor: Naji Amin Atalla
CPC classification number: F01K25/10 , F01K7/22 , F01K9/003 , F01K25/065 , F01K25/106 , F25B30/02
Abstract: A system for recycling heat or energy of a working medium of a heat engine for producing mechanical work is described. The system may comprise a first heat exchanger (204) for transferring heat from a working medium output from an energy extraction device (202) to a heating agent to vaporize the heating agent; a second heat exchanger (240) for transferring further heat to the vaporized heating agent; a compressor (231) coupled to the second heat exchanger (240) arranged to compress the further-heated heating agent; and a third heat exchanger (211) for transferring heat from the compressed heating agent to the working medium. A heat pump is also described.
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公开(公告)号:US20180093902A1
公开(公告)日:2018-04-05
申请号:US15833745
申请日:2017-12-06
Applicant: Morningside Venture Investments Limited
Inventor: Frank Schubert
CPC classification number: C02F1/048 , C02F1/14 , C02F9/00 , C02F2103/20 , F01K3/18 , F01K9/003 , F01K17/00 , F01K23/10 , Y02W10/37
Abstract: A system reclaiming contaminated water includes a heat exchanger that receives the contaminated water and converts at least a portion of the contaminated water into steam and collects at least a portion of the contaminants within the heat exchanger. A thermal transfer fluid is heated by a heat exchanger is communication with a heat source. The heated fluid is circulated through the heat exchanger to heat the contaminated water. A steam engine is coupled to a generator, the steam engine receives the steam from the heat exchanger to drive the generator to provide power for the system. Steam exhausted from the steam engine is supplied to supplemental heat loads and then condensed in a modular condensing system. The collected contaminants are directed to an evaporation device to remove residual liquid.
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公开(公告)号:US09927178B1
公开(公告)日:2018-03-27
申请号:US15149152
申请日:2016-05-08
Applicant: TDA Research, Inc.
Inventor: Girish Srinivas , Steven Charles Gebhard , Robert James Copeland , David P. Eisenberg
CPC classification number: F28C1/04 , F01K9/003 , F02C6/18 , F05D2220/31 , F05D2220/32 , F05D2260/213
Abstract: A seasonal process that captures stores and uses water in an ambient temperature-dependent manner to improve the efficiency of a natural gas power plant, comprising: (a) providing a natural gas power plant, the natural gas power plant having a flue gas stream, a cooling tower, and a gas turbine; (b) providing a water collection system; (c) providing a water storage facility; wherein the flue gas stream comprises uncondensed water vapor; wherein the water collection system is operably connected to the flue gas stream and the flue gas stream is directed to flow, at least in part, into the water collection system; wherein the water collection system is operably connected to the water storage facility; wherein the water storage facility is operably connected to the cooling tower and the water storage facility is operably connected to the gas turbine; wherein the process comprises the following steps of condensing flue gas water or using water that has been condensed from the flue gas stream based on outdoor ambient dry bulb temperature: (I) Only condensing water from the flue gas stream to produce a condensed water stream if outdoor ambient dry bulb temperature is less than 85° F.; (II) Only using condensed water to spray cool the cooling tower if outdoor ambient dry bulb temperature is at least 85° F.; (III) Only using condensed water to fog cool the gas turbine if outdoor ambient dry bulb temperature is at least 55° F.; wherein condensed water that is not immediately used to cool the cooling tower or to fog cool the gas turbine is stored in the water storage facility; and wherein the process uses a total amount of water on an annual basis to cool the cooling tower and to fog cool the gas turbine that does not exceed the annual amount of water condensed from the flue gas stream. Optionally, the process has a cooling tower that is a dry cooling tower and condensed water is used to spray cool the dry cooling tower, or the cooling tower is a wet cooling tower, or the cooling tower is a hybrid wet-dry cooling tower. The process may further comprise a water collection system having a three stage desiccant cycle and a calcium chloride desiccant that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure or comprises plastic piping or plastic vessels. Or the process may further comprise using a water collection system having at least one direct contact condensing column that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure or comprises plastic piping or plastic vessels. Or the process may further comprise using a water collection system having at least one direct contact condenser and a rotating wheel heat exchanger that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure, or further comprises plastic piping or plastic vessels. The coefficient of performance for the cooling process is optionally at least 2.0.
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公开(公告)号:US09920658B2
公开(公告)日:2018-03-20
申请号:US15642388
申请日:2017-07-06
Applicant: Applied Research Associates, Inc.
Inventor: Aly H. Shaaban , Gong Zhou , Sergio Escobar , Joshua J Mormile , Desiree Kettell
IPC: F01K7/16 , F01K17/02 , C09K5/16 , F25B30/06 , F01K9/00 , F25B23/00 , F28B9/06 , F28D20/00 , F01K3/00 , F25B5/04 , F25B13/00
CPC classification number: F01K17/02 , C09K5/16 , F01K3/004 , F01K7/16 , F01K9/003 , F25B5/04 , F25B13/00 , F25B23/00 , F25B30/06 , F25B2313/02732 , F28B9/06 , F28D20/003 , F28D2020/006 , Y02E60/142
Abstract: A system and method for providing dry cooling of a source liquid, having a plurality of heat exchangers which depolymerize and polymerize a polymer. Specifically, the depolymerization process is endothermic and draws heat from a source liquid in a first heat exchanger, and the polymerization process is exothermic and expels heat from a second heat exchanger. Additional heat exchangers and holding tanks may be incorporated in the system and method. In some embodiments the system further provides additional cooling of the polymer prior to depolymerization using cooler night ambient air.
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