| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 201 | 플라이애쉬 정제 설비 | KR1020190024751 | 2019-03-04 | KR101977056B1 | 2019-05-10 | |
| 202 | 옥외용 정전식 먼지 집진 장치 및 그 제어 방법 | KR1020180081026 | 2018-07-12 | KR101945259B1 | 2019-04-17 | |
| 203 | 자력선별기용 건식 전자석 | KR20160105882 | 2016-08-22 | KR20180021405A | 2018-03-05 | BAE JOON HAN |
| 본발명은, 자력선별기용건식(oilless) 전자석에있어서, 코어영역에배치되며표면에세라믹이코팅된보빈과; 외표면에세라믹이코팅된알루미늄(Al) 또는알루미늄합금(Al alloy) 소재로이루어지며, 상기보빈의축을따라권선(winding)되는코일과; 상기보빈및 상기코일이내부에배치되며, 상기코일로부터방출되는열이전도및 복사로전달되도록상기코일로부터이격되어내부공간을형성하는내부및 외부가세라믹코팅된외함과; 상기외함의외표면에형성되어상기코일로부터방출되는열이복사및 대류로외부로방출되도록형성된알루미늄또는알루미늄합금소재의열방출핀을포함하며, 상기열방출핀은복사열전도율이증가하도록표면에세라믹이코팅되거나, 또는표면이양극산화되어표면적이증가된것을기술적요지로한다. 이에의해자력선별기용건식(oilless) 전자석은내부에절연유를포함하지않아도열방출이우수하여열에의해손상되지않는효과를얻을수 있다. | ||||||
| 204 | 에멀젼 및 기타 혼합물의 단극 분리를 위한 시스템 및 방법 | KR1020157032581 | 2014-04-16 | KR1020150143734A | 2015-12-23 | 마무디셰예드레자; 바라나시크리파케이. |
| 본원에논의된양태들은에멀젼또는기타혼합물의 2개이상의상들을분리시키기위한시스템및 방법에관한것이다. 상기방법은, 상기혼합물에 (예를들면, 그안의인접액적들이순 전하및 단극전하를획득하도록) 순전하및 단극전하를제공함으로써, 그안의유사상액적들의융합을향상시키고, 상기 2개이상의통합된상들을생성시키거나생성을향상시키고; 상기 2개이상의통합된상들을수집함을포함한다. | ||||||
| 205 | 정전 코어레서 및 정전기 합체를 위한 방법 | KR1020147019642 | 2013-01-02 | KR1020140109966A | 2014-09-16 | 티엔하라미카크리스티안수레비; 람머스프레데릭알버트 |
| 본 발명은 튜브(4)의 정면측에 위치된 공급 개구(5)와 튜브(4)의 대향측에 위치된 배출 개구(20)를 가지는 튜브(4), 및 난류를 감소시키거나 튜브(4)를 통해 유동하는 유체 혼합물(3)에 회전 운동을 부여하기 위한, 튜브(4) 내에 배열되고 개방된 인피드측과 대향하는 개방된 아웃피드측 사이에 위치된 유동 안내 베인들(10-18)을 갖는 적어도 하나의 배열구조를 포함하는, 유동 유체 혼합물(3)에서 액체 입자들(2)의 정전기 합체를 위한 장치(1)에 관한 것이다.
|
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| 206 | Ｏｘｙ-ＰＣ용 복합 전기집진장치 | KR1020080098772 | 2008-10-08 | KR1020100039698A | 2010-04-16 | 김용진; 한방우; 김학준 |
| PURPOSE: A complex electro dust collector for OXY-PC is provided to remove micro dust using a dry electro dust collecting device and a wet electro dust collecting device by reducing the load from a sulfur removing device. CONSTITUTION: A complex electro dust collector for OXY-PC comprises the following: a combustion chamber burning fuel by providing pure oxygen; an electro dust collecting device removing micro dust from exhausted gas burnt in the combustion chamber; a sulfur removing device removing sulfur from the gas; and an EGR device supplying the exhausted gas without the micro dust and the sulfur. The electro dust collecting device includes a dry electro dust collecting device(2a) and a wet electro dust collecting device(2b). | ||||||
| 207 | BI-PHASE (SCOTT-T) TRANSFORMER DOUBLE VOLTED AC ELECTROSTATIC COALESCER | US18459506 | 2023-09-01 | US20230405493A1 | 2023-12-21 | Simone Mulas; Pier Domini |
| An electrostatic coalescer apparatus for separating water from a crude oil emulsion comprises a vessel housing having a cavity, an inlet for receiving a crude oil emulsion and outlets for water and purified crude oil. First and second pairs of electrodes are positioned in the vessel cavity. A first Scott-T transformer circuit is coupled to the first pair of electrodes and a second Scott-T transformer circuit is coupled to the second pair of electrodes. The first and second Scott-T transformer circuit receive as an input a 3-phase power supply and output a 2-phase high voltage signal pairs of electrodes. The 2-phase voltage generated between the first pair of electrodes is of the same amplitude and phase as the voltage generated between the second pair of electrodes via the respective Scott-T transformer circuits. A method comprises steps performed during operation of the apparatus. | ||||||
| 208 | BI-PHASE (SCOTT-T) TRANSFORMER DOUBLE VOLTED AC ELECTROSTATIC COALESCER | US17453415 | 2021-11-03 | US20230136607A1 | 2023-05-04 | Simone Mulas; Pier Domini |
| An electrostatic coalescer apparatus for separating water from a crude oil emulsion comprises a vessel housing having a cavity, an inlet for receiving a crude oil emulsion and outlets for water and purified crude oil. First and second pairs of electrodes are positioned in the vessel cavity. A first Scott-T transformer circuit is coupled to the first pair of electrodes and a second Scott-T transformer circuit is coupled to the second pair of electrodes. The first and second Scott-T transformer circuit receive as an input a 3-phase power supply and output a 2-phase high voltage signal pairs of electrodes. The 2-phase voltage generated between the first pair of electrodes is of the same amplitude and phase as the voltage generated between the second pair of electrodes via the respective Scott-T transformer circuits. A method comprises steps performed during operation of the apparatus. | ||||||
| 209 | Desalting plant systems and methods for enhanced tight emulsion crude oil treatment | US17241805 | 2021-04-27 | US11542444B2 | 2023-01-03 | Mohamed Soliman; Khalid Alanazi; Samusideen Adewale Salu; Talal Al-Zahrani |
| Systems and methods for treating a rag layer in a gas oil separation plant. The method includes withdrawing the rag layer from a vessel proximate an oil water interface, conveying the rag layer to a separation device, and recycling separated oil from the separation device back to the gas oil separation plant process. | ||||||
| 210 | CAPTURING SPECIFIC NUCLEIC ACID MATERIALS FROM INDIVIDUAL BIOLOGICAL CELLS IN A MICRO-FLUIDIC DEVICE | US17654938 | 2022-03-15 | US20220379320A1 | 2022-12-01 | Kevin T. Chapman; Eric D. Hobbs; Steven W. Short; Mark P. White; Daniele Malleo |
| Individual biological cells can be selected in a micro-fluidic device and moved into isolation pens in the device. The cells can then be lysed in the pens, releasing nucleic acid material, which can be captured by one or more capture objects in the pens. The capture objects with the captured nucleic acid material can then be removed from the pens. The capture objects can include unique identifiers, allowing each capture object to be correlated to the individual cell from which the nucleic acid material captured by the object originated. | ||||||
| 211 | Methods for the Separation of at Least One Emulsion by Applying an Electrical Field and Device for Carrying Out Said Method | US17530608 | 2021-11-19 | US20220152528A1 | 2022-05-19 | Andreas Leitner; Michael Schadenböck; Udo Muster |
| The present invention relates to a method for the break-up of at least one emulsion and separation of the light and heavy phase with at least an de-emulsification rate of more than 95% in only one apparatus (module) within less than 5 min by applying at least one time dependent or temporal changeable electrical field wherein the at least one electrical field is a high frequency (HF) singular alternating current (AC) field with an electrical field strength between 2,000 and 100,000 V/m and a frequency (HF) between 12,000 Hz and 200,000 Hz. The present invention relates furthermore to a method for the treatment of at least one emulsion by applying at least one direct current (DC) field and at least one high frequency alternating current-HF/AC field wherein the at least one DC field, in particular a pulsed DC-field, and the at least one HF/AC field are applied in series to the emulsion to be treated. The present invention refers further to a device for conducting said methods. | ||||||
| 212 | ADAPTER FOR ELECTRO-COALESCER INSULATED ELECTRODES WITH METAL SEALING FOR ELECTRODES | US17420951 | 2020-01-03 | US20220072450A1 | 2022-03-10 | Arturo Ernesto Menchaca Lobato |
| Electro-coalescer systems herein may include a vessel, a base plate separating a process chamber and an electric enclosure, rod-shaped ceramic insulated electrodes, and a sealing assembly. An end of the electrodes is located within the electric enclosure. The electrodes traverse respective through-holes of the base plate into or through the process chamber, where a second portion is supported by a spacer, configured to maintain a position of the electrodes while allowing fluid passage. The sealing assembly forms a seal between the through-holes and the rod-shaped insulated electrodes, preventing fluid traversing from the process chamber into the electric enclosure. The sealing assembly may include: a metal fitting disposed around the rod-shaped insulated electrode; metal o-rings; metal seats; and a closing nut. The metal fitting has a coefficient of thermal expansion similar to that of the ceramic insulator, thereby preventing breakage of the electrodes during use. | ||||||
| 213 | Methods for the separation of at least one emulsion by applying an electrical field and device for carrying out said method | US17140325 | 2021-01-04 | US11224828B2 | 2022-01-18 | Andreas Leitner; Michael Schadenböck; Udo Muster |
| The present invention relates to a method for the break-up of at least one emulsion and separation of the light and heavy phase with at least an de-emulsification rate of more than 95% in only one apparatus (module) within less than 5 min by applying at least one time dependent or temporal changeable electrical field wherein the at least one electrical field is a high frequency (HF) singular alternating current (AC) field with an electrical field strength between 2,000 and 100,000 V/m and a frequency (HF) between 12,000 Hz and 200,000 Hz. The present invention relates furthermore to a method for the treatment of at least one emulsion by applying at least one direct current (DC) field and at least one high frequency alternating current—HF/AC field wherein the at least one DC field, in particular a pulsed DC-field, and the at least one HF/AC field are applied in series to the emulsion to be treated. The present invention refers further to a device for conducting said methods. | ||||||
| 214 | Simultaneous crude oil dehydration, desalting, sweetening, and stabilization | US16943718 | 2020-07-30 | US11193071B2 | 2021-12-07 | Mohamed Soliman |
| Integrated gas oil separation plant systems and methods are disclosed. Systems and methods include treating a crude oil inlet feed stream with a high pressure production trap (HPPT), a low pressure production trap (LPPT), a low pressure degassing tank (LPDT), a first heat exchanger, a second heat exchanger, a LPPT recycle water stream, a fresh wash water supply stream, and a LPDT recycle water stream, where the LPDT recycle water stream is operable to supply recycle water from the LPDT to an output stream from the HPPT to form the LPPT inlet feed stream. | ||||||
| 215 | Methods for the Separation of at Least One Emulsion by Applying an Electrical Field and Device for Carrying Out Said Method | US17140325 | 2021-01-04 | US20210170306A1 | 2021-06-10 | Andreas Leitner; Michael Schadenböck; Udo Muster |
| The present invention relates to a method for the break-up of at least one emulsion and separation of the light and heavy phase with at least an de-emulsification rate of more than 95% in only one apparatus (module) within less than 5 min by applying at least one time dependent or temporal changeable electrical field wherein the at least one electrical field is a high frequency (HF) singular alternating current (AC) field with an electrical field strength between 2,000 and 100,000 V/m and a frequency (HF) between 12,000 Hz and 200,000 Hz. The present invention relates furthermore to a method for the treatment of at least one emulsion by applying at least one direct current (DC) field and at least one high frequency alternating current—HF/AC field wherein the at least one DC field, in particular a pulsed DC-field, and the at least one HF/AC field are applied in series to the emulsion to be treated. The present invention refers further to a device for conducting said methods. | ||||||
| 216 | Method and apparatus for promoting droplets coalescence in oil continuous emulsions | US16707445 | 2019-12-09 | US10926195B2 | 2021-02-23 | Simone Less; Sebastien A. Duval; Abderrazak Traidia; Regis D. Vilagines |
| Separation apparatuses for the separation of a mixture of two fluids, such as a water-in-oil emulsion, via electrocoalescence, are provided. A separation apparatus may include a series of flow conditioners each having a different permittivity, such that the flow conditioner having a permittivity that is similar or equal to the permittivity of the flowing medium is selected. Another separation apparatus may include a flow conditioner having a frequency-dependent permittivity, such that the frequency of the electric field generated is selected so that the permittivity of the flow conditioner is as similar as possible to or equal to the permittivity of the flowing medium. Another separation apparatus may include a replaceable flow conditioner that may be replaced with a flow conditioner having a permittivity that is as similar to or equal to the permittivity of the flowing medium. | ||||||
| 217 | Simultaneous crude oil dehydration, desalting, sweetening, and stabilization | US16291814 | 2019-03-04 | US10767121B2 | 2020-09-08 | Mohamed Soliman |
| Integrated gas oil separation plant systems and methods are disclosed. Systems and methods include treating a crude oil inlet feed stream with a high pressure production trap (HPPT), a low pressure production trap (LPPT), a low pressure degassing tank (LPDT), a first heat exchanger, a second heat exchanger, a LPPT recycle water stream, a fresh wash water supply stream, and a LPDT recycle water stream, where the LPDT recycle water stream is operable to supply recycle water from the LPDT to an output stream from the HPPT to form the LPPT inlet feed stream. | ||||||
| 218 | System to reduce interface emulsion layer formation in an electrostatic dehydrator or desalter vessel through use of a low voltage electrostatic interface emulsion treatment system inside the vessel | US16164314 | 2018-10-18 | US10745301B2 | 2020-08-18 | S. Pavankumar B. Mandewalkar; Marcus D. Sprenkel; Gary W. Sams |
| A system for separating the components of an incoming oil-water mixture includes two electrode sets, one set arranged to apply an electrostatic field to an oil layer residing within a separator vessel and the other set arranged to apply an electrostatic field to the interface emulsion layer residing within the separator vessel. The first set of electrodes is in communication with a high voltage power source that ranges from 1 to 60 kV; the second set of electrodes is in communication with a low voltage power source that is no greater than 5 kV. Each set of electrodes may also be in communication with a second voltage source to provide increased power to promote effective coalescence. The system may also include power electronics to produce a variable amplitude and a variable frequency voltage supply to one or both electrode sets. | ||||||
| 219 | Method and Apparatus for Promoting Droplets Coalescence in Oil Continuous Emulsions | US16707462 | 2019-12-09 | US20200114281A1 | 2020-04-16 | Simone Less; Sebastien A. Duval; Abderrazak Traidia; Regis D. Vilagines |
| Separation apparatuses for the separation of a mixture of two fluids, such as a water-in-oil emulsion, via electrocoalescence, are provided. A separation apparatus may include a series of flow conditioners each having a different permittivity, such that the flow conditioner having a permittivity that is similar or equal to the permittivity of the flowing medium is selected. Another separation apparatus may include a flow conditioner having a frequency-dependent permittivity, such that the frequency of the electric field generated is selected so that the permittivity of the flow conditioner is as similar as possible to or equal to the permittivity of the flowing medium. Another separation apparatus may include a replaceable flow conditioner that may be replaced with a flow conditioner having a permittivity that is as similar to or equal to the permittivity of the flowing medium. | ||||||
| 220 | Method and Apparatus for Promoting Droplets Coalescence in Oil Continuous Emulsions | US16707445 | 2019-12-09 | US20200114280A1 | 2020-04-16 | Simone Less; Sebastien A. Duval; Abderrazak Traidia; Regis D. Vilagines |
| Separation apparatuses for the separation of a mixture of two fluids, such as a water-in-oil emulsion, via electrocoalescence, are provided. A separation apparatus may include a series of flow conditioners each having a different permittivity, such that the flow conditioner having a permittivity that is similar or equal to the permittivity of the flowing medium is selected. Another separation apparatus may include a flow conditioner having a frequency-dependent permittivity, such that the frequency of the electric field generated is selected so that the permittivity of the flow conditioner is as similar as possible to or equal to the permittivity of the flowing medium. Another separation apparatus may include a replaceable flow conditioner that may be replaced with a flow conditioner having a permittivity that is as similar to or equal to the permittivity of the flowing medium. | ||||||
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