RU2019120009A - Самоподдерживающиеся структуры, имеющие структуры с геометрией пены и активные материалы - Google Patents
Самоподдерживающиеся структуры, имеющие структуры с геометрией пены и активные материалы Download PDFInfo
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Claims (36)
1. Блок обработки, содержащий:
корпус, формирующий внутреннюю область;
самоподдерживающуюся структуру, расположенную во внутренней области, где самоподдерживающаяся структура содержит более чем 50 масс.% активного материала в самоподдерживающейся структуре, где самоподдерживающаяся структура представляет собой структуру с геометрией пены, выполненную с возможностью обеспечения одного или более извилистых каналов для путей течения текучей среды сквозь самоподдерживающуюся структуру;
множество клапанов, прикрепленных к корпусу, где каждый из множества клапанов выполнен с возможностью регулирования течения текучей среды вдоль траектории течения, проходящей между самоподдерживающейся структурой и областью, внешней относительно корпуса.
2. Блок по п. 1, где блок обработки представляет собой блок циклической короткоцикловой адсорбции со слоем адсорбента, выполненный с возможностью удаления примеси из потока газового сырья, проходящего через один или более каналов в самоподдерживающейся структуре.
3. Блок по любому из пп. 1, 2, в котором самоподдерживающаяся структура содержит более чем 60 масс.% активного материала в самоподдерживающейся структуре.
4. Блок по любому из пп. 1, 2, в котором самоподдерживающаяся структура содержит более чем 70 масс.% активного материала в самоподдерживающейся структуре.
5. Блок по любому из пп. 1-4, в котором блок со слоем адсорбента дополнительно содержит распределитель потока, расположенный между слоем адсорбента и множеством клапанов.
6. Блок по любому из пп. 1-5, в котором корпус выполнен с возможностью поддерживания абсолютного давления от 5 фунтов на квадратный дюйм (0,035 МПа) до 1400 фунтов на квадратный дюйм (9,8 МПа).
7. Блок по любому из пп. 1-6, в котором самоподдерживающаяся структура имеет поры в интервале от 10 пор на линейный дюйм до 100 пор на линейный дюйм .
8. Блок по любому из пп. 1-6, в котором самоподдерживающаяся структура имеет поры в интервале от 20 пор на линейный дюйм до 40 пор на линейный дюйм.
9. Блок по любому из пп. 1-6, в котором самоподдерживающаяся структура содержит множество первых листов, имеющих первый состав и первую плотность пор, и множество вторых листов, имеющих второй состав и вторую плотность пор, где первая плотность пор находится в интервале от 1 поры на линейный дюйм пор на линейный дюйм до 20 пор на линейный дюйм, а вторая плотность пор находится в интервале от 20 пор на линейный дюйм до 100 пор на линейный дюйм.
10. Блок по любому из пп. 1-7, в котором самоподдерживающаяся структура имеет низкую термическую массу.
11. Способ удаления примесей из исходного потока, в котором:
а) выполняют один или более этапов адсорбции в блоке с адсорбционным слоем, где в каждом из одного или более этапов адсорбции: пропускают исходный газовый поток сквозь самоподдерживающуюся структуру, расположенную во внутренней области корпуса блока с адсорбционным слоем, для удаления одной или более примесей из исходного газового потока, где самоподдерживающаяся структура имеет более чем 50 масс.% активного материала в самоподдерживающейся структуре, где самоподдерживающая структура представляет собой структуру с геометрией пены, выполненную с возможностью обеспечения одного или более извилистых каналов для путей течения текучей среды через самоподдерживающуюся структуру;
b) выполняют один или более этапов регенерации, где в каждом из одного или более этапов регенерации удаляют, по меньшей мере, часть одной или более примесей в выходящем потоке примесей; и
с) повторяют этапы от а) до b) в течение, по меньшей мере, одного дополнительного цикла.
12. Способ по п. 11, где способ представляет собой короткоцикловую адсорбцию, и продолжительность цикла имеет период более чем 1 секунда и меньше чем 600 секунд.
13. Способ по п. 11, в котором продолжительность цикла имеет период более чем 1 секунда и меньше чем 300 секунд с отделением одной или более примесей из исходного газового потока с образованием потока продукта.
14. Способ по любому из пп. 11-13, в котором во время выполнения одного или более этапов регенерации выполняют один или более этапов продувки, где в каждом из одного или более этапов продувки пропускают поток продувки через самоподдерживающуюся структуру с извлечением, по меньшей мере, части одной или более примесей в выходной поток примесей.
15. Способ по любому из пп. 11-14, в котором исходный газовый поток представляет собой углеводородсодержащий поток, имеющий более чем один объемный процент углеводородов в расчете на полный объем исходного газового потока.
16. Способ по любому из пп. 11-15, в котором абсолютное исходное давление исходного газового потока находится в интервале от 400 фунтов на квадратный дюйм (2,8 МПа) до 1400 фунтов на квадратный дюйм (9,8 МПа).
17. Способ по любому из пп. 11-16, в котором один или более этапов адсорбции выполняют так, что уровень диоксида углерода (СО2) снижают до менее чем 50 частей на миллион по объему.
18. Способ по любому из пп. 11-17, в котором один или более этапов адсорбции выполняют так, что уровень воды (Н2О) снижают до менее чем 105 частей на миллион по объему.
19. Способ по любому из пп. 11-18, в котором самоподдерживающаяся структура имеет низкую термическую массу.
20. Способ по любому из пп. 11-19, в котором самоподдерживающаяся структура имеет поры в интервале от 15 пор на дюйм до 60 пор на дюйм.
21. Способ получения блока обработки, в котором:
смешивают активный материал со связующим материалом, где смесь имеет более чем 50 масс.% активного материала, и оставшаяся часть смеси включает связующий материал;
формируют самоподдерживающуюся структуру из смеси, где самоподдерживающаяся структура представляет собой структуру с геометрией пены, выполненную с возможностью обеспечения одного или более извилистых каналов для путей течения текучей среды через самоподдерживающуюся структуру;
сушат самоподдерживающуюся структуру; и
размещают самоподдерживающуюся структуру внутри корпуса блока обработки, имеющего внутреннюю область.
22. Способ по п. 21, в котором формирование самоподдерживающейся структуры дополнительно включает спекание связующего материала и активного материала в связанную твердую структуру, которая представляет собой самоподдерживающуюся структуру.
23. Способ по п. 22, в котором при спекании дополнительно подвергают самоподдерживающуюся структуру воздействию температур в интервале от 400°С до 800°С.
24. Способ по любому из пп. 21-23, в котором дополнительно:
создают множество портов для клапанов в корпусе; и
крепят клапаны к корпусу в каждом из множества портов для клапанов, образуя множество клапанов, где каждый из множества клапанов выполнен с возможностью регулирования течения текучей среды между самоподдерживающейся структурой и областью снаружи от корпуса.
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CA3003169A1 (en) | 2015-10-27 | 2017-05-04 | Exxonmobil Upstream Research Company | Apparatus and system for swing adsorption processes related thereto having actively-controlled feed poppet valves and passively controlled product valves |
EA201891041A1 (ru) | 2015-10-27 | 2018-09-28 | Эксонмобил Апстрим Рисерч Компани | Устройство и система для процессов короткоцикловой адсорбции, имеющие множество клапанов |
US10744449B2 (en) | 2015-11-16 | 2020-08-18 | Exxonmobil Upstream Research Company | Adsorbent materials and methods of adsorbing carbon dioxide |
JP2019508221A (ja) * | 2015-12-22 | 2019-03-28 | シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー | 酸化窒素を減少させるための反応器 |
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US10434458B2 (en) | 2016-08-31 | 2019-10-08 | Exxonmobil Upstream Research Company | Apparatus and system for swing adsorption processes related thereto |
BR112019002106B1 (pt) | 2016-09-01 | 2023-10-31 | ExxonMobil Technology and Engineering Company | Processo para remover água de corrente de alimentação gasosa,sistema cíclico adsorvente por variação de ciclo rápido e contator de canal substancialmente paralelo |
US10549230B2 (en) | 2016-12-21 | 2020-02-04 | Exxonmobil Upstream Research Company | Self-supporting structures having active materials |
EP3558487A1 (en) | 2016-12-21 | 2019-10-30 | ExxonMobil Upstream Research Company | Self-supporting structures having active materials |
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US11331620B2 (en) | 2018-01-24 | 2022-05-17 | Exxonmobil Upstream Research Company | Apparatus and system for swing adsorption processes |
US20190262765A1 (en) | 2018-02-28 | 2019-08-29 | William Barnes | Apparatus and System for Swing Adsorption Processes |
EP3758828A1 (en) | 2018-02-28 | 2021-01-06 | ExxonMobil Upstream Research Company | Apparatus and system for swing adsorption processes |
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2017
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- 2017-11-29 JP JP2019534402A patent/JP7021226B2/ja active Active
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US20200114299A1 (en) | 2020-04-16 |
EP3558490B1 (en) | 2022-06-29 |
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JP7021226B2 (ja) | 2022-02-16 |
EP3558490A1 (en) | 2019-10-30 |
AU2017379685A1 (en) | 2019-07-04 |
CA3045040A1 (en) | 2018-06-28 |
AU2017379685B2 (en) | 2020-03-12 |
CA3045040C (en) | 2022-04-26 |
US20180169565A1 (en) | 2018-06-21 |
RU2019120009A3 (ru) | 2021-01-22 |
WO2018118361A1 (en) | 2018-06-28 |
CN110099730A (zh) | 2019-08-06 |
US11148091B2 (en) | 2021-10-19 |
KR20190097233A (ko) | 2019-08-20 |
JP2020514024A (ja) | 2020-05-21 |
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