JP7312217B2 - 構造化要素および使用方法 - Google Patents
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Description
体的に閉鎖される場合がある。当該ユニットセルの各々に持たせる直径は0.5ないし50ミリメートルの範囲の場合がある。当該構造化要素に複数の相互連結したユニットセルを持つ場合があり、そのユニットセルは当該構造化要素の中を貫く曲がりくねったフロー通路を複数含む場合があり、当該流れは前記複数の曲がりくねったフロー通路の中を通ることでそれらの表面と接触する場合がある。
本開示主題は、プロセス装置への、からのおよび/または内の流れの処理を向上させる材料および方法に関する。前記装置はこの装置の中に入りそして/またはその中に存在する流れを調整するための内容物を有するのが典型的である。装置にはまた所望の装置操作、例えば触媒反応および/または質量移動などを起こさせるための内容物も含む。流れ処理機能は、望ましくない種を引き付け、保持しそして/または他の方法で軽減させそして/または有効な流れフロー分割および分配を確保することが含まる場合がある。望ましくない種は、固体状微粒子、分子種および同伴流体を含むが、これらに限られない場合がある。
て置き換える目的で装置全体をオフラインにする必要があり得る。
)そのような装置の加工ゾーンの能力を最大限に利用しながらまたそのような処理ゾーンの解決法の費用を低くしそして(iv)結果として装置の利益率を実質的に向上させる能力を有する。
の望ましくない種がより軽減されることで直接的に装置の性能が向上する。
し500ミクロンの範囲の種を引き付けて保持する能力を有する。
かつ閉鎖、粗さおよび凹凸を好適に組み合わせることを条件として、1立方メートル当たり1,000,000平方メートルを超える表面積を示すより詳細なモデル化を実施した。図12Aに示した構造物では、濾過システムのサイズを非常に小さくし、かつ、層の数を妥当な機能に必要な数にすることによって図11A-11Dと同じ機能を果たすのに十分なばらつきを提供するかもしれない。図12B、CおよびDについても同様な比較を行うことができるが、また、特定の例示態様において、図12A-12Dに示した構造物の表面積は図11A-11Dが物理的に達成することができなかった表面積を2桁以上の規模で上回るということも可能である。
以下に本発明の主な特徴と態様を列挙する。
1. プロセス装置への流れをフロー分割および分配する方法であって、該流れを前記装置内の構造化要素の中に通すことを含み、該構造化要素は表面積が構造化要素1立方メートル当たり200ないし800,000平方メートルの範囲の接触表面を有しかつ前記構造化要素は前記流れのフロー分割および分配を促すに充分な量が存在する、方法。
2. 前記構造化要素の接触表面は、100ナノメートルないし11ミリメートルのサイズの流れの望ましくない種の濾過および軽減を促す、1.記載の方法。
3. 前記構造化要素は表面積が構造化要素1立方メートル当たり少なくとも10,000平方メートルの接触表面を有する、1.記載の方法。
4. 前記構造化要素は表面積が構造化要素1立方メートル当たり800,000平方メートルまでの接触表面を有する、1.記載の方法。
5. 前記構造化要素は、相互に接続された1個以上のユニットセルを含み、各ユニットセルは骨組みおよび複数の面を有する、1.記載の方法。
6. 前記骨組みおよび複数の面は三次元構造を形成する、4.記載の方法。
7. 前記相互に連結されたユニットセルは三次元構造を形成する、5.記載の方法。
8. 前記構造化要素は、複数の凹凸が形成された接触表面を有する、1.記載の方法。9. 前記凹凸は、チャネル、フルート、スパイク、フィブリルおよびフィラメントの中の1つ以上を含む、8.記載の方法。
10. 前記接触表面は、前記枠組みの表面と、前記凹凸の表面と、前記面の表面とを含む、8.記載の方法。
11. 装置への流れから望ましくない種を軽減させる方法であって、
前記流れを前記装置内の構造化要素の中に通すこと、および
前記流れを前記構造化要素の接触表面に接触させることで前記流れに入っている望ましくない種を軽減させることを含み、
前記構造化要素は前記流れの中の前記望ましくない種を軽減させるに充分な量で存在し、
前記構造化要素は表面積が構造化要素1立方メートル当たり200ないし800,000平方メートルの範囲の接触表面を有する、
方法。
12. 前記表面は望ましくない種を引き付け、保持しかつ軽減させる能力を提供する幾何学的特性を有する、11.記載の方法。
13. 装置への流れのフロー分割および分配を促す方法であって、該流れを前記装置内の構造化要素の中に通すこと、および
前記流れを前記構造化要素の接触表面に接触させることで前記流のフロー分割および分配を促すことを含み、
前記構造化要素を前記流れのフロー分割および分配を促すに充分な量で存在させ、
前記構造化要素は表面積が構造化要素1立方メートル当たり200ないし800,00
0平方メートルの範囲の接触表面を有する、
方法。
14. 前記構造化要素は、濾過能力を有し、大きさ100ナノメートルないし11ミリメートルの微粒子を有効に除去し得る濾過能力を有する、13.記載の方法。
15. 前記流れは工業的プロセス流れであり、前記装置は工業用プロセス装置である、1.記載の方法。
16. 前記工業的プロセス流れは炭化水素または無機物を含む、15.記載の方法。
17. 前記工業用プロセス装置は水素化処理装置、蒸留装置または抽出装置を含む、15.記載の方法。
18. 前記三次元構造は、複数のユニットセルを含む多面体であり、前記ユニットセルの面は開放、部分的開放または閉鎖されており、前記凹凸は前記ユニットセルの骨組みの上に形成されている、1.記載の方法。
Claims (11)
- プロセス装置への流れをフロー分割および分配する方法であって、
前記流れを前記装置内の構造化要素の中に通すこと、および
前記流れを前記構造化要素の表面に接触させることを含み、
前記構造化要素の表面は、100ナノメートルから11ミリメートルまでの範囲のサイズを有する濾過可能な固体を前記流れから濾過し、
前記構造化要素は表面積が構造化要素1立方メートル当たり625ないし305,000平方メートルの範囲の接触表面を有しかつ前記構造化要素は前記流れのフロー分割および分配を促すに充分な量が存在し、そして
前記構造化要素は、相互に接続された1個以上のユニットセルを含み、各ユニットセルは骨組みおよび複数の面を有し、個々の前記面は開放、部分的開放または閉鎖されることができ、前記骨組みおよび複数の面は多面体である三次元構造を形成し、前記相互に連結されたユニットセルは三次元構造を形成し、前記構造化要素はユニットセル上に形成された複数の凹凸を含む、
方法。 - 前記構造化要素は表面積が構造化要素1立方メートル当たり少なくとも10,000平方メートルの接触表面を有する、請求項1記載の方法。
- 前記構造化要素は表面積が構造化要素1立方メートル当たり800,000平方メートルまでの接触表面を有する、請求項1記載の方法。
- 前記凹凸は、チャネル、フルート、スパイク、フィブリルおよびフィラメントの中の1つ以上を含む、請求項1記載の方法。
- 前記接触表面は、前記枠組みの表面と、前記凹凸の表面と、前記面の表面とを含む、請求項1記載の方法。
- 装置への流れから望ましくない種を軽減させる方法であって、
前記流れを前記装置内の構造化要素の中に通すこと、および
前記流れを前記構造化要素の接触表面に接触させることで前記流れに入っている望ましくない種を軽減させることを含み、
前記構造化要素の表面は、100ナノメートルから11ミリメートルまでの範囲のサイズを有する濾過可能な固体を前記流れから濾過し、
前記構造化要素は前記流れの中の前記望ましくない種を軽減させるに充分な量で存在し、
前記構造化要素は表面積が構造化要素1立方メートル当たり625ないし305,000平方メートルの範囲の接触表面を有し、そして
前記構造化要素は、相互に接続された1個以上のユニットセルを含み、各ユニットセルは骨組みおよび複数の面を有し、個々の前記面は開放、部分的開放または閉鎖されることができ、記骨組みおよび複数の面は多面体である三次元構造を形成し、前記相互に連結されたユニットセルは三次元構造を形成し、前記構造化要素はユニットセル上に形成された複数の凹凸を含む、
方法。 - 前記接触表面は望ましくない種を引き付け、保持しかつ軽減させる能力を提供する幾何学的特性を有する、請求項6記載の方法。
- 装置への流れのフロー分割および分配を促す方法であって、
前記流れを前記装置内の構造化要素の中に通すこと、および
前記流れを前記構造化要素の接触表面に接触させることで前記流れのフロー分割および分配を促すことを含み、
前記構造化要素の表面は、100ナノメートルから11ミリメートルまでの範囲のサイズを有する濾過可能な固体を前記流れから濾過し、
前記構造化要素は前記流れのフロー分割および分配を促すに充分な量で存在し、
前記構造化要素は表面積が構造化要素1立方メートル当たり625ないし305,000平方メートルの範囲の接触表面を有し、そして
前記構造化要素は、相互に接続された1個以上のユニットセルを含み、各ユニットセルは骨組みおよび複数の面を有し、個々の前記面は開放、部分的開放または閉鎖されることができ、前記骨組みおよび複数の面は多面体である三次元構造を形成し、前記相互に連結されたユニットセルは三次元構造を形成し、前記構造化要素はユニットセル上に形成された複数の凹凸を含む、
方法。 - 前記流れは工業的プロセス流れであり、前記装置は工業用プロセス装置である、請求項8記載の方法。
- 前記工業的プロセス流れは炭化水素または無機物を含む、請求項8記載の方法。
- 前記工業用プロセス装置は水素化処理装置、蒸留装置または抽出装置を含む、請求項8記載の方法。
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US7722832B2 (en) | 2003-03-25 | 2010-05-25 | Crystaphase International, Inc. | Separation method and assembly for process streams in component separation units |
US8728387B2 (en) * | 2005-12-06 | 2014-05-20 | Howmedica Osteonics Corp. | Laser-produced porous surface |
US10744426B2 (en) * | 2015-12-31 | 2020-08-18 | Crystaphase Products, Inc. | Structured elements and methods of use |
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KR102423461B1 (ko) | 2022-07-20 |
KR20210081447A (ko) | 2021-07-01 |
CA3009845C (en) | 2021-06-22 |
BR112018013488A2 (pt) | 2018-12-04 |
JP2019508246A (ja) | 2019-03-28 |
CA3009845A1 (en) | 2017-07-06 |
SG11201805491XA (en) | 2018-07-30 |
US20180093207A1 (en) | 2018-04-05 |
WO2017117492A1 (en) | 2017-07-06 |
US20200376413A1 (en) | 2020-12-03 |
EP3397364A1 (en) | 2018-11-07 |
KR20180098401A (ko) | 2018-09-03 |
JP2023123847A (ja) | 2023-09-05 |
AU2016381170A1 (en) | 2018-07-19 |
US10744426B2 (en) | 2020-08-18 |
US20170189834A1 (en) | 2017-07-06 |
KR102239550B1 (ko) | 2021-04-13 |
JP6916811B2 (ja) | 2021-08-11 |
CL2018001799A1 (es) | 2018-09-28 |
US20200376414A1 (en) | 2020-12-03 |
MY195107A (en) | 2023-01-10 |
NZ743891A (en) | 2019-11-29 |
US11000785B2 (en) | 2021-05-11 |
MX2018007939A (es) | 2018-08-09 |
KR20200044159A (ko) | 2020-04-28 |
JP2021169089A (ja) | 2021-10-28 |
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