JPWO2020146337A5 - - Google Patents
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- JPWO2020146337A5 JPWO2020146337A5 JP2021539958A JP2021539958A JPWO2020146337A5 JP WO2020146337 A5 JPWO2020146337 A5 JP WO2020146337A5 JP 2021539958 A JP2021539958 A JP 2021539958A JP 2021539958 A JP2021539958 A JP 2021539958A JP WO2020146337 A5 JPWO2020146337 A5 JP WO2020146337A5
- Authority
- JP
- Japan
- Prior art keywords
- jet mill
- fluid
- circulating fluid
- particle size
- grinding chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000000463 material Substances 0.000 claims 33
- 239000012530 fluid Substances 0.000 claims 30
- 239000002245 particle Substances 0.000 claims 17
- 239000011368 organic material Substances 0.000 claims 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 2
- 239000003245 coal Substances 0.000 claims 2
- 239000000126 substance Substances 0.000 claims 2
- 229920002678 cellulose Polymers 0.000 claims 1
- 239000001913 cellulose Substances 0.000 claims 1
- 239000003077 lignite Substances 0.000 claims 1
- 239000004058 oil shale Substances 0.000 claims 1
- 239000011269 tar Substances 0.000 claims 1
Claims (24)
ジェットミルの粉砕チャンバ内に、(i)循環流体と(ii)材料の粒子とを含む第1の流れを配置して、(a)前記循環流体と(b)粉砕済み材料とを含む第2の流れを生成するとともに、前記ジェットミルを前記循環流体によって加圧することと、
前記第2の流れを、サイクロン分離器へと移送するとともに、前記サイクロン分離器を、前記粉砕済み材料の第1部分と、前記粉砕済み材料の第2部分と、を分離するように構成し、前記粉砕済み材料の前記第1部分を、しきい値粒子サイズ以上の粒子サイズを有した粒子を含むものとし、前記材料の前記第2部分を、前記しきい値粒子サイズ未満の粒子サイズを有した粒子を含むものとすることと、
前記粉砕済み材料の前記第1部分を、第1収集器内に収集することと、
第2収集器へと、(1)前記循環流体と(2)前記粉砕済み材料の前記第2部分とを含む第3の流れを移送するとともに、前記第2収集器を、前記第3の流れから前記粉砕済み材料の前記第2部分を分離することにより、前記循環流体を含む第4の流れを生成するように構成することと、
前記第4の流れを、前記材料の追加的な粒子と接触させて、第5の流れを生成することと、を含む、方法。 A method for comminuting one or more substances, comprising:
disposing a first stream comprising (i) a circulating fluid and (ii) particles of material in a grinding chamber of a jet mill, and a second stream comprising (a) said circulating fluid and (b) ground material; and pressurizing the jet mill with the circulating fluid;
conveying the second stream to a cyclonic separator and configuring the cyclonic separator to separate a first portion of the comminuted material and a second portion of the comminuted material; said first portion of said milled material comprising particles having a particle size greater than or equal to a threshold particle size and said second portion of said material having a particle size less than said threshold particle size comprising particles;
collecting the first portion of the pulverized material in a first collector;
transferring a third stream comprising (1) said circulating fluid and (2) said second portion of said comminuted material to a second collector and transferring said second collector to said third stream; separating the second portion of the comminuted material from to produce a fourth stream comprising the circulating fluid;
contacting the fourth stream with additional particles of the material to produce a fifth stream.
前記粉砕チャンバと、
少なくとも1つの第1流体入口を含むマニホールドであり、前記粉砕チャンバを包囲するマニホールドと、
(i)第2流体入口と(ii)材料入口とを有した中空体を含む供給管アセンブリと、を含むものとし、
前記粉砕チャンバを、前記マニホールドに対して及び前記供給管アセンブリの前記中空体に対して流体連通しているものとする、請求項1~6のいずれか一項に記載の方法。 the jet mill,
the grinding chamber;
a manifold including at least one first fluid inlet, the manifold surrounding the grinding chamber;
(i) a second fluid inlet and (ii) a feed tube assembly including a hollow body having a material inlet;
A method according to any preceding claim, wherein the grinding chamber is in fluid communication with the manifold and with the hollow body of the feed tube assembly.
前記供給管アセンブリの前記材料入口内に前記材料を配置することと、
前記少なくとも1つの第1流体入口を介して前記粉砕チャンバ内に前記循環流体を配
置するとともに、前記第2流体入口を介して前記供給管アセンブリ内に前記循環流体を配置することと、を含む、請求項7に記載の方法。 Disposing the first stream in the grinding chamber of the jet mill comprises:
placing the material within the material inlet of the feed tube assembly;
disposing the circulating fluid within the grinding chamber via the at least one first fluid inlet and disposing the circulating fluid within the feed tube assembly via the second fluid inlet; 8. The method of claim 7 .
前記ジェットミルの前記供給管アセンブリの前記材料入口内に前記材料を配置するように構成されたコンベヤフィーダ上に、前記材料を配置することと、をさらに含む、請求項8に記載の方法。 providing a feed hopper containing said material;
9. The method of claim 8 , further comprising placing the material on a conveyor feeder configured to place the material within the material inlet of the feed tube assembly of the jet mill.
材料の平均粒子サイズを減少させることにより粉砕済み材料を生成するように構成されたジェットミルと、
粉砕済み材料の第1部分と、粉砕済み材料の第2部分と、を分離するように構成されたサイクロン分離器であり、前記粉砕済み材料の前記第1部分は、しきい値粒子サイズ以上のサイズを有した粒子を含み、前記粉砕済み材料の前記第2部分は、前記しきい値粒子サイズ未満のサイズを有した粒子を含む、サイクロン分離器と、
前記粉砕済み材料の前記第1部分を収集するように構成された第1収集器と、
前記粉砕済み材料の前記第2部分を収集するように構成された第2収集器と、
コンプレッサと、を含み、
前記ジェットミルは、前記サイクロン分離器と流体連通しており、前記サイクロン分離器は、前記第1収集器及び前記第2収集器と流体連通しており、前記第2収集器は、前記コンプレッサと流体連通しており、前記コンプレッサは、前記ジェットミルと流体連通しており、
前記コンプレッサは、前記ジェットミル、前記サイクロン分離器、及び前記第2収集器に対して、循環流体を連続的に提供するように構成されている、システム。 A system for comminuting material, comprising:
a jet mill configured to produce a ground material by reducing the average particle size of the material;
A cyclone separator configured to separate a first portion of ground material and a second portion of ground material, wherein said first portion of ground material has a threshold particle size or greater. a cyclone separator comprising particles having a size, wherein the second portion of the ground material comprises particles having a size less than the threshold particle size;
a first collector configured to collect the first portion of the comminuted material;
a second collector configured to collect the second portion of the comminuted material;
a compressor;
The jet mill is in fluid communication with the cyclonic separator, the cyclonic separator is in fluid communication with the first collector and the second collector, the second collector with the compressor. in fluid communication, said compressor being in fluid communication with said jet mill;
The system, wherein the compressor is configured to continuously provide circulating fluid to the jet mill, the cyclone separator, and the second collector.
前記供給ホッパーから前記ジェットミルへと材料を輸送するように構成されたコンベヤフィーダと、をさらに含む、請求項17に記載のシステム。 a feed hopper;
18. The system of claim 17 , further comprising a conveyor feeder configured to transport material from the feed hopper to the jet mill.
粉砕チャンバと、
少なくとも1つの第1流体入口を有したマニホールドであり、前記粉砕チャンバを包囲するマニホールドと、
(i)第2流体入口と(ii)材料入口とを有した中空体を含む供給管アセンブリと、を含み、
前記粉砕チャンバは、前記マニホールドに対して及び前記供給管アセンブリの前記中空体に対して流体連通しており、前記少なくとも1つの第1流体入口は、前記粉砕チャンバに対して前記循環流体を供給するように構成され、前記第2流体入口は、前記フィーダに対して前記循環流体を供給するように構成されている、請求項17に記載のシステム。 The jet mill is
a grinding chamber;
a manifold having at least one first fluid inlet and surrounding the grinding chamber;
(i) a feed tube assembly including a hollow body having a second fluid inlet and (ii) a material inlet;
The grinding chamber is in fluid communication with the manifold and with the hollow body of the feed tube assembly, and the at least one first fluid inlet supplies the circulating fluid to the grinding chamber. 18. The system of claim 17 , wherein the second fluid inlet is configured to supply the circulating fluid to the feeder.
請求項17~23のいずれか一項に記載のシステムを準備することと、
前記コンプレッサによって、前記循環流体を、前記システムを通して循環させることと、
前記ジェットミル内に、前記材料の粒子を配置することと、を含む、方法。 A method for comminuting one or more substances, comprising:
Providing a system according to any one of claims 17-23 ;
circulating the circulating fluid through the system with the compressor;
placing particles of said material in said jet mill.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201962790297P | 2019-01-09 | 2019-01-09 | |
US62/790,297 | 2019-01-09 | ||
PCT/US2020/012522 WO2020146337A1 (en) | 2019-01-09 | 2020-01-07 | Methods of jet milling and systems |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2022517956A JP2022517956A (en) | 2022-03-11 |
JPWO2020146337A5 true JPWO2020146337A5 (en) | 2023-01-20 |
Family
ID=69528960
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2021539958A Pending JP2022517956A (en) | 2019-01-09 | 2020-01-07 | Methods and systems for crushing with a jet mill |
Country Status (11)
Country | Link |
---|---|
US (1) | US11731142B2 (en) |
EP (1) | EP3908405A1 (en) |
JP (1) | JP2022517956A (en) |
KR (1) | KR20210114015A (en) |
CN (1) | CN113646090B (en) |
AU (1) | AU2020207237A1 (en) |
CA (1) | CA3126137A1 (en) |
MX (1) | MX2021008273A (en) |
TW (1) | TW202039083A (en) |
WO (1) | WO2020146337A1 (en) |
ZA (1) | ZA202105756B (en) |
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DE102020006724A1 (en) * | 2020-11-03 | 2022-05-05 | Netzsch Trockenmahltechnik Gmbh | Method of operation for a sifter and sifter for classification |
US11827854B2 (en) | 2021-07-30 | 2023-11-28 | Qwave Solutions, Inc. | Methods and systems for liquefaction of carbonaceous materials |
US20230356236A1 (en) * | 2022-05-03 | 2023-11-09 | Mccormick & Company, Inc. | Milling system for edible material |
WO2024167502A1 (en) * | 2023-02-10 | 2024-08-15 | CR Nano, Inc. | Mechanochemical production of tunable planar materials |
US11801514B1 (en) | 2023-02-10 | 2023-10-31 | CR Nano, Inc. | Mechanochemical production of tunable planar materials |
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-
2020
- 2020-01-07 CA CA3126137A patent/CA3126137A1/en active Pending
- 2020-01-07 CN CN202080019747.5A patent/CN113646090B/en active Active
- 2020-01-07 MX MX2021008273A patent/MX2021008273A/en unknown
- 2020-01-07 WO PCT/US2020/012522 patent/WO2020146337A1/en active Application Filing
- 2020-01-07 JP JP2021539958A patent/JP2022517956A/en active Pending
- 2020-01-07 US US17/421,990 patent/US11731142B2/en active Active
- 2020-01-07 KR KR1020217024883A patent/KR20210114015A/en not_active Application Discontinuation
- 2020-01-07 EP EP20704639.2A patent/EP3908405A1/en active Pending
- 2020-01-07 AU AU2020207237A patent/AU2020207237A1/en active Pending
- 2020-01-09 TW TW109100802A patent/TW202039083A/en unknown
-
2021
- 2021-08-04 ZA ZA2021/05756A patent/ZA202105756B/en unknown
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