JPS63164902U - - Google Patents

Info

Publication number
JPS63164902U
JPS63164902U JP3091488U JP3091488U JPS63164902U JP S63164902 U JPS63164902 U JP S63164902U JP 3091488 U JP3091488 U JP 3091488U JP 3091488 U JP3091488 U JP 3091488U JP S63164902 U JPS63164902 U JP S63164902U
Authority
JP
Japan
Prior art keywords
dispersion
contact section
flow path
cyclone
extends
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.)
Granted
Application number
JP3091488U
Other languages
Japanese (ja)
Other versions
JPH0630241Y2 (en
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Publication of JPS63164902U publication Critical patent/JPS63164902U/ja
Application granted granted Critical
Publication of JPH0630241Y2 publication Critical patent/JPH0630241Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions

Description

【図面の簡単な説明】[Brief explanation of the drawing]

第１図は、本考案の接触装置の概略図である。
第２図は、装置の分離セクシヨンの変形例を示す
図である。第３図は、装置の他実施例を示す図で
ある。第４図は、装置のさらに他の実施例を示す
図である。第５図は、第４図の５−５に沿う断面
図である。第６図は、接触セクシヨンの変形例を
示す概略図である。第７図は、第６図の混合セク
シヨンの平面図である。第８図および第９図は接
触セクシヨンのさらに他の変形例を示す概略図で
ある。 １０……入口、１２……入口ノズル、１４……
インゼクタ、１６……ノズル、１８……ノズル、
２０……接触セクシヨン、２２……流れ方向変更
部材、２４……中央ロツド、２６……サイクロン
、２８……渦流フアインダ、３０……出口。 FIG. 1 is a schematic diagram of the contact device of the present invention.
FIG. 2 shows a modification of the separation section of the device. FIG. 3 is a diagram showing another embodiment of the apparatus. FIG. 4 is a diagram showing still another embodiment of the device. FIG. 5 is a sectional view taken along line 5-5 in FIG. 4. FIG. 6 is a schematic diagram showing a modification of the contact section. 7 is a plan view of the mixing section of FIG. 6; FIG. FIGS. 8 and 9 are schematic diagrams showing still other modifications of the contact section. 10...Inlet, 12...Inlet nozzle, 14...
Injector, 16... nozzle, 18... nozzle,
20...Contact section, 22...Flow direction changing member, 24...Central rod, 26...Cyclone, 28...Vortex flow finder, 30...Outlet.

Claims (1)

【実用新案登録請求の範囲】 (1) 混和しないまたは部分的に混和する流体を
接触する装置において、流体の少なくとも１つの
初期運動エネルギーによつて流体を混和して分散
液を形成する混合装置と、分散液の流体成分を互
いに分離するサイクロン装置と、混合装置からサ
イクロン装置に分散液を運ぶ接触セクシヨンと、
を有し、接触セクシヨンは分散液が混合装置から
サイクロン装置に通過する際分散液の流れの方向
を反復的にまたは連続的に変更する手段を含むこ
とを特徴とする装置。 (2) 請求項１記載の装置において、接触セクシ
ヨンを通る分散液の流路は接触セクシヨン内の分
散液の残留時間が混合装置および（または）サイ
クロン装置のものより大きいようなものであるこ
とを特徴とする装置。 (3) 請求項２記載の装置において、接触セクシ
ヨン内の前記残留時間が混合装置および（または
）サイクロン装置より少なくとも１つ大きなオー
ダーであることを特徴とする装置。 (4) 請求項１，２または３のいずれか１つに記
載の装置において、接触セクシヨンを通る流路は
湾曲、リビリンスまたは迷路形状であることを特
徴とする装置。 (5) 請求項１ないし４のいずれか１つに記載の
装置において、接触セクシヨンが接触セクシヨン
を通る分散液の流路中にランダムなまたは規則的
な詰め物を組込んでいることを特徴とする装置。 (6) 請求項１ないし５のいずれか１つに記載の
装置において、サイクロン装置が接触セクシヨン
内に少なくとも途中までのびていることを特徴と
する装置。 (7) 請求項６記載の装置において、接触セクシ
ヨン内の分散液の流路がサイクロン装置のまわり
に少なくとも部分的に延びていることを特徴とす
る装置。 (8) 請求項６または７記載の装置において、サ
イクロンによつて発生される渦流の軸線が接触セ
クシヨンによつて形成される流路の長手方向に延
びていることを特徴とする装置。 (9) 請求項１ないし５のいずれか１つに記載の
装置において、接触セクシヨンがサイクロン装置
または混合装置の軸線を囲む流路に分散液を拘束
する手段を含むことを特徴とする装置。 (10) 請求項９記載の装置において前記流路が平
面内で広がるらせん状に延びていることを特徴と
する装置。 〓(11)１１〓 請求項９記載の装置において、前
記流路が軸線方向にらせん状に延びていることを
特徴とする装置。 〓(12)１２〓 請求項９記載の装置において、前
記流路が半径方向に波形状であることを特徴とす
る装置。[Claims for Utility Model Registration] (1) A device for contacting immiscible or partially miscible fluids, which includes a mixing device that mixes the fluids to form a dispersion using at least one initial kinetic energy of the fluid; , a cyclone device for separating the fluid components of the dispersion from each other, and a contact section for conveying the dispersion from the mixing device to the cyclone device;
, wherein the contact section includes means for repeatedly or continuously changing the direction of flow of the dispersion as it passes from the mixing device to the cyclone device. (2) Apparatus according to claim 1, characterized in that the flow path of the dispersion through the contacting section is such that the residence time of the dispersion in the contacting section is greater than that of the mixing device and/or the cyclone device. Featured device. 3. Apparatus according to claim 2, characterized in that the residence time in the contact section is at least one order of magnitude greater than the mixing device and/or cyclone device. 4. Device according to claim 1, 2 or 3, characterized in that the flow path through the contact section is curved, liberinous or maze-shaped. (5) A device according to any one of claims 1 to 4, characterized in that the contact section incorporates random or regular packings in the flow path of the dispersion through the contact section. Device. 6. Device according to claim 1, characterized in that the cyclone device extends at least partway into the contact section. 7. Device according to claim 6, characterized in that the flow path of the dispersion in the contact section extends at least partially around the cyclone device. 8. Device according to claim 6, characterized in that the axis of the vortex generated by the cyclone extends in the longitudinal direction of the flow path formed by the contact section. 9. Device according to claim 1, characterized in that the contact section comprises means for confining the dispersion in a channel surrounding the axis of the cyclone device or the mixing device. (10) The device according to claim 9, wherein the flow path extends in a spiral shape that spreads within a plane. (11) 11 The device according to claim 9, wherein the flow path extends in a spiral shape in the axial direction. 〓(12)12〓 The device according to claim 9, wherein the flow path has a wave shape in the radial direction.
JP3091488U 1987-03-17 1988-03-08 Fluid-fluid contact device Expired - Lifetime JPH0630241Y2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8706251 1987-03-17
GB8706251A GB2202166B (en) 1987-03-17 1987-03-17 Liquid-liquid contacting apparatus

Publications (2)

Publication Number Publication Date
JPS63164902U true JPS63164902U (en) 1988-10-27
JPH0630241Y2 JPH0630241Y2 (en) 1994-08-17

Family

ID=10614055

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3091488U Expired - Lifetime JPH0630241Y2 (en) 1987-03-17 1988-03-08 Fluid-fluid contact device

Country Status (3)

Country Link
JP (1) JPH0630241Y2 (en)
DE (1) DE8803095U1 (en)
GB (1) GB2202166B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002542008A (en) * 1999-04-15 2002-12-10 ハイドロ インターナショナル ピーエルシー Hydrodynamic vortex separator

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4206981A1 (en) * 1992-03-05 1993-09-16 Ensle Paul Stiftung DEVICE FOR MIXING FINE GRAIN MATERIALS AND / OR LIQUIDS
CN106984061A (en) * 2017-05-17 2017-07-28 南京工业大学 A kind of 1,5 pentanediamine continuous countercurrent extraction Processes and apparatus
CN114712892A (en) * 2022-04-29 2022-07-08 太原科技大学 Cyclone separation extraction tank

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB911906A (en) * 1960-05-24 1962-11-28 Fujinagata Zosensho Kk An inclined pipe-type extractor
GB989778A (en) * 1960-06-23 1965-04-22 Coal Industry Patents Ltd Improvements in or relating to the heat treatment of particulate solid materials
NL278630A (en) * 1961-05-19 1900-01-01
GB1115288A (en) * 1965-06-14 1968-05-29 Equipment Engineers Inc Methods and apparatus for effecting dispersions of gas in liquid materials
US3881895A (en) * 1972-12-26 1975-05-06 Entoleter Multistage vortical mass contact between media
US4017263A (en) * 1974-10-18 1977-04-12 Texaco Inc. Apparatus for sulfuric acid catalyzed alkylation process
DE2943537A1 (en) * 1979-10-27 1981-05-07 Hermann Berstorff Maschinenbau Gmbh, 3000 Hannover METHOD AND SYSTEM FOR CONVERTING COAL WITH HYDROGEN INTO HYDROCARBON

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002542008A (en) * 1999-04-15 2002-12-10 ハイドロ インターナショナル ピーエルシー Hydrodynamic vortex separator

Also Published As

Publication number Publication date
JPH0630241Y2 (en) 1994-08-17
GB8706251D0 (en) 1987-04-23
DE8803095U1 (en) 1988-04-21
GB2202166B (en) 1991-07-03
GB2202166A (en) 1988-09-21

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