KR900004408A - centrifugal - Google Patents

centrifugal Download PDF

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Publication number
KR900004408A
KR900004408A KR1019890013472A KR890013472A KR900004408A KR 900004408 A KR900004408 A KR 900004408A KR 1019890013472 A KR1019890013472 A KR 1019890013472A KR 890013472 A KR890013472 A KR 890013472A KR 900004408 A KR900004408 A KR 900004408A
Authority
KR
South Korea
Prior art keywords
housing
centrifuge
diameter portion
fluid outlet
outlet tube
Prior art date
Application number
KR1019890013472A
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Korean (ko)
Other versions
KR0152963B1 (en
Inventor
에기디우스 안토니아 반덴악커 헨드리쿠스
조세푸스마리아드 코르트 코르넬리우스
Original Assignee
오노 알버어스
셀 인터나쵸 나아레 레사아치 마아츠 샤피 비이부이
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.)
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Publication date
Application filed by 오노 알버어스, 셀 인터나쵸 나아레 레사아치 마아츠 샤피 비이부이 filed Critical 오노 알버어스
Publication of KR900004408A publication Critical patent/KR900004408A/en
Application granted granted Critical
Publication of KR0152963B1 publication Critical patent/KR0152963B1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/103Bodies or members, e.g. bulkheads, guides, in the vortex chamber
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/081Shapes or dimensions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/12Construction of the overflow ducting, e.g. diffusing or spiral exits
    • B04C5/13Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow

Landscapes

  • Physics & Mathematics (AREA)
  • Geometry (AREA)
  • Cyclones (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Centrifugal Separators (AREA)

Abstract

내용 없음No content

Description

원심 분리기centrifugal

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는 본 발명에 따른 원심분리기의 개략 단면도.1 is a schematic cross-sectional view of a centrifuge according to the present invention.

제2도는 본 발명에 따른 다른 원심분리기의 개략단면도이다.2 is a schematic cross-sectional view of another centrifuge according to the present invention.

Claims (11)

유체와 고체의혼합물로부터 고체를 분리하기 위한 원심분리기로서:As a centrifuge for separating solids from a mixture of fluids and solids: 중간 부분이 원통형인 하우징 :Housing with cylindrical middle part: 상기 하우징의 제1단부 근방에 배열된 혼합물 유입구 : 상기 하우징의 제2단부 근방에 배열된 고체 유출구 : 작은 직격부, 큰 직경부, 및 상기 작은 직경부와 상기 큰 직경부를 연결하는 절두원추형 n분으로 구성되며, 상기 하우징안에 동심으로 배열된 유체 유출관으로서, 상기 작은 직경부의 자유단부가 상기 하우징의 내부와 직접적인 유체소통 관계에 있고 상기 큰 직경부가 상기 하우징의 상기 제1단부를 통해 뻗는 상기 유체 유출관 : 그리고 상기 분리기의 사용중, 상기 유입구 근방에서 상기 고체 유출구 근방의 장소까지 상기 하우징의 내부를 통해 뻗는 와동지역 ; 으로 구성되는 상기 원심분리기에 있어서, 상기 유체 유출관이 작은 직경부의 상기 자유단부에서, 상기 와동 지역이 연장하는 상기 고체 유출구 근방의 상기 장소까지의 비거리가 1.0과 3.0사이인 것을 특징으로 하는 상기 원심분리기.Mixture inlet arranged near the first end of the housing: Solid outlet arranged near the second end of the housing: Small straight portion, large diameter portion, and truncated cone n minutes connecting the small diameter portion and the large diameter portion A fluid outlet tube arranged concentrically in said housing, said fluid having a free end portion of said small diameter portion in direct fluid communication with said interior of said housing and said large diameter portion extending through said first end of said housing; Outlet tube: and during use of the separator, a vortex region extending through the interior of the housing from the vicinity of the inlet to a location near the solid outlet; The centrifugal separator comprising the centrifuge wherein the fluid outlet pipe has a specific distance from 1.0 to 3.0 at the free end of the small diameter portion from the free end to the place near the solid outlet through which the vortex region extends. Separator. 제1항에 있어서, 와동지역이 연장하는 상기 고체 유출구 근방의 상기 장소가, 하우징안에 와동 안정기가 설치되어 있는 장소에 의해 형성되는 원심분리기.The centrifugal separator according to claim 1, wherein the place near the solid outlet extending from the vortex area is formed by a place where a vortex ballast is provided in the housing. 제1항에 있어서, 상기 고체 유출구가 상기 하우징의 테이퍼진 절두원추형 담부에 의해 형성되고, 상기 와동 지역이 연장하는 상기 장소가 상기 하우징의 상기 절두원추형 단부의 하류단부에 의해 성형되는 원심분리기.The centrifuge of claim 1, wherein the solid outlet is formed by a tapered frustoconical convex portion of the housing, and wherein the location where the vortex region extends is shaped by a downstream end of the frustoconical end of the housing. 제1항에 있어서, 와류 발생수단이 상기 하우징의 제1단부 근방의 유입부안에 배열되어 있는 원심분리기.The centrifugal separator according to claim 1, wherein the vortex generating means is arranged in the inlet portion near the first end of the housing. 제1-4항중 어느한 항에 있어서, 상기 유체 유출관의 상기 작은 직경부의 비길이가 0.25와 1.0사이인 원심분리기.The centrifuge of any one of claims 1-4, wherein the specific length of the small diameter portion of the fluid outlet tube is between 0.25 and 1.0. 제1-5항중 어느 한 항에 있어서, 상기 유체 유출관의 상기 절두원추형 부분의 비길이가 0.20과 0.30사이인 원심분리기.6. The centrifuge of claim 1, wherein the specific length of the truncated cone portion of the fluid outlet tube is between 0.20 and 0.30. 7. 제1-6항중 어느 한 항에 있어서, 상기 유체 유출관의 상기 작은 직경부의 비내경이 0.20과 0.40사이인 원심분리기.The centrifuge of any one of claims 1-6, wherein the specific diameter of the small diameter portion of the fluid outlet tube is between 0.20 and 0.40. 제1-7항중 어느 한 항에 있어서, 상기 유체 유출관의 상기 큰 직경부의 비내경이 0.55과 0.75사이인 원심분리기.The centrifuge of any one of claims 1-7, wherein the specific diameter of the large diameter portion of the fluid outlet pipe is between 0.55 and 0.75. 제1-8항중 어느 한 항에 있어서, 상기 유체 유출관의 상기 큰 직경부의 비길이가 1.0과 1.4사이인 원심분리기.The centrifuge of any one of claims 1-8, wherein the specific length of the large diameter portion of the fluid outlet tube is between 1.0 and 1.4. 제4-9항중 어느 한 항에 있어서, 상기 하우징의 상기 유입부의 비길이가 0.50과 0.70사이인 원심분리기.The centrifuge of any one of claims 4-9, wherein the specific length of the inlet of the housing is between 0.50 and 0.70. 제1-10항중 어느 한 항에 있어서, 상기 절두원추형 부분의 최대 내경이 상기 유체 유출관의 상기 큰 직경부이 내경과 동일하거나 그보다 작은 원심분리기.The centrifuge of any one of claims 1-10, wherein the maximum inner diameter of the truncated conical portion is less than or equal to the inner diameter of the large diameter portion of the fluid outlet tube. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019890013472A 1988-09-22 1989-09-19 Swirl tube separator KR0152963B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB888822348A GB8822348D0 (en) 1988-09-22 1988-09-22 Swirl tube separator
GB8822348.2 1988-09-22
NL8822348.2 1988-09-22

Publications (2)

Publication Number Publication Date
KR900004408A true KR900004408A (en) 1990-04-12
KR0152963B1 KR0152963B1 (en) 1998-10-15

Family

ID=10644103

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019890013472A KR0152963B1 (en) 1988-09-22 1989-09-19 Swirl tube separator

Country Status (8)

Country Link
EP (1) EP0360360B1 (en)
JP (1) JP2907458B2 (en)
KR (1) KR0152963B1 (en)
AU (1) AU616800B2 (en)
CA (1) CA1336899C (en)
DE (1) DE68913882T2 (en)
ES (1) ES2050785T3 (en)
GB (1) GB8822348D0 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0486560U (en) * 1990-11-30 1992-07-28
DE4303405C2 (en) * 1992-02-07 1997-09-11 Aisin Seiki Shock detection device
JPH05221284A (en) * 1992-02-14 1993-08-31 Aisin Seiki Co Ltd Impact detecting device
US5483846A (en) * 1992-11-02 1996-01-16 Aisin Seiki Kabushiki Kaisha Impact sensing apparatus
JP3625980B2 (en) * 1997-03-12 2005-03-02 株式会社日立製作所 Cyclone system for separating solid components in gas
US7648544B2 (en) 2002-07-19 2010-01-19 Shell Oil Company Swirl tube separator
CN100415381C (en) * 2002-07-19 2008-09-03 国际壳牌研究有限公司 Cyclone separator with a vortex extender pin
WO2008020051A1 (en) 2006-08-18 2008-02-21 Shell Internationale Research Maatschappij B.V. Process to separate particles from a particles-containing gas stream
RU2471565C2 (en) 2007-06-01 2013-01-10 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Gases and solids separator
WO2016156947A1 (en) * 2015-03-30 2016-10-06 Reliance Industries Limited A gas-solid separator and a process for gas-solid separation
CN112146087B (en) * 2020-09-17 2023-02-17 北京盛赢节能技术有限公司 Separator for circulating fluidized bed heat exchanger
WO2024047123A1 (en) * 2022-08-30 2024-03-07 Katholieke Universiteit Leuven Swirl reactor

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2667944A (en) * 1949-12-10 1954-02-02 Combustion Eng Cyclone separator
US2890764A (en) * 1953-12-07 1959-06-16 Gerald D Arnold Method and apparatus for centrifugal separation with uni-directional flow at the point of separation
US3273320A (en) * 1963-07-15 1966-09-20 Exxon Research Engineering Co Cyclone separator for high temperature operations
US3636682A (en) * 1968-03-08 1972-01-25 Phillips Petroleum Co Cyclone separator
EP0108058A4 (en) * 1982-05-07 1985-06-26 Bauer Bros Co Hydrocyclone featuring hydraulic jump in overflow passage.
US4455220A (en) * 1982-12-23 1984-06-19 Shell Oil Company Separation of fluid cracking catalyst particles from gaseous hydrocarbons

Also Published As

Publication number Publication date
GB8822348D0 (en) 1988-10-26
AU4159189A (en) 1990-03-29
EP0360360A3 (en) 1991-01-30
KR0152963B1 (en) 1998-10-15
DE68913882D1 (en) 1994-04-21
CA1336899C (en) 1995-09-05
ES2050785T3 (en) 1994-06-01
DE68913882T2 (en) 1994-06-30
JP2907458B2 (en) 1999-06-21
JPH02115056A (en) 1990-04-27
EP0360360A2 (en) 1990-03-28
EP0360360B1 (en) 1994-03-16
AU616800B2 (en) 1991-11-07

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