GB1112303A - Clarifying centrifuge for separating a suspension into liquid and solid - Google Patents

Clarifying centrifuge for separating a suspension into liquid and solid

Info

Publication number
GB1112303A
GB1112303A GB25536/65A GB2553665A GB1112303A GB 1112303 A GB1112303 A GB 1112303A GB 25536/65 A GB25536/65 A GB 25536/65A GB 2553665 A GB2553665 A GB 2553665A GB 1112303 A GB1112303 A GB 1112303A
Authority
GB
United Kingdom
Prior art keywords
drum
solid
suspension
liquid
partitions
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.)
Expired
Application number
GB25536/65A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sulzer Escher Wyss AG
Original Assignee
Escher Wyss AG
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 by Escher Wyss AG filed Critical Escher Wyss AG
Publication of GB1112303A publication Critical patent/GB1112303A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B11/00Feeding, charging, or discharging bowls
    • B04B11/02Continuous feeding or discharging; Control arrangements therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B11/00Feeding, charging, or discharging bowls
    • B04B11/04Periodical feeding or discharging; Control arrangements therefor

Landscapes

  • Centrifugal Separators (AREA)

Abstract

1,112,303. Centrifugal separators. ESCHER WYSS A.G. 16 June, 1965 [24 June, 1964], No. 25536/65. Heading B2P. A centrifuge for separating the components of a liquid-solid suspension comprises a conically flared, solid-wall drum 1 the interior of which is sub-divided in the axial direction into two or more separating chambers 4<SP>1</SP>-4<SP>3</SP>. through which the suspension flows successively by means of partitions 6<SP>1</SP>-6<SP>3</SP> extending at least to the vicinity of the inner surface of the drum wall with which each partition defines or is adapted to define a gap 7<SP>1</SP>, 7<SP>2</SP> or 7<SP>3</SP> for the discharge of separated solid deposited on the wall surface, each partition being provided with an overflow aperture 8<SP>1</SP>, 8<SP>2</SP> or 8<SP>3</SP> for the passage of the suspension or discharge of clarified liquid. The drum 1 is secured to a rotatable shaft 2. The partitions 6<SP>1</SP>-6<SP>3</SP> are connected by a tubular support 9 connected to a sleeve 10 by means of cross-pieces 9<SP>1</SP> extending through openings into the hub disc of the drum. The width of the gaps 7<SP>1</SP>-7<SP>3</SP> may be adjusted by axial movement of the sleeve 10. Adjustment of the sleeve 10 can be effected in accordance with the quantity of solid discharged into the housing 15. A vibratory motion may be superimposed on the adjusting movement of the sleeve 10 to prevent solid clogging the gaps. Instead of a common adjustment, each partition may be independently adjusted by leaving the partition 6<SP>1</SP>, 6<SP>2</SP> slidably mounted on the support 9 and connected by cross-pieces to sleeves 10<SP>1</SP>, 10<SP>2</SP>. Adjustment of the partitions may be effected in accordance with the amount of solid present in the separating chambers, the sleeves at the start of an operation being drawn by a spring in to a position corresponding to the closure position of the partitions. As the amount of solid increases in any one chamber the pressure on the respective partition increases and the partitio moves against the biasing action of the spring to provide the necessary width of gap. The suspension is fed through a stationary pipe 5 and passes successively through the chambers 4<SP>1</SP>, 4<SP>2</SP>, 4<SP>3</SP> where the liquid is increasingly clarified. The clarified liquid discharges via a funnel 11 into a discharge housing 14. The path of the liquid being clarified may be further extended by providing one or more of the partitions with an additional wall 30, Fig. 4 (not shown) in front of or after the corresponding overflow aperture 8. In another embodiment, Fig. 2 (not shown), the drum 1 is connected at its wider end to a conical screwtype centrifuge, the solid discharging from the drum 1 being conveyed to a discharge 22 by the screw-conveyor 17, which rotates at a speed different from that the centrifuge drums 1, 16. The suspension is fed to the narrower end of the drum 1 via the inlet 5 and a distributor head 23 carried by the shaft 2. The clarified liquid discharging from the drum 1 flows via a take-off device 21 into a stationary discharge pipe 20. In a modification of the last embodiment, Fig. 3 (not shown), the suspension is fed to the larger end of the drum 1, the clarified liquid discharging at the narrower end and the solid at the larger end and into the drum 16. In a further embodiment, Fig. 5 (not shown), the drum 1 is connected to a scraper centrifuge drum 31 into which the suspension is fed via the pipe 5 and an annular duct 38. The partially clarified liquid passes via the opening 35 of the drum 31 into the drum 1 for further clarification. Solids deposited in the drum 31 are removed periodically by means of a scraping device 40.
GB25536/65A 1964-06-24 1965-06-16 Clarifying centrifuge for separating a suspension into liquid and solid Expired GB1112303A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH825864A CH418982A (en) 1964-06-24 1964-06-24 Clarifying centrifuge for separating a suspension into liquid and solid

Publications (1)

Publication Number Publication Date
GB1112303A true GB1112303A (en) 1968-05-01

Family

ID=4337584

Family Applications (1)

Application Number Title Priority Date Filing Date
GB25536/65A Expired GB1112303A (en) 1964-06-24 1965-06-16 Clarifying centrifuge for separating a suspension into liquid and solid

Country Status (4)

Country Link
US (1) US3322336A (en)
CH (1) CH418982A (en)
DE (1) DE1482714C3 (en)
GB (1) GB1112303A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2128904A (en) * 1982-10-09 1984-05-10 Edward L Simonds Centrifugal separator
CN109013071A (en) * 2018-09-13 2018-12-18 安徽普源分离机械制造有限公司 Gu a kind of liquid-liquid efficiently separated-three-phase high speed horizontal-spiral centrifuge

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH452441A (en) * 1966-08-23 1968-05-31 Escher Wyss Ag Pusher centrifuge
US3527401A (en) * 1968-07-11 1970-09-08 Krueger As I Drum centrifuge with rotating worm conveyor
US3782623A (en) * 1970-06-11 1974-01-01 Krueger As I Decanting centrifuge for draining off water from sewage sludge
US4347971A (en) * 1977-03-03 1982-09-07 Joy Manufacturing Company Centrifuge apparatus
CH624858A5 (en) * 1977-11-25 1981-08-31 Escher Wyss Ag
US4299352A (en) * 1979-03-23 1981-11-10 Kobe, Inc. Centrifuge apparatus
DE3627826C2 (en) * 1986-08-16 1995-02-09 Westfalia Separator Ag Centrifugal drum
JP3032283B2 (en) * 1990-11-27 2000-04-10 月島機械株式会社 Decanter centrifuge
AU640258B2 (en) * 1991-08-16 1993-08-19 Kotobuki Techrex Ltd. Sedimentation centrifuge
US5310399A (en) * 1991-08-20 1994-05-10 Kotobuki Techrex Ltd. Sedimentation centrifuge containing screw conveyor with fins
US5314399A (en) * 1991-08-20 1994-05-24 Kotobuki Techrex Ltd. Sedimentation centrifuge with helical fins mounted on the screw conveyor
SE9802116D0 (en) * 1998-06-15 1998-06-15 Alfa Laval Ab decanter
US6589154B2 (en) 2001-05-30 2003-07-08 Alfa Laval Inc. Decanter centrifuge with a gear box mounted on the bowl
KR102504657B1 (en) * 2019-11-18 2023-02-27 주식회사 엘지화학 Pressurizing centrifugal dehydrator
CN110760623A (en) * 2019-11-26 2020-02-07 广西叶茂食品有限责任公司 Sugarcane juice heating, bacteriostasis and floating impurity removing system and technology

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1640707A (en) * 1923-09-29 1927-08-30 Laughlin Filter Corp Machine for separating solids from liquids or liquids from liquids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2128904A (en) * 1982-10-09 1984-05-10 Edward L Simonds Centrifugal separator
CN109013071A (en) * 2018-09-13 2018-12-18 安徽普源分离机械制造有限公司 Gu a kind of liquid-liquid efficiently separated-three-phase high speed horizontal-spiral centrifuge

Also Published As

Publication number Publication date
CH418982A (en) 1966-08-15
DE1482714C3 (en) 1974-10-31
DE1482714B2 (en) 1974-04-04
DE1482714A1 (en) 1969-06-12
US3322336A (en) 1967-05-30

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