GB853733A - Centrifuge apparatus - Google Patents

Centrifuge apparatus

Info

Publication number
GB853733A
GB853733A GB2518556A GB2518556A GB853733A GB 853733 A GB853733 A GB 853733A GB 2518556 A GB2518556 A GB 2518556A GB 2518556 A GB2518556 A GB 2518556A GB 853733 A GB853733 A GB 853733A
Authority
GB
United Kingdom
Prior art keywords
fraction
discharged
heavy
rotor
returned
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
GB2518556A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to GB2518556A priority Critical patent/GB853733A/en
Publication of GB853733A publication Critical patent/GB853733A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • B04B1/10Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
    • B04B1/12Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with continuous discharge
    • 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

Abstract

853,733. Centrifugal separators. WOLSTENHOLM, R. A. (Dorr-Oliver Inc.). Nov. 4 1956, No. 25185/56. Class 23 Apparatus for separating liquid material into heavy, light and intermediate fractions has provision for the recirculation of at least part of the heavy fraction and for regulating during separation the amount of intermediate fraction discharged. Liquid material is supplied to the separator rotor 101 (Fig. 1), through a feed pipe 121 after passing through a screen 132. Heavy fraction is discharged through nozzles 105 into a volute 106 which is connected by an external circuit to a return passage 109, water being introduced into the circuit if desired. The returned heavy fraction is impelled by vanes 113 through passages 114 to the part 116 of the separating chamber. The light fraction passes through the liner plates 151, through passages 142 and is discharged by a skimming device 141. The intermediate fraction from outside the liner plates passes through tubes 153 and passages 154, and is discharged by a skimming device 157, a valve 167 controlling the discharge. In the modification shown in Fig. 5, some of the heavy fradtion discharged from nozzles 234 into the volute 236 is returned with addition of water, if desired, to the rotor through valve controlled orifice 240. The intermediate fraction is discharged by the skimming device 273 into a chamber 275. Some of the intermediate fraction is discharged from the chamber 275 through a valve 279 and the rest is returned to the rotor through the annulus between sleeves 251 and 252 which also serves to feed the liquid material to the rotor. Cooling or heating fluid may be introduced into compartments 281, 282 of the casing 237. In the modification shown in Fig. 8 the walls 292, 293 of the volute 294 and the part 303 of the internal walls of the rotor are formed from synthetic rubber. The intermediate fraction is discharged by a skimming device 311, part of the discharging fraction being returned by passage 314 to the feed space 316. In a further modification (Fig. 9, not shown), some of the intermediate fraction is introduced into the return circuit for the heavy fraction. In the separation of a starch solution, starch solids, gluten, and fibrous solids constitute the heavy, light and intermediate fractions respectively.
GB2518556A 1956-11-04 1956-11-04 Centrifuge apparatus Expired GB853733A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2518556A GB853733A (en) 1956-11-04 1956-11-04 Centrifuge apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2518556A GB853733A (en) 1956-11-04 1956-11-04 Centrifuge apparatus

Publications (1)

Publication Number Publication Date
GB853733A true GB853733A (en) 1960-11-09

Family

ID=10223619

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2518556A Expired GB853733A (en) 1956-11-04 1956-11-04 Centrifuge apparatus

Country Status (1)

Country Link
GB (1) GB853733A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3698877A1 (en) 2019-02-19 2020-08-26 Alfa Laval Corporate AB Method of controlling centrifugal separator and centrifugal separator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3698877A1 (en) 2019-02-19 2020-08-26 Alfa Laval Corporate AB Method of controlling centrifugal separator and centrifugal separator
WO2020169343A1 (en) 2019-02-19 2020-08-27 Alfa Laval Corporate Ab Method of controlling centrifugal separator and centrifugal separator

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