GB499024A - Improvements in or relating to centrifugal separation - Google Patents

Improvements in or relating to centrifugal separation

Info

Publication number
GB499024A
GB499024A GB13678/37A GB1367837A GB499024A GB 499024 A GB499024 A GB 499024A GB 13678/37 A GB13678/37 A GB 13678/37A GB 1367837 A GB1367837 A GB 1367837A GB 499024 A GB499024 A GB 499024A
Authority
GB
United Kingdom
Prior art keywords
partitions
particles
section
tube
helix
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
GB13678/37A
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
Publication of GB499024A publication Critical patent/GB499024A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/0208Separation of non-miscible liquids by sedimentation
    • B01D17/0211Separation of non-miscible liquids by sedimentation with baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/0217Separation of non-miscible liquids by centrifugal force

Abstract

499,024. Centrifugal separators. LOUMIET ET LAVIGNE, J. May 14, 1937, No. 13678. Convention date, May 14, 1936. [Class 23] A fluid mixture is separated into its component parts by its passage under pressure through an helical tube H, the cross-section of which has its major dimension arranged transversely to the axis A of the helix; the tube is divided longitudinally by partitions to segregate the separated components. The entry portion T is of circular section and it is gradually broadened while its sectional area remains constant until it joins the first turn S of the helix. As the tube of the helix broadens, it is divided by an increasing number of partitions 55, 56, 59 and the heavier particles of the mixture in the sections so formed move towards the outer walls of their sections. Consecutive sets of partitions, for instance the sets 56, 59, are arranged so that the heavy particles from one section with the light particles from its adjacent outer section pass together to the next section ahead for re-treatment. All the heavy particles thus eventually arrive at the extreme outer wall where they can be discharged at various stages through the tubes Ex, while the light particles are similarly discharged from the inner wall through tubes E<3> to a common discharge pipe E. Various devices for skimming the heavy or light particles from the sections for re-treatment are described, and carrier fluids may be injected into the flow to assist in the separating action. When, for instance, a flow has been established through the helical tube H, Fig. 22, a fluid mixture may be injected through the pipe I and its components extracted by side tubes E<1>, E<11>. The Specification as open to inspection under Sect. 91 comprises also modifications in which baffles are used instead of partitions, and also a modification in which gas is allowed to expand in a helical tube with an elongated flange-like extension to increase the frictional effect; this produces local heat which may be absorbed by a fluid circulating in a channel about the extension. This subject-matter does not appear in the Specification as accepted.
GB13678/37A 1936-05-14 1937-05-14 Improvements in or relating to centrifugal separation Expired GB499024A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CU499024X 1936-05-14

Publications (1)

Publication Number Publication Date
GB499024A true GB499024A (en) 1939-01-16

Family

ID=5460797

Family Applications (1)

Application Number Title Priority Date Filing Date
GB13678/37A Expired GB499024A (en) 1936-05-14 1937-05-14 Improvements in or relating to centrifugal separation

Country Status (1)

Country Link
GB (1) GB499024A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990015256A1 (en) * 1989-06-07 1990-12-13 Aerosep Societe Anonyme Curved fluid translation systems
WO2003031015A1 (en) * 2001-10-05 2003-04-17 Preventor U Tbc Gmbh Method for the separation of suspensions and device
EP1352679A1 (en) * 2002-04-08 2003-10-15 Cooper Cameron Corporation Separator
US7152682B2 (en) 2002-04-08 2006-12-26 Cameron International Corporation Subsea process assembly
US7363982B2 (en) 2003-09-24 2008-04-29 Cameron International Corporation Subsea well production flow system
US10478753B1 (en) 2018-12-20 2019-11-19 CH International Equipment Ltd. Apparatus and method for treatment of hydraulic fracturing fluid during hydraulic fracturing
US11083984B2 (en) 2015-09-03 2021-08-10 Aqua Hd Separation & Filtration Systems Ltd Duct for use in a system for separating particles suspended in a fluid, and a method of designing such duct
US11498019B2 (en) 2018-12-20 2022-11-15 Haven Technology Solutions Llc Apparatus and method for gas-liquid separation of multi-phase fluid

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990015256A1 (en) * 1989-06-07 1990-12-13 Aerosep Societe Anonyme Curved fluid translation systems
WO2003031015A1 (en) * 2001-10-05 2003-04-17 Preventor U Tbc Gmbh Method for the separation of suspensions and device
EP1352679A1 (en) * 2002-04-08 2003-10-15 Cooper Cameron Corporation Separator
WO2003086570A1 (en) * 2002-04-08 2003-10-23 Cooper Cameron Corporation Separator
GB2402632A (en) * 2002-04-08 2004-12-15 Cooper Cameron Corp Separator
GB2402632B (en) * 2002-04-08 2005-06-29 Cooper Cameron Corp Separator
US7152682B2 (en) 2002-04-08 2006-12-26 Cameron International Corporation Subsea process assembly
US7363982B2 (en) 2003-09-24 2008-04-29 Cameron International Corporation Subsea well production flow system
US11083984B2 (en) 2015-09-03 2021-08-10 Aqua Hd Separation & Filtration Systems Ltd Duct for use in a system for separating particles suspended in a fluid, and a method of designing such duct
US10478753B1 (en) 2018-12-20 2019-11-19 CH International Equipment Ltd. Apparatus and method for treatment of hydraulic fracturing fluid during hydraulic fracturing
US11498019B2 (en) 2018-12-20 2022-11-15 Haven Technology Solutions Llc Apparatus and method for gas-liquid separation of multi-phase fluid

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