US2313541A - Machine for purifying liquids - Google Patents

Machine for purifying liquids Download PDF

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Publication number
US2313541A
US2313541A US395153A US39515341A US2313541A US 2313541 A US2313541 A US 2313541A US 395153 A US395153 A US 395153A US 39515341 A US39515341 A US 39515341A US 2313541 A US2313541 A US 2313541A
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Prior art keywords
bowl
liquid
impurities
discs
centrifugal
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Expired - Lifetime
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US395153A
Inventor
Alan E Flowers
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De Laval Separator Co
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De Laval Separator Co
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Priority to US395153A priority Critical patent/US2313541A/en
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    • 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
    • B04B1/04Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
    • B04B1/08Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B5/00Other centrifuges
    • B04B5/06Centrifugal counter-current apparatus

Definitions

  • My invention relates to the removal of objectionable matter from liquids, and comprises a novel type of centrifugal separator adapted to effect this result with maximum efficiency.
  • the invention is particularly adapted for removal of reaction products from vegetable and animal and other oils which have been chemically treated to neutralize deleterious constituents therein.
  • the object of my invention is to provide a centrifugal bowl in which these primary and secondary purification steps may be effected in a single centrifugal operation, that is, to provide a single centrifugal bowl in which the primary separation of a major portion of the impurities takes place rst, followed by the dissemination of a washing liquid through the partially purified liquid and the separation of that wash liquid and its contained impurities therefrom so that both operations can be eected in " ⁇ a single pass.
  • Each of the channels I2 terminates at the entrance I3 to a tube I 4 which communicates with the interior of the-separating chamber of the bow1 through only tiny slits or holes I5 in the tube wall so arranged that they feed to the spaces between the discs 2l.
  • a top disc I6 provides a division wall between the separating chamber of the bowl and the passages I'I leading to the discharge outlet 6. Passages also lead from the inner edges of the discs 2l upward inside the neck of the top disc I6 to the outlet I8 for the discharge of the light oil.
  • While the bowl is useful for the removal of reaction products from any liquids, among which are vegetable, animal and mineral oils and other substances. in which chemical or physical treatment has produced materials having a specific gravity different from that or the liquid being i treated andl soluble in or combinable with some washing liquids, I will describe its use for only one class, vegetable oils, which. when separated from the vegetable matter in which they originated, contain objectionable acid materials that can be neutralized with alkalies and then form water soluble soaps.
  • alkali treated oil containing the resultant soap is fed to the bowl through the tube 24, flows downward through passages 8 inside the tube 1 and outward through channels s to the entrance to the distributing holes 25 in the discs 2
  • There a major portion ofthe soap is separated from the oil and flows outward to the periphery of the bowl, then upward and inward between the top disc It and the bowl top, and v soapmot previouslyiremcved.
  • 'water' and soap flows outward between the; discs and .10ml with. and flaws out of the bowl with,
  • a centrifugal separator for the separation from a liquid containing impurities of heavier specific gravity than the liquid, comprising a separating bowl and contained therein a plurality of frusto-conical discs providing a plurality of a frusta-conical separating chambers, means to feed the impure liquid to said separating chambers through said discs between their inner and outer edges, in which chambers, under the action of centrifugal force, said liquid with a.
  • said means including a. supply conduit extending through said bowl and having outlets which open into the inner parts of said separating chambers and nearer the axis oi.' the bowl'than the admission] means for the impure liquid andfwhich' are so restricted as to effect 'distribution, ther'eby causing combination ofs'aid washing liquid 'g with the impurities in the partially purined liquid.- yand the.
  • the separator having the usual outlets for lighter and heavier separated constituents through which are respectiveb' discharged the purified liquid and the washing liquid and impurities.

Description

A. E. FLOWERS MACHINE FOR PURIFYING LIQUIDS Filed May 2e, 1941 /mz E F/wefs March 9, 1943.
Patented Mar. 9, 1943 2,313,541 MACHINE Foa PURIFYING LrQUms Alan E. Flowers, Poughkeepsie, N. Y., assignor to The De Laval Separator Company, New York, N. Y., a corporation of New Jersey Application May 26, 1941, Serial No. 395,153
1 Claim.
My invention relates to the removal of objectionable matter from liquids, and comprises a novel type of centrifugal separator adapted to effect this result with maximum efficiency. The invention is particularly adapted for removal of reaction products from vegetable and animal and other oils which have been chemically treated to neutralize deleterious constituents therein.
It is well known that in both gravity and centrifugal treatments it is relatively easy to remove a major portion of reaction products while it is relatively dimcult to remove a small minor portion of these products. It is also Well known that many of these products are easily soluble in water or other liquids having a greater speciflc gravity than the oil being treated and it is II enclosing another feed passage from which common practice to carry out rst a gravity or centrifugal separation of most of the reaction products and then follow with a wash with a suitable liquid and cause a second independent gravity or centrifugal separation of the wash liquid and accompanying impurities.
When such a two-step separation has been carried on in the past it has required the use of two centrifugal machines in series, or the storage of primarily separated liquid until after treatment of an entire batch and then the use of the same separator, perhaps with a different adjustment, for the removal of wash liquid with its contained impurities.
Specifically, the object of my invention is to provide a centrifugal bowl in which these primary and secondary purification steps may be effected in a single centrifugal operation, that is, to provide a single centrifugal bowl in which the primary separation of a major portion of the impurities takes place rst, followed by the dissemination of a washing liquid through the partially purified liquid and the separation of that wash liquid and its contained impurities therefrom so that both operations can be eected in "`a single pass.
several -channels l2 lead. Up to this pointthe construction is in the manner of the Hall patent before mentioned and is therein clearly shown and described.
Each of the channels I2 terminates at the entrance I3 to a tube I 4 which communicates with the interior of the-separating chamber of the bow1 through only tiny slits or holes I5 in the tube wall so arranged that they feed to the spaces between the discs 2l. In the upper part of the bowl a top disc I6 provides a division wall between the separating chamber of the bowl and the passages I'I leading to the discharge outlet 6. Passages also lead from the inner edges of the discs 2l upward inside the neck of the top disc I6 to the outlet I8 for the discharge of the light oil. I Y
Wings I9 between the bowl top 5 and the top disc I6 and wings 20 secured to the bowl shell and extending inward' to near the outer edge of the discs 2|, force the bowl contents to continue rotating at the same speed as the bowl. Wings 28 and 21 attached to the walls of the tubes Il and I respectively, force the incoming liquids to assume a speed of rotation equal to that of the bowl. Covers 22 are supplied to provide chambers to catch the materials discharged from the bowl. .Supported by suitable means are two concentric supply tubes 23 and 24 which extend down inside the upper ends of the tubes II and 1 respectively.
While the bowl is useful for the removal of reaction products from any liquids, among which are vegetable, animal and mineral oils and other substances. in which chemical or physical treatment has produced materials having a specific gravity different from that or the liquid being i treated andl soluble in or combinable with some washing liquids, I will describe its use for only one class, vegetable oils, which. when separated from the vegetable matter in which they originated, contain objectionable acid materials that can be neutralized with alkalies and then form water soluble soaps.
Only a few o'f these In the operation of the bowl, alkali treated oil containing the resultant soap is fed to the bowl through the tube 24, flows downward through passages 8 inside the tube 1 and outward through channels s to the entrance to the distributing holes 25 in the discs 2|, thence upward through the distributing holes and spreads out between the discs. There a major portion ofthe soap is separated from the oil and flows outward to the periphery of the bowl, then upward and inward between the top disc It and the bowl top, and v soapmot previouslyiremcved. 'water' and soap flows outward between the; discs and .10ml with. and flaws out of the bowl with,
' the previously separated maior portion of the p. e washed oil continues its flow toward the vcenter ofthe bowl, thence upward and ldischarges at i8. -1
By placing the distributing holes 25 near `the periphery of the discs and the wash water feeding tubes Il near their inner edges. a long counterilow of the water and oil with consequent good washing of the oil is obtained.
What I claim and desire to protect by Letters Patent is:
-In a centrifugal separator for the separation from a liquid containing impurities of heavier specific gravity than the liquid, comprising a separating bowl and contained therein a plurality of frusto-conical discs providing a plurality of a frusta-conical separating chambers, means to feed the impure liquid to said separating chambers through said discs between their inner and outer edges, in which chambers, under the action of centrifugal force, said liquid with a. minor part of its impurities is separable from vthe major part of its impurities and is displaced inward toward the bowls axis while the separated impurities move outward toward the periphery, and means to disseminate a washingliquid heavier than the-1iquld to be puried throughout said separated partially puried liquid, said means including a. supply conduit extending through said bowl and having outlets which open into the inner parts of said separating chambers and nearer the axis oi.' the bowl'than the admission] means for the impure liquid andfwhich' are so restricted as to effect 'distribution, ther'eby causing combination ofs'aid washing liquid 'g with the impurities in the partially purined liquid.- yand the. separation of saidwashing liquid and impurities fromvsubstantially purified liquid and movement of said washingliquid and impurities outward through said separating .chambers'toward the bowls periphery, the separator having the usual outlets for lighter and heavier separated constituents through which are respectiveb' discharged the purified liquid and the washing liquid and impurities.
ma FLOWERS. i
US395153A 1941-05-26 1941-05-26 Machine for purifying liquids Expired - Lifetime US2313541A (en)

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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2504261A (en) * 1946-06-24 1950-04-18 Int Harvester Co Self-washing cream separator
US2557629A (en) * 1946-02-21 1951-06-19 Alais & Froges & Camarque Cie Method and apparatus for continuous centrifugal separation
US2599619A (en) * 1947-06-13 1952-06-10 Separator Ab Method and apparatus for centrifugal separation
US2619280A (en) * 1948-10-25 1952-11-25 Shell Dev Centrifugal contactor and method of contacting
US2628021A (en) * 1949-05-03 1953-02-10 Separator Ab Centrifuge with auxiliary feed arrangement
US2715994A (en) * 1948-10-06 1955-08-23 Steinacker Peter Countercurrent extraction centrifuges
US2973896A (en) * 1956-01-19 1961-03-07 Dorr Oliver Inc Centrifuge apparatus
US3027389A (en) * 1958-06-23 1962-03-27 Benjamin H Thurman Refining of fatty oils
US3027390A (en) * 1959-03-13 1962-03-27 Benjamin H Thurman Apparatus and method for centrifugal purification of fatty oils
US3133880A (en) * 1959-12-21 1964-05-19 Vernon D Jarvis Centrifugal extractor
US3187998A (en) * 1964-03-31 1965-06-08 Vernon D Jarvis Centrifugal extractor
US3202347A (en) * 1960-05-02 1965-08-24 Benjamin H Thurman Countercurrent flow centrifugal separator
US3217982A (en) * 1958-10-17 1965-11-16 Westfalia Separator Ag Apparatus for the sterilization of liquids
US3291387A (en) * 1964-01-16 1966-12-13 Technicon Instr Continuous centrifugal separator
DE102004042888A1 (en) * 2004-09-04 2006-03-23 Westfalia Separator Ag Self-draining separator with disc package
US20190184313A1 (en) * 2017-12-15 2019-06-20 Minextech Llc Method and apparatus for separating insoluble liquids of different densities

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2557629A (en) * 1946-02-21 1951-06-19 Alais & Froges & Camarque Cie Method and apparatus for continuous centrifugal separation
US2504261A (en) * 1946-06-24 1950-04-18 Int Harvester Co Self-washing cream separator
US2599619A (en) * 1947-06-13 1952-06-10 Separator Ab Method and apparatus for centrifugal separation
US2715994A (en) * 1948-10-06 1955-08-23 Steinacker Peter Countercurrent extraction centrifuges
US2619280A (en) * 1948-10-25 1952-11-25 Shell Dev Centrifugal contactor and method of contacting
US2628021A (en) * 1949-05-03 1953-02-10 Separator Ab Centrifuge with auxiliary feed arrangement
US2973896A (en) * 1956-01-19 1961-03-07 Dorr Oliver Inc Centrifuge apparatus
US3027389A (en) * 1958-06-23 1962-03-27 Benjamin H Thurman Refining of fatty oils
US3217982A (en) * 1958-10-17 1965-11-16 Westfalia Separator Ag Apparatus for the sterilization of liquids
US3027390A (en) * 1959-03-13 1962-03-27 Benjamin H Thurman Apparatus and method for centrifugal purification of fatty oils
US3133880A (en) * 1959-12-21 1964-05-19 Vernon D Jarvis Centrifugal extractor
US3202347A (en) * 1960-05-02 1965-08-24 Benjamin H Thurman Countercurrent flow centrifugal separator
US3291387A (en) * 1964-01-16 1966-12-13 Technicon Instr Continuous centrifugal separator
US3187998A (en) * 1964-03-31 1965-06-08 Vernon D Jarvis Centrifugal extractor
DE102004042888A1 (en) * 2004-09-04 2006-03-23 Westfalia Separator Ag Self-draining separator with disc package
US20070270298A1 (en) * 2004-09-04 2007-11-22 Westfalia Separator Ag Self-dumping separator with a disk stack
US7537559B2 (en) 2004-09-04 2009-05-26 Westfalia Separator Ag Self-dumping separator with a disk stack and fins arranged radially outside the disc stack
US20190184313A1 (en) * 2017-12-15 2019-06-20 Minextech Llc Method and apparatus for separating insoluble liquids of different densities

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