US2313540A - Machine for purifying liquids - Google Patents

Machine for purifying liquids Download PDF

Info

Publication number
US2313540A
US2313540A US395151A US39515141A US2313540A US 2313540 A US2313540 A US 2313540A US 395151 A US395151 A US 395151A US 39515141 A US39515141 A US 39515141A US 2313540 A US2313540 A US 2313540A
Authority
US
United States
Prior art keywords
liquid
bowl
compartment
chamber
wash
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 - Lifetime
Application number
US395151A
Inventor
Selden H Hall
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.)
De Laval Separator Co
Original Assignee
De Laval Separator Co
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 De Laval Separator Co filed Critical De Laval Separator Co
Priority to US395151A priority Critical patent/US2313540A/en
Application granted granted Critical
Publication of US2313540A publication Critical patent/US2313540A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

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
    • B04B1/04Centrifuges 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
    • B04B15/00Other accessories for centrifuges
    • B04B15/12Other accessories for centrifuges for drying or washing the separated solid particles

Definitions

  • My invention relates to the removal of objectionable matter from liquids, and comprises a novel type of centrifugal separator adapted to eect this result with maximum eiciency.
  • 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 bowl shell I has a lbottom 2 with a socket 3 fitting the driving and supporting spindle 4.
  • the bowl has a top 5 secured to the shell I by a coupling ring 30. At the inner end of the bowl top is a discharge 6. In the center of the bowl are concentric tubes 1 and Il.
  • the inner tube 1 carrying the oil and soap or other materials which are to be separated from the oil, encloses passages 8 thatlead to the entrancesv to distributing holes 9 near the peripheries of the discs I0 primarily separated liquid until after treatment of an entire batch and then the use of the same.
  • the single gure oi the accompanying drawing is a section, in a plane, passing through the axis,
  • a top disc 22 provides a division wall between the separating chamber or the bowl and the passage 23 leading to the discharge outlet 6. Passages also lead from the inner edges of the discs I8o upward inside the neck of the top disc 22 to the outlet 24 for the discharge of light oil.
  • Covers 29 are supplied to provide chambers to catch the materials discharged from the bowl.
  • 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 specliic gravity different from that of the liquid being treated and soluble in or combinable with some washing liquid, I will describe its use for only containing soap, is fed to the bowl through tubev 20, flows downward inside tube 1 and outward through channels 8 to the entrance of the distributing holes 9 in the discs I0, thence upward and distributes between the discs, where separation of a major'portion of the soap takes place in the usual manner.
  • the soapstock flows outward to the bowl periphery and is discharged through opening 6 in the bowl top 5.
  • the partially purified oil flows inward toward the center of the bowl to, and then outward through, opening I directly beneath the channels I2.
  • Clean water fed through the passages I2 to the chambers at their ends. passes through the porous wall I3 and is finely disseminated through the oil flowing outward from the opening I5.
  • the mixture flows through the holes I1 to the spaces between the upper discs I8 where the soap and water are separated from the oil and iiow toward the periphery of the bowl, where they mix with the previously separated soap, then upward around the edge of the top disc 22 and escape at 6, while the purified and washed oil flows inward between the discs I8 to their inner edges, thence upward inside the neck of the top disc and escapes at 24.
  • a centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating chamber and a secondary chamber, said chambers being radially substantially coextensive and surrounding the axis of the bowl along different lengths thereof, a set of frustro-conical discs in the primary chamber, means to distribute the liquid to be purified within the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, a similar set of discs in the secondary chamber, there being communication between the two chambers through which the separated liquid containing residual impurities flows from the primary chamber into the secondary chamber, and means to feed a wash iiuid into the secondary chamber, wherein the wash fluid combines with said residual impurities and a further purification of the liquid is effected by its separation therein from the combined wash liquid and residual impurities.
  • a centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating chamber and a secondary chamber, said chambers being radially substantially coextensive and surrounding the axis of the bowl along different lengths thereof, a set of frustro-conical discs in the primary chamber, means to distribute the liquid to be purified within the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, there being communication between the secondary chamber into a the two chambers through which the separated liquid containing residual impurities flows from the primary chamber into the secondary chamber, means to feed a wash fluid into the secondary chamber and a set of frustro-conical discs in the secondary chamber substantially radially coextensive with the discs in the primary chamber and within the spaces between which the wash fluid and the residual impurities combined therewith separate from the liquid to thereby effect the latters more complete purification, said bowl having an outlet for the finally pur
  • a centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating chamber and a secondary chamber, a set of frustro-conical discs in the primary chamber, means to distribute the liquid to be purified within the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, there being communication between the two chambers through which the separated liquid containing residual impurities flows from the primary chamber into the secondary chamber, a feed tube for washing fiuid, a porous wall through which the wash iiuid enters the secondary chamber and is therein disseminated through the partially purified liquid flowing from the primary chamber to thereby combine with said residual impurities and be separated with said impurities from said liquid,
  • a centrifugal purifier for separating impurif ties from a liquid which comprises a rotatable bowl and means therein dividing it into a primary separating chamber and a secondary chamber, said chambers being radially substantially coextensive and surrounding the axis of the bowl along different lengths thereof, means affording communication between said chambers at the zones thereof nearest the axis, a feed conduit adapted to supply liquid to be purified to the primary chamber wherein occurs a primary separation from the liquid of the major part of the impurities, the partly purified liquid containing the residual impurities then flowing through said communicating means into the inner zone of the secondary chamber, a feed conduit adapted to supply a washing iiuid to the zone of the secondary chamber nearest the axis and disseminate the same throughout the partly purified liquid flowing into said zone from the primary chamber and combine with said residual impurities, said liquid being separated in the secondary chamber from said washing fluid and residual impurities, the bowl having outlets for the finally purified liquid and for the washing liquid and all separated
  • a centrifugal purifier for separating impurities from a liquid which comprises a rotatable bowl, a frustro-conical disc dividing the bowl into a primary separating chamber anda secondary chamber, a frustro-conical disc dividing wash compartment and a final separating compartment, piles of frustro-conical discs in the primary separating chamber and in the last named compartment, means affording communication between the primary separating chambers and the washing compartment at the zones thereof nearest the axis of the bowl, a feed conduit for supplying impure liquid to the primary separating chamber, another feed conduit for supplying washing uid to the zone of the washing compartment nearest the axis of the bowl, the bowl having outlets for the finally purified liquid and for the washing liquid and all separated impurities.
  • a centrifugal purifier for separating impurities from a Aliquid which comprises a rotatable bowl, a frustro-conical disc dividing the bowl into a primary separating chamber and a secondary chamber, a frustro-conical disc dividing the secondary chamber into a Wash compartment and a final separating compartment, piles of frustro-conical discs in the primary separating chamber land in the last named compartment, means affording communication between the primary separating chambers and the washing compartment at the zones thereof nearest the axis of the bowl, a feed conduit for supplying impure liquid to the primary separating chamber, another feed conduit for supplying washing iiuid to the zone of the washing compartment nearest the axis of the bowl, passages, relatively far from the axis, from the washing compartment to the final separating compartment, the bowl having outlets from the peripheries of all three compartments for discharge of washing fluid and impurities and an outlet from the final separating compartment for the finally purified liquid.
  • a centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means dividing the bowl into a primary separating chamber, and a chamber having a wash compartment and a nal separating compartment, said chambers surrounding the areas of the bowl along different lengths thereof, the primary separating chamber and the final separating compartment being radially substantially coextensive, a set of frustro-conical discs in the primary separating chamber, a set of frustro-conical discs in the final separating compartment, both sets of discs being substantially radially coextensive, means to distribute the liquid to be purified within the spaces between the discs in the primary separating chamber, wherein the major part of the impurities is separated from the liquid containing residual impurities, there being communication between the primary separating chamber and the wash compartment, means to supply a wash iiuid to the wash compartment, there being communication between the wash compartment and the nal separating compartment in which latter are effected a further pur
  • a centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl and two frustro-conical partitions therein dividing the bowl into three compartments, one above another, namely, a primary separating chamber, a wash compartment and a secondary separating compartment, said compartments all surrounding the axis of the bowl along'dierent lengths thereof, means to feed the liquid to be purified to the primary separating chamber wherein the major part of the impurities is separated from the liquid containing residual-impurities, there being communication between the zone of the primary separating chamber containing separated partially purified liquid and the wash compartment through which said partially purified liquid is adapted to fiow from said chamber to said wash compartment, means to supply a wash fluid to the wash compartment and wherein itk is disseminated through the partially purified liquid admitted thereto from the primary separating chamber, there being communication between the ,wash compartment and the final separating compartment wherein the liquid is separated from the wash fluid and -residual impurities
  • a centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating compartment, a wash compartment and a secondary separating compartment, a set of frustro-conical discs in each separating compartment, all said discs being similar and of substantially equal size, means, including a series of vertically aligned holes in the discs in the primary separating compartment, through which liquid to be purified is distributed to the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, means to conduct partially purified liquidfto said wash compartment, and means to disseminate a washing fluid through the liquid in said wash compartment wherein the wash uid combines with the residual impurities, there being vertically aligned holes in the discs of the secondary separating compartment, through which the mixture of partially purified liquid and wash liquid and impurities is distributed to the spaces between the discs in the secondary separating compartment, wherein further purification of
  • a centrifugal purifier for separating impurities from a liquid which comprises a rotatable bowl and means therein dividing it into a primary separating compartment, a. secondary compartment and a wash compartment, said compartments surrounding the axis of the bowl along different lengths thereof and being radially substantially coextensive, means affording communication between the primary and wash compartments at the zones thereof nearest the axis,
  • a feed conduit adapted to supply liquid to be purified tothe primary compartment wherein occurs a primary separation from the liquid of the major part of the impurities, the partly purified liquid containing the residual impurities then owing through the communicating means into the wash compartment.
  • a feed conduit adapted to supply a washing fluid to the zone of the wash compartment nearest the axis and disseminate the same throughout the partially purified liquid flowing thereinto from the primary compartment, the washing fiuid therein combining with said residual impurities, the liquid being then conducted, through. the communicating ⁇ means specified,
  • the bowl having outlets for the ilnally purified liquid and for the washing uid and all separated taining residual impurities, there being communication, in a zone relatively near the axis, between the primary separating chamber and the wash compartment for the flow of partially purified liquid from said chamber to the wash compartment, means to supply a wash fluid to the wash compartment and wherein it is disseminated Athrough the partially purified liquid admitted thereto from the primary separating chamber, there being communication, in a zone relatively distant from the axis, between the wash compartment and the final separating compartment wherein the liquid is separated from the wash fluid and residual impurities, the bowl having outlets for the purified liquid and for the wash fluid and all separated impurities.

Description

March 9, 1943; s. H. HALL MACHINE FOR PURIFYING LIQUIDS Filed May 26I 1941 Win/raf? Patented Mar. 9, 1943 MACHINE `FOR PURIFYING LIQUIDS Selden H. Hall, 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. 395,151
12 Claims.
My invention relates to the removal of objectionable matter from liquids, and comprises a novel type of centrifugal separator adapted to eect this result with maximum eiciency. 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 difficult 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 e. greater speciiic gravity than the oil being treated and it is common practice to carry out rst a gravity or centrifugal separation of most of the soap 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 carlried on in the past it has required the use of two centrifugal machines in series, or the storage of The bowl shell I has a lbottom 2 with a socket 3 fitting the driving and supporting spindle 4.
The bowl has a top 5 secured to the shell I by a coupling ring 30. At the inner end of the bowl top is a discharge 6. In the center of the bowl are concentric tubes 1 and Il. The inner tube 1, carrying the oil and soap or other materials which are to be separated from the oil, encloses passages 8 thatlead to the entrancesv to distributing holes 9 near the peripheries of the discs I0 primarily separated liquid until after treatment of an entire batch and then the use of the same.
of the impurities takes place first, 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 effected in a single pass.
The single gure oi the accompanying drawing is a section, in a plane, passing through the axis,
t of a bowl adapted for practicing the described process. Certain structural features of the bowl are found in the patent issued to me April 4, 1922, No. 1,411,782, which provides means for independently feeding two separate' liquids to two separate zones in a separating bowl; but the construction embodying the invention herein described dliers essentially from that of my prior patent in respect to features particularly adapted for the'practice or the described process. Certain other structural features of the bowl are in the lower portion of the bowl. The outer tube I I, carrying the wash liquid, communicates with a plurality of channels I2 feeding a chamber inside a pervious wall I3 of clay or other suitable material. .Above the-group of discs I0, separated therefrom by a blank disc I4 and having communication therefrom through passages I5 is a. wash chamber I6 in communication through distributing holes I1 with an upper group of discs I8 similar to those in the lower group. The pervious wall I3 is located at the inner edge of this wash chamber.
Supported by suitable means `are two concen-l tric supply tubes 20 and 2l, which extend down into the tubes 1 and Ilf respectively.
- In the upper part of the bowl a top disc 22 provides a division wall between the separating chamber or the bowl and the passage 23 leading to the discharge outlet 6. Passages also lead from the inner edges of the discs I8o upward inside the neck of the top disc 22 to the outlet 24 for the discharge of light oil.
' Wings 25 between the bowl top 5 and the top disc 22 and wings 26secured to the bowl shell and extending inward to near the outer edges ot the discs, force. the bowl contents to continue rotating at the same speed as the bowl. Wings 21 and 28 attached to the walls of the tubes 1 and II respectively, force the incoming liquids to assume a speed of rotation equal to that of the bowl. Covers 29 are supplied to provide chambers to catch the materials discharged from the bowl. l
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 specliic gravity different from that of the liquid being treated and soluble in or combinable with some washing liquid, I will describe its use for only containing soap, is fed to the bowl through tubev 20, flows downward inside tube 1 and outward through channels 8 to the entrance of the distributing holes 9 in the discs I0, thence upward and distributes between the discs, where separation of a major'portion of the soap takes place in the usual manner. The soapstock flows outward to the bowl periphery and is discharged through opening 6 in the bowl top 5. The partially purified oil flows inward toward the center of the bowl to, and then outward through, opening I directly beneath the channels I2.
Clean water, fed through the passages I2 to the chambers at their ends. passes through the porous wall I3 and is finely disseminated through the oil flowing outward from the opening I5. Here it combines with the residual soap in the oil and the mixture flows through the holes I1 to the spaces between the upper discs I8 where the soap and water are separated from the oil and iiow toward the periphery of the bowl, where they mix with the previously separated soap, then upward around the edge of the top disc 22 and escape at 6, while the purified and washed oil flows inward between the discs I8 to their inner edges, thence upward inside the neck of the top disc and escapes at 24.
What I claim and desire to protect by Letters Patent is:
1. A centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating chamber and a secondary chamber, said chambers being radially substantially coextensive and surrounding the axis of the bowl along different lengths thereof, a set of frustro-conical discs in the primary chamber, means to distribute the liquid to be purified within the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, a similar set of discs in the secondary chamber, there being communication between the two chambers through which the separated liquid containing residual impurities flows from the primary chamber into the secondary chamber, and means to feed a wash iiuid into the secondary chamber, wherein the wash fluid combines with said residual impurities and a further purification of the liquid is effected by its separation therein from the combined wash liquid and residual impurities.
2. A centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating chamber and a secondary chamber, said chambers being radially substantially coextensive and surrounding the axis of the bowl along different lengths thereof, a set of frustro-conical discs in the primary chamber, means to distribute the liquid to be purified within the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, there being communication between the secondary chamber into a the two chambers through which the separated liquid containing residual impurities flows from the primary chamber into the secondary chamber, means to feed a wash fluid into the secondary chamber and a set of frustro-conical discs in the secondary chamber substantially radially coextensive with the discs in the primary chamber and within the spaces between which the wash fluid and the residual impurities combined therewith separate from the liquid to thereby effect the latters more complete purification, said bowl having an outlet for the finally purified liquid and a common outlet for the impurities separated in the primary chamber and the wash fluid and residual impurities separated in the secondary chamber.
3. A centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating chamber and a secondary chamber, a set of frustro-conical discs in the primary chamber, means to distribute the liquid to be purified within the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, there being communication between the two chambers through which the separated liquid containing residual impurities flows from the primary chamber into the secondary chamber, a feed tube for washing fiuid, a porous wall through which the wash iiuid enters the secondary chamber and is therein disseminated through the partially purified liquid flowing from the primary chamber to thereby combine with said residual impurities and be separated with said impurities from said liquid,
4. A centrifugal purifier for separating impurif ties from a liquid which comprises a rotatable bowl and means therein dividing it into a primary separating chamber and a secondary chamber, said chambers being radially substantially coextensive and surrounding the axis of the bowl along different lengths thereof, means affording communication between said chambers at the zones thereof nearest the axis, a feed conduit adapted to supply liquid to be purified to the primary chamber wherein occurs a primary separation from the liquid of the major part of the impurities, the partly purified liquid containing the residual impurities then flowing through said communicating means into the inner zone of the secondary chamber, a feed conduit adapted to supply a washing iiuid to the zone of the secondary chamber nearest the axis and disseminate the same throughout the partly purified liquid flowing into said zone from the primary chamber and combine with said residual impurities, said liquid being separated in the secondary chamber from said washing fluid and residual impurities, the bowl having outlets for the finally purified liquid and for the washing liquid and all separated impurities.
5. A centrifugal purifier for separating impurities from a liquid which comprises a rotatable bowl, a frustro-conical disc dividing the bowl into a primary separating chamber anda secondary chamber, a frustro-conical disc dividing wash compartment and a final separating compartment, piles of frustro-conical discs in the primary separating chamber and in the last named compartment, means affording communication between the primary separating chambers and the washing compartment at the zones thereof nearest the axis of the bowl, a feed conduit for supplying impure liquid to the primary separating chamber, another feed conduit for supplying washing uid to the zone of the washing compartment nearest the axis of the bowl, the bowl having outlets for the finally purified liquid and for the washing liquid and all separated impurities.
6. A centrifugal purifier for separating impurities from a Aliquid which comprises a rotatable bowl, a frustro-conical disc dividing the bowl into a primary separating chamber and a secondary chamber, a frustro-conical disc dividing the secondary chamber into a Wash compartment and a final separating compartment, piles of frustro-conical discs in the primary separating chamber land in the last named compartment, means affording communication between the primary separating chambers and the washing compartment at the zones thereof nearest the axis of the bowl, a feed conduit for supplying impure liquid to the primary separating chamber, another feed conduit for supplying washing iiuid to the zone of the washing compartment nearest the axis of the bowl, passages, relatively far from the axis, from the washing compartment to the final separating compartment, the bowl having outlets from the peripheries of all three compartments for discharge of washing fluid and impurities and an outlet from the final separating compartment for the finally purified liquid.
7. A centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means dividing the bowl into a primary separating chamber, and a chamber having a wash compartment and a nal separating compartment, said chambers surrounding the areas of the bowl along different lengths thereof, the primary separating chamber and the final separating compartment being radially substantially coextensive, a set of frustro-conical discs in the primary separating chamber, a set of frustro-conical discs in the final separating compartment, both sets of discs being substantially radially coextensive, means to distribute the liquid to be purified within the spaces between the discs in the primary separating chamber, wherein the major part of the impurities is separated from the liquid containing residual impurities, there being communication between the primary separating chamber and the wash compartment, means to supply a wash iiuid to the wash compartment, there being communication between the wash compartment and the nal separating compartment in which latter are effected a further purification of the 'liquid and its separation from the combined wash liquid and residual impurities, the bowl having outlets for the purified liquid and for the wash fluid and all separated impurities.
8. A centrifugal purifier in accordance with claim 7 wherein the communication between the primary separating chamber and the wash compartment is in a zone near the axis and wherein the communication between the wash compartment and the nal separating compartment is in a zone relatively distant from the axis.
9. A centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl and two frustro-conical partitions therein dividing the bowl into three compartments, one above another, namely, a primary separating chamber, a wash compartment and a secondary separating compartment, said compartments all surrounding the axis of the bowl along'dierent lengths thereof, means to feed the liquid to be purified to the primary separating chamber wherein the major part of the impurities is separated from the liquid containing residual-impurities, there being communication between the zone of the primary separating chamber containing separated partially purified liquid and the wash compartment through which said partially purified liquid is adapted to fiow from said chamber to said wash compartment, means to supply a wash fluid to the wash compartment and wherein itk is disseminated through the partially purified liquid admitted thereto from the primary separating chamber, there being communication between the ,wash compartment and the final separating compartment wherein the liquid is separated from the wash fluid and -residual impurities, the bowl having outlets for the purified liquid and'for the wash fiuid and all separated impurities.
10. A centrifugal purifier for separating from a liquid impurities heavier than the liquid comprising a rotatable bowl, means therein dividing it into a primary separating compartment, a wash compartment and a secondary separating compartment, a set of frustro-conical discs in each separating compartment, all said discs being similar and of substantially equal size, means, including a series of vertically aligned holes in the discs in the primary separating compartment, through which liquid to be purified is distributed to the spaces between said discs wherein the major part of the impurities are separated from the liquid containing residual impurities, means to conduct partially purified liquidfto said wash compartment, and means to disseminate a washing fluid through the liquid in said wash compartment wherein the wash uid combines with the residual impurities, there being vertically aligned holes in the discs of the secondary separating compartment, through which the mixture of partially purified liquid and wash liquid and impurities is distributed to the spaces between the discs in the secondary separating compartment, wherein further purification of the liquid is effected by separation therefrom of the wash fluid and residual impurities.
11. A centrifugal purifier for separating impurities from a liquid which comprises a rotatable bowl and means therein dividing it into a primary separating compartment, a. secondary compartment and a wash compartment, said compartments surrounding the axis of the bowl along different lengths thereof and being radially substantially coextensive, means affording communication between the primary and wash compartments at the zones thereof nearest the axis,
means affording communication between the Wash compartment and the secondary separating compartment at a greater distance from the axis, a feed conduit adapted to supply liquid to be purified tothe primary compartment wherein occurs a primary separation from the liquid of the major part of the impurities, the partly purified liquid containing the residual impurities then owing through the communicating means into the wash compartment. a feed conduit adapted to supply a washing fluid to the zone of the wash compartment nearest the axis and disseminate the same throughout the partially purified liquid flowing thereinto from the primary compartment, the washing fiuid therein combining with said residual impurities, the liquid being then conducted, through. the communicating `means specified,
to the secondary separating compartment wherein the liquid is separated from the washing iluid and residual impurities, the bowl having outlets for the ilnally purified liquid and for the washing uid and all separated taining residual impurities, there being communication, in a zone relatively near the axis, between the primary separating chamber and the wash compartment for the flow of partially purified liquid from said chamber to the wash compartment, means to supply a wash fluid to the wash compartment and wherein it is disseminated Athrough the partially purified liquid admitted thereto from the primary separating chamber, there being communication, in a zone relatively distant from the axis, between the wash compartment and the final separating compartment wherein the liquid is separated from the wash fluid and residual impurities, the bowl having outlets for the purified liquid and for the wash fluid and all separated impurities.
SELDEN H. HALL. l
US395151A 1941-05-26 1941-05-26 Machine for purifying liquids Expired - Lifetime US2313540A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US395151A US2313540A (en) 1941-05-26 1941-05-26 Machine for purifying liquids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US395151A US2313540A (en) 1941-05-26 1941-05-26 Machine for purifying liquids

Publications (1)

Publication Number Publication Date
US2313540A true US2313540A (en) 1943-03-09

Family

ID=23561914

Family Applications (1)

Application Number Title Priority Date Filing Date
US395151A Expired - Lifetime US2313540A (en) 1941-05-26 1941-05-26 Machine for purifying liquids

Country Status (1)

Country Link
US (1) US2313540A (en)

Cited By (14)

* 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
US2546186A (en) * 1947-03-11 1951-03-27 Charles F Hall Convection-compensating centrifuge
US2603413A (en) * 1947-09-08 1952-07-15 Int Harvester Co Power washing centrifugal separator
US2628021A (en) * 1949-05-03 1953-02-10 Separator Ab Centrifuge with auxiliary feed arrangement
US2641363A (en) * 1947-07-08 1953-06-09 Henri G Chatain Apparatus for clarifying liquids
US2694520A (en) * 1951-12-03 1954-11-16 Goument Vear Oliver Apparatus for separating butterfat from milk
US3036759A (en) * 1957-01-22 1962-05-29 Separator Ab Centrifugal bowl for separating sludge-containing liquids
US3117928A (en) * 1960-04-22 1964-01-14 Separator Ab Centrifugal separator
US3341094A (en) * 1964-04-14 1967-09-12 Ceskoslovenska Akademie Ved Centrifuge for continuously effecting concentration of solids from a suspension thereof in liquid
US3350296A (en) * 1961-08-01 1967-10-31 Exxon Research Engineering Co Wax separation by countercurrent contact with an immiscible coolant
US3529767A (en) * 1962-02-28 1970-09-22 Pennwalt Corp Centrifuge for separating solids from liquid
US5509882A (en) * 1994-09-12 1996-04-23 Tetra Laval Holdings & Finance S.A. Decanter centrifuge having an offset conveyor flight to aid rinsing
US6572524B1 (en) 2000-07-14 2003-06-03 Alfa Laval Inc. Decanter centrifuge having a heavy phase solids baffle
US10940489B2 (en) 2015-04-24 2021-03-09 Alfa Laval Corporate Ab Centrifugal separator with disc stack having discs of different diameters

Cited By (14)

* 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
US2546186A (en) * 1947-03-11 1951-03-27 Charles F Hall Convection-compensating centrifuge
US2641363A (en) * 1947-07-08 1953-06-09 Henri G Chatain Apparatus for clarifying liquids
US2603413A (en) * 1947-09-08 1952-07-15 Int Harvester Co Power washing centrifugal separator
US2628021A (en) * 1949-05-03 1953-02-10 Separator Ab Centrifuge with auxiliary feed arrangement
US2694520A (en) * 1951-12-03 1954-11-16 Goument Vear Oliver Apparatus for separating butterfat from milk
US3036759A (en) * 1957-01-22 1962-05-29 Separator Ab Centrifugal bowl for separating sludge-containing liquids
US3117928A (en) * 1960-04-22 1964-01-14 Separator Ab Centrifugal separator
US3350296A (en) * 1961-08-01 1967-10-31 Exxon Research Engineering Co Wax separation by countercurrent contact with an immiscible coolant
US3529767A (en) * 1962-02-28 1970-09-22 Pennwalt Corp Centrifuge for separating solids from liquid
US3341094A (en) * 1964-04-14 1967-09-12 Ceskoslovenska Akademie Ved Centrifuge for continuously effecting concentration of solids from a suspension thereof in liquid
US5509882A (en) * 1994-09-12 1996-04-23 Tetra Laval Holdings & Finance S.A. Decanter centrifuge having an offset conveyor flight to aid rinsing
US6572524B1 (en) 2000-07-14 2003-06-03 Alfa Laval Inc. Decanter centrifuge having a heavy phase solids baffle
US10940489B2 (en) 2015-04-24 2021-03-09 Alfa Laval Corporate Ab Centrifugal separator with disc stack having discs of different diameters

Similar Documents

Publication Publication Date Title
US2313540A (en) Machine for purifying liquids
US2313541A (en) Machine for purifying liquids
US2599619A (en) Method and apparatus for centrifugal separation
US2628021A (en) Centrifuge with auxiliary feed arrangement
GB726596A (en) Improvements in or relating to centrifuges for separating, sludge containing liquids
US3027390A (en) Apparatus and method for centrifugal purification of fatty oils
GB414558A (en) Improved process and apparatus for the continuous extraction or treatment of liquids
US3117928A (en) Centrifugal separator
JPS6045921B2 (en) Continuously working full-wall countercurrent centrifugal extractor
US3162510A (en) Mixing and separating apparatus
US2500100A (en) Centrifugal bowl
US2083809A (en) Bowl centrifuge
US2973896A (en) Centrifuge apparatus
US1575116A (en) Process and apparatus for securing temporary intimate contact between immiscible liquids
US1492168A (en) Process of refining sugar-cane juice
GB299422A (en) Improvements in or relating to centrifugal separators
US3228598A (en) Centrifuge discharge means
US3250462A (en) Method and apparatus for sludge concentration by centrifugation
US1411782A (en) Centrifugal separator
GB260071A (en) Improvements in and relating to centrifugal separators
US2302382A (en) Removal of impurities from soap nigre
US2089122A (en) Apparatus for separating wax from oil
GB480943A (en) A unit of centrifugal separators for the purification of highly contaminated liquids
US3192149A (en) Separation of components of liquidsolids mixtures
US1634242A (en) Method and mechanism for removing centrifuge effluents