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US1257235A - Centrifugal liquid-purifier. - Google Patents

Centrifugal liquid-purifier. Download PDF

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Publication number
US1257235A
US1257235A US20692017A US20692017A US1257235A US 1257235 A US1257235 A US 1257235A US 20692017 A US20692017 A US 20692017A US 20692017 A US20692017 A US 20692017A US 1257235 A US1257235 A US 1257235A
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Prior art keywords
receptacle
shaft
liquid
water
purifier
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US20692017A
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William G Howell
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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
    • B04B1/10Centrifuges 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

Definitions

  • This invention relates to employing centrifugal force for removing sedimentary matter from liquids.
  • specific gravity such matter often differs but little from the liquid in which it is suspended.
  • the water need not be completely freed from sediment, but for drinking purposes it must be made clear. aware, centrifugal systems have not gone into permanent practical use, partly no doubt because it has not proved practicable to use fully effective speed, to avoid bad results from wear, to secure a very large output, and at the same time to avoid prohibitime cost.
  • T have found it highly advantageous, under proper conditions, to give the advancing stream of water the form of a small hollow cylinder and to rotate this thin cylindrical body at unusually high speed, centrifugal force increasing with the square of the speed of travel about the axis of rotation,-
  • Figure 1 is a vertical axial section of the apparatus.
  • Fig. 2 is a section on the line 2-2, Fig.1;
  • 5 represents any suitable base and 6' rigid supports rising therefrom and provided with alined hearings 7 for the I rotary hollow shaft 8 of a. drum 9 which is driven by a belt 10 and a pulley l1 rigidly fixed to the head of the drum.
  • the mterior of the drum is provided with numerous spaced annular ribs or diaphragms 12 extending inwardly to some distance from the drum wall and further provided with a concentric hollow cylinder 13 extending from end to end ofthe drum.
  • the space between the cylinder and drum wall is divided by a series bf regularly spaced radial longitudinal partitions or ribs 12 which extend between the ribs 12 approximately to the drum wall, and the cylinder is similarly divided So far as I am' by longitudinal partitions 13.
  • the hollow shaft is provided with transverse partitions let, 14 which are spaced apart, and from the compartment thus formed a small axial tube 15 leads outward .and communicates with a pipe 16. From the same compartment pipes 17 project radially into the pockets formed by the annular and longitudinal ribs 12, 12. The annular space be?
  • the longitudinal partitions in the hollow cylinder compel the entering water to rotate with the apparatus before it enters the annular outer separating space in the drum, and the like partitions in the latter space prevent any lag in rotation during separation.
  • Centrifugal force varies with the distance from the axis and this construction separates from the more central body athin cylindrical body of water at some distance from the axis andprevents any portion of this outer stratum from mixing with the more central impure body, the travel of whichabout the axis is comparatively slow.
  • a stream of water continually flowing through the supply pipe is expanded to form a thin hollow cylindrical body and rotated at very high velocity, whereby prac- 1 tically all matters mechanically suspended are thrown to the outer part of said body; That such matter may not still go on with the longitudinally advancing water, the
  • discharge pipe 25 is opened to allow part direction of the water entering the same reduce the rate of flow for a given entering pressure, and this reduction has been experi- 'mentally made such as to give the. best results, the separation of sediment depending on time as well as the degree of centrifugal force.
  • the inflow and discharge pipes 19, 24 are closed, a valved of the water in the drum 9 to escape, the air inlet pipe 16 being also opened to admit air through 15, 17, 17, and then, the pipe 25 being closed if desired, the drum is rotated at relatively slow speed so that the splashare restored to initial position and operated as first set forth.
  • the apparatus may be small. There is no mixing of pure and impure water, even after wear, there are practically as many purifiers as there are pockets and the product is delivered rapidly and entirely clear when any natural water with which I am acquainted is used.
  • the apertures or-passages 20, 21 22 progressively increase inesize of courde, so that the same amount of water may pass although the speed decreases. It may be further noted that use of many small pockets prevents dis-.
  • a liquid purifier the combination with a conduit for flowing liquid to be purified, of means for retarding the normal rate of flow and changing the form of the flowing mass to that of a relatively large thin hollow cylinder, means for rapidly rotating the mass about its axes while it slowly advances in its changed form, and means for collecting the sediment thrown outward by rotation.
  • a centrifugal liquid purifier the combination with a liquid receptacle having a partition dividing it into an axial chamber and a relatively thin annular compartment communicating with said chamber near one end and discharging near the opposite end, of means for rapidly rotating the re.- ceptacle and means for continuously introducing liquid into said chamber.
  • a centrifugal liquid purifier the combination with an elongated receptacle divided longitudinally into an axial chamber transversely divided and surrounded by a narrow annular separating compartment communicating near one end with said chamber and discharging near the opposite end, means for discharging liquid into said chamber at a distance from the end first mentioned, and means for rapidly rotating said receptacle.

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  • Centrifugal Separators (AREA)

Description

w. G, HOWELL.
CENTRIFUGAL LIQUID PURIFIER APPLICATION FILED 05c. 13. 1911.
Patented Feb. 19,1918.
2 SHEETS-SHEET 1.
far/164257 w. s. HOWELL. CENTRKFUGAL LIQUID PURIFIER.
APPLICATIQN FILED DEC. 13. I917.
- Patented Feb/19,1918.
' 2 SHEETS-SHEET 2.
WILLIAM G. HOWELL, or w annnn'ron, VIRGINIA.
CENTRIFUGAL LIQU'ID-PURIFIER.
Specification of Letters Patent. Patented Feb. 19, 1918.
Application filed December 13, 1917. Serial No. 206,920.
To all whom it may concern:
Be it known that I, WILLIAM G. HOWELL, a citizen of the United States, and resident of VVarrenton in the county of Fauquier and State of Virginia, have invented certain new and useful Improvements in Centrifugal Liquid-Purifiers, of which the following is a specification, reference being had therein to the accompanying drawing.
This invention relates to employing centrifugal force for removing sedimentary matter from liquids. In specific gravity, such matter often differs but little from the liquid in which it is suspended. For certain uses, the water need not be completely freed from sediment, but for drinking purposes it must be made clear. aware, centrifugal systems have not gone into permanent practical use, partly no doubt because it has not proved practicable to use fully effective speed, to avoid bad results from wear, to secure a very large output, and at the same time to avoid prohibitime cost.
T have found it highly advantageous, under proper conditions, to give the advancing stream of water the form of a small hollow cylinder and to rotate this thin cylindrical body at unusually high speed, centrifugal force increasing with the square of the speed of travel about the axis of rotation,-
and theelimination of matter in suspension depending upon-this speed and upon the time during which centrifugal force acts upon the suspended particles.
In the accompanying drawings, Figure 1 is a vertical axial section of the apparatus.
Fig. 2 is a section on the line 2-2, Fig.1;
In these figures, 5 represents any suitable base and 6' rigid supports rising therefrom and provided with alined hearings 7 for the I rotary hollow shaft 8 of a. drum 9 which is driven by a belt 10 and a pulley l1 rigidly fixed to the head of the drum. The mterior of the drum is provided with numerous spaced annular ribs or diaphragms 12 extending inwardly to some distance from the drum wall and further provided with a concentric hollow cylinder 13 extending from end to end ofthe drum. The space between the cylinder and drum wall is divided by a series bf regularly spaced radial longitudinal partitions or ribs 12 which extend between the ribs 12 approximately to the drum wall, and the cylinder is similarly divided So far as I am' by longitudinal partitions 13. The hollow shaft is provided with transverse partitions let, 14 which are spaced apart, and from the compartment thus formed a small axial tube 15 leads outward .and communicates with a pipe 16. From the same compartment pipes 17 project radially into the pockets formed by the annular and longitudinal ribs 12, 12. The annular space be? tween the hollow shaft and the hollow cylinder is divided, like the shaft, by transverse partitions 18, 18, registering with the partitions 14;, 14, respectively, and apertures 17 connect the two compartments between the two sets of partitions. Water to be acted upon enters the hollow shaft through a valved pipe 19, passes to the partition 14, flows outward through apertures 20 into the hollow cylinder and back to openings 21 by which it enters the subdivided drum space outside the hollow cylinder. Thence it passes to the opposite end of the drum, through openings 22 intothe corresponding compartment of the hollow cylinder, through apertures 23 into the analogous compartment in the hollow shaft, whence it escapes through a valved pipe at forming a conduit for pure water to'pass to an elevated container 24, v
The longitudinal partitions in the hollow cylinder compel the entering water to rotate with the apparatus before it enters the annular outer separating space in the drum, and the like partitions in the latter space prevent any lag in rotation during separation.
Centrifugal force varies with the distance from the axis and this construction separates from the more central body athin cylindrical body of water at some distance from the axis andprevents any portion of this outer stratum from mixing with the more central impure body, the travel of whichabout the axis is comparatively slow. -In effect, therefore, a stream of water continually flowing through the supply pipe is expanded to form a thin hollow cylindrical body and rotated at very high velocity, whereby prac- 1 tically all matters mechanically suspended are thrown to the outer part of said body; That such matter may not still go on with the longitudinally advancing water, the
numerous pockets are provided, and from these-no sediment escapes so long as rapid rotation continuea' Varying the length of the receptacle and reversing, repeatedly, the
; discharge pipe 25 is opened to allow part direction of the water entering the same reduce the rate of flow for a given entering pressure, and this reduction has been experi- 'mentally made such as to give the. best results, the separation of sediment depending on time as well as the degree of centrifugal force.
When a large amount of sediment has accumulated in the pockets, the inflow and discharge pipes 19, 24 are closed, a valved of the water in the drum 9 to escape, the air inlet pipe 16 being also opened to admit air through 15, 17, 17, and then, the pipe 25 being closed if desired, the drum is rotated at relatively slow speed so that the splashare restored to initial position and operated as first set forth.
It may be noted that the entire body of water and the containing parts rotate together, there being no. slip or water friction other than that due to the relatively slow longitudinal advance of the rotating water, that consequently the power required for high speed rotation is very slight, and that since the speed can readily be made as high as is desired, the apparatus may be small. There is no mixing of pure and impure water, even after wear, there are practically as many purifiers as there are pockets and the product is delivered rapidly and entirely clear when any natural water with which I am acquainted is used. The apertures or-passages 20, 21 22 progressively increase inesize of courde, so that the same amount of water may pass although the speed decreases. It may be further noted that use of many small pockets prevents dis-.
lodging of mud by eddy currents.
lVhat I claim is:
1. In a liquid purifier, the combination with a conduit for flowing liquid to be purified, of means for retarding the normal rate of flow and changing the form of the flowing mass to that of a relatively large thin hollow cylinder, means for rapidly rotating the mass about its axes while it slowly advances in its changed form, and means for collecting the sediment thrown outward by rotation.
2. In a centrifugal liquid purifier, the combination with a liquid receptacle having a partition dividing it into an axial chamber and a relatively thin annular compartment communicating with said chamber near one end and discharging near the opposite end, of means for rapidly rotating the re.- ceptacle and means for continuously introducing liquid into said chamber.
3. In a centrifugal liquid purifier, the combination with an elongated receptacle divided longitudinally into an axial chamber transversely divided and surrounded by a narrow annular separating compartment communicating near one end with said chamber and discharging near the opposite end, means for discharging liquid into said chamber at a distance from the end first mentioned, and means for rapidly rotating said receptacle.
l. The combination with an elongated closed approximately horizontal receptacle divided by a fixed wall into an axial chamher and a relatively narrow annular peripheral compartment having near its ends respectively, an inlet from said chamber and an outlet and formed with peripheral sediment-receiving pockets, means for delivering liquid in said chamber at a distance from said inlet through which alone it can escape, and means for rotating the receptacle.
5. The combination with a closed receptacle mounted upon a hollow shaft internally divided by a transverse partition and provided with lateral discharge apertures near said partition, of a closed receptacle mounted upon and concentric with said shaft, means for introducing liquid into the portion of the shaft provided with said apertures, a. sleeve concentric with the shaft and dividing the closed space surrounding it into an inner annular chamber and an outer annular separating compartment communicating with said chamber near the end opposite said apertures and discharging at the opposite end, and means for rapidly irotating the receptacle. r
6. In combination with a closed elongated, approximately horizontal receptacle longitudinally' divided into three concentric chambers by a hollow shaft and a larger hollow cylinder, partitions dividing the inmeans for introducing liquid at one end of the shaft and for discharging liquid at the opposite end of the shaft, said shaft and hollow cylinder being laterally perforated on opposite sides of their transverse partitions. substantially as set forth. r 7. The combinatlon with an approximately horizontal closed feceptacle, of a hollow shaft exten ing axially through the receptacle and ving a transverse partition at some distance from the ends of-the receptacle, a hollow concentric cylinder dividin the receptacle space outside the shaft and provided with lateral perforations near its ends, a transverse partition dividin the annular space between the shaft an hollow cylinder, means for rapidly rotating the receptacle, a valved conduit for introducin liquid at one end of the shaft, and a valve conduit for discharging liquid at the opposite end of the shaft.
8. The combination with an approximately horizontal closed receptacle, of a hollow shaft extending axially through the receptacle and having a transverse partition at some. distance from the ends of the receptacle, a hollow concentric cylinder dividing the receptacle space outside the shaft and provided with lateral perforations near its ends, a transverse partition dividing the annul'ar space between the shaft and hollow cylinder, means for rapidly rotating the receptacle, a valved conduit for introducin liquid at one end of the shaft, a valve conduit for discharging liquid at the oppo- 9. The combination with a rotary receptacle having internal peripheral pockets and suitable discharge openings, of an axial conduit extending into the same and laterally perforated near the closed inner end of its passage, and a concentric larger conduit closed at its inner, end and laterally perforated near its opposite end, whereby liquid admitted to the inner conduit is twice reversed in direction as it passes from the admission to the discharge end of the apparatus.
In testimony whereof I h'ereunto aflix my signature.
w. e. HOWELL.
US20692017A 1917-12-13 1917-12-13 Centrifugal liquid-purifier. Expired - Lifetime US1257235A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2559917A (en) * 1945-12-22 1951-07-10 Paul J Gresham Centrifuge bowl with reciprocating valve for discharging solids from the bowl
US2661150A (en) * 1947-12-17 1953-12-01 Jr William G Abbott Centrifuge
US2947472A (en) * 1944-09-20 1960-08-02 Skarstrom Charles Centrifuge apparatus
US3854658A (en) * 1973-05-07 1974-12-17 Dorr Oliver Inc Solid bowl conveyer type centrifuge
US3880347A (en) * 1973-08-07 1975-04-29 Samuel A Kirk Inertia centrifuge
US3904109A (en) * 1973-12-14 1975-09-09 Gene E Underwood Multiple density separator
US3905546A (en) * 1973-07-10 1975-09-16 Pavel Semenovich Vlasov Centrifugal extractor
US4108354A (en) * 1974-07-23 1978-08-22 Asea Aktiebolag Gaseous mixture ultracentrifuge

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2947472A (en) * 1944-09-20 1960-08-02 Skarstrom Charles Centrifuge apparatus
US2559917A (en) * 1945-12-22 1951-07-10 Paul J Gresham Centrifuge bowl with reciprocating valve for discharging solids from the bowl
US2661150A (en) * 1947-12-17 1953-12-01 Jr William G Abbott Centrifuge
US3854658A (en) * 1973-05-07 1974-12-17 Dorr Oliver Inc Solid bowl conveyer type centrifuge
US3905546A (en) * 1973-07-10 1975-09-16 Pavel Semenovich Vlasov Centrifugal extractor
US3880347A (en) * 1973-08-07 1975-04-29 Samuel A Kirk Inertia centrifuge
US3904109A (en) * 1973-12-14 1975-09-09 Gene E Underwood Multiple density separator
US4108354A (en) * 1974-07-23 1978-08-22 Asea Aktiebolag Gaseous mixture ultracentrifuge

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