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US2373099A - Liquid division - Google Patents

Liquid division Download PDF

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Publication number
US2373099A
US2373099A US402041A US40204141A US2373099A US 2373099 A US2373099 A US 2373099A US 402041 A US402041 A US 402041A US 40204141 A US40204141 A US 40204141A US 2373099 A US2373099 A US 2373099A
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US
United States
Prior art keywords
liquid
projections
channels
receiving surface
separating
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
US402041A
Inventor
Robert E Burk
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Standard Oil Co
Original Assignee
Standard Oil 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 Standard Oil Co filed Critical Standard Oil Co
Priority to US402041A priority Critical patent/US2373099A/en
Application granted granted Critical
Publication of US2373099A publication Critical patent/US2373099A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/008Liquid distribution
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006Controlling or regulating processes
    • B01J19/0013Controlling the temperature of the process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/19Details relating to the geometry of the reactor
    • B01J2219/194Details relating to the geometry of the reactor round
    • B01J2219/1941Details relating to the geometry of the reactor round circular or disk-shaped
    • B01J2219/1942Details relating to the geometry of the reactor round circular or disk-shaped spherical
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/8593Systems
    • Y10T137/85938Non-valved flow dividers

Definitions

  • the equal division or distribution of liquid is a problem'which has received much attention 10 Claims. (0!. 137-166) feed at the top.
  • the number of fins or projections of liquid channels 5 may be as dein various relations, as for instance in fractionation, supply of absorbent or contact liquids, etc.
  • the commonly used construction involves. a plurality of tubes, the number depending upon the extent of distribution desired, but these have I features hereinafter fully described, and particularly pointed out in the claims, the following description and the annexed drawing setting forth in detail certain illustrative embodiments of the invention, these being indicative however, of but a few of the various ways in which the principle of the invention may be employed.
  • FIG. 1 is a plan view
  • Fig. 2 is a side elevational view, showing construction embodying the invention
  • Fig. 3 is a side elevation of a modification.
  • the capillary forces and surface tension cause the liquid to spread evenly and thus'flow downwardly to a lower zone where it encounters dividingfins or projections which divert it into segregated streams of the number desired in any given instance, and more or less than the number illustrated may be arranged.
  • the rounded surface 2 is at least symmetrical to the down-flowing liquid, and it may be an oblate spheroid, but preferably, the surface is mathematically spherical.
  • the separating portion therebelow may be in the general form of a cylindrical extension providing diverting chan-' nels of desired number for separating discharge streams.
  • the dividing fins or projections may satisfactorily be formed of dividing apices 3,
  • a pipe I' may continue as a central bore which opens at the top of the rounded or spherical surface 2 as in Fig. 3, so that the liquid overflows onto the surface and distributes to the dividers or fins which are as above described.
  • Liquid dividing means comprising a hemispherical receiving surface with a cylindrical exwhence sloping ledges 4 lead to channels 5, and
  • the fins are along the horizontal great circle, or circle whose diameter is that of the sphere and whose plane is perpendicular to the tension below provided with projections having liquid separating apices sloping to channels between projections and means for delivering liquid to the top of said hemispherical surface.
  • Liquid dividing means comprising a receiving surface of revolution curved outwardly and downwardly in rounded form and having an extension below with diameter at least as great, liquid separating projections on said extension, and a bore opening through the rounded surface at the top for supplying liquid to be divided.
  • Liquid dividing means comprising a spherical receiving surface and means for delivering lid-inseam spherical Sulfa at substantially I said cylindrical extension separating liquid into respective streams.
  • Liquid dividing means comprising a surface of a sphere having a cylindrical extension below, means for feeding liquid to the top of said surface, and liquid-dividing projections along the horizontal great circle of the surface.
  • Liquid dividing means comprising a receiv ing surface curved outwardly and downwardly in dome-like circular form and having an extension below with diameter at least as great as the circle of said dome, liquid separating projections on said extension, and means for supplying liquid to the top of said receiving surface.
  • Liquid dividing means comprising a spherical liquid receiving surface provided with projections adjacent thereto below said receiving surasraooa face having liquid separating aplc'es sloping downwardly to channels between said projections. and means for delivering liquid to the top of said spherical liquid receiving surface.
  • Liquid dividing means comprising a spheroidal surface, means to discharge liquid on the top of said surface, and projections below said liquid receiving surface having liquid separating apices sloping to channels between said projections for dividing the. liquid flowing downwardly on said surface between said "spices and directing it to the channel.
  • Liquid dividing means comprising a spheroidal liquid receiving surface provided with projections adjacent thereto below saidliquid receiving surface having liquid separating apices sloping downwardly to channels between said projections, and means for delivering liquid to the top of said spheroidal liquid receiving surface.
  • a liquid fuel divider comprising a receiving surface curved outwardly and downwardly in rounded form and circular in cross section and having an extension below with diameter as great, means for discharging liquid fuel on the top of said surface, separating projections for dividing the downflow liquid on said elrtension, and means for conducting the divided liquid fuel to the points of use.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

April 10, 1945. R BURK 2,373,099
LIQUID DIVISION Filed July 11. 1941 INVENTOR. ROBERT 6. Buk'k ATTO RNEY5 2 UNITED sw Patented Apr. 10, 1945 NT orrica lmoumnrvrsron I Robert E. Burk,- CIeveIand H di. 'OhIm-assignor to The Standard i! Company, Cleveland, Ohio,
a corporation of Ohio I Application July 1m. Serial No. 402,041
The equal division or distribution of liquid is a problem'which has received much attention 10 Claims. (0!. 137-166) feed at the top. 'As noted, the number of fins or projections of liquid channels 5 may be as dein various relations, as for instance in fractionation, supply of absorbent or contact liquids, etc. The commonly used construction involves. a plurality of tubes, the number depending upon the extent of distribution desired, but these have I features hereinafter fully described, and particularly pointed out in the claims, the following description and the annexed drawing setting forth in detail certain illustrative embodiments of the invention, these being indicative however, of but a few of the various ways in which the principle of the invention may be employed.
In said annexed drawing- Fig. 1 is a plan view, and Fig. 2 is a side elevational view, showing construction embodying the invention; and Fig. 3 is a side elevation of a modification.
The liquid to be distributed or divided into portions, and as forwarded by any suitable means, as for instance pipe I, Fig. 2, is directed onto a rounded receiving surface 2. Here, the capillary forces and surface tension cause the liquid to spread evenly and thus'flow downwardly to a lower zone where it encounters dividingfins or projections which divert it into segregated streams of the number desired in any given instance, and more or less than the number illustrated may be arranged. The rounded surface 2 is at least symmetrical to the down-flowing liquid, and it may be an oblate spheroid, but preferably, the surface is mathematically spherical. Desirably also, the separating portion therebelow may be in the general form of a cylindrical extension providing diverting chan-' nels of desired number for separating discharge streams. The dividing fins or projections may satisfactorily be formed of dividing apices 3,
sired in' any given case in accordance with the number of final discharge streams coming from the channels, as may be predetermined. The de- .tail of the projections or flnsmay vary, within general qualifications of providing diverting surfaces or channels for the'respective'number of ultimate discharge streams required. Thus, in the operation, liquid supplied from the pipe I at the top of the round surface 2 flows downin even distribution on-all sides, and discharges in separated streams as indicated by the arrows, Fig. 2. Where the liquid divided is to be received by vertical surface fractionating columns for instance, reflux liquid is given an initial distribution into areas at the top of the column, and the quality of distribution is maintained whether the feed be large or small. Where'the streams as discharged from the channels 5 are not to be further spread, the discharge frqm the channels may be receivedinto respective tubes or pipes 6, as indicated in dotted lines,
Fig.2. Thus, also for an internal combustion engine thefuel as evenly divided is directed in even feed to each cylinder.
Instead of supplyingthe feed from a pipe i as in Fig. 2, above the rounded surface 2, a pipe I' may continue as a central bore which opens at the top of the rounded or spherical surface 2 as in Fig. 3, so that the liquid overflows onto the surface and distributes to the dividers or fins which are as above described.
Other modes of applying the principle of the invention may be employed, change being made as regards the details described, provided the features stated in any of the following claims, or the equivalent of such, be employed.
I therefore particularly point out and distinctly claim as my invention: I
1. Liquid dividing means, comprising a hemispherical receiving surface with a cylindrical exwhence sloping ledges 4 lead to channels 5, and
preferably the fins are along the horizontal great circle, or circle whose diameter is that of the sphere and whose plane is perpendicular to the tension below provided with projections having liquid separating apices sloping to channels between projections and means for delivering liquid to the top of said hemispherical surface.
2. Liquid dividing means, comprising a receiving surface of revolution curved outwardly and downwardly in rounded form and having an extension below with diameter at least as great, liquid separating projections on said extension, and a bore opening through the rounded surface at the top for supplying liquid to be divided.
3. Liquid dividing means, comprising a spherical receiving surface and means for delivering lid-inseam spherical Sulfa at substantially I said cylindrical extension separating liquid into respective streams.
5. Liquid dividing means, comprising a surface of a sphere having a cylindrical extension below, means for feeding liquid to the top of said surface, and liquid-dividing projections along the horizontal great circle of the surface.
6. Liquid dividing means, comprising a receiv ing surface curved outwardly and downwardly in dome-like circular form and having an extension below with diameter at least as great as the circle of said dome, liquid separating projections on said extension, and means for supplying liquid to the top of said receiving surface.
7. Liquid dividing means, comprising a spherical liquid receiving surface provided with projections adjacent thereto below said receiving surasraooa face having liquid separating aplc'es sloping downwardly to channels between said projections. and means for delivering liquid to the top of said spherical liquid receiving surface.
8. Liquid dividing means, comprising a spheroidal surface, means to discharge liquid on the top of said surface, and projections below said liquid receiving surface having liquid separating apices sloping to channels between said projections for dividing the. liquid flowing downwardly on said surface between said "spices and directing it to the channel.
9. Liquid dividing means, comprising a spheroidal liquid receiving surface provided with projections adjacent thereto below saidliquid receiving surface having liquid separating apices sloping downwardly to channels between said projections, and means for delivering liquid to the top of said spheroidal liquid receiving surface.
10. A liquid fuel divider comprising a receiving surface curved outwardly and downwardly in rounded form and circular in cross section and having an extension below with diameter as great, means for discharging liquid fuel on the top of said surface, separating projections for dividing the downflow liquid on said elrtension, and means for conducting the divided liquid fuel to the points of use.
ROBERT E. BURK.
US402041A 1941-07-11 1941-07-11 Liquid division Expired - Lifetime US2373099A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2884006A (en) * 1955-03-08 1959-04-28 James E Hoback Fuel distributor for internal combustion engines
US2884754A (en) * 1956-04-05 1959-05-05 Int Harvester Co Cotton picking spindle moistening assembly
US3423913A (en) * 1966-01-27 1969-01-28 Int Harvester Co Cotton picker spindle moistener assembly
US4712581A (en) * 1985-04-17 1987-12-15 Volkswagen Aktiengesellschaft Distribution device for a two-phase flow
US5154353A (en) * 1989-11-16 1992-10-13 Plachy Richard F Optimized weir construction for liquid distributors
US6073685A (en) * 1994-12-23 2000-06-13 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Fluid inlet/outlet chamber and corresponding fluid circulation apparatus
US6325091B1 (en) * 2001-01-19 2001-12-04 Precision Plumbing Products, Inc. Water distribution apparatus for multiple sewer drain trap primer systems

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2884006A (en) * 1955-03-08 1959-04-28 James E Hoback Fuel distributor for internal combustion engines
US2884754A (en) * 1956-04-05 1959-05-05 Int Harvester Co Cotton picking spindle moistening assembly
US3423913A (en) * 1966-01-27 1969-01-28 Int Harvester Co Cotton picker spindle moistener assembly
US4712581A (en) * 1985-04-17 1987-12-15 Volkswagen Aktiengesellschaft Distribution device for a two-phase flow
US5154353A (en) * 1989-11-16 1992-10-13 Plachy Richard F Optimized weir construction for liquid distributors
US6073685A (en) * 1994-12-23 2000-06-13 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Fluid inlet/outlet chamber and corresponding fluid circulation apparatus
US6325091B1 (en) * 2001-01-19 2001-12-04 Precision Plumbing Products, Inc. Water distribution apparatus for multiple sewer drain trap primer systems

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