US1770221A - Bubble tower - Google Patents

Bubble tower Download PDF

Info

Publication number
US1770221A
US1770221A US191250A US19125027A US1770221A US 1770221 A US1770221 A US 1770221A US 191250 A US191250 A US 191250A US 19125027 A US19125027 A US 19125027A US 1770221 A US1770221 A US 1770221A
Authority
US
United States
Prior art keywords
bubble
liquid
plates
plate
bubble tower
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
US191250A
Inventor
Perry J Sweeny
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.)
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 US191250A priority Critical patent/US1770221A/en
Application granted granted Critical
Publication of US1770221A publication Critical patent/US1770221A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • B01D3/16Fractionating columns in which vapour bubbles through liquid
    • B01D3/18Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
    • B01D3/20Bubble caps; Risers for vapour; Discharge pipes for liquid

Definitions

  • This invention relates to improvements in fractionating columns and particularly to columns of the bubble cap type.
  • overflow pipes 16 which contain a liquid seal or trap and are .provided with an outlet located above the liquid level of the plate next below.
  • Each of the overflow pipes 16 preferably comprises an upstanding nipple 17. a flange 18 therebeneath for attachment toa bubble cap plate, and a lower body portion constituted by sides 19 and a wall portion 20 which extends downwardly from said flange, closes the bottom of the nipple 17 and then proceeds upwardly forming with the sides 19 a well 21.
  • the wall 20 then bends downwardly again and together with extensionsof the sides 19 forms a spout 22 which terminates, somewhat above the level of the liquid maintained in the next inferior plate.
  • a septum 23 extends between the sides 19 and from the flange 18 into the well 21 so as to establish a liquid seal therein.
  • the septum 23 preferably conver es downwardly towards the vertical part o .the wall portion 20 so as to create a scavenging eifect in the ⁇ well 21 thus aiding in preventing accumulation of rust or scale therein.
  • the overflows 16 are attached to the bubble plates 11 at a.
  • the liquid sealed spouts 18 extend toward the central portion of each of the bubble plates 11.
  • the overflow devices of the present invention pick up the liquid on their respective bubble plates at a point adjacent the margin thereof, and discharge it centrally of the bubble plate therebeneath and above the level of the liquid thereon.
  • asubstantially uniform composition is realized for the pools of liquid maintained on the bubble plates and consequently more accurate vapor fractionation is possible.
  • a bubble tower provided with super imposed bubble cap plates, the successive bubble-cap plates being provided with overflow pipe plates, each comprising a nipple projecting above the bubble plate to which it is attached near the margin thereof, a spout below the plate and emptying centrally above the level of liquid on the plate beneath, whereby a flow of liquid is established from the central portion to the margin of said plates and means providing a liquid seal between said overflow and the spout.
  • a bubble tower provided with superimposed bubble cap plates, the successive bubble-cap plates being provided with overflow pipes for said bubble cap plates, each comprising a nipple projecting above the bubble plate to which it is attached near the margin thereof, a well portion, a spout extending therefrom and emptying centrally above the level of li uid on the plate beneath, whereby a flow of liquid is established from the central portion to the margin of said plates and means providing al liquid seal in said wel] portion.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

July 8, 1930. y P J, SWEENY 1,770,221
BUBBLE TOWER Filed May l5. 1927 Patented July 8, 193D UNITED STATES APATENT OFFICE PERRY J'. SWEENY, OF WHITING, INDIANA, ASSIGNOR TO STANDARD OIL COMPANY, OF WHITING, INDIANA,.A CORPORATION OF INDIANA.
BUBBLE TOWER Application filed May 13,
.This invention relates to improvements in fractionating columns and particularly to columns of the bubble cap type.
The invention will be readily understood from the following description taken in conand at its upper end with a liquid supply pipe 14 and a vapor outlet 15.
Instead of the ordinary overflow pipes which are mounted on each bubble plate and extend into the liquid maintained on the bubble plate next below I provide overflow pipes 16 which contain a liquid seal or trap and are .provided with an outlet located above the liquid level of the plate next below.
Each of the overflow pipes 16 preferably comprises an upstanding nipple 17. a flange 18 therebeneath for attachment toa bubble cap plate, and a lower body portion constituted by sides 19 and a wall portion 20 which extends downwardly from said flange, closes the bottom of the nipple 17 and then proceeds upwardly forming with the sides 19 a well 21. The wall 20 then bends downwardly again and together with extensionsof the sides 19 forms a spout 22 which terminates, somewhat above the level of the liquid maintained in the next inferior plate. A septum 23 extends between the sides 19 and from the flange 18 into the well 21 so as to establish a liquid seal therein. The septum 23 preferably conver es downwardly towards the vertical part o .the wall portion 20 so as to create a scavenging eifect in the `well 21 thus aiding in preventing accumulation of rust or scale therein.
As shown in the drawings, the overflows 16 are attached to the bubble plates 11 at a.
point near the margins thereof. It is preferred to place the overflows 16 at opposite 1927. Serial No. 191,250.
points on alternate bubble plates. The liquid sealed spouts 18 extend toward the central portion of each of the bubble plates 11. By means of this structure the overflow devices of the present invention pick up the liquid on their respective bubble plates at a point adjacent the margin thereof, and discharge it centrally of the bubble plate therebeneath and above the level of the liquid thereon. By means of this structure, asubstantially uniform composition is realized for the pools of liquid maintained on the bubble plates and consequently more accurate vapor fractionation is possible.
Although the present invention has been described in connection with the details of a specific embodiment thereof, it is not intended that such details shall be regarded as limitations upon the scope of the invention except in so far as included in the accompanying claims.
I claim:
1. A bubble tower provided with super imposed bubble cap plates, the successive bubble-cap plates being provided with overflow pipe plates, each comprising a nipple projecting above the bubble plate to which it is attached near the margin thereof, a spout below the plate and emptying centrally above the level of liquid on the plate beneath, whereby a flow of liquid is established from the central portion to the margin of said plates and means providing a liquid seal between said overflow and the spout.
2. A bubble tower provided with superimposed bubble cap plates, the successive bubble-cap plates being provided with overflow pipes for said bubble cap plates, each comprising a nipple projecting above the bubble plate to which it is attached near the margin thereof, a well portion, a spout extending therefrom and emptying centrally above the level of li uid on the plate beneath, whereby a flow of liquid is established from the central portion to the margin of said plates and means providing al liquid seal in said wel] portion.
In testimony whereof I have hereunto set my hand this 10th day of May, 1927.
PERRY J. SW'EENY.
US191250A 1927-05-13 1927-05-13 Bubble tower Expired - Lifetime US1770221A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US191250A US1770221A (en) 1927-05-13 1927-05-13 Bubble tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US191250A US1770221A (en) 1927-05-13 1927-05-13 Bubble tower

Publications (1)

Publication Number Publication Date
US1770221A true US1770221A (en) 1930-07-08

Family

ID=22704720

Family Applications (1)

Application Number Title Priority Date Filing Date
US191250A Expired - Lifetime US1770221A (en) 1927-05-13 1927-05-13 Bubble tower

Country Status (1)

Country Link
US (1) US1770221A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2678200A (en) * 1949-11-26 1954-05-11 Koch Eng Co Inc Apparatus for effecting intimate contact between liquids and gases
US2792070A (en) * 1952-02-25 1957-05-14 Phillips Petroleum Co Refinery blowdown and relief system
FR2400379A1 (en) * 1977-08-16 1979-03-16 Union Carbide Corp LIQUID-VAPOR CONTACT PLATE
US4159291A (en) * 1977-08-16 1979-06-26 Union Carbide Corporation Outlet means for vapor-liquid contacting tray
WO2005016493A1 (en) * 2003-08-13 2005-02-24 Shell Internationale Research Maatschappij B.V. Gas-liquid contacting tray
US20090155147A1 (en) * 2007-12-13 2009-06-18 Petroleo Brasileiro S.A- Petrobras Distributor nozzle for a two-phase charge in fixed-bed reactors

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2678200A (en) * 1949-11-26 1954-05-11 Koch Eng Co Inc Apparatus for effecting intimate contact between liquids and gases
US2792070A (en) * 1952-02-25 1957-05-14 Phillips Petroleum Co Refinery blowdown and relief system
FR2400379A1 (en) * 1977-08-16 1979-03-16 Union Carbide Corp LIQUID-VAPOR CONTACT PLATE
US4159291A (en) * 1977-08-16 1979-06-26 Union Carbide Corporation Outlet means for vapor-liquid contacting tray
WO2005016493A1 (en) * 2003-08-13 2005-02-24 Shell Internationale Research Maatschappij B.V. Gas-liquid contacting tray
US20050046051A1 (en) * 2003-08-13 2005-03-03 Sastry Asheesh Viswanatha Gas-liquid contacting tray
US7232115B2 (en) 2003-08-13 2007-06-19 Shell Oil Company Gas-liquid contacting tray
US20090155147A1 (en) * 2007-12-13 2009-06-18 Petroleo Brasileiro S.A- Petrobras Distributor nozzle for a two-phase charge in fixed-bed reactors
US7972570B2 (en) * 2007-12-13 2011-07-05 Petróleo Brasileiro S.A.—Petrobas Distributor nozzle for a two-phase charge in fixed-bed reactors

Similar Documents

Publication Publication Date Title
US1702612A (en) Oil-separating apparatus
US1741519A (en) Dephlegmator or fractionating column
US1520230A (en) Storage tank
US1770221A (en) Bubble tower
US1191741A (en) Gasolene-strainer.
US2010010A (en) Apparatus for contacting liquids with vapors or gases
US1694668A (en) Oil-tank baffle
US1770658A (en) Interfacial-contact apparatus
JPH0427118B2 (en)
GB500896A (en) Improvements in clarifiers for separating solids from liquids by sedimentation
US1797697A (en) Septic tank
US1655639A (en) Septic tank
US3067877A (en) Means and method for the automatic separating and purifying of liquids of different specific gravities
US1574157A (en) Means for separating liquids of different specific gravities
US1805635A (en) Reflux tower
US2495512A (en) Bubble tower
US1578625A (en) Multiple-deck pulp thickener
US1680060A (en) Manhole coveb fob oil tanks
US2223556A (en) Fractionating tower
US1417516A (en) Settling tank
US1677923A (en) Gasoline filling station and the like
US1011483A (en) Apparatus for heating boiler feed-water.
US1780438A (en) Fluid-mixing device
US2153411A (en) Drainage system for separating oil from waste water
US1867104A (en) Fuel feeding tank