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US2518574A - Reflux splitter - Google Patents

Reflux splitter Download PDF

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Publication number
US2518574A
US2518574A US669217A US66921746A US2518574A US 2518574 A US2518574 A US 2518574A US 669217 A US669217 A US 669217A US 66921746 A US66921746 A US 66921746A US 2518574 A US2518574 A US 2518574A
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Prior art keywords
nozzle
reflux
conduit
conduits
splitter
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US669217A
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George R Skopecek
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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
    • B01D3/42Regulation; Control
    • B01D3/4205Reflux ratio control splitter
    • 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
    • Y10T137/86389Programmer or timer
    • Y10T137/86405Repeating cycle
    • 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
    • Y10T137/877With flow control means for branched passages
    • Y10T137/87788With valve or movable deflector at junction
    • Y10T137/87804Valve or deflector is tubular passageway

Definitions

  • This invention relates to a reflux splitter and has for one of its objects the provision of a device that is adapted for splitting reflux coming from a bubble tower in a manner for returning a more accurate portion thereof t9 the tower than heretofore.
  • Fig. 1 is a plan view of the reflux splitter.
  • Fig. 2 is a part elevational, part sectional view of the splitter of Fig. 1.
  • Fig. 3 is a reduced, semi-diagrammatic view showing a packed bubble tower with the reflux splitter indicated.
  • a housing I which housing comprises a hollow body formed with a bottom having a pair of openings into which are secured the open ends of a pair of conduits 2, 3, which conduits are preferably cylindrical pipe extending divergently downwardly. Conduit 2 may then extend horizontally back into the upper end of the bubble tower 4 (Fig. 3) while conduit 3 may extend to any desired point away from said tower.
  • the housing I has a top Wall 5 (Figs. 1, 2) that may be removably secured on the body I in fluid tight relation to the latter, and a pipe 6 extends downwardly through said top wall into said body and terminates in the latter in a downwardly directed open end spaced above the upwardly directed open ends of conduits 2, 3.
  • conduits 2, 3 are closely adjacent each other and a vertically extending cut-off baflie plate I0 extends upwardly between said conduits to a point intermediate the open ends of said conduits and the lower open end of pipe 6.
  • Said baflie plate is integral with body I and is preferably rounded on its upper edge 1 Claim. (01. 2 61-110) so that any liquid striking the same will promptly be drained to one side or the other or both, and
  • conduits 2, 3 provide inlets for liquid and the sides of the housing I as well as the sides of battle plate I0 extending substantially vertically to the edges of said inlets so that liquid deposited at opposite sides of the baflle Ill will flow directly into the inlets with the least resistance.
  • a vertically extending, tubular open-ended nozzle I I having a discharge outlet I2 in its lower end, and which lower end is preferably tapered substantially as shown.
  • the outlet I2 is preferably elliptical in contour in direction longitudinally of the bafiie as indicated in Fig. 1.
  • the diameter of the upper end of the nozzle is larger than that of the pipe 6, and horizontally axially aligned pivots I3 (only one shown in Fig. 2) connect the upper end of the nozzle with the pipe 5, the lower end of pipe 6 being within the upper end of nozzle II.
  • nozzle I I Extending from one side of nozzle I I is an arm I5 that is secured to said nozzle at one of its ends while the opposite end of said arm is pivotally secured to one end of a relatively short link I6.
  • the opposite end of link It is pivotally secured to the lower end of a vertical extension I! that extends downwardly from a vertically disposed solenoid core I3, said core being in a solenoid I9.
  • Solenoid I9 is supported and enclosed in a case 26 that may form part of the housing or housing cover 5.
  • the casing is liquid tight and is preferably secured on the top 5 of the housing with the extension I3 of the solenoid core freely reciprocable vertically upon vertical movement of the core I8 up or down according to whether the coil I9 is energized or not.
  • the coil [9 may be energized in any suitable manner but in any event, the control should be such that any desired ratio of the amount of reflux deposited with conduit 2 to the amount deposited in conduit 3 should be obtainable.
  • One method would be to provide a motor driven switch 25 in an electrical circuit leading to coil [9.
  • the segments 25 of said switch may be driven by a synchronous electric motor 2 1, and as long as contact between segments 25 and contact 2! is established, the core 58 will be elevated and reflux will be deposited in conduit 3, but as soon as the contact is broken, the nozzle will instantly swing to the opposite side of the baflle plate It for discharge into conduit ihe time during which said nozzle will discharge into conduit 2 is dependent upon the time during which the contact is broken.
  • a typical arrangement of the reflux splitter of this invention relative to a packs as a bubble tower is diagrammatically i licated in Fig: 3 in which vapor is condensed in the upper portion of the tower by a condenser 5 i, and the condensate or reflux is received in a receptacle from which it goes to the splitter gen erally designated
  • the housing I inciuding the cover and all conduit and pipe attachments are fluid tight, and the for the solenoid is also in tight relation with the cover, it will be seen that no packing is required, and all moving elements may be freely movable with the minitower to such 1 mum friction.
  • a reflux splitter comprising a hollow body, a supply pipe for reflux extending through one of the walls of said body and into the upper portion of the latter, a pair of conduits opening into said body in the lower portion thereof, an open ended generally vertically extending nozzle positioned within said body with its upper open end positioned for receiving reflux from said supply pipe during swinging of said nozzle about a horizontal axis, pivot means supporting said nozzle within said body fo; said swinging, the sides of the lower open end of said nozzle being flattened to provide a horizontally elongated discharge opening at said lower end extending parallel with the axis about which said nozzle is adapted to swing on said pivot means, the open ends of said pair of conduits being respectivel positioned below said discharge opening at opposite ends of its stroke d1.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

G. R. SKOPECEK REFLUX SPLITTER Aug. 15, 1950 Fil ed May 13, 1946 IN V EN TOR. GEORGE R. SKOPECEK 1 ATTORNYS Patented Aug. 15, 1950 UNITED STATES PATENT OFFICE REFLUX SPLITTER George R. Skopecek, Berkeley, Calif.
Application May 13, 1946, Serial No. 669,217
This invention relates to a reflux splitter and has for one of its objects the provision of a device that is adapted for splitting reflux coming from a bubble tower in a manner for returning a more accurate portion thereof t9 the tower than heretofore.
In the commercial process of refining petroleum and other refining processes, where stills, bubble towers, fractionating towers, or the like, are employed and a certain amount of the reflux is returned to the tower, it is not particularly important that the amount of reflux so returned be as exact as in pilot installations. Hence in commercial installations, conventional valve of the globe, plug or gate type, and others may be employed even though inaccuracy is inescapable by reason of their structure and method of operation.
In a pilot installation the utmost accuracy is essential. If a 1:20 or a 1:1 or any intermediate ratio between the reflux returned and that which is carried away is desired, there can be no inaccuracy. The ratio must be accurate.
By the present invention this accuracy is made possible.
In the drawings, Fig. 1 is a plan view of the reflux splitter.
Fig. 2 is a part elevational, part sectional view of the splitter of Fig. 1.
Fig. 3 is a reduced, semi-diagrammatic view showing a packed bubble tower with the reflux splitter indicated.
In detail, a housing I is provided, which housing comprises a hollow body formed with a bottom having a pair of openings into which are secured the open ends of a pair of conduits 2, 3, which conduits are preferably cylindrical pipe extending divergently downwardly. Conduit 2 may then extend horizontally back into the upper end of the bubble tower 4 (Fig. 3) while conduit 3 may extend to any desired point away from said tower.
The housing I has a top Wall 5 (Figs. 1, 2) that may be removably secured on the body I in fluid tight relation to the latter, and a pipe 6 extends downwardly through said top wall into said body and terminates in the latter in a downwardly directed open end spaced above the upwardly directed open ends of conduits 2, 3.
Preferably, the upper ends of conduits 2, 3 are closely adjacent each other and a vertically extending cut-off baflie plate I0 extends upwardly between said conduits to a point intermediate the open ends of said conduits and the lower open end of pipe 6. Said baflie plate is integral with body I and is preferably rounded on its upper edge 1 Claim. (01. 2 61-110) so that any liquid striking the same will promptly be drained to one side or the other or both, and
, the plane bisecting the downwardly directed open end of pipe 3 and also bisecting the space between the upper ends of conduits 2, 3.
The open ends of said conduits 2, 3 provide inlets for liquid and the sides of the housing I as well as the sides of battle plate I0 extending substantially vertically to the edges of said inlets so that liquid deposited at opposite sides of the baflle Ill will flow directly into the inlets with the least resistance.
Pivotally secured to the end of pipe 6 that projects into the housing is a vertically extending, tubular open-ended nozzle I I having a discharge outlet I2 in its lower end, and which lower end is preferably tapered substantially as shown. The outlet I2 is preferably elliptical in contour in direction longitudinally of the bafiie as indicated in Fig. 1.
The diameter of the upper end of the nozzle, is larger than that of the pipe 6, and horizontally axially aligned pivots I3 (only one shown in Fig. 2) connect the upper end of the nozzle with the pipe 5, the lower end of pipe 6 being within the upper end of nozzle II.
If the nozzle were to hang vertically from the pivots, the discharge end of the nozzle would be directly over the upper edge of bafile plate Ill close to said edge. Upon swinging the nozzle, the lower end will move to one side or the other of the baflie and directly over either inlet 2 or inlet 3 as the case may be.
Extending from one side of nozzle I I is an arm I5 that is secured to said nozzle at one of its ends while the opposite end of said arm is pivotally secured to one end of a relatively short link I6. The opposite end of link It is pivotally secured to the lower end of a vertical extension I! that extends downwardly from a vertically disposed solenoid core I3, said core being in a solenoid I9. Solenoid I9 is supported and enclosed in a case 26 that may form part of the housing or housing cover 5. The casing is liquid tight and is preferably secured on the top 5 of the housing with the extension I3 of the solenoid core freely reciprocable vertically upon vertical movement of the core I8 up or down according to whether the coil I9 is energized or not.
When the core I8 is at the bottom of its stroke, to which position it moves by gravity when the current tothe coil I8 is broken, the nozzle II will be swung to a position in which its discharge end is over conduit 2. When the coil I9 is energized, the core I8 will be lifted and held elevated coil It with the nozzle ii swung to a position in which its discharge end is over the conduit 3. This swinging movement is rapid and the discharge of reflux from the nozzle is not discontinued at any time nor is there any noticeable change in the quantity steadily delivered, which would not be the case were plug, gate, globe or other conventional valves used.
The coil [9 may be energized in any suitable manner but in any event, the control should be such that any desired ratio of the amount of reflux deposited with conduit 2 to the amount deposited in conduit 3 should be obtainable. One method would be to provide a motor driven switch 25 in an electrical circuit leading to coil [9. The segments 25 of said switch may be driven by a synchronous electric motor 2 1, and as long as contact between segments 25 and contact 2! is established, the core 58 will be elevated and reflux will be deposited in conduit 3, but as soon as the contact is broken, the nozzle will instantly swing to the opposite side of the baflle plate It for discharge into conduit ihe time during which said nozzle will discharge into conduit 2 is dependent upon the time during which the contact is broken. As segments may be rotated relatively to provide a short or a long gap 23, it will be seen that any desired ratio can be established between the amount of reflux discharged into conduit 22 and that die hargcd into conduit 3. There are many d erent types of motor driven switohes that may be e nloyed, so no claim is made to this feature in itsell.
A typical arrangement of the reflux splitter of this invention relative to a packs as a bubble tower is diagrammatically i licated in Fig: 3 in which vapor is condensed in the upper portion of the tower by a condenser 5 i, and the condensate or reflux is received in a receptacle from which it goes to the splitter gen erally designated Inasmuch as the housing I inciuding the cover and all conduit and pipe attachments are fluid tight, and the for the solenoid is also in tight relation with the cover, it will be seen that no packing is required, and all moving elements may be freely movable with the minitower to such 1 mum friction. These features together with the fact that the cut-ofi from one conduit to the other is practically instantaneous and without noticeable change in the velocity and volume of liquid being discharged through the nozzle, results in a highly accurate proportioning of the flow of reflux from one conduit to the other. As already stated, this latter result is of vital inportance in pilot plant operations.
I claim:
A reflux splitter comprising a hollow body, a supply pipe for reflux extending through one of the walls of said body and into the upper portion of the latter, a pair of conduits opening into said body in the lower portion thereof, an open ended generally vertically extending nozzle positioned within said body with its upper open end positioned for receiving reflux from said supply pipe during swinging of said nozzle about a horizontal axis, pivot means supporting said nozzle within said body fo; said swinging, the sides of the lower open end of said nozzle being flattened to provide a horizontally elongated discharge opening at said lower end extending parallel with the axis about which said nozzle is adapted to swing on said pivot means, the open ends of said pair of conduits being respectivel positioned below said discharge opening at opposite ends of its stroke d1. ing swinging of said nozzle, and a vertically attending cutoff bafile positioned between the upper open ends of said pair of conduits, the up edge of said bafiie being horizontally elongated a d paraliel with said discharge opening and p ioned to provide a relatively slight clearance between it and the discharge end of said nozzle during swinging or" the latter across said bafie.
GEORGE R. SKO'PECEK.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 2,185,970 Zieoolz Jan. 2, 1940 2,251,185 Carter et al July 29, 1941
US669217A 1946-05-13 1946-05-13 Reflux splitter Expired - Lifetime US2518574A (en)

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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2699356A (en) * 1950-10-14 1955-01-11 Askania Regulator Co Jet pipe signal device
US2903401A (en) * 1954-07-16 1959-09-08 Distillation Engineering Compa Automatic reflux head for fractionating columns
US3210940A (en) * 1963-03-11 1965-10-12 Fmc Corp Variable speed coupling
US3220936A (en) * 1960-11-02 1965-11-30 Loing Verreries Reflux condenser with adjustable reflux head
US3366552A (en) * 1964-01-17 1968-01-30 Q V F Ltd Refluxing apparatus with adjustable head
US3428083A (en) * 1965-12-20 1969-02-18 George L Fish Proportioning device
US3511100A (en) * 1968-11-18 1970-05-12 Kennecott Copper Corp Material-screening sampler
US4108206A (en) * 1976-08-30 1978-08-22 Mountain Donald C Hermetically sealed four-way valve
US4150574A (en) * 1977-12-28 1979-04-24 Harry Wolf Fluid sampling system
US4852892A (en) * 1984-08-07 1989-08-01 Reid Richard M Convenient dual fuel tank system
US5205909A (en) * 1991-12-04 1993-04-27 Union Carbide Chemicals & Plastics Technology Corporation Apparatus for measuring reflux flow in a distillation column
US5803118A (en) * 1997-05-20 1998-09-08 Van Bruggen; Eugene E. Metered feed valve
CN101347683B (en) * 2008-08-27 2010-06-09 江阴康爱特化工有限公司 Novel mechanism for regulating reflux in tower
US20140262796A1 (en) * 2013-03-13 2014-09-18 Taiwan Semiconductor Manufacturing Company, Ltd. Metal Plating Apparatus and Method Using Solenoid Coil

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2185970A (en) * 1936-12-21 1940-01-02 Askania Werke Ag Apparatus for controlling the flow of fluids
US2251185A (en) * 1939-04-17 1941-07-29 Du Pont Distillation apparatus

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2185970A (en) * 1936-12-21 1940-01-02 Askania Werke Ag Apparatus for controlling the flow of fluids
US2251185A (en) * 1939-04-17 1941-07-29 Du Pont Distillation apparatus

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2699356A (en) * 1950-10-14 1955-01-11 Askania Regulator Co Jet pipe signal device
US2903401A (en) * 1954-07-16 1959-09-08 Distillation Engineering Compa Automatic reflux head for fractionating columns
US3220936A (en) * 1960-11-02 1965-11-30 Loing Verreries Reflux condenser with adjustable reflux head
US3210940A (en) * 1963-03-11 1965-10-12 Fmc Corp Variable speed coupling
US3366552A (en) * 1964-01-17 1968-01-30 Q V F Ltd Refluxing apparatus with adjustable head
US3428083A (en) * 1965-12-20 1969-02-18 George L Fish Proportioning device
US3511100A (en) * 1968-11-18 1970-05-12 Kennecott Copper Corp Material-screening sampler
US4108206A (en) * 1976-08-30 1978-08-22 Mountain Donald C Hermetically sealed four-way valve
US4150574A (en) * 1977-12-28 1979-04-24 Harry Wolf Fluid sampling system
US4852892A (en) * 1984-08-07 1989-08-01 Reid Richard M Convenient dual fuel tank system
US5205909A (en) * 1991-12-04 1993-04-27 Union Carbide Chemicals & Plastics Technology Corporation Apparatus for measuring reflux flow in a distillation column
US5314587A (en) * 1991-12-04 1994-05-24 Union Carbide Chemicals & Plastics Technology Corporation Method for measuring reflux flow in a distillation process
US5803118A (en) * 1997-05-20 1998-09-08 Van Bruggen; Eugene E. Metered feed valve
CN101347683B (en) * 2008-08-27 2010-06-09 江阴康爱特化工有限公司 Novel mechanism for regulating reflux in tower
US20140262796A1 (en) * 2013-03-13 2014-09-18 Taiwan Semiconductor Manufacturing Company, Ltd. Metal Plating Apparatus and Method Using Solenoid Coil
US9809897B2 (en) * 2013-03-13 2017-11-07 Taiwan Semiconductor Manufacturing Company, Ltd. Metal plating apparatus and method using solenoid coil

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