US1905733A - Flow divider - Google Patents
Flow divider Download PDFInfo
- Publication number
- US1905733A US1905733A US599648A US59964832A US1905733A US 1905733 A US1905733 A US 1905733A US 599648 A US599648 A US 599648A US 59964832 A US59964832 A US 59964832A US 1905733 A US1905733 A US 1905733A
- Authority
- US
- United States
- Prior art keywords
- fluid
- vane
- casing
- streams
- stream
- 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
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F15—FLUID-PRESSURE ACTUATORS; HYDRAULICS OR PNEUMATICS IN GENERAL
- F15D—FLUID DYNAMICS, i.e. METHODS OR MEANS FOR INFLUENCING THE FLOW OF GASES OR LIQUIDS
- F15D1/00—Influencing flow of fluids
- F15D1/14—Diverting flow into alternative channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L41/00—Branching pipes; Joining pipes to walls
- F16L41/02—Branch units, e.g. made in one piece, welded, riveted
- F16L41/023—Y- pieces
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/2496—Self-proportioning or correlating systems
- Y10T137/2514—Self-proportioning flow systems
- Y10T137/2521—Flow comparison or differential response
- Y10T137/2524—Flow dividers [e.g., reversely acting controls]
Definitions
- This invention relates to a device for dividing a flowing stream of'fluid and more particularly to a mechanism which is adapted to divide a stream of fluid into two streams of equal volume and to maintain the volume of these streams constant.
- F ig. 2 is a vertical sectional view
- Fig. 3 is an enlarged fragmentary view of a spring andv stop assembly used for limiting the movement of the movable member of the mechanism; and l Fig. 4 is a vertical section on the line 4-4 of Fig. 2.
- the numeral 10 designates a casingsubstanti'ally triangular-shaped in cross section and having a fluid conductor 11 entering it at the apex Which is the inlet end of the structure.
- Two eonductors 12 and 13 enter the casing at the opposite base vertices, these conduetors serving as outlets for the fluid entering at 11.
- a wedge-Shaped, vane-like member 14 is supported on a pivot 9 within the casing 10 in such a manner that its center line normally coincides with the center line of the casing.
- the base 15 of the vane-like 'member is adjacent to the base 16 of the triangular-Shaped easing, while the leading edge 17 points directly toward the apex of the casing.
- the fluid passages in the casing conform substantially to a Y shape, the leg 18 of Which coincides with the inlet portion of the casing while the arms 19 and 20 constitute the diverging fluid passages leading to'the Outlet conductors.
- the after portion 21 of the vane-like member is symmetrically hollow so that the center of mass 22 of the structure is on the center line and, in the forward portion of the vane.
- the base of the vane is curved and eonforms to the are of a circle having a radius equal to the distance between the center of mass or pivotal point and either of the vertices of the base angles of the vane.
- the surface of thev casing against which the vane abuts is likewise curved and acts as a'bearing surface.
- the side walls of the vane are extended beyond the curved lbase of the vane-like member resulting in projections 23 and 24.
- the base ofv the casing is recessed to .receive these projections and to allow aflimited rotation of the pivoted member.
- I Resilient means, 25 and 26, eooperate lwith projections 24 and 25 to normally' maintain the 'i stud bolts 28 are provided to maintain this plate in close contact with the casing.
- Both the cover plate and the bottom plate of the casing are provided with recessed bearings 29 and 30 to cooperate with the pivot 9 of the vane-like member and are so designed as to allow free rotation of this member. Since the pivot 9 coincides with the center of mass 22, the vane member will normally be balanced and will swing freely except as limited by the projections 23 and 24 and the resilient means 25 and 26.
- the operation of the flow divider is most easily understood by a consideration of its .action under conditions of both straight line flow and turbulent flow.
- the cross section of such a fluid contains no points having velocities higher or lower than the average Velocity.
- the vane being ositioned in its normally central position, ivides the oncoming fluid into two equal streams which follow the channels 19 and 20.
- the kinetic energies of each of the divided streams are equal and the clockwise moment acting on one side of the after portion of the vane equals the counter-clockwise moment acting on the other side of the after portion of the vane. Therefore, there cannot be a resultant torque and the vane'remains in its normally central position.
- the cross section of the fluid contains eddy currents 'or localized streams having velocities higher or lower than the average Velocity.
- the kinetic energies of the divided streams are unequal.
- the moments acting on each side of the after portion of the vane are unequal and there is a resultant torque causing rotation of the vane.
- Fig. 1 it will be seen that if the vane is caused to swing out of its normally central position in a clockwise direction, the channel 19 is constricted b the knife edge 17, and a larger volume o fluid passes through channel 20.
- the Velocity of the fluid adjacent to the after portion of the vane on the 20 side is increased which then produces a counter-clockwise moment greater than that tending to cause clockwise rotation, and the vane returns to its normally central position.
- the projections 23 and 24 have been provided.
- resilient means 25 and 26 Cooperating with these projections are resilient means 25 and 26, for decreasing the sensitivity of the mechanism and for damping or preventing the rapid vibrations or flutterings of the vane that might be caused by slight eddy currents normally present in any flowing body of fluid.
- the fluid divider may be efiiciently applied in all cases where it is desirable to divide a fiowing body of fluid into two streams of equal volumes.
- it may be applied to container filling mechanisms, to the charging of oil to duplicate cracking units with one charge pump, to the supplying oflriquid or gaseous fuel to duplicate burners, and the like.
- By changing the materials used in constructing the mechanism it may be adapted for the handling of all types of fluids, both gaseous and liquid.
- several flow dividers similar to the one I have described may be used in series. For example, by connecting the respective inlet conductors of two flow dividers to the fluid eductors 12 and 13 of the flow divider shown in Fig. 1, it is possible to divide a stream of fluid into four equal streams.
- a device for dividing a stream of fluid into two equal streams comprising a casing interposed in the stream of fluid, a wedgeshaped vane pivoted centrally in the casing,
- a device for dividing a stream of fluid into two equal streams comprising a casing interposed in the stream of fluid, a wedge- Shaped vane pivoted centrally in the casing and adapted to equally divide the flow of' fluid through the casing and resilient means cooperating with the vane and adapted to limit the extent of its rotation and to return the same to its normal position.
- a device for dividing a stream of fluid into two equal streams comprising a casing provided with a fluid inlet and a plurality of fluid outlets, a wedge-Shaped vane centrally pivoted in the casing and adapted to equally divide the flow of fluid through the casing, stops and resilient means cooperating with the vane and adapted to coact with it and to limit the extent of its rotation.
- a device for dividing the flow of a fluid into two equal streams which comprises. a casing triangular Shaped in cross section having a fluid conductor entering it at its apex and two fluid eduetors parallel to the fluid conductor leaving the casing at opposite ends of its base, a wedge-Shaped vane pvoted Within the casing, and centrally positoned theren so that the fluid passages formed thereby conform substantially to a Y shape, and projections and resilient means operatively attached to the vane to limit the extent of its rotation.
Description
Patented pr. 25, 1933 UNITED sTATEs PATENT OFFICE WILLIAI F. MOORE, OF FL'USHING, NEW YORK, ASSIGNOR TO THE TEXAS 00mm OF NEW YORK, N". Y., A CORPORATION OF DEIAW'ARE- FLOW DIVIDER pplication filed March 18, 1932. Serial No. 599,648.
This invention relates to a device for dividing a flowing stream of'fluid and more particularly to a mechanism which is adapted to divide a stream of fluid into two streams of equal volume and to maintain the volume of these streams constant.
In the case of those fittings and arrangements Which have been used up to the present time for attempting to divide a stream into two' streams of equal volume and which usually eomprise a Y pipe fitting and valves for regulating the volumes of the streams, great diiiieulty has been experienced in attaining the desired result. Slight differences in the Characteristics of the internal- Structures of the Y fitting and the valves always result in Wide Variations of the vol-- umes of the two resultant streams. i By means of my invention, I am enabled to accurately divide a given stream of fluid into two streams vof equal volume and to maintain these volumes constant at all times Without recourse to the use of any valves or similar control fittings.
In accordance with my invention, I interpose in the stream of fluid a casing within which is ivoted a wedge-Shaped vane Which is limited in the extent of its rotation and is adapted to divide the fluid into two equal streams; For a better understanding of my invention, reference maybe had to the following description and accompanying drawing which illustrate a preferred embodiment of the invention in Which Fig. 1 is a horizontal seetional view;
F ig. 2 is a vertical sectional view;
Fig. 3 is an enlarged fragmentary view of a spring andv stop assembly used for limiting the movement of the movable member of the mechanism; and l Fig. 4 is a vertical section on the line 4-4 of Fig. 2.
In the drawing the numeral 10 designates a casingsubstanti'ally triangular-shaped in cross section and having a fluid conductor 11 entering it at the apex Which is the inlet end of the structure. Two eonductors 12 and 13 enter the casing at the opposite base vertices, these conduetors serving as outlets for the fluid entering at 11.
A wedge-Shaped, vane-like member 14 is supported on a pivot 9 within the casing 10 in such a manner that its center line normally coincides with the center line of the casing. The base 15 of the vane-like 'member is adjacent to the base 16 of the triangular-Shaped easing, while the leading edge 17 points directly toward the apex of the casing. As a result of this alloeation of the members, the fluid passages in the casing conform substantially to a Y shape, the leg 18 of Which coincides with the inlet portion of the casing while the arms 19 and 20 constitute the diverging fluid passages leading to'the Outlet conductors.
The after portion 21 of the vane-like member is symmetrically hollow so that the center of mass 22 of the structure is on the center line and, in the forward portion of the vane. As a direct resultl of this, the density of the head or leading portion is considerably greater than the density of the after, or tail portion. The base of the vane is curved and eonforms to the are of a circle having a radius equal to the distance between the center of mass or pivotal point and either of the vertices of the base angles of the vane. The surface of thev casing against which the vane abuts "is likewise curved and acts as a'bearing surface. I
The side walls of the vane are extended beyond the curved lbase of the vane-like member resulting in projections 23 and 24. The base ofv the casing is recessed to .receive these projections and to allow aflimited rotation of the pivoted member. I Resilient means, 25 and 26, eooperate lwith projections 24 and 25 to normally' maintain the 'i stud bolts 28 are provided to maintain this plate in close contact with the casing. Both the cover plate and the bottom plate of the casing are provided with recessed bearings 29 and 30 to cooperate with the pivot 9 of the vane-like member and are so designed as to allow free rotation of this member. Since the pivot 9 coincides with the center of mass 22, the vane member will normally be balanced and will swing freely except as limited by the projections 23 and 24 and the resilient means 25 and 26.
The operation of the flow divider is most easily understood by a consideration of its .action under conditions of both straight line flow and turbulent flow. Considering a fluid entering the mechanism through the conductor 11 travelling with a Velocity less than its critical Velocity, the cross section of such a fluid contains no points having velocities higher or lower than the average Velocity. The vane, being ositioned in its normally central position, ivides the oncoming fluid into two equal streams which follow the channels 19 and 20. The kinetic energies of each of the divided streams are equal and the clockwise moment acting on one side of the after portion of the vane equals the counter-clockwise moment acting on the other side of the after portion of the vane. Therefore, there cannot be a resultant torque and the vane'remains in its normally central position.
If there is a condition of turbulent flow in the incomzing fluid, the cross section of the fluid contains eddy currents 'or localized streams having velocities higher or lower than the average Velocity. Considering the vane positioned in a normally central position, the kinetic energies of the divided streams are unequal. The moments acting on each side of the after portion of the vane are unequal and there is a resultant torque causing rotation of the vane. Referring to Fig. 1, it will be seen that if the vane is caused to swing out of its normally central position in a clockwise direction, the channel 19 is constricted b the knife edge 17, and a larger volume o fluid passes through channel 20. As a result, the Velocity of the fluid adjacent to the after portion of the vane on the 20 side is increased which then produces a counter-clockwise moment greater than that tending to cause clockwise rotation, and the vane returns to its normally central position.
In order to limit the extent of rotation of the vane, the projections 23 and 24 have been provided. Cooperating with these projections are resilient means 25 and 26, for decreasing the sensitivity of the mechanism and for damping or preventing the rapid vibrations or flutterings of the vane that might be caused by slight eddy currents normally present in any flowing body of fluid.
The fluid divider, as described, may be efiiciently applied in all cases where it is desirable to divide a fiowing body of fluid into two streams of equal volumes. For example, it may be applied to container filling mechanisms, to the charging of oil to duplicate cracking units with one charge pump, to the supplying oflriquid or gaseous fuel to duplicate burners, and the like. By changing the materials used in constructing the mechanism, it may be adapted for the handling of all types of fluids, both gaseous and liquid. It is apparent that several flow dividers similar to the one I have described may be used in series. For example, by connecting the respective inlet conductors of two flow dividers to the fluid eductors 12 and 13 of the flow divider shown in Fig. 1, it is possible to divide a stream of fluid into four equal streams.
Obviously many modifications and variations of the invention, as hereinbefore set forth, may be made without departing from the spirit and scope thereof, and therefore only such limitations should be imposed as are indicated in the appended claims.
I claim:
1. A device for dividing a stream of fluid into two equal streams comprising a casing interposed in the stream of fluid, a wedgeshaped vane pivoted centrally in the casing,
limited in the extent of its rotation and adapted to divide equally thekflow of fluid through the casing.
2. A device for dividing a stream of fluid into two equal streams comprising a casing interposed in the stream of fluid, a wedge- Shaped vane pivoted centrally in the casing and adapted to equally divide the flow of' fluid through the casing and resilient means cooperating with the vane and adapted to limit the extent of its rotation and to return the same to its normal position.
3. A device for dividing a stream of fluid into two equal streams comprising a casing provided with a fluid inlet and a plurality of fluid outlets, a wedge-Shaped vane centrally pivoted in the casing and adapted to equally divide the flow of fluid through the casing, stops and resilient means cooperating with the vane and adapted to coact with it and to limit the extent of its rotation.
4. A device for dividing the flow of a fluid into two equal streams which comprises. a casing triangular Shaped in cross section having a fluid conductor entering it at its apex and two fluid eduetors parallel to the fluid conductor leaving the casing at opposite ends of its base, a wedge-Shaped vane pvoted Within the casing, and centrally positoned theren so that the fluid passages formed thereby conform substantially to a Y shape, and projections and resilient means operatively attached to the vane to limit the extent of its rotation.
In witness Whereof, I have hereunto set my hand this 7th day of March, 1932.
WILLIAM F. MOORE.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US599648A US1905733A (en) | 1932-03-18 | 1932-03-18 | Flow divider |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US599648A US1905733A (en) | 1932-03-18 | 1932-03-18 | Flow divider |
Publications (1)
Publication Number | Publication Date |
---|---|
US1905733A true US1905733A (en) | 1933-04-25 |
Family
ID=24400486
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US599648A Expired - Lifetime US1905733A (en) | 1932-03-18 | 1932-03-18 | Flow divider |
Country Status (1)
Country | Link |
---|---|
US (1) | US1905733A (en) |
Cited By (35)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2440059A (en) * | 1943-09-16 | 1948-04-20 | United Aircraft Prod | Fluid flow regulator |
US3048372A (en) * | 1958-03-25 | 1962-08-07 | Jr Robert P Newton | Waste water heat reclaimer |
US3139104A (en) * | 1961-11-20 | 1964-06-30 | Herman F Love | Flow controlling device |
US3282297A (en) * | 1964-07-30 | 1966-11-01 | Sperry Rand Corp | Fluid channel divider |
US3319656A (en) * | 1963-11-08 | 1967-05-16 | Sperry Rand Corp | Bistable device |
US3342198A (en) * | 1965-01-15 | 1967-09-19 | Sperry Rand Corp | Fluid oscillator |
US3541801A (en) * | 1967-09-07 | 1970-11-24 | Bertin & Cie | Thermal separator |
US3690341A (en) * | 1971-04-21 | 1972-09-12 | Continental Oil Co | Equal flow distributor |
US4241760A (en) * | 1979-02-01 | 1980-12-30 | The United States Of America As Represented By The Secretary Of The Army | Fluidic valve |
FR2475649A1 (en) * | 1980-02-12 | 1981-08-14 | Creusot Loire | DEVICE FOR DISTRIBUTING A MAIN CURRENT INTO SEVERAL SECONDARY CURRENTS |
DE3239897A1 (en) * | 1982-10-28 | 1984-05-03 | Trützschler GmbH & Co KG, 4050 Mönchengladbach | METHOD AND DEVICE FOR CONVEYING FIBER-SHAPED SUBSTANCES, IN PARTICULAR TEXTILE FIBER FLAKES CONTAINED IN AIR-FLOATING, IN SPINNING PREPARATION MACHINES |
US4622992A (en) * | 1983-01-17 | 1986-11-18 | Sutherland Ivan E | Reaction control valve |
US4875846A (en) * | 1985-11-16 | 1989-10-24 | Heinz Reinbold | Spinning apparatus |
US5045874A (en) * | 1990-11-05 | 1991-09-03 | Eastman Kodak Company | Water distributor system for crossover assemblies in a film processor |
NO326080B1 (en) * | 2005-11-11 | 2008-09-15 | Norsk Hydro Produksjon As | Arrangement for sharing of current stream and separation system |
EP2525126A1 (en) * | 2011-05-20 | 2012-11-21 | NORMA Germany GmbH | Connector for a heatable fluid conduit and heatable fluid conduit |
US20130100759A1 (en) * | 2011-10-24 | 2013-04-25 | United States Gypsum Company | Multiple-leg discharge boot for slurry distribution |
US20150083751A1 (en) * | 2013-09-20 | 2015-03-26 | Nordson Corporation | Fluid dispenser and method for simultaneously dispensing fluids from multiple cartridges |
US8991426B2 (en) * | 2013-06-13 | 2015-03-31 | Haven Technology Solutions Llc | Apparatus and method for fluid control |
US9296124B2 (en) | 2010-12-30 | 2016-03-29 | United States Gypsum Company | Slurry distributor with a wiping mechanism, system, and method for using same |
US9506595B2 (en) | 2011-05-20 | 2016-11-29 | Norma Germany Gmbh | Fluid line |
US9579822B2 (en) | 2010-12-30 | 2017-02-28 | United States Gypsum Company | Slurry distribution system and method |
US9616591B2 (en) | 2010-12-30 | 2017-04-11 | United States Gypsum Company | Slurry distributor, system and method for using same |
US9671053B2 (en) | 2011-05-20 | 2017-06-06 | Norma Germany Gmbh | Fluid line |
US9999989B2 (en) | 2010-12-30 | 2018-06-19 | United States Gypsum Company | Slurry distributor with a profiling mechanism, system, and method for using same |
US10052793B2 (en) | 2011-10-24 | 2018-08-21 | United States Gypsum Company | Slurry distributor, system, and method for using same |
US10059033B2 (en) | 2014-02-18 | 2018-08-28 | United States Gypsum Company | Cementitious slurry mixing and dispensing system with pulser assembly and method for using same |
US10076853B2 (en) | 2010-12-30 | 2018-09-18 | United States Gypsum Company | Slurry distributor, system, and method for using same |
US10293522B2 (en) | 2011-10-24 | 2019-05-21 | United States Gypsum Company | Multi-piece mold and method of making slurry distributor |
EP3419434A4 (en) * | 2016-02-26 | 2019-10-23 | Erik Garfinkel | Concrete delivery subsystem for automated concrete fabrication system |
US10537054B2 (en) | 2017-07-18 | 2020-01-21 | Cnh Industrial Canada, Ltd. | Dynamic baffle for air flow balancing between adjacent product lines |
US20210222501A1 (en) * | 2020-01-20 | 2021-07-22 | Mark Eilam | Vacuum Manifold Assembly |
CN113167427A (en) * | 2018-11-27 | 2021-07-23 | 美国圣戈班性能塑料公司 | Fluid manifold |
US11350561B2 (en) * | 2019-11-22 | 2022-06-07 | Cnh Industrial Canada, Ltd. | Balanced fan plenum for distributing particulate material |
US11565439B2 (en) | 2017-09-19 | 2023-01-31 | Yoshino Gypsum Co., Ltd. | Slurry delivery conduit of mixer and slurry delivery method |
-
1932
- 1932-03-18 US US599648A patent/US1905733A/en not_active Expired - Lifetime
Cited By (40)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2440059A (en) * | 1943-09-16 | 1948-04-20 | United Aircraft Prod | Fluid flow regulator |
US3048372A (en) * | 1958-03-25 | 1962-08-07 | Jr Robert P Newton | Waste water heat reclaimer |
US3139104A (en) * | 1961-11-20 | 1964-06-30 | Herman F Love | Flow controlling device |
US3319656A (en) * | 1963-11-08 | 1967-05-16 | Sperry Rand Corp | Bistable device |
US3282297A (en) * | 1964-07-30 | 1966-11-01 | Sperry Rand Corp | Fluid channel divider |
US3342198A (en) * | 1965-01-15 | 1967-09-19 | Sperry Rand Corp | Fluid oscillator |
US3541801A (en) * | 1967-09-07 | 1970-11-24 | Bertin & Cie | Thermal separator |
US3690341A (en) * | 1971-04-21 | 1972-09-12 | Continental Oil Co | Equal flow distributor |
US4241760A (en) * | 1979-02-01 | 1980-12-30 | The United States Of America As Represented By The Secretary Of The Army | Fluidic valve |
FR2475649A1 (en) * | 1980-02-12 | 1981-08-14 | Creusot Loire | DEVICE FOR DISTRIBUTING A MAIN CURRENT INTO SEVERAL SECONDARY CURRENTS |
DE3239897A1 (en) * | 1982-10-28 | 1984-05-03 | Trützschler GmbH & Co KG, 4050 Mönchengladbach | METHOD AND DEVICE FOR CONVEYING FIBER-SHAPED SUBSTANCES, IN PARTICULAR TEXTILE FIBER FLAKES CONTAINED IN AIR-FLOATING, IN SPINNING PREPARATION MACHINES |
US4622992A (en) * | 1983-01-17 | 1986-11-18 | Sutherland Ivan E | Reaction control valve |
US4875846A (en) * | 1985-11-16 | 1989-10-24 | Heinz Reinbold | Spinning apparatus |
US5045874A (en) * | 1990-11-05 | 1991-09-03 | Eastman Kodak Company | Water distributor system for crossover assemblies in a film processor |
NO326080B1 (en) * | 2005-11-11 | 2008-09-15 | Norsk Hydro Produksjon As | Arrangement for sharing of current stream and separation system |
US10076853B2 (en) | 2010-12-30 | 2018-09-18 | United States Gypsum Company | Slurry distributor, system, and method for using same |
US9999989B2 (en) | 2010-12-30 | 2018-06-19 | United States Gypsum Company | Slurry distributor with a profiling mechanism, system, and method for using same |
US10245611B2 (en) | 2010-12-30 | 2019-04-02 | United States Gypsum Company | Slurry distribution system and method |
US10239230B2 (en) | 2010-12-30 | 2019-03-26 | United States Gypsum Company | Slurry distributor, system and method for using same |
US9296124B2 (en) | 2010-12-30 | 2016-03-29 | United States Gypsum Company | Slurry distributor with a wiping mechanism, system, and method for using same |
US9579822B2 (en) | 2010-12-30 | 2017-02-28 | United States Gypsum Company | Slurry distribution system and method |
US9616591B2 (en) | 2010-12-30 | 2017-04-11 | United States Gypsum Company | Slurry distributor, system and method for using same |
US9464747B2 (en) | 2011-05-20 | 2016-10-11 | Norma Germany Gmbh | Connector for a heatable fluid line and heatable fluid line |
US9506595B2 (en) | 2011-05-20 | 2016-11-29 | Norma Germany Gmbh | Fluid line |
EP2525126A1 (en) * | 2011-05-20 | 2012-11-21 | NORMA Germany GmbH | Connector for a heatable fluid conduit and heatable fluid conduit |
US9671053B2 (en) | 2011-05-20 | 2017-06-06 | Norma Germany Gmbh | Fluid line |
US10052793B2 (en) | 2011-10-24 | 2018-08-21 | United States Gypsum Company | Slurry distributor, system, and method for using same |
US20130100759A1 (en) * | 2011-10-24 | 2013-04-25 | United States Gypsum Company | Multiple-leg discharge boot for slurry distribution |
US10293522B2 (en) | 2011-10-24 | 2019-05-21 | United States Gypsum Company | Multi-piece mold and method of making slurry distributor |
US9909718B2 (en) * | 2011-10-24 | 2018-03-06 | United States Gypsum Company | Multiple-leg discharge boot for slurry distribution |
US8991426B2 (en) * | 2013-06-13 | 2015-03-31 | Haven Technology Solutions Llc | Apparatus and method for fluid control |
US9656286B2 (en) * | 2013-09-20 | 2017-05-23 | Nordson Corporation | Fluid dispenser and method for simultaneously dispensing fluids from multiple cartridges |
US20150083751A1 (en) * | 2013-09-20 | 2015-03-26 | Nordson Corporation | Fluid dispenser and method for simultaneously dispensing fluids from multiple cartridges |
US10059033B2 (en) | 2014-02-18 | 2018-08-28 | United States Gypsum Company | Cementitious slurry mixing and dispensing system with pulser assembly and method for using same |
EP3419434A4 (en) * | 2016-02-26 | 2019-10-23 | Erik Garfinkel | Concrete delivery subsystem for automated concrete fabrication system |
US10537054B2 (en) | 2017-07-18 | 2020-01-21 | Cnh Industrial Canada, Ltd. | Dynamic baffle for air flow balancing between adjacent product lines |
US11565439B2 (en) | 2017-09-19 | 2023-01-31 | Yoshino Gypsum Co., Ltd. | Slurry delivery conduit of mixer and slurry delivery method |
CN113167427A (en) * | 2018-11-27 | 2021-07-23 | 美国圣戈班性能塑料公司 | Fluid manifold |
US11350561B2 (en) * | 2019-11-22 | 2022-06-07 | Cnh Industrial Canada, Ltd. | Balanced fan plenum for distributing particulate material |
US20210222501A1 (en) * | 2020-01-20 | 2021-07-22 | Mark Eilam | Vacuum Manifold Assembly |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1905733A (en) | Flow divider | |
EP0043188A1 (en) | Method of attenuating fluid flow passing through a valve and a valve therefor | |
US1751591A (en) | Valve | |
US2158737A (en) | Control valve for liquids of variable viscosities | |
US2315370A (en) | Fluid pressure regulator | |
US2934084A (en) | Butterfly check valves | |
US2351613A (en) | Three-way valve | |
US2946555A (en) | Valve | |
KR880010959A (en) | Dual pump | |
US3343805A (en) | Disc or butterfly valves | |
US3756079A (en) | Turbine flowmeter | |
US2596817A (en) | Slide valve | |
US545769A (en) | Plug-cock | |
US2042462A (en) | Fluid flow control device | |
US623194A (en) | Carl wilhelm vollmann | |
US1673041A (en) | Rate of flow controller | |
US2317657A (en) | Conduit valve | |
US4222408A (en) | Check valve | |
US1406799A (en) | Valve | |
US1854918A (en) | Switch valve | |
US2213256A (en) | Fluid compressor | |
US930635A (en) | Valve. | |
US1839616A (en) | Fluid lines | |
GB1379675A (en) | Gate valve | |
US2588775A (en) | Pivoted valve apparatus |