US2563002A - Mixing device - Google Patents

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US2563002A
US2563002A US5304648A US2563002A US 2563002 A US2563002 A US 2563002A US 5304648 A US5304648 A US 5304648A US 2563002 A US2563002 A US 2563002A
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Prior art keywords
pipe
throat
venturi
liquid
venturi tube
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William W Bissell
Delmer G Debo
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Standard Oil Co
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Standard Oil Co
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3121Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31242Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the central area of the venturi, creating an aspiration in the circumferential part of the conduit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3141Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit with additional mixing means other than injector mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3142Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3142Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
    • B01F25/31423Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction with a plurality of perforations in the circumferential direction only and covering the whole circumference
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/432Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/834Mixing in several steps, e.g. successive steps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • 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
    • Y10T137/87571Multiple inlet with single outlet
    • Y10T137/87587Combining by aspiration

Definitions

  • This application relates to apparatus for injection of a liquid, especially a corrosive liquid, into admixture with a liquid flowing in a pipe.
  • a treatment of liquids with other fluids or the proportioning of liquids, and particularly their proper admixture when the liquids are immiscible has required the development of diverse mixing devices, such, for example, as turbine or pump mixers.
  • the treating fluid which is ordinarily added in minor proportion, is corrosive to the conduit. transporting or pump handling the liquid of major proportion, the aforesaid mixers have necessarily been made of resistant alloys which are in many instances prohibitively expensive.
  • the simple injection, on the other hand, of such a corrosive liquid even into the center of a stream of liquid flowing in a pipe results in rapid corrosionof the pipe near the point of introduction of the corrosive liquid.
  • the invention has, for other objects, those other advantages or results as will appear in the following description of the apparatus of invention.
  • the foregoing objects are accomplished in simple manner by providing a pipe spool of standard dimensions in which is inserted a Venturi tube, preferably of resistant alloy material, about the throat of which tube there is encircled a pipe ring to which, in turn, there is attached piping which feeds from an extraneous source the corrosive liquid additive;
  • a Venturi tube preferably of resistant alloy material
  • thesaid Venturi-type tube is fitted into the pipe spool and includes a protective sleeve which is an extension of the down stream side of the Venturi tube, the said sleeve being annularly contiguous with the aforesaid pipe spool.
  • the introduction of the corrosive liquid additive at the Venturi throat advantageously exploits the turbulence provided by the Venturi tube so that a rapid mixing of treated liquid and liquid additive is obtained.
  • the tube is preferably constructed of a resistant alloy and will, in such instances, provide uninterrupted service, it can be made of ordinary materials and will nevertheless have an extended life because of the enhanced mixing provided by the described device of introducing the corrosive liquid additiveat the said Venturi throat.
  • the Venturi can insuch instances be readily removed from the pipe spool when corrosion has set in. It is preferable, however, to construct the Venturi tube of a resistant alloy.
  • a further improvement provided by the present apparatus permits the employment of thin gauge sheet in the manufacture of the said Venturi tubes so that the initial expense when resistant alloys are employed is itself reduced.
  • This improvement consists of providing holes in the conical interfaces of both the inlet and outlet cones of the Venturi tube, these holes being arranged circularly near the base of each cone.
  • the pressure differential across the Venturi walls will be substantially eliminated and, therefore, extremely thin walls can be employed.
  • the outside pipe usually of carbon steel, is thereby maintained at the same temperature as the Venturi tube, thus minimizing thermal expansion difierences between the pipes and the Venturi tubes, and the flow of oil in the annular space around the Venturi eliminates a dead space and prevents either accumulation of any corrosive materials in this space or the tendency of coke formation.
  • Fig. 1 is a cross sectional, longitudinal view of a preferred apparatus embodying the features of the invention
  • Fig. 2 is a cross-section taken along the line II--II of Fig. 1 and showing a side view of the injection device employed for introducing the corrosive liquid additive.
  • a Venturi tube 4 constructed of a resistant alloy.
  • the Venturi-tube conventionally consists of a short conical inlet section 6, a throat 8, and an elongated conical outlet section III.
  • An extension I2 of the Venturi tube down stream thereof is of a length approximately equal to that of the Venturi tube and fits as an inner sleeve annularly contiguous against the said pipe spool 2.
  • the Venturi tube 4 is fitted at the circular base [4 of the inlet section 6 of the Venturi tube against the up-stream flange it of the pipe 2.
  • the circular base [4 is seated in a recess in the flange l6, relative movement caused by differences in thermal expanson of the tube and of the pipe being permitted by the fact that the sleeve I2 is not fixed in the pipe 2 but can slide therein.
  • An injection feeder pipe i9 is attached at right angles to the longitudinal dimension of the pipe 2 and extends through the wall of the pipe to the throat S of the Venturi tube.
  • the pipe i9 is provided with a flange 20, packing gland 22 and an outer sleeve 24 so that the pipe 19 can readily be removed from communication with the said Venturi tube.
  • Encircling the Venturi throat 8 at about the longitudinal center thereof is an annularly fitted tube or ring 25 consisting of a longitudinally split pipe.
  • the tube formedv by the semi-pipe section is welded around the said throat so that the throat itself forms half of the conduit provided by the ring 25. That part of the throatv 8. which provides the inner wall of the ring-like conduitZlsw is perforated with holes 28 spaced equally apart.
  • the section IIII illustrates a sectional view of the annular ring 25 and shows more clearly the positionof the holes 28 and the attached coupling 36 welded thereto.
  • a pipe connection can be supplied between the up-stream side of the pipe spool and a tank not shown providing the supply of corrosive additive liquid so that the characteristic decrease in pressure at the throat of the Venturi can be utilized for increasing the force of injection of additive liquid.
  • an aqueous caustic solution was introduced through the injection pipe i9 and was injected through the-holes 28 into sour oil flowing from left to right (as shown on the drawing) through the pipe 2.
  • the Venturi tube, the annular ring and the feeder pipe 19 was made of an 188 alloy containing approximately 73% iron, 18% chromium, 8-9% nickel and 0.5% manganese.
  • the tube proper was of A; inch thickness and the extended sleeve of only inch thickness. Twelve M inch diameter holes were equidistantly spaced around the base of the inlet section and an equal number were arranged in the outlet section near the base thereof.
  • a slow flow of the oil through the annular space between the Venturi tube and the pipe provided the hereinabove, described advantages.
  • a mixing device as above described has been used for a period three times as long as the longest period during which previous devices were usable and yet no indication of corrosion has arisen.
  • Apparatus for admixing a corrosive fluid with a liquid flowing in a pipe section which apparatus comprises: a Venturi tube assembly longitudinally fitted within the pipe section and having an upstream cone, a downstream cone oppositely disposed along the same axis, the bases of the said cones being contiguous with the inner walls of the pipe section, and a throat disposed between the cones; a space between the said cones and throat and the said inner walls; at
  • a feeder consisting of a conduit communicating with the throat through at least one perforation in the wall of said throat; and an inlet conduit extending through a wall of the pipe section for introducing corrosive, fluid from a point outside the said pipe section to the feeder.
  • Venturi tube assembly includes a cylindrical sleeve that extends from the downstream, cone and is slidable and annularly disposed within the said pipe section, substantially contiguous therewith.
  • Apparatus for admixing a corrosive fluid with a liquid flowing in a pipe section which apparatus comprises: a Venturi' tube assembly longitudinally fitted Within the pipe section and having an upstream cone, a downstream cone oppositely disposed along the same axis, the bases of the said cones being contiguous with the inner walls of the pipe section, and a throat of smaller diameter than the said section, disposed between and connecting the cones whereby a space is provided between the said cones andthroat and the said inner walls; at least one. opening in each cone adjacent the bases thereof whereby a part of the liquid flowing through the pipe section bypasses the throat of the Venturi tube assembly and flows through the space.
  • a feeder in the form of aringlike tube surrounding the throat and enclosing perforations in the throat. wall through which corrosive fluid passes from the feeder into the throat; and an inlet conduit extending through the wall of;-a pipe sectionfor introducing corrosive fluid from a point outsidethe said pipe section to the feeder.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)

Description

/ 7, 1951 w. w. BlSSELL ET AL 2,563,002
MIXING DEVICE Filed Oct. e, 1948 INVENTORS: r; Delmar G. Debo Q & William W; Bissel/ 5 Wig/5661M A T'TO/M/E Y Patented Aug. 7, 1951 ff'UNlT-ED STATES PATENT OFFICE William W. Bissell, New Castle, Pa., and Delmar G. Debo, Chicago, 111., assignors to Standard :Oil Company, Chicago, 111., a corporation of Indiana Application October 6, 1948, Serial No. 53,046
4 Claims.
. 1 g This application relates to apparatus for injection of a liquid, especially a corrosive liquid, into admixture with a liquid flowing in a pipe.
- A treatment of liquids with other fluids or the proportioning of liquids, and particularly their proper admixture when the liquids are immiscible has required the development of diverse mixing devices, such, for example, as turbine or pump mixers. When the treating fluid, which is ordinarily added in minor proportion, is corrosive to the conduit. transporting or pump handling the liquid of major proportion, the aforesaid mixers have necessarily been made of resistant alloys which are in many instances prohibitively expensive. The simple injection, on the other hand, of such a corrosive liquid even into the center of a stream of liquid flowing in a pipe results in rapid corrosionof the pipe near the point of introduction of the corrosive liquid.
It is a primary object of the present invention to provide simple, relatively inexpensive means for introducing a corrosive liquid into and effectively mixing it with another liquid.
It is another object of the invention to provide simple means whereby a corrosive liquid can be admixed with a liquid flowing in a pipe and may be rapidly intermixed therewith so that the pipe at the downstream point of the admixture will not be subjected to the corrosive action of the introduced liquid.
The invention has, for other objects, those other advantages or results as will appear in the following description of the apparatus of invention.
The foregoing objects are accomplished in simple manner by providing a pipe spool of standard dimensions in which is inserted a Venturi tube, preferably of resistant alloy material, about the throat of which tube there is encircled a pipe ring to which, in turn, there is attached piping which feeds from an extraneous source the corrosive liquid additive; As will appear more clearly in the detailed description of the drawings hereinafter supplied,thesaid Venturi-type tube is fitted into the pipe spool and includes a protective sleeve which is an extension of the down stream side of the Venturi tube, the said sleeve being annularly contiguous with the aforesaid pipe spool. The introduction of the corrosive liquid additive at the Venturi throat advantageously exploits the turbulence provided by the Venturi tube so that a rapid mixing of treated liquid and liquid additive is obtained. While the tube is preferably constructed of a resistant alloy and will, in such instances, provide uninterrupted service, it can be made of ordinary materials and will nevertheless have an extended life because of the enhanced mixing provided by the described device of introducing the corrosive liquid additiveat the said Venturi throat. The Venturi can insuch instances be readily removed from the pipe spool when corrosion has set in. It is preferable, however, to construct the Venturi tube of a resistant alloy. A further improvement provided by the present apparatus permits the employment of thin gauge sheet in the manufacture of the said Venturi tubes so that the initial expense when resistant alloys are employed is itself reduced. This improvement consists of providing holes in the conical interfaces of both the inlet and outlet cones of the Venturi tube, these holes being arranged circularly near the base of each cone. In this manner, a small flow of liquid is permitted in the space between the Venturi tube of the pipe and thereby several advantages are obtained. The pressure differential across the Venturi walls will be substantially eliminated and, therefore, extremely thin walls can be employed. The outside pipe, usually of carbon steel, is thereby maintained at the same temperature as the Venturi tube, thus minimizing thermal expansion difierences between the pipes and the Venturi tubes, and the flow of oil in the annular space around the Venturi eliminates a dead space and prevents either accumulation of any corrosive materials in this space or the tendency of coke formation.
In the accompanying drawing, which is provided solely for purposes of illustration, Fig. 1 is a cross sectional, longitudinal view of a preferred apparatus embodying the features of the invention, and Fig. 2 is a cross-section taken along the line II--II of Fig. 1 and showing a side view of the injection device employed for introducing the corrosive liquid additive.
Referring now to Fig. 1, there is mounted in a pipe spool 2 of ordinary material, a Venturi tube 4 constructed of a resistant alloy. The Venturi-tube conventionally consists of a short conical inlet section 6, a throat 8, and an elongated conical outlet section III. An extension I2 of the Venturi tube down stream thereof is of a length approximately equal to that of the Venturi tube and fits as an inner sleeve annularly contiguous against the said pipe spool 2. The Venturi tube 4 is fitted at the circular base [4 of the inlet section 6 of the Venturi tube against the up-stream flange it of the pipe 2. Preferably, the circular base [4 is seated in a recess in the flange l6, relative movement caused by differences in thermal expanson of the tube and of the pipe being permitted by the fact that the sleeve I2 is not fixed in the pipe 2 but can slide therein.
Annularly arranged around the inlet section 6 a short and uniform distance from the base I4 are equidistantly spaced holes ll. Similarly arranged are equidistantly spacedholes l8 placed a short uniform distance from the down-stream end of outlet section Iii. These holes permit a slight flow of liquid between the Venturi tube 4 and pipe spool 2 thus reducing the pressure on the Venturi tube and permitting its manufacture of thin sheet metal, and also protecting the inner wall of the pipe from corrosion by accidental con- 7 tact with liquid additive.
An injection feeder pipe i9 is attached at right angles to the longitudinal dimension of the pipe 2 and extends through the wall of the pipe to the throat S of the Venturi tube. The pipe i9 is provided with a flange 20, packing gland 22 and an outer sleeve 24 so that the pipe 19 can readily be removed from communication with the said Venturi tube. Encircling the Venturi throat 8 at about the longitudinal center thereof is an annularly fitted tube or ring 25 consisting of a longitudinally split pipe. The tube formedv by the semi-pipe section is welded around the said throat so that the throat itself forms half of the conduit provided by the ring 25. That part of the throatv 8. which provides the inner wall of the ring-like conduitZlsw is perforated with holes 28 spaced equally apart. Usually some twelve to twenty-four holes are employed and these are of varying dimension so that a uniform flow of additive. is injected from every point around the Venturi throat. The said ring 26 is connected with the secondary pipe ie with a hreaded coupling 39.
The section IIII illustrates a sectional view of the annular ring 25 and shows more clearly the positionof the holes 28 and the attached coupling 36 welded thereto.
A pipe connection can be supplied between the up-stream side of the pipe spool and a tank not shown providing the supply of corrosive additive liquid so that the characteristic decrease in pressure at the throat of the Venturi can be utilized for increasing the force of injection of additive liquid.
. In one example in which the above described device was employed, an aqueous caustic solution was introduced through the injection pipe i9 and was injected through the-holes 28 into sour oil flowing from left to right (as shown on the drawing) through the pipe 2. In this instance, the Venturi tube, the annular ring and the feeder pipe 19 was made of an 188 alloy containing approximately 73% iron, 18% chromium, 8-9% nickel and 0.5% manganese. The tube proper was of A; inch thickness and the extended sleeve of only inch thickness. Twelve M inch diameter holes were equidistantly spaced around the base of the inlet section and an equal number were arranged in the outlet section near the base thereof. A slow flow of the oil through the annular space between the Venturi tube and the pipe provided the hereinabove, described advantages. A mixing device as above described has been used for a period three times as long as the longest period during which previous devices were usable and yet no indication of corrosion has arisen.
Having now described our invention, what we claim is:
1. Apparatus for admixing a corrosive fluid with a liquid flowing in a pipe section, which apparatus comprises: a Venturi tube assembly longitudinally fitted within the pipe section and having an upstream cone, a downstream cone oppositely disposed along the same axis, the bases of the said cones being contiguous with the inner walls of the pipe section, and a throat disposed between the cones; a space between the said cones and throat and the said inner walls; at
least one opening in each cone adjacent the bases thereof whereby apart of the liquid flowing through the pipe section by-passes the throat of the Venturi tube assembly and flows through the space between the outer walls of the said throat and the inner Walls of the pipe section; a feeder consisting of a conduit communicating with the throat through at least one perforation in the wall of said throat; and an inlet conduit extending through a wall of the pipe section for introducing corrosive, fluid from a point outside the said pipe section to the feeder.
2. The apparatus of claim 1 wherein the one end of the Venturi tube assembly is fixed to the pipe section and the other end is free to move in response to thermal changes, the said apparatus being further characterized by a packing gland between the said inlet conduit and the said wall of the pipe section, the said inlet conduit bein removably connected to the feeder and being removable so that the Venturi tube assembly can be readily removed from the pipe section.
3., The apparatus of. claim 1 in which the Venturi tube assembly includes a cylindrical sleeve that extends from the downstream, cone and is slidable and annularly disposed within the said pipe section, substantially contiguous therewith.
4. Apparatus for admixing a corrosive fluid with a liquid flowing in a pipe section, which apparatus comprises: a Venturi' tube assembly longitudinally fitted Within the pipe section and having an upstream cone, a downstream cone oppositely disposed along the same axis, the bases of the said cones being contiguous with the inner walls of the pipe section, and a throat of smaller diameter than the said section, disposed between and connecting the cones whereby a space is provided between the said cones andthroat and the said inner walls; at least one. opening in each cone adjacent the bases thereof whereby a part of the liquid flowing through the pipe section bypasses the throat of the Venturi tube assembly and flows through the space. between the outer walls of the said throat and the inner walls of the pipe section; a feeder in the form of aringlike tube surrounding the throat and enclosing perforations in the throat. wall through which corrosive fluid passes from the feeder into the throat; and an inlet conduit extending through the wall of;-a pipe sectionfor introducing corrosive fluid from a point outsidethe said pipe section to the feeder.
WILLIAM W. BISSELL.
DELMER.v G. DEBO.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,831,265 Schonberg Nov. 10, 1931 1,890,439 Pier Dec. 6, 1932 1,920,886 Pier et a1; Aug; 1, 1933' 2 ,075,867 Sampsel Apr. 6, 1937 2,093,011 Grosz Sept. 14, 1937 2,155,315 Kremers Apr. 18, 1939 2,307,509 Joachim'et al. Jan. 5, 1943 2,321,879 Valdez June 15, 1943 2,357,266 Malcom Aug; 29, 1944 2,361,150 Petroe Oct. 24, 1944 FOREIGN PATENTS;
Number Country" Date 585,553 Great'Britain' Feb. 11, 1947-
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Cited By (31)

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US2746735A (en) * 1951-10-04 1956-05-22 Combined Metals Reduction Comp Material mixing burner for processing furnaces
US2747934A (en) * 1951-10-05 1956-05-29 Emery J Fisher Chemical spray gun
US2981596A (en) * 1956-06-18 1961-04-25 Diamond Alkali Co Preparation of alkaline earth metal carbonates
US3434698A (en) * 1966-09-19 1969-03-25 Millard F Smith Fluid mixing,moving and atomizing methods and apparatus
US3528764A (en) * 1967-11-28 1970-09-15 Research Corp Method and apparatus for retarding evaporation from water surfaces
US4123800A (en) * 1977-05-18 1978-10-31 Mazzei Angelo L Mixer-injector
FR2500324A1 (en) * 1981-02-24 1982-08-27 Stein Industrie DEVICE FOR THE HOMOGENEOUS MIXTURE OF LIQUIDS IN FLOW AT DIFFERENT TEMPERATURES
FR2599437A1 (en) * 1986-05-27 1987-12-04 Roy Philippe Duct inducing nozzle.
EP0322647A1 (en) * 1987-12-24 1989-07-05 Bayer Ag Process for the continuous production of mono- or polyisocyanates
EP0350556A2 (en) * 1988-07-12 1990-01-17 Henkel Iberica, S.A. Continuous process for the manufacture of a hypochlorite bleaching composition
US5893641A (en) * 1998-05-26 1999-04-13 Garcia; Paul Differential injector
US6076955A (en) * 1996-12-19 2000-06-20 Tetra Laval Holdings & Finance S.A. Method and an apparatus for the continuous mixing of two flows
US6341888B1 (en) * 1997-10-14 2002-01-29 Kvaerner Pulping, Ab Apparatus for introduction of a first fluid into a second fluid
US6347883B1 (en) * 1999-01-26 2002-02-19 Kvaerner Pulping Ab Apparatus for adding a first fluid into a second fluid with means to prevent clogging
US6395175B1 (en) * 2000-04-03 2002-05-28 Battelle Memorial Institute Method and apparatus for energy efficient self-aeration in chemical, biochemical, and wastewater treatment processes
US20030024485A1 (en) * 2001-06-08 2003-02-06 Freidell James E. Animal bathing system
US20030137897A1 (en) * 2000-10-30 2003-07-24 Whiteley Bruce Alan Fluid mixer with rotatable eductor tube and metering orifices
US6623154B1 (en) 2000-04-12 2003-09-23 Premier Wastewater International, Inc. Differential injector
US6659635B2 (en) * 1999-01-26 2003-12-09 Kvaerner Pulping Ab Method for introducing a first fluid into a second fluid, preferably introduction of steam into flowing cellulose pulp
US20040083899A1 (en) * 2000-10-30 2004-05-06 Rolf Nilsson Method and an apparatus for mixing two phases of a food product
US20060087910A1 (en) * 2003-02-15 2006-04-27 Darrell Knepp Water injection method and apparatus for concrete mixer
US20060153002A1 (en) * 2005-01-10 2006-07-13 Mr. Peter Ryan Jet Mixer With Adjustable Orifices
US20060169627A1 (en) * 2003-09-30 2006-08-03 Ok Technologies Llc Mixing eductor
US20070258315A1 (en) * 2003-10-08 2007-11-08 Wetend Technologies Oy Method and Apparatus for Feeding Chemical Into a Liquid Flow
US20100103766A1 (en) * 2007-03-29 2010-04-29 Polimeri Euroopa S.P.A. Low-pressure -drop mixing device and use thereof in the mixing of two gases/vapours
US20150007900A1 (en) * 2013-07-02 2015-01-08 Johnson Electric S.A. Venturi mixer
US20160346744A1 (en) * 2015-06-01 2016-12-01 Cameron International Corporation Apparatus for mixing of fluids flowing through a conduit
US20160362785A1 (en) * 2015-06-15 2016-12-15 Samsung Electronics Co., Ltd. Apparatus for manufacturing semiconductor device having a gas mixer
US20170356404A1 (en) * 2016-06-14 2017-12-14 Dayco Ip Holdings, Llc Bypass valve in an apparatus for producing vacuum
US20210046434A1 (en) * 2016-03-23 2021-02-18 Alfa Laval Corporate Ab Apparatus for dispersing particles in a liquid
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US6623154B1 (en) 2000-04-12 2003-09-23 Premier Wastewater International, Inc. Differential injector
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US6877890B2 (en) * 2000-10-30 2005-04-12 Bruce Alan Whiteley Fluid mixer with rotatable educator tube and metering orifices
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US7731163B2 (en) 2003-09-30 2010-06-08 Laurent Olivier Mixing eductor
US20060169627A1 (en) * 2003-09-30 2006-08-03 Ok Technologies Llc Mixing eductor
US9616399B2 (en) 2003-10-08 2017-04-11 Wetend Technologies Oy Method for feeding chemical into a liquid flow
US20070258315A1 (en) * 2003-10-08 2007-11-08 Wetend Technologies Oy Method and Apparatus for Feeding Chemical Into a Liquid Flow
US8602634B2 (en) * 2003-10-08 2013-12-10 Wetend Technologies Oy Method and apparatus for feeding chemical into a liquid flow
US20060153002A1 (en) * 2005-01-10 2006-07-13 Mr. Peter Ryan Jet Mixer With Adjustable Orifices
US20100103766A1 (en) * 2007-03-29 2010-04-29 Polimeri Euroopa S.P.A. Low-pressure -drop mixing device and use thereof in the mixing of two gases/vapours
US8303164B2 (en) * 2007-03-29 2012-11-06 Polimeri Europa S.P.A. Low-pressure-drop mixing device and use thereof in the mixing of two gases/vapours
US20150007900A1 (en) * 2013-07-02 2015-01-08 Johnson Electric S.A. Venturi mixer
US20160346744A1 (en) * 2015-06-01 2016-12-01 Cameron International Corporation Apparatus for mixing of fluids flowing through a conduit
US10058828B2 (en) * 2015-06-01 2018-08-28 Cameron International Corporation Apparatus for mixing of fluids flowing through a conduit
US20160362785A1 (en) * 2015-06-15 2016-12-15 Samsung Electronics Co., Ltd. Apparatus for manufacturing semiconductor device having a gas mixer
US20210046434A1 (en) * 2016-03-23 2021-02-18 Alfa Laval Corporate Ab Apparatus for dispersing particles in a liquid
US20170356404A1 (en) * 2016-06-14 2017-12-14 Dayco Ip Holdings, Llc Bypass valve in an apparatus for producing vacuum
US9919689B2 (en) * 2016-06-14 2018-03-20 Dayco Ip Holdings, Llc Bypass valve in an apparatus for producing vacuum
US11673104B2 (en) * 2018-12-07 2023-06-13 Produced Water Absorbents Inc. Multi-fluid injection mixer and related methods

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