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Publication numberUS3338560 A
Publication typeGrant
Publication dateAug 29, 1967
Filing dateApr 15, 1965
Priority dateApr 15, 1965
Publication numberUS 3338560 A, US 3338560A, US-A-3338560, US3338560 A, US3338560A
InventorsRichard A Gierak, Melvin F Katzer
Original AssigneeDow Chemical Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Mixing apparatus
US 3338560 A
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Description  (OCR text may contain errors)

United States Patent 3,338,560 MIXING APPARATUS Melvin F. Katzer, Danville, and Richard A. Gierak, Glendale, Calif., assignors to The Dow Chemical Company, Midland, Mich., a corporation of Delaware Filed Apr. 15, 1965, Ser. No. 448,529 6 Claims. (Cl. 259-4) This invention relates to devices for dispersing powdered solids in liquids and particularly to a portable device of simple structure for preparing and dispersing such dispersions.

Commercially available devices for dispersing solids in liquids commonly include eductors which employ an eductor developed vacuum in their operation.

Some commercially available units marketed for mixing fire-retardants with water are of the vacuum developing eductor type.

In such devices a powdered solid is discharged through a port into a partial vacuum created by the flow of water through the eductor. If the water flow changes, so does the degree of vacuum produced and so the rate of flow of the particulated solids changes too. So-called slugs of powder may be introduced into the dispersing devices which result a non-homogenous (lumpy) output of the dispersing device.

If the solid feed port plugs or is closed and the water flow is appreciably reduced, water tends to back flow, effectively disabling the device. Disassembling, cleaning and drying are required before the device may again be operated.

The main problem sought to be solved by the prior art resides in the fact that powdered particles resist wetting. The individual particles tend to cling together in lumps and wetting at the surface of the lump as a whole is favored.

Often, where such action is permitted, the problem is solved by pre-mixing the solutions or dispersions in large agitated tanks. The mixed material may then be pumped through more or less conventional piping to wherever it is to be used or stored.

The above mentioned pre-mixing procedure is usually not practical for field use in preparing solutions or dispersions for agricultural or fire-fighting applications.

In fire-fighting, particularly, natural water supplies must be used whenever possible to minimize Water haulmg.

Efiicient fire-fighting operation requires on the spot mixing with the lightest, simplest, most rugged equipment available.

Similarly, on the spot mixing is highly preferable for agricultural applications such as charging sprayers or introducing chemicals into irrigation Water.

Accordingly, a principal object of this invention is to provide an improved apparatus for making solutions or dispersions from particulated materials and liquids.

Another object of this invention is to provide an improved, more reliable to operate apparatus for making solutions or dispersions from particulated materials and liquids.

A further object of this invention is to provide an improved, reliable and economical apparatus for making solutions and dispersions from particulated materials and liquids.

In accordance with this invention there is provided mixing apparatus comprising a mixing head having coupled to it valve and screen apparatus adapted to be coupled to a source of liquid which is under pressure.

A particulated materials reservoir is coupled to a gas inlet tube which extends from said mixing head. The gas inlet tube extends axially into said mixing head and ends downstream from the part of said mixing head to which the valve and screen apparatus are coupled.

A nozzle is coupled to the output end of the mixer head.

The invention, as well as additional objects and advantages thereof, will best be understood when the following detailed description is read in connection with the accompanying drawing in which the single figure shows an elevational view, partly broken away and in section, of apparatus in accordance with this invention.

Referring to the drawing, there is shown mixing apparatus, indicated generally by the numeral 10, which comprises a mixing head, indicated generally by the numeral 12, a particulated materials reservoir, indicated generally by the numeral 14, and a liquid feed assembly, indicated generally by the numeral 16.

The mixing head 12 is a hollow T-shaped member which has a bushing 18 coupled to one end and a nozzle or snout 20 coupled to its other or output end 22. The bushing 18 has a tube 24 coupled thereto which extends axially into the interior of the mixing head 12, ending at a point well beyond the bore 26 (the side entry bore of the T) towards the output end 22 of the head 12. The outer diameter of the tube 24 is a major fraction of the inner diameter of the head 12.

A second tube 28 is coupled in end-to-end relationship with respect to the tube 24 and extends outside of the head 12 in the opposite direction in which the nozzle 20 extends.

The particulated materials reservoir 14, which may have venting means 30 therein, is fixedly coupled to the tube 28 through a valve 32 and tubing 34. The reservoir 14 is coupled so that, during operation, the reservoir 30 is disposed above the mixing head 12.

The liquid feed assembly 16 is coupled at one end to a source of liquid (water, for example) as from the tubing 36 and at the other end to the bore 26 in the mixing head 12.

The assembly 16, as shown, comprises a T-like element 38 which has a strainer screen 40 disposed across the output flow path of the element. The side port 42 is coupled to a valve 44.

The output end 46 of the element 38 is coupled to the side inlet 48 of a T -coupling 50. A liquid flow control valve 52 is coupled between the bore 26 of the mixing head 12 and one end of the T-coupling 50. A bleed valve 54 is coupled to the other end of the T-element 50.

In operation, with the tubing 36 coupled to a source of liquid which is under pressure and with the valves 44 and 54 closed and valve 52 open, water (or other suitable liquid) enters the mixing head 12 through the side bore 26 and then exits through the nozzle 20. A partial vacuum is created in the tubes 24 and 28 which communicate with the atmosphere (at the end 56 of the tube 28). The partial vacuum causes air to flow from the tube 28 into the mixing head 12, carrying with it particulated material from the reservoir 14 (with the valve 32 opened to permit a suitable flow of powder).

The powder, which flows by gravity into the tube 28, then is carried by air flow into the tube 24, becoming pre-dispersed during its passage down the tubes 24 and 28 before it enters the stream of liquid near the output end of the mixing head 12.

If, during operation, the nozzle is elevated above the Patented Aug. 29, 1967 ations in the water flow. Experience has shown that adequate proportioning control of the powder to liquid ratio is readily obtained if the pumping rate is reasonably steady.

One use to which this apparatus is particularly Well suited is for producing and applying dispersions of fire retardant materials.

Because so-called natural sources of water are so often used in fire fighting operations, the screen 40 catches material from the liquid which might tend to clog the mixing head 12. The screen 40 may usually be cleaned by opening the valve 44 and closing the valve 52, thereby sweeping adhering material from the screen.

The valve 54 may be coupled to a sample bleed line or to a pressure gauge, for example.

It should be emphasized that having the outer diameter of the tube 24 be a major fraction of the inner diameter of the head 12 results in, for a given volume rate of flow of liquid, a higher linear flow rate or water velocity, for example, giving better mixing where the powder-air and water streams come together downstream and prevents any splash back of water into the inner tube. Further, the higher water velocity and the cylindrical shape of the water stream just below the outlet of the inner tube ensures that no solids will contact or adhere to the mixing head wall.

What is claimed is:

1. Mixing apparatus for preparing solutions or dispersions from a mixture of particulated materials and liquids, comprising a tubular mixing head having side walls, an input end and an output end, said side walls having a liquid entry port disposed a substantial distance from said output end and between said input end and output end, said input end being closed and having a fluid impervious walled tubular element extending therethrough which has an input and output end, the output end of said tubular element extending beyond said liquid entry port in the direction of the output end of said mixing head, the tubular element being in alignment with the longitudinal axis of said mixing head, the input end of said tubular element extending externally of said mixing head substantially beyond said input end of the mixing head, a particulated materials reservoir, valved means rigidly coupling said reservoir to said tubular element between said mixing head and the input end of said tubular element, a nozzle, said nozzle being coupled to the output end of said mixing head, valved means coupled to said liquid entry port for introducing liquid under pressure to said mixing head, and means for introducing gas into said tubular element at a location further from said mixing head than where said reservoir is coupled to said tubular element.

2. Apparatus in accordance with claim 1, wherein said valved means for introducing liquid includes a filter screen.

3. Apparatus in accordance with claim 1, wherein said particulated materials reservoir is vented.

4. Apparatus in accordance with claim 1, wherein the diameter of the tubular element within the mixing head is a major fraction of the diameter of said mixing head.

5. Apparatus in accordance with claim 1, wherein said nozzle is flexible.

6. Apparatus in accordance with claim 1, wherein a filter screen and screen cleaning means are incorporated into said means for introducing liquid.

References Cited UNITED STATES PATENTS 2,747,974 5/1956 Felger 2594 2,784,948 3/1957 Pahl et al. 2594 2,992,084 7/1961 Schropp 2594 3,147,717 10/1964 Smith 259-4 3,147,955 10/1964 Harvey et al 2594 WALTER A. SCHEEL, Primary Examiner.

ROBERT W. JENKINS, Examiner.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2747974 *Aug 18, 1953May 29, 1956Olin MathiesonMixer
US2784948 *Nov 14, 1952Mar 12, 1957Crown Cork & Seal CoLiquid mixing device
US2992084 *Aug 16, 1957Jul 11, 1961Four Industriel BelgeApparatus for regulating the composition of a mixture of air and fuel-gas
US3147717 *Feb 12, 1963Sep 8, 1964Smith Verle DBlending apparatus
US3147955 *Aug 15, 1960Sep 8, 1964Union Carbide CorpApparatus for dispersing finely-divided solids in liquids
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3425669 *Nov 13, 1967Feb 4, 1969Preston G GaddisDry chemical feeder method and apparatus
US3695586 *Nov 5, 1970Oct 3, 1972Warren R GriffinMixing apparatus
US3737148 *Nov 3, 1971Jun 5, 1973Minnich RMethod of and mixer block for feeding a stream of viscous material
US3759491 *Sep 29, 1971Sep 18, 1973A PfeufferDissolver for solid and liquid materials
US3819157 *Feb 1, 1973Jun 25, 1974Universal Oil Prod CoMixing apparatus
US3838847 *Jan 19, 1972Oct 1, 1974Fischer Ag GeorgDrum mixer for continuous processing of a granular bulk material
US3861652 *Nov 15, 1972Jan 21, 1975Du PontMixing device
US3902558 *Dec 20, 1973Sep 2, 1975Mobil Oil CorpMethod of recovering oil using a chemical blending system
US3979172 *Mar 18, 1974Sep 7, 1976Snow Brand Milk Products Co., Ltd.Ice cream freezer
US4050677 *Jan 13, 1976Sep 27, 1977A/S HotacoMixing device
US4103351 *Mar 14, 1977Jul 25, 1978Alexandr Sergeevich MamvriiskyApparatus for controlling the density of a plugging fluid
US4482343 *Feb 10, 1983Nov 13, 1984Commissariat A L'energie AtomiqueApparatus for dissolving a powder in a liquid solvent
US7871194 *Oct 12, 2007Jan 18, 2011Malvern Instruments LimitedDilution apparatus and method
US8128726Jun 22, 2007Mar 6, 2012Heggset Teknologi AsMethod and device for admixture of powder in a liquid
CN101506396BJun 22, 2007Mar 21, 2012赫格塞特技术公司A method and device for admixture of powder in a liquid
DE2945361A1 *Nov 9, 1979May 21, 1981Maizena GmbhAnlage zur kontinuierlichen staerkemilch-aufbereitung
EP1499447A1 *Apr 30, 2002Jan 26, 2005Avrom R. HandlemanEductor mixer system
WO2008010721A1 *Jun 22, 2007Jan 24, 2008Heggset Bjarne AndersA method and device for admixture of powder in a liquid
Classifications
U.S. Classification366/101
International ClassificationB01F15/02, B01F3/06, B01F5/04, B01F3/12, B01F13/10, B01F15/04, A62C99/00
Cooperative ClassificationB01F5/043, A62C99/009, B01F15/0429, B01F15/026, B01F13/1025, B01F15/0234, B01F5/0413, B01F15/0202, B01F3/12, B01F3/06, B01F5/0426
European ClassificationB01F5/04C12S2, B01F15/02B40U, B01F5/04C12S6, B01F15/02B40F, B01F15/04G4, B01F13/10C, B01F5/04C12, B01F3/12, B01F3/06, B01F15/02B3, A62C99/00F