Fluid processing apparatus and processing method

Patent metadata

Field	Value
Publication number	US-10046296-B2
Application number	US-201414161171-A
Country	US
Kind code	B2
Filing date	Jan 22, 2014
Priority date	Jul 6, 2007
Publication date	Aug 14, 2018
Grant date	Aug 14, 2018

Abstract

A fluid is processed between processing surfaces capable of approaching to and separating from each other, at least one of which rotates relative to the other. A first fluid is introduced between processing surfaces, by using a micropump effect acting with a depression arranged on the processing surfaces from the center of the rotating processing surfaces. A second fluid, independent of this introduced fluid, is introduced from another fluid path that is provided with an opening leading to the processing surfaces, whereby the processing is done by mixing and stirring between the processing members.

First claim

The invention claimed is:

1. A fluid processing apparatus for processing at least two kinds of fluids including a first fluid and a second fluid, wherein at least one kind of the at least two kinds of fluids contains at least one kind of materials to be processed, the fluid processing apparatus comprising:
at least two processing members including opposing processing surfaces, the at least two processing members being capable of approaching to and separating from each other, at least one of the at least two processing members rotating relative to the other, wherein a depression is arranged on at least one of the opposing processing surfaces from inside to outside of the radial direction of the at least one of the opposing processing surfaces and is configured to receive a first fluid by a micropump effect via a first flow path, and a second flow path that is independent of the first flow path for introducing the first fluid is configured to receive the second fluid and is provided with an opening leading between the processing surfaces, whereby the processing of the fluids is done by mixing and stirring between the processing surfaces,
wherein:
an introducing direction from the opening of the second flow path into the processing surfaces is inclined relative to the processing surfaces,
the micropump effect produces an effect such that a force is generated in the direction of separating the processing surfaces from each other by rotating at least one of the opposing processing surfaces provided with the depression,
the opening in the second flow path is arranged at a position nearer to an outer diameter of the processing surfaces than a position where a direction of the first fluid introduced by the micropump effect from the depression arranged on at least one of the opposing processing surfaces is converted into a direction of a spiral laminar flow formed between the processing surfaces,
the opening is arranged radially outward, from an axis of rotation of the at least one processing member, of an outermost end of the depression and apart from the outermost end of the depression, and
the introduction direction of the second fluid from the opening to the processing surfaces is inclined at more than 0° and less than 90°, relative to the processing surfaces.

2. The fluid processing apparatus according to claim 1 , wherein the bore diameter of the opening or the diameter of the second flow path is 0.2 μm to 3000 μm.

3. The fluid processing apparatus according to claim 1 , wherein the depression arranged on at least one of the opposing processing surfaces has a depth of 1 μm to 50 μm.

4. The fluid processing apparatus according to claim 1 , wherein a total plane area of the depressions arranged on at least one of the opposing processing surfaces is 5% to 50% of the total plane area of at least one of the opposing processing surfaces provided with the depressions.

5. The fluid processing apparatus according to claim 1 , wherein the number of the depressions arranged on at least one of the opposing processing surfaces is 3 to 50.

6. The fluid processing apparatus according to claim 1 , wherein the depression arranged on at least one of the opposing processing surfaces is at least one kind selected from a depression extending in a curved form, a depression extending in a spiral form, a depression extending in bending at a right angle and a depression having depth changing continuously, in its plane form.

7. The fluid processing apparatus according to claim 1 , wherein the opening in the second flow path is arranged in a place apart 0.5 mm or more from the outermost end of the depression in the radial direction.

8. The fluid processing apparatus according to claim 1 , wherein a plurality of the openings are arranged for the same kinds of fluids, and the plurality of the openings for the same kinds of fluids are concentrically arranged.

9. The fluid processing apparatus according to claim 1 , wherein a plurality of the openings are arranged for the different kinds of fluids, and the plurality of the openings for the different kinds of fluids are arranged in positions different in radius.

10. The fluid processing apparatus according to claim 1 , wherein the processing members are dipped in a fluid, and a fluid obtained by processing between the processing surfaces is directly fed into a liquid outside the processing members or into a gas other than air.

11. The fluid processing apparatus according to claim 1 , wherein ultrasonic energy can be applied to the processed material just after being discharged from the space between the processing surfaces or from the processing surfaces.

12. The fluid processing apparatus according to claim 1 , wherein the fluids join together between the processing surfaces to form a thin film fluid, the material to be processed being processed in the thin film fluid,
wherein the fluid processing apparatus is configured to provide a temperature gradient to the at least two kinds of fluids.

13. The fluid processing apparatus according to claim 12 , wherein of the processing surfaces, the temperature of one of the processing surfaces is made higher than that of the other processing surface, thereby giving the temperature gradient in the fluid between the processing surfaces.

14. The fluid processing apparatus according to claim 13 , wherein the temperature difference between one of the processing surfaces and the other processing surface is 1° C. to 400° C.

15. The fluid processing apparatus according to claim 12 , wherein the processing members are provided with a temperature regulating mechanism for cooling and heating the processing surfaces.

16. The fluid processing apparatus according to claim 15 , wherein the temperature regulating mechanism is at least one member selected from a pipe for passing a temperature regulating medium, a cooling element, and a heating element.

17. The fluid processing apparatus according to claim 12 , wherein a flow of the fluid between the processing surfaces is generated by the temperature gradient, and a directional factor of this flow contains at least a directional factor perpendicular to the processing surfaces.

18. The fluid processing apparatus according to claim 12 , wherein Benard convection or Marangoni convection is generated in the fluid between the processing surfaces by the temperature gradient.

19. The fluid processing apparatus according to claim 12 , wherein the temperature difference ΔT between the processing surfaces and the distance L between the processing surfaces satisfy the following condition:
Rayleigh number Ra defined by the following equation is 1700 or more:
Ra=L 3 ·g·β·ΔT /(α·ν)

wherein g is gravitational acceleration; β is coefficient of volumetric thermal expansion of fluid; ν is dynamic viscosity of fluid; and α is heat diffusivity of fluid.

20. The fluid processing apparatus according to claim 12 , wherein the temperature difference ΔT between the processing surfaces and the distance L between the processing surfaces satisfy the following condition:
Marangoni number defined by the following equation is 80 or more:
Ma=σ·ΔT·L /(ρ·ν·α)

wherein ν is dynamic viscosity of fluid; α is heat diffusivity of fluid; ρ is density of fluid; and σ is temperature coefficient of surface tension (temperature gradient of surface tension).

21. The fluid processing apparatus according to claim 1 , wherein the fluids join together between the processing surfaces to form a thin film fluid, the material t

Assignees

• M Technique Co Ltd

Inventors

• Enomura Masakazu

Classifications

• B01J2219/00137

  Peltier cooling elements · CPC title

• C09B67/0022

  Wet grinding of pigments · CPC title

• C09B67/0091

  Process features in the making of dispersions, e.g. ultrasonics · CPC title

• B01J19/1887

  forming a thin film · CPC title

• Y10T137/85978

  With pump · CPC title