IP Library Granted Patent US 7,648,033
Granted Patent B2
US 7,648,033 · App. 11/236,824 · Granted Jan 19, 2010

Method of producing particle-dispersed liquid

Assignee: Fuji Xerox Co., Ltd.
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Quick Facts
Patent No.
US 7,648,033
App. No.
11/236,824
Granted
Jan 19, 2010
Kind
B2
Abstract

A method of producing a particle-dispersed liquid, using a channel of micro width having a core flow channel, includes: sending the particle-dispersed liquid containing larger particles to an inner portion of the core flow channel; separating and removing the larger particles from the particle-dispersed liquid; and sending the removed larger particles to an outermost part of the core flow channel. An outer diameter of the core flow channel is 50 to 5,000 μm.

Claims (40)

1. A method of producing a particle-dispersed liquid, using a channel of micro width having a core flow channel, comprising:

sending the particle-dispersed liquid containing larger particles to an inner portion of the core flow channel;

separating and removing the larger particles from the particle-dispersed liquid based on an outward force resulting from a velocity gradient of the particle-dispersed liquid; and

sending the removed larger particles to an outermost part of the core flow channel;

wherein the core flow channel is circular in cross-section, an outer diameter of the core flow channel is 50 to 5,000 μm, and wherein the larger particles have a 2.5 times larger diameter than a volume average diameter of the particles in the particle-dispersed liquid.

2. The method according to claim 1 , wherein in the step of sending and removing, a core flow in the core flow channel is a laminar flow.

3. The method according to claim 1 , wherein the core flow channel makes an angle in a range of 0 to 45 degrees to a direction of gravitational or buoyant force.

4. The method according to claim 1 , wherein volume average diameter of the particles in the particle-dispersed liquid is in a range of 0.1 μm to 1,000 μm.

5. The method according to claim 1 , wherein a velocity of flow at a sending liquid portion of the particle-dispersed liquid is in a range of 1 to 1000 mm per second.

6. The method according to claim 1 , wherein a circular cross-section of the core flow channel is in a range of 10 to 4000 times as large as a volume average diameter of the particles in the particle-dispersed liquid.

7. The method according to claim 1 , wherein a specific gravity of the particles is in a range of 0.87 to 21 times as large as that of a medium liquid of the particle-dispersed liquid.

8. The method according to claim 1 , wherein a content of the particles in the particle-dispersed liquid is in a range of 0.1 to 60 vol. %.

9. A method of producing a particle-dispersed liquid, using a micro-channel having a core flow channel, comprising:

sending the particle-dispersed liquid containing indeterminately shaped particles to an inner portion of the core flow channel;

separating and removing the indeterminately shaped particles from the particle-dispersed liquid based on an outward force resulting from a velocity gradient of the particle-dispersed liquid; and

sending the removed indeterminately shaped particles to an outermost part of the core flow channel;

wherein the core flow channel is circular in cross-section, an outer diameter of the core flow channel is 50 to 5,000 μm, and a form factor,

SF

1

=

(

ML

)

2

A

π

4

100

of the indeterminately shaped particles is 20 or more larger than an average form factor of the particles in the particle-dispersed liquid.

10. The method according to claim 9 , wherein in the step of sending and removing, a core flow in the core flow channel is a laminar flow.

11. The method according to claim 9 , wherein the core flow channel makes an angle in a range of 0 to 45 degrees to a direction of gravitational or buoyant force.

12. The method according to claim 9 , wherein volume average diameter of the particles in the particle-dispersed liquid is in a range of 0.1 μm to 1,000 μm.

13. The method according to claim 9 , wherein a velocity of flow at a sending liquid portion of the particle-dispersed liquid is in a range of 1 to 1000 mm per second.

14. The method according to claim 9 , wherein a circular cross-section of the core flow channel is in a range of 10 to 4000 times as large as a volume average diameter of the particles in the particle-dispersed liquid.

15. The method according to claim 9 , wherein a specific gravity of the particles is in a range of 0.87 to 21 times as large as that of a medium liquid of the particle-dispersed liquid.

16. The method according to claim 9 , wherein a content of the particles in the particle-dispersed liquid is in a range of 0.1 to 60 vol. %.

Assignments (2)
CONFIRMATORY LICENSE Recorded May 24, 2011
From: NEW MEXICO STATE UNIVERSITY
To: NATIONAL INSTITUTES OF HEALTH (NIH), U.S. DEPT. OF HEALTH AND HUMAN SERVICES (DHHS), U.S. GOVERNMENT
Reel/Frame 026328/0697 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 28, 2005
From: TAKAGI, SEIICHI; OHTA, TETSUO
To: FUJI XEROX CO., LTD.
Reel/Frame 017039/0882 →
Priority Claims (1)
JP 2005-184518 · Jun 24, 2005 · national
Continuity (1)
Related Publication 20070007220A1 · Jan 11, 2007