IP Library › Granted Patent US 10,130,950
Granted Patent B2
US 10,130,950 · App. 15/039,637 · Granted Nov 20, 2018

Microfluidic droplet packing

Inventors: Tony Hung (Cambridge, MA); Sepehr Kiani (Watertown, MA); Scott Powers (Cambridge, MA); Adnan Esmail (Boston, MA)
Assignee: Bio-Rad Laboratories, Inc.
B01L3/502784B01J19/0093B01L3/502715B01J2219/0086B01J2219/00783B01J2219/00792B01J2219/00828B01J2219/00831B01J2219/00833B01J2219/00837B01J2219/00855B01J2219/00873B01J2219/00889B01J2219/00894B01J2219/00903B01J2219/00934B01L3/502776B01L7/525B01L2200/0673B01L2300/0816B01L2300/0858B01L2300/0867B01L2400/0487
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Quick Facts
Patent No.
US 10,130,950
App. No.
15/039,637
Granted
Nov 20, 2018
Kind
B2
Abstract

Systems and methods for confining droplets within a microfluidic channel as well as systems and methods for packing droplets are provided. More specifically, a system and method are provided for controlling the introduction and removal of oil into a microfluidic channel in order to control where drops are allowed to flow within that channel.

Claims (17)

1. A method of controlling aqueous droplets in an emulsion comprising a non-aqueous continuous fluid, the method comprising,

providing a microfluidic channel defined by two substantially parallel or non-parallel walls, wherein each wall comprises two or more opposing ports, wherein said microfluidic channel contains an emulsion comprising aqueous droplets in the continuous non-aqueous fluid, and wherein the two or more opposing ports include an upstream port and a downstream port and wherein the upstream port in each wall introduces non-emulsion continuous non-aqueous fluid into the microfluidic channel at a first pressure and wherein the downstream port in each wall introduces non-emulsion continuous non-aqueous fluid into the microfluidic channel at a second pressure;

causing the emulsion to flow from an upstream position in the microfluidic channel to a downstream position in the channel while introducing non-emulsion continuous non-aqueous fluid into the microfluidic channel from the ports, such that the aqueous droplets in the emulsion are moved away from the walls of the microfluidic channel at the downstream position and are more densely packed at the downstream position compared to the upstream position.

2. The method of claim 1 , wherein non-emulsion continuous non-aqueous fluid from one or more port on a first wall of the microfluidic channel flows at a higher pressure than non-emulsion continuous non-aqueous fluid from port(s) of the opposing wall such that a majority of droplets at the downstream position are closer to the opposing wall than to the first wall of the microfluidic channel.

3. The method of claim 1 , wherein the first pressure and the second pressure are the same.

4. The method of claim 1 , wherein the first pressure is higher than the second pressure.

5. The method of claim 1 , wherein the first pressure is lower than the second pressure.

6. The method of any of claim 1 , wherein the ports provide fluid communication between the microfluidic channel and one or more side channels, wherein the side channels and the microfluidic channel form an angle less than 90 degrees as measured from the side channel and the upstream portion of the microfluidic channel.

7. The method of claim 6 , wherein the angle is between 30-60 degrees.

8. A method of removing continuous non-aqueous fluid from an emulsion, the method comprising

providing a microfluidic channel defined by two substantially parallel walls, wherein at least one wall comprises one or more port(s), wherein the ports provide fluid communication between the microfluidic channel and one or more side channels, wherein said microfluidic channel contains an emulsion comprising aqueous droplets in the continuous non-aqueous fluid;

causing the emulsion to flow from an upstream position in the microfluidic channel to a downstream position in the microfluidic channel while removing non-emulsion continuous non-aqueous fluid from the emulsion in the microfluidic channel via the port(s), wherein opposing walls of the side channels are parallel and the microfluidic channel form angles less than 90 degrees as measured from the side channel and the upstream position of the microfluidic channel, thereby removing continuous non-aqueous fluid from the emulsion.

9. The method of claim 8 , wherein the angle is between 30-60 degrees.

10. The method of claim 8 , further comprising providing at the downstream position a fluid pressure opposing the flow of the emulsion, thereby packing the droplets of the emulsion into a more dense arrangement than occurred at the upstream position.

11. The method of claim 10 , wherein the fluid pressure is provided by a fluid inserted into the microfluidic channel by a downstream port in fluid communication with the microfluidic channel.

12. The method of claim 11 , wherein the fluid inserted by the downstream port is a continuous non-aqueous fluid.

13. The method of claim 11 , wherein the fluid is an aqueous fluid.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 27, 2017
From: GNUBIO INC
To: BIO-RAD LABORATORIES, INC
Reel/Frame 043121/0324 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 17, 2017
From: HUNG, TONY; KIANI, SEPEHR; POWERS, SCOTT; ESMAIL, ADNAN
To: GNUBIO INC
Reel/Frame 042411/0028 →
Continuity (3)
Provisional Application 61909543 · Nov 27, 2013
Provisional Application 61934190 · Jan 31, 2014
Related Publication 20170165669A1 · Jun 15, 2017
Cited By (6)
US 12,252,745 US 12,265,088 US 12,270,815 US 12,319,964 US 12,540,948 US 12,631,651