Device and method for handling a particle suspension

1. A device for handling a particle suspension comprising:

i. at least one channel for flowing the particle suspension, wherein the channel has an average cross-section comprised between 0.1 mm 2 and 9 mm 2 and a standard hydraulic resistance of less than 1013 Pa·s/m 3 , wherein at least a portion of the channel representing half of the length of the channel is compacted in such a way that the largest distance between two points of the volume occupied by the portion of the channel is less than half of the total length of the channel;

ii. a pumping unit configured to move a driving fluid for driving the particle suspension in the channel, wherein the driving fluid is separated from the particle suspension by an interface; and

iii. control means for programmed to control the pumping unit as a function of the position of the interface along the channel, the position of the interface being monitored and/or, in the case of an incompressible driving fluid, determined from the volume of the driving fluid injected in the channel by the pumping unit.

2. The device according to claim 1 , wherein the driving fluid is compressible.

3. The device according to claim 1 , wherein the interface between the driving fluid and the particle suspension is formed by a contact surface between the driving fluid and the particle suspension, the inlet of the channel being connected to a filter having a pore diameter less than or equal to 1 μm.

4. The device according to claim 1 , wherein the device comprises a fluid driven gasket in the channel, in such a way that the interface between the driving fluid and the particle suspension is formed by the fluid driven gasket.

5. The device according to claim 1 , wherein the device comprises calibrated volumetric graduations along the channel establishing a relationship between a position along the channel and a displaced volume of the particle suspension.

6. The device according to claim 1 , wherein the channel is transparent or translucent.

7. The device according to claim 1 , wherein, over at least 10% of its length, the channel is curved with a radius of curvature comprised between 2 mm and 50 mm.

8. The device according to claim 1 , wherein the channel is configured to sustain a pressurization with water of at least 0.5 bars above the ambient pressure without breakage and with a leak or permeation flow of the channel inferior to 60 μg/min per mL of the total channel volume filled with water.

9. The device according to claim 1 , wherein one end of the channel is connected to the pumping unit, and the pumping unit is capable of creating a pressure variation of at least 0.5 bar.

10. The device according to claim 1 , wherein the channel is placed within a fluid-tight container filled with a high thermal inertia fluid, or the channel is contained within a layer of thermally insulating material.

11. The device according to claim 1 , comprising at least two channels connected to a manifold at their outlets.

12. The device according to claim 1 , wherein the driving fluid is a gas.

13. A method for handling a particle suspension comprising flowing the particle suspension in or out of at least one channel by means of a driving fluid for driving the particle suspension in the channel, wherein the driving fluid is separated from the particle suspension by an interface, wherein the channel has an average cross-section comprised between 0.1 mm 2 and 9 mm 2 and a standard hydraulic resistance of less than 10 13 Pa·s/m 3 , and at least a portion of the channel representing half of the length of the channel is compacted in such a way that the largest distance between two points of the volume occupied by the portion of the channel is less than half of the total length of the channel, the method comprising moving the driving fluid by means of a pumping unit and controlling the pumping unit as a function of the position of the interface along the channel, the position of the interface being monitored and/or, in the case of an incompressible driving fluid, determined from the volume of the driving fluid injected in the channel by the pumping unit.

14. The method according to claim 13 , wherein the driving fluid is compressible.

15. The method according to claim 13 , wherein the flow rate for flowing the particle suspension in or out of the channel is, for at least one period of one second, greater than Kq*S 3/2 mL/s, where Kq is equal to ⅓ mL/s/mm 3 and S is the average cross section of the channel expressed in mm 2 .

16. The method according to claim 13 , wherein the step of flowing the particle suspension in or out of the channel is carried out by applying pulses of flow in opposite directions in the channel, each pulse having a duration of at least one second and a flow rate greater than Kq*S 3/2 mL/s, where Kq is equal to ⅓ mL/s/mm 3 and S is the channel average cross section expressed in mm 2 .

17. The method according to claim 13 , wherein position of the interface along the channel is monitored visually.

18. The method according to claim 13 , wherein position of the interface along the channel is monitored by means of a tracking system.

19. The method according to claim 13 , wherein the driving fluid is a gas.