Method and device for transporting powders
A method for transporting non-flowable powders includes the following steps: mixing and suspending powders and carbon dioxide in the solid form, with the introduction of a cryogenic fluid, to obtain a cryogenic suspension; setting the cryogenic suspension in motion to enable transport thereof, controlling the motion of the cryogenic suspension according to one or more parameter(s) related to the first mixing and suspending step.
1 . A method for transporting non-flowable powders, wherein it includes the following steps:
a) mixing and suspending powders and carbon dioxide in the solid form (CO 2 (s)), with the introduction of a cryogenic fluid, to obtain a cryogenic suspension, the volumetric mass proportions of the powders and of the carbon dioxide (CO 2 (s)) meeting the following equation (i):
40%<[powders] vol +[CO 2 (s)] vol <80%, (i):
where:
[powders] vol is the volumetric mass proportion of the powders,
[CO 2 (s)] vol is the volumetric mass proportion of carbon dioxide in the solid form (CO 2 (s)),
b) setting the cryogenic suspension in motion to enable transport thereof,
c) controlling the motion of the cryogenic suspension according to one or more parameter(s) (Co) related to the mixing and suspending step a).
2 . The method according to claim 1 , wherein it includes step a′) of weighing the powders to be transported and step a″) of weighing the carbon dioxide in the solid form (CO 2 (s)), steps a′) and a″) being prior to the mixing and suspending step a).
3 . The method according to claim 1 , wherein step b) of setting the cryogenic suspension in motion comprises depressurising, pumping or pressurising the cryogenic suspension.
4 . The method according to claim 1 , wherein step c) of controlling the motion of the cryogenic suspension comprises step c′) of acquiring and processing the measurement of the stirring torque (Co) of the cryogenic suspension.
5 . The method according to claim 1 , wherein step c) of controlling the motion of the cryogenic suspension comprises step c″) of measuring the pressure and/or the opening of a pump performed during step b) of setting the cryogenic suspension in motion.
6 . The method according to claim 1 , wherein step b) of setting the cryogenic suspension in motion is followed by a transport step d) and a phase separation step e) to obtain transported powders (Pt) and the implementing of a step f) for recycling the cryogenic fluid.
7 . The method according to claim 1 , wherein the average diameter of the particle size of the carbon dioxide in the solid form (CO 2 (s)) is comprised between 0.1 and 10 times that of the particle size of the powders to be transported.
8 . The method according to claim 1 , wherein the carbon dioxide charge level in the solid form (CO 2 (s)) is comprised between 0.1 and 10 times that of the powders to be transported.
9 . The method according to claim 1 , wherein the viscosity of the cryogenic suspension as a function of the charge level and of the particle size of the constituent solid of this cryogenic suspension is expressed by the following equation (ii):
μ/μ 0 =(1+½ ·[N ]·Φ/(1−Φ/Φ m ) 2 , (ii):
where:
μ is the viscosity of the cryogenic suspension;
μ 0 is the viscosity of the liquid phase;
[N] is a constant;
Φ is the volume of solid in the volume of the cryogenic suspension;
Φ m is the maximum volume of solid in the volume of the cryogenic suspension.
10 . A device for transporting non-flowable powders, for the implementation of the method according to claim 1 , including:
a system for mixing and suspending powders, carbon dioxide in the solid form (CO 2 (s)) and cryogenic fluid to form the cryogenic suspension,
a system for setting the cryogenic suspension in motion,
a system for controlling the motion of the cryogenic suspension,
wherein the mixing and suspending system comprises:
a mixing tank,
a mixing and blending device, located inside the mixing tank,
means for the controlled introduction of the powders to be transported and of carbon dioxide in the solid form (CO 2 (s)) into the mixing tank,
a means for measuring the level of the formed cryogenic suspension, located at least partially inside the mixing tank.
11 . The device according to claim 10 , wherein the system for setting the cryogenic suspension in motion comprises a pressure difference transport device.
12 . The device according to claim 11 , wherein the pressure difference transport device comprises means for pressurising, pumping or depressurising the cryogenic suspension.