Seed treatment method
Provided is a seed treatment method, using a composition that may be obtained extemporaneously by mixing at least one powder substance and an aqueous medium. The seed treatment method may include producing the mixture in an automatic and cyclic manner, in at least one first vessel, by introducing into same first at least a portion of the aqueous medium and next the powder substance, the latter being sucked into the aqueous medium in the vessel by a vacuum created in the vessel, at least partially draining the content of the vessel, by at least one blast of compressed gas in the vessel, to a seed treatment device where the mixture may be brought into contact with the seeds.
1. A seed treatment process, using a composition obtained extemporaneously by mixing at least one pulverulent substance and an aqueous medium, comprising the steps consisting in:
automatically and cyclically carrying out the mixing in at least a first tank by introducing into said tank first at least one portion of the aqueous medium and then the pulverulent substance, the latter being sucked into the aqueous medium in the tank by virtue of a negative pressure created in the tank,
at least partially emptying its content to a seed treatment device where the mixture is brought into contact with the seeds, said emptying being carried out by means of at least one blast of a compressed gas in the tank.
2. The process as claimed in claim 1 , wherein the pulverulent substance is a hydratable compound.
3. The process as claimed in claim 1 , wherein the volume of the mixture in the tank is less than or equal to 15 l.
4. The process as claimed in claim 1 , wherein at least one blast includes a first blast and a final blast, wherein the first blast is carried out at the latest 60 s after the end of the introduction of the pulverulent substance into the tank and the final blast is carried out at the latest 30 min after the end of the introduction of the pulverulent substance into the tank.
5. The process as claimed in claim 1 wherein the introduction of the pulverulent substance into the tank is carried out through a tapping with an internal diameter of less than or equal to 17 mm.
6. The process as claimed in claim 5 , wherein the mixture is subjected to stirring according to a condition that is weaker at the time of the at least partial emptying, compared with the sequence going from the beginning of the introduction of the pulverulent substance to the beginning of the emptying,
wherein the condition is a rotational stirring rpm (revolution per minute).
7. The process as claimed in claim 1 , wherein a minimum level of negative pressure in the tank just before the suctioning of the pulverulent substance is between −0.05 and −1 bar.
8. The process as claimed in claim 7 , wherein the minimum level of negative pressure is maintained in the tank throughout the introduction of the pulverulent substance.
9. The process as claimed in claim 1 , wherein a level of overpressure in the tank during the at least partial emptying operation is between 0.05 and 2 bar.
10. The process as claimed in claim 1 , wherein a discharging of the content of the tank is carried out at the latest 5 min after the end of the introduction of the pulverulent substance into the tank.
11. The process as claimed in claim 1 , wherein a hydration resulting from the application of the content of the tank on the seeds does not allow for the treated seeds to either agglomerate or germinate during their storage.
12. The process of claim 1 , wherein the tank is in fluidic communication with and upstream of the seed treatment device.
13. The process of claim 1 , wherein the first tank and the seed treatment device are connected.
14. The process of claim 1 , wherein the seed treatment device is directly connected to an emptying outlet on the tank.