Condensible gas botanical extraction systems and methods

1. Apparatus for the extraction of compounds from botanical material, the apparatus comprising:

(a) an extraction chamber;

(b) a first cyclonic separation stage comprising at least one first stage cyclonic separator wherein the at least one first stage cyclonic separator is configured to remove a first series of extracted compounds comprising terpenes having a first average molecular weight from a first solvent stream obtained from the extraction chamber;

(c) a first solvent flow path extending from the extraction chamber to the first cyclonic separation stage;

(d) a second cyclonic separation stage comprising at least one second stage cyclonic separator wherein the at least one second stage cyclonic separator is configured to remove a second series of extracted compounds from a second solvent stream obtained from the extraction chamber wherein the second series of extracted compounds comprising terpenes and has a second average molecular weight that is higher than the first average molecular weight;

(e) a second solvent flow path extending from the extraction chamber to the second cyclonic separation stage; and

(f) at least one first sonic flow nozzle positioned in the first solvent flow path adjacent a first fluid inlet of the at least one corresponding first stage cyclonic separator and/or at least one second sonic flow nozzle positioned in the second solvent flow path adjacent a second fluid inlet of the at least one corresponding second stage cyclonic separator.

2. The apparatus of claim 1 , further comprising:

a third cyclonic separation stage comprising at least one third stage cyclonic separator wherein the at least one third cyclonic stage separator is configured to remove a third series of extracted compounds from a solvent stream wherein the third series of extracted compounds comprises terpenes and has a third average molecular weight that is higher than the second average molecular weight;

a third solvent flow path extending from the extraction chamber to the third cyclonic separation stage; and

at least one third sonic flow nozzle positioned in the third solvent flow path adjacent a third fluid inlet of the at least one corresponding third stage cyclonic separator.

3. The apparatus of claim 2 , wherein solvent obtained from the extraction chamber rotates at a first speed in the at least one first stage cyclonic separator, solvent obtained from the extraction chamber rotates at a second speed in the at least one second stage cyclonic separator wherein the second speed is different than the first speed, and solvent obtained from the extraction chamber rotates at a third speed in the at least one third cyclonic separator wherein the third speed is different than the first speed and the second speed.

4. The apparatus of claim 2 , further comprising at least one third solvent return path extending from a third fluid outlet of the corresponding at least one third stage cyclonic separator to the extraction chamber.

5. The apparatus of claim 1 , wherein solvent obtained from the extraction chamber rotates at a first speed in the at least one first stage cyclonic separator and solvent obtained from the extraction chamber rotates at a second speed in the at least one second stage cyclonic separator wherein the second speed is different than the first speed.

6. The apparatus of claim 1 , wherein the first average molecular weight is lighter than the second average molecular weight and solvent obtained from the extraction chamber rotates at a first speed in the at least one first stage cyclonic separator and solvent obtained from the extraction chamber rotates at a second higher speed in the at least one second stage cyclonic separator.

7. The apparatus of claim 1 , wherein the at least one first sonic flow nozzle is positioned at an upstream end of the first fluid inlet whereby the solvent passing through the at least one first sonic flow nozzle enters the corresponding at least one first stage cyclonic separator at sonic velocity and/or the at least one second sonic flow nozzle is positioned at an upstream end of the second fluid inlet whereby the solvent passing through the at least one second sonic flow nozzle enters the corresponding at least one second stage cyclonic separator at sonic velocity.

8. The apparatus of claim 1 , wherein the at least one first sonic flow nozzle comprises the first fluid inlet of the corresponding at least one first stage cyclonic separator and/or the at least one second sonic flow nozzle comprises the second fluid inlet of the corresponding at least one second stage cyclonic separator.

9. The apparatus of claim 1 , further comprising at least one first solvent return path extending from a first fluid outlet of the corresponding at least one first stage cyclonic separator to the extraction chamber and/or at least one second solvent return path extending from a second fluid outlet of the corresponding at least one second stage cyclonic separator to the extraction chamber.

10. An apparatus for the extraction of compounds from botanical material, the apparatus comprising:

(a) an extraction chamber;

(b) a first cyclonic separation stage comprising at least one first stage cyclonic separator wherein the at least one first stage cyclonic separator is configured to remove a first series of extracted compounds comprising terpenes having a first average molecular weight from a solvent stream obtained from the extraction chamber;

(c) a first solvent flow path extending from the extraction chamber to the first cyclonic separation stage;

(d) a second cyclonic separation stage comprising at least one second stage cyclonic separator wherein the at least one second stage cyclonic separator is configured to remove a second series of extracted compounds comprising terpenes_from a solvent stream obtained from the first cyclonic separation stage wherein the second series of extracted compounds has a second average molecular weight that is lower than the first average molecular weight;

(e) a second solvent flow path extending from the first cyclonic separation stage to the second cyclonic separation stage; and

(f) at least one first sonic flow nozzle positioned in the first solvent flow path adjacent a first fluid inlet of the at least one corresponding first stage cyclonic separator and/or at least one second sonic flow nozzle positioned in the second solvent flow path adjacent a second fluid inlet of the at least one corresponding second stage cyclonic separator.

11. The apparatus of claim 10 , further comprising:

a third cyclonic separation stage comprising at least one third stage cyclonic separator wherein the at least one third cyclonic stage separator is configured to remove a third series of extracted compounds from a solvent stream wherein the third series of extracted compounds has a third average molecular weight that is lighter than the second average molecular weight; and,

a third solvent flow path extending from the second cyclonic separation stage to the third cyclonic separation stage.

12. The apparatus of claim 11 , wherein solvent obtained from the extraction chamber rotates at a first speed in the at least one first stage cyclonic separator, solvent obtained from the extraction chamber rotates at a second speed in the at least one second stage cyclonic separator wherein the second speed is higher than the first speed, and solvent obtained from the extraction chamber rotates at a third speed in the at least one third cyclonic separator wherein the third speed is higher than the second speed.

13. The apparatus of claim 10 , wherein solvent obtained from the extraction chamber rotates at a first speed in the at least one first stage cyclonic separator and solvent obtained from the extraction chamber rotates at a second speed in the at least one second stage cyclonic separator wherein the second speed is higher than the first speed.

14. An apparatus for the extraction of compounds from botanical material, the apparatus comprising:

(a) an extraction chamber having a solvent outlet;

(b) a cyclonic separator comprising a cyclone chamber having a cyclonic tangential fluid inlet and a fluid outlet;

(c) a solvent flow path extending from the solvent outlet of the extraction chamber to the cyclonic tangential fluid inlet; and

(d) a sonic flow nozzle positioned in the solvent flow path adjacent the cyclonic tangential fluid inlet.

15. The apparatus of claim 14 , wherein the sonic flow nozzle is positioned at an upstream end of the cyclonic tangential fluid inlet whereby the solvent passing through the sonic flow nozzle enters the cyclone chamber at sonic velocity.

16. The apparatus of claim 15 , wherein the sonic flow nozzle comprises the cyclonic tangential fluid inlet.

17. The apparatus of claim 14 , wherein the extraction chamber is operated below 0o C and with the solvent in a liquid or a supercritical phase, and the solvent flow path further comprises a heater proximate an inlet of the sonic flow nozzle wherein the solvent exiting the heater is gaseous.

18. The apparatus of claim 14 , further comprising a solvent return path extending from the fluid outlet of the cyclonic separator to the extraction chamber.

19. The apparatus of claim 14 , wherein the outlet of the sonic flow nozzle is positioned at an inlet port of the cyclone separator.