Botanical Quick Freeze Method and System

Abstract

A method and system providing for comminution and concurrent flash freezing of botanical biomass. The botanical biomass is introduced into a pneumatic loop where it is subject to comminution and a cryogenic process within said pneumatic loop and subsequently discharged from said pneumatic loop.

Claims

1. A method for comminution and flash freezing of botanical biomass comprising of: a. introducing the botanical biomass into a pneumatic loop; b. subjecting the botanical biomass to comminution within the pneumatic loop; c. further subjecting the botanical biomass to a cryogenic process within the pneumatic loop; and d. discharging the comminuted cryogenic processed botanical biomass.

2. A system for comminution and flash freezing of botanical biomass comprising of: a. a pneumatic loop; b. a miller within the pneumatic loop to comminute botanical biomass; c. a cryogenic heat exchanger in fluid communication with the miller to move heat from the botanical biomass; and d. a diverter valve connected to an outlet of the cryogenic heat exchanger to discharge botanical biomass from the system.

3. The method of claim 1 further comprising the step of pre-screening the botanical biomass.

4. The method of claim 1 further including the step of directing the botanical biomass to a first cyclone and connecting an outlet of the first cyclone to a heat exchange.

5. The method of claim 4 further including the step of directing the output of the heat exchanger to a second cyclone.

6. The method of claim 5 further including the step of discharge ing the contents of the cyclone to a conveyor for further processing.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0012] For a detailed description of the preferred embodiment of this invention, reference will be made to the accompany drawing. FIG. 1 is a schematic flow diagram of a process and apparatus according to an embodiment of the invention

DETAILED DESCRIPTION OF AN EMBODIMENT

[0013] FIG. 1 depicts flow diagram 100 of the process of this invention. Flow diagram 100 includes feed conveyor 110 that includes outlet 120. Outlet 120 is mechanically coupled to and in mechanical conveyance communication with Inlet 130 of cyclone 140. Outlet 150 of cyclone 140 is mechanically coupled to and in pneumatic communication with Inlet 160 of radial miller 170. Outlet 180 of radial miller 170 is mechanically coupled to and in pneumatic communication with Inlet 190 of heat exchanger 200. Outlet 220 of heat exchanger 200 is mechanically coupled to and in pneumatic communication with inlet 230 of diverter valve 360. Outlet 240 of diverter valve 360 is mechanically coupled to and in pneumatic communication with inlet 250 of cyclone 140.

[0014] Outlet 260 of diverter valve 360 is mechanically coupled to and in pneumatic communication with inlet 270 of cyclone 300. Outlet 290 of cyclone 140 is mechanically coupled to and in pneumatic communication with Inlet 280 of Cyclone 300. Outlet 330 of cyclone 300 is mechanically coupled to and in mechanical conveyance communication with inlet 340 of discharge conveyor 350. Outlet 310 of cyclone 300 is mechanically coupled to and in pneumatic communication with atmospheric vent 320.

[0015] A pneumatic loop is formed via outlet 150 of cyclone 140, inlet 160 of radial miller 170, radial miller 170, Outlet 180 of radial miller 170, inlet 190 of heat exchanger 200, heat exchanger 200, outlet 220 of heat exchanger 200, inlet 230 of diverter valve 360, diverter valve 360, outlet 240 of diverter valve 360, inlet 250 of cyclone 140, and cyclone 140. The pneumatic loop will be referenced herein as the operating loop.

[0016] Again, referring to FIG. 1. and now describing in detail a method according to an embodiment of this invention.

[0017] Processing begins with initialization of the system in preparation of receiving botanical biomass including confirmation that diverter valve 360 is configured so that inlet 230 of diverter, valve 360 is in pneumatic communication with outlet 240 of diverter valve 360, radial miller 170 is operating at a sufficient speed, and the pneumatic velocity within the operating loop is stable and sufficient. The just describe initialization, resultant configuration, and intended functionality is referred to as milling cycle. Subsequent to initialization and now describing the milling cycle, previously screened botanical biomass suitable for solvent extraction and compatible with the method of this invention is received at feed conveyor 110. Botanical biomass received at feed conveyor 110 is discharged at outlet 120 of feed conveyor 110. Botanical biomass discharged at outlet 120 of feed conveyor 110 is mechanically conveyed to and received at inlet 130 of cyclone 140.

[0018] Feed conveyor 110 is of a variable conveyance rate design. The conveyance rate of feed conveyor 110 is modulated based on the pressure within the operating loop measured near, but downstream, of outlet 180 of radial miller 170. Botanical biomass from the feed source is mechanically conveyed via feed conveyor 110, Outlet 120 of feed conveyor 110, and inlet 130 of cyclone 140 into the operating loop at cyclone 140. Once a sufficient amount of botanical biomass has been introduced into the operating loop, based on the measured pressure at outlet 180 of radial miller 170, feed conveyor 110 will pause, reducing the conveyance rate to zero.

[0019] Botanical biomass received at cyclone 140 is, pneumatically conveyed via outlet 150 of cyclone 140 and inlet 160 of radial miller 170 into radial miller 170 very near the axis of rotation of radial miller 170.

[0020] Radial miller 170 is of a radial blade design. Each radial blade of radial miller 170 features a precision, replaceable, cutting blade. Radial miller 170 is designed to create both centrifugal and pneumatic forces. The centrifugal and pneumatic forces act upon both the gas and botanical biomass within radial miller 170 affecting the gas within radial miller 170 to compress at the periphery of the housing of radial miller 170 and affecting the botanical biomass to congregate at the periphery of the housing of radial miller 170. The compressed gas and the botanical biomass are subsequently discharged at Outlet 180 of radial miller 170. Outlet 180 of radial miller 170 is located principally tangent to, the axis of rotation at the periphery of the housing of radial miller 170.

[0021] Outlet 180 of radial miller 170 features a cutting blade designed to interface with the cutting blade of the radial blade feature of radial miller 170. As botanical biomass transitions from the interior portion of the housing of radial miller 170 to outlet 180 it is exposed to the interfacing cutting blade of outlet 180 and the cutting blade of the radial blade of radial miller 170.

[0022] Radial miller 170 may feature one or more radial blades. Additionally, outlet 180 of radial miller 170 may future one or more cutting blades.

[0023] The gas and botanical biomass discharged at outlet 180 of radial miller 170 is pneumatically conveyed to and received at inlet 190 of heat exchanger 200.

[0024] Heat exchanger 200 is of a cryogenic design where a cryogenic liquid, such as cotton dioxide or nitrogen is sprayed, in a fine mist, onto the exposed surfaces of the milled botanical biomass. Heat exchanger 200 is of sufficient capacity to flash freeze the botanical biomass as it passes through heat exchanger 200.

[0025] Flash freezing is a known art and commonly used in biomass preparation such as fruits and vegetables for human consumption.

[0026] The compressed gas and flash frozen botanical biomass are discharged at outlet 220 of heat exchanger 200. The compressed gas and flash frozen botanical biomass discharged at outlet 220 of heat exchanger 240 is pneumatically conveyed to and received at inlet 230 of diverter valve 360. As previously disclosed, diverter valve 360 is configured, during milling operations, to discharge at outlet 240. Compressed gas and botanical biomass discharged at outlet 240 of diverter valve 360 is pneumatically conveyed to and received at inlet 250 of cyclone 140.

[0027] Cyclone 140 allows for the velocity of the pneumatic transport gas and the gas produced by the evaporating cryogenic fluid to slow sufficiently enough to no longer support conveyance of the botanical biomass. Cyclone 140 is vented to atmosphere via outlet 290 of cyclone 140, inlet 280 of cyclone 300, cyclone 300, outlet 310 of cyclone 300, and atmospheric vent 320. Cyclone 300 is vented to atmosphere via outlet 310 and atmospheric vent 320 to allow pressure equilibrium within the pneumatic loop.

[0028] Botanical biomass received at inlet 250 of cyclone 140 is discharged at outlet 150 of cyclone 140. Botanical biomass discharged at outlet 150 of cyclone 140 is pneumatically conveyed to and received at inlet 160 of radial miller 170.

[0029] Botanical biomass will continue to loop through the described operating loop for a certain amount of time with each loop causing a certain size reduction of the botanical biomass.

[0030] After a sufficient amount of time necessary to reduce the botanical biomass to an optimal extraction size, diverter valve 360 is configured to discharge at outlet 260.

[0031] This configuration where diverter valve 360 is configured to discharge at outlet 260 is herein referred to as the discharge cycle.

[0032] Compressed gas and botanical biomass discharged at outlet 260 of diverter valve 360 is pneumatically conveyed to and received at inlet 270 of cyclone 300.

[0033] Cyclone 300 allows for the velocity of the pneumatic transport gas and the gas produced by the evaporating cryogenic fluid to slow sufficiently enough to no longer support conveyance of the botanical biomass. Cyclone 300 is vented to atmosphere via outlet 310 of cyclone 300 and atmospheric vent 320.

[0034] Botanical biomass received at runlet 270 of cyclone 300 is discharged at outlet 330 of cyclone 300. Botanical biomass discharged at outlet 330 of cyclone 300 is conveyed to and received at Inlet 340 of discharge conveyor 350.

[0035] The just described cycles where the system of the invention is first configured for a milling cycle and subsequently configured for a discharge cycle constitutes one complete batch cycle. As many batch cycles as necessary to meet the demands of production requirements are completed in a fully automated, computer-controlled sequence.

[0036] Utilizing the new and unique features of the current invention provides for a fully automatic method and system to precisely control the comminution and concurrent flash freezing of botanical biomass in preparation for a solvent extraction process.

[0037] Although the present invention and its advantages have been described in detail, it should be understood that various changes, substitutions and alterations may be made herein without departing from the spirit and scope of the invention as defined by the appended claims.