Catalyzing pressure wave extraction method and apparatus
Apparatus and methods are provided for extracting compounds from raw materials. One such apparatus may include an extraction column where it is a one column, one pass design capable of withstanding high temperatures and pressure. Additionally, the extraction column may also be capable of containing a self-perpetuating energy cycle used to achieve the required solubilization and mass transfer temperatures necessary for optimal extraction. The apparatus may also include a first opening and a second opening to control the flow of incoming solvent and filter extraneous sediment trapped within the fully extracted effluent. Additionally, the apparatus may be configured to create a self-perpetuating and self-sustaining energy cycle by manipulating the pressure and temperature generated within the apparatus. While the generated temperatures may help achieve a dynamic and efficient extraction process, a trailing cool layer of solvent is also present to effectively preserve the heat sensitive compounds extracted from the raw materials.
1. A method of extracting a compound from a raw material comprising:
distributing an incoming flow of solvent entering a base of an extraction column via a hydraulic force, the solvent having an inlet temperature between an ambient temperature of a source of the solvent and 160° F., wherein the incoming flow of solvent enters the base of the extraction column under pressure and flows through two or more restrictive perforated disks that break the turbulent flow of solvent creating a substantially flat, solvent surface layer that continuously remains substantially flat as the solvent rises up the extraction column to extract under pressure an evenly packed column of raw materials, wherein said incoming flow of solvent under pressure generates heat as the solvent rises up the evenly packed column of raw materials.
2. The method of claim 1 , further comprising penetrating the raw materials with the upward flow of solvent propelled by hydraulic force, such that the hydraulic force compresses the raw materials.
3. The method of claim 2 , further comprising releasing carbon dioxide and/or other gasses from the raw materials as the raw materials become compressed, wherein releasing the carbon dioxide and/or other gases causes the raw materials to become further compressed resulting in frictional forces to generate thermal energy, such that heat from thermal energy causes the carbon dioxide and/or other gases to expand and close off nearby interstitial spaces and low resistance migration channels within the raw materials.
4. The method of claim 3 , further comprising locking the raw materials to a side of the extraction column as a result of a first coefficient of friction generated from static friction between the raw materials and the side of the extraction column, wherein the raw materials break free and disengage from the side of the extraction column and proceed upward when the hydraulic force beneath the solvent surface layer overcomes the first coefficient of friction.
5. The method of claim 4 , wherein the raw materials reengage with the side of the extraction column when a second coefficient of friction locks the raw materials to the side of the extraction column vis static friction, such that the solvent surface layer driven by greater inertia proceeds to penetrate again, but more deeply each time, into the raw materials causing a greater release of thermal energy and carbon dioxide and/or other gases with each successive repetition.
6. The method of claim 5 , wherein the greater release of more thermal energy and carbon dioxide and/or other gases results in further compression of the raw materials to be more heavily compresses as the interstitial spaces and low resistance migration channels become more closed so that greater resistance to flow and backpressure is created within the extraction column, thus requiring greater hydraulic pressure and inertia beneath the solvent surface layer to overcome the repetition of friction coefficients being produced at a boundary and reactive layers.
7. The method of claim 1 , wherein a self-perpetuating energy cycle is generated from a hydraulic compression of the raw materials, such that each subsequent energy cycle with the self-perpetuating energy cycle releases greater energy.
8. The method of claim 7 , wherein the self-perpetuating energy cycle plateaus when a hydraulic pressure at the solvent surface layer equals a predetermined pressure range, wherein the predetermined pressure range is selected to achieve an optimal temperature range that allows the raw materials near the solvent surface layer to achieve full saturation and equilibrium with the solvent.