What is claimed is:
1. An apparatus for the separation of a desired product from a supercritical fluid extraction solution, comprising
(a) a restrictor nozzle through which the supercritical fluid extraction solution passes and which causes decompression of the solution;
(b) a coarse-pore sintered-glass or sintered metal enclosure member surrounding the restrictor nozzle and at which the decompressed fluid stream is directed, the coarse-pore sintered-glass enclosure member being saturated with an oil; and
(c) collecting means for collecting an oil suspension of a desired product.
2. An apparatus as defined by claim 1, further including a separation vessel in which the restrictor nozzle, the enclosure member and the collecting means are arranged.
3. An apparatus as defined by claim 2, further including an oil inlet for supplying oil to the enclosure member, an oil suspension outlet, and a water outlet.
4. An apparatus as defined by claim 3, further including means for continuously monitoring the concentration of a desired product in the collected oil suspension and means for activating the oil suspension outlet when a predetermined concentration of desired product is detected in the collected oil suspension.
5. An apparatus as defined by claim 4, wherein the continuous concentration monitoring means comprises an ultraviolet-visible sensor and spectrophotometer.
6. An apparatus as defined by claim 3, further including means for monitoring the moisture content of the collected oil suspension and means for actuating the water outlet when a predetermined moisture content is detected in the collected oil suspension.
7. An apparatus as defined by claim 6, wherein the moisture content monitoring means comprises conductivity sensor and measuring means.
8. An apparatus as defined by claim 2, wherein the separation vessel includes a gas outlet for gaseous components of the decompressed solution which pass through the coarse-pore enclosure member.
9. A method for the separation of a desired product from a supercritical fluid extraction solution, comprising
(a) decompressing the supercritical fluid extraction solution by passing it through a restrictor nozzle;
(b) directing the decompressed fluid stream at a coarse-pore sintered-glass or sintered metal enclosure member which is saturated with a oil in which the desired product is soluble, causing gaseous solvent to escape through the coarse pores of the enclosure member and at least one solute comprising the desired product to dissolve in the oil; and
(c) collecting the oil containing the desired product.
10. A method as defined by claim 9, wherein the oil containing the desired product is collected in a separation vessel
11. A method as defined by claim 10, further including continuously monitoring the concentration of the desired product in the collected oil and removing oil containing the desired product from the separation vessel once a predetermined concentration of desired product is detected in the collected oil.
12. A method as defined by claim 11, wnerein the concentration of desired product is monitored by an ultraviolet-visible spectrophotometer.
13. A method as defined by claim 10, wherein carryover water from the supercritical fluid extraction solution is collected in a water layer located under a layer of the collected oil.
14. A method as defined by claim 10, further including monitoring the moisture content of the collected oil and removing collected water from the separation vessel once a predetermined moisture content is detected in the collected oil.
15. A method as defined by claim 14, wherein the moisture content is monitored by a conductivity measuring means.
16. A method as defined by claim 9, wherein the desired product comprises .beta.-carotene.
17. A method as defined by claim 16, wherein the supercritical fluid extraction solution comprises .beta.-carotene in carbon dioxide.
18. A method as defined by claim 16, wherein the oil comprises cottonseed oil.
19. A method as defined by claim 9, wherein the method is conducted at ambient pressure and temperature.
20. A method as defined by claim 9, wherein the method is conducted at an elevated temperature and pressure.