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The present invention pertains to methods and apparatus for removal of one or more solutes from a supercritical process solution. Solute additives and contaminants are removed from supercritical processing solutions via a contaminant removal system that is either part of the process vessel itself or

The present invention pertains to methods and apparatus for removal of one or more solutes from a supercritical process solution. Solute additives and contaminants are removed from supercritical processing solutions via a contaminant removal system that is either part of the process vessel itself or is part of a local recirculation loop in fluid communication with the process vessel. This invention provides supercritical processing methods and apparatus for the removal of additives and contaminants during circulation so that depressurization and substrate removal can occur without contamination. The removal in some cases, for example cleaning residue, can be done continuously during a process to improve its efficiency. Removal mechanisms may include separation, destruction, conversion of the contaminant to acceptable species, or combinations thereof.

대표청구항 ▼

1. An apparatus for removing one or more solutes from a supercritical solution, the apparatus comprising:a process vessel configured to treat semiconductor wafers with the supercritical solution;a supercritical solution generator directly connected to the process vessel;a recirculation loop coupled

1. An apparatus for removing one or more solutes from a supercritical solution, the apparatus comprising:a process vessel configured to treat semiconductor wafers with the supercritical solution;a supercritical solution generator directly connected to the process vessel;a recirculation loop coupled to the process vessel and allowing fluid communication with the process vessel; anda contaminant removal mechanism for removing said one or more solutes from the supercritical solution to provide a purified solvent,wherein at least one of the process vessel and the recirculation loop comprise components of the containment removal mechanism. 2. The apparatus of claim 1, wherein the process vessel includes components of the contaminant removal mechanism. 3. The apparatus of claim 1, wherein the purified solvent is a supercritical solvent. 4. The apparatus of claim 1, wherein the contaminant removal system consists of at least one of an irradiation mechanism, a heating mechanism, a cooling mechanism, a pressurization mechanism, a depressurization mechanism, a chemical addition mechanism, a filtration mechanism, a phase transfer mechanism, and a fluid pumping mechanism. 5. The apparatus of claim 4, wherein the chemical addition mechanism is configured to introduce a liquid to the supercritical processing solution without loss of supercritical conditions within the process vessel or the recirculation loop. 6. The apparatus of claim 4, wherein the filtration mechanism consists of at least one of an adsorbent, a semipermeable membrane, a sieve, a zeolite, a molecular sieve, a nanotube composite, a ceramic filter, and a sintered metal filter. 7. The apparatus of claim 5, wherein the adsorbent consists of at least one of activated carbon, a zeolite, an ion exchange resin, and a polymeric resin. 8. The apparatus of claim 4, wherein the irradiation mechanism consist of at least one of an ultraviolet light source, a high intensity discharge source, and a visible to near IR source. 9. The apparatus of claim 4, wherein the heating mechanisms consists of at least one of internal electrical or heating fluid circulation coils, external electrical or heating fluid circulation coils, a tube in tube heat exchanger, a shell and tube heat exchanger, and a radiative heating mechanism. 10. The apparatus of claim 4, wherein the cooling mechanism consists of at least one of an internal or circulated cooling fluid coils, refridgeration coils, and an evaporative cooling mechanism. 11. The apparatus of claim 4, wherein the contaminant removal mechanism comprises a primary removal mechanism for removing between about 51 and 99% of the one or more solutes, and a secondary removal mechanism for further purifying the process fluid by removing substantially all of the one or more solutes that remain in the fluid after the first removal mechanism. 12. The apparatus of claim 5, wherein the chemical addition mechanism comprises a pump or compressor configured to deliver the liquid uni-directionally to the supercritical solution such that supercritical conditions are not lost during chemical addition to the supercritical solution. 13. The apparatus of claim 1, wherein the recirculation loop comprises valves for isolating the recirculation loop from fluid communication with the process vessel. 14. The apparatus of claim 1, wherein the recirculation loop is part of a primary circulation loop, said primary circulation loop configured for adding the one or more solutes to a supercritical solvent in order to form the supercritical solution and recirculating the supercritical solution through the process vessel, said recirculation loop comprising the contaminant removal mechanism. 15. The apparatus of claim 14, wherein the recirculation loop comprises valves for isolating the recirculation loop from fluid communication with the primary circulation loop. 16. A method of removing one or more solutes from a supercritical processing solution, the method comprising:generating a s upercritical processing solution in a supercritical solution generator that is directly connected to a process vessel;flowing the supercritical processing solution through the process vessel and a recirculation loop, at least one of the process vessel and the recirculation loop comprising components of a contaminant removal mechanism;removing at least a portion of said one or more solutes with the contaminant removal mechanism to produce a purified solvent, said purified solvent having a reduced concentration of the one or more solutes; andrecirculating the purified solvent through the process vessel and the recirculation loop;wherein removing at least a portion of said one more contaminants with the contaminant removal mechanism comprises exposing the supercritical processing solution to a set of conditions which separate the portion of said one or more solutes from the supercritical processing solution to produce the purified solvent and a contaminant phase. 17. The method of claim 16, wherein the purified solvent is a supercritical solvent. 18. The method of claim 16, wherein the set of conditions consists of at least one of heating, cooling, irradiation, pressurization, depressurization, chemical addition, filtration, adsorption, oxidation, reduction, precipitation, and combinations thereof. 19. The method of claim 18, wherein chemical addition consist of introducing at least one of a reagent, a reactant, and a catalyst to the supercritical processing solution. 20. The method of claim 19, wherein the reagent consists of at least one of a complexing agent, a solvent, an antisolvent, a catalyst, an adsorbent, and a surfactant. 21. The method of clam 19 , wherein the reactant or the catalyst consist of at least one of an oxidant, a reductant, an acid, a base, a nucleophile, an electophile, a free radical source, a radical initiator, a metal, and a metal oxide. 22. The method of claim 21, wherein the oxidant consists of at least one of hydrogen peroxide, oxygen, ozone, water, an organic peroxide, a peroxide generator, and a hydroxyl radical generator. 23. The method of claim 21, wherein the catalyst consists of at least one of titanium dioxide, metal oxides, metal/metal oxide mixtures, substrate supported precious metals, tetrabutylammonium fluoride, di-tert-butylperoxide, azoisobis-butyromitrile, dicumyl peroxide, an organic acid, an activated carbon supported catalyst, an enzyme, Ziegler-Nalta catalyst, a free radical generator or initiator, and a phase transfer catalyst. 24. The method of claim 21, wherein the acid consists of at least one of a mineral acid and an organic acid. 25. The method of claim 21, wherein the base consists of at least one of ammonium hydroxide, ammonia, an alki ammonium hydroxide, an amine, and a metal hydroxide. 26. The method of claim 18, wherein adsorption comprises passing said supercritical processing solution through an adsorbent material selective towards the one or more solutes. 27. The method of claim 26, wherein the adsorbent material consists of at least one of activated carbon, a zeolite, an ion exchange resin, and a polymeric resin. 28. The method of claim 18, wherein filtration comprises passing said supercritical processing solution through filtration mechanism, said filtration mechanism selective towards the one or more solutes. 29. The method of claim 27, wherein the filtration mechanism comprises at least one element selected from a group consisting of a semi-permeable membrane, a zeolite, a molecular sieve, a nanotube composite, a ceramic filter, and a sintered metal filter. 30. The method of claim 17, wherein irradiation comprises exposing the supercritical processing solution to at least one radiation selected from a list consisting of ultraviolet radiation, infrared radiation, and high intensity visible light. 31. Tho method of claim 15, wherein conditions which separate the portion of said one or more solutes from the supercritical processing solution to produce the purified s olvent and the contaminant phase comprise converting said one or more solutes to other solute species in situ. 32. An apparatus for removing one or more solutes from a supercritical solution, the apparatus comprising:a process vessel having a flow inlet and a flow outlet and configured to treat semiconductor wafers with the supercritical solution;a contaminant removal mechanism for removing one or more solutes from the supercritical solution to provide a purified solvent, the contaminant removal mechanism including:a single inlet connecting the flow outlet of the process vessel and the contaminant removal system; anda single outlet connecting the flow inlet of the process vessel and the contaminant removal system; anda recirculation loop coupled to the process vessel and allowing supercritical solution to flow in and out of the process vessel,wherein at least one of the process vessel and the recirculation loop comprise components of the contaminant removal mechanism.