IPC분류정보
| 국가/구분 |
United States(US) Patent
등록
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| 국제특허분류(IPC7판) |
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| 출원번호 |
UP-0613862
(2006-12-20)
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| 등록번호 |
US-7704908
(2010-05-20)
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발명자
/ 주소 |
- Matusz, Marek
- Fragnito, Richard Anthony
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| 출원인 / 주소 |
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| 인용정보 |
피인용 횟수 :
0 인용 특허 :
44 |
초록
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A method for reusing rhenium from a donor spent epoxidation catalyst, the method comprising: providing a donor comprising spent epoxidation catalyst comprising rhenium, the donor having a cumulative alkylene oxide production of 0.16 kT/m3 of the spent epoxidation catalyst or more; contacting the don
A method for reusing rhenium from a donor spent epoxidation catalyst, the method comprising: providing a donor comprising spent epoxidation catalyst comprising rhenium, the donor having a cumulative alkylene oxide production of 0.16 kT/m3 of the spent epoxidation catalyst or more; contacting the donor with an aqueous liquid to produce rhenium-depleted donor and aqueous extract comprising extracted rhenium; separating the aqueous extract and the rhenium-depleted donor; and, using the extracted rhenium as a source of rhenium in a subsequent process.
대표청구항
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We claim: 1. A method for reusing rhenium from a donor spent epoxidation catalyst, the method comprising: providing a donor comprising spent epoxidation catalyst comprising rhenium, the donor having a cumulative alkylene oxide production of 0.16 kT/m3 of the spent epoxidation catalyst or more; cont
We claim: 1. A method for reusing rhenium from a donor spent epoxidation catalyst, the method comprising: providing a donor comprising spent epoxidation catalyst comprising rhenium, the donor having a cumulative alkylene oxide production of 0.16 kT/m3 of the spent epoxidation catalyst or more; contacting the donor with an aqueous liquid to produce a rhenium-depleted donor and an aqueous extract comprising extracted rhenium; separating the aqueous extract and the rhenium-depleted donor; and, using the extracted rhenium as a source of rhenium in a subsequent process. 2. The method of claim 1 further comprising separating the extracted rhenium from the aqueous extract to produce recovered rhenium. 3. The method of claim 2 comprising removing diluent from the aqueous extract by a procedure selected from the group consisting of sublimation, distillation, concentration, and combinations thereof. 4. The method of claim 2 comprising passing the aqueous extract through a resin bed and collecting the recovered rhenium from the resin bed. 5. The method of claim 2 comprising depositing the recovered rhenium on a donee to form an epoxidation catalyst or an epoxidation catalyst precursor. 6. The method of claim 5 further comprising washing the donee before depositing the recovered rhenium on the donee. 7. The method of claim 1 further comprising depositing the extracted rhenium on a donee to form an epoxidation catalyst or an epoxidation catalyst precursor. 8. The method of claim 7 further comprising washing the donee before depositing the extracted rhenium on the donee. 9. The method of claim 7 comprising contacting the donee with a deposition mixture comprising the aqueous extract without first separating the extracted rhenium from the aqueous extract. 10. The method of claim 7 wherein the donee comprises spent epoxidation catalyst for preparing a rejuvenated epoxidation catalyst. 11. The method of claim 10 further comprising depositing silver on the donee in an amount of 0.2% w or more, based on the weight of the spent epoxidation catalyst. 12. The method of claim 10 further comprising depositing silver on the donee in an amount of 5% w or more, based on the weight of the spent epoxidation catalyst. 13. The method of claim 10 further comprising depositing on the donee one or more rejuvenating rhenium copromoter components selected from the group consisting of tungsten, chromium, molybdenum, sulfur, phosphorus, boron, and mixtures thereof. 14. The method of claim 10 further comprising depositing on the donee one or more rejuvenating further elements selected from the group consisting of nitrogen, fluorine, alkali metals, alkaline earth metals, titanium, hafnium, zirconium, vanadium, thallium, thorium, tantalum, niobium, gallium, germanium, and mixtures thereof. 15. The method of claim 10 further comprising depositing on the donee one or more rejuvenating alkali metals selected from the group consisting of lithium, cesium, and combinations thereof. 16. The method of claim 7 wherein the donee comprises a carrier material for preparing a fresh epoxidation catalyst. 17. The method of claim 16 further comprising depositing silver on the donee in a quantity of 10 g/kg or more, based on the weight of the fresh epoxidation catalyst. 18. The method of claim 16 further comprising depositing on the donee one or more rhenium copromoter components selected from the group consisting of tungsten, chromium, molybdenum, sulfur, phosphorus, boron, and mixtures thereof. 19. The method of claim 16 further comprising depositing on the donee one or more further elements selected from the group consisting of nitrogen, fluorine, alkali metals, alkaline earth metals, titanium, hafnium, zirconium, vanadium, thallium, thorium, tantalum, niobium, gallium, germanium, and mixtures thereof. 20. The method of claim 16 further comprising depositing on the donee one or more alkali metals selected from the group consisting of lithium, cesium, and combinations thereof. 21. The method of claim 1 wherein the donor has a cumulative alkylene oxide production of 0.2 kT/m3 of the donor spent epoxidation catalyst or more. 22. The method of claim 1 wherein the donor has a cumulative alkylene oxide production of 1 kT/m3 of the donor spent epoxidation catalyst or more. 23. The method of claim 1 wherein the aqueous liquid is selected from the group consisting of: just water; an aqueous liquid comprising one or more additives selected from salts, acids, bases, and peroxides; an aqueous organic diluent; and, mixtures thereof. 24. The method of claim 1 wherein the aqueous liquid consists of just water. 25. The method of claim 1 comprising contacting a weight of the donor with a first aliquot of the aqueous liquid under first extraction conditions which extracts a first portion of rhenium from the donor, producing a first extracted donor and a first aqueous extract comprising a first amount of extracted rhenium; and, contacting the first extracted donor with a second aliquots of the aqueous liquid under further extraction conditions which produces a second aqueous extracts comprising a second amounts of extracted rhenium. 26. The method of claim 25 wherein the first aliquot and second aliquots comprise substantially the same weight of the aqueous liquid as the weight of the donor. 27. The method of claim 1 wherein the total amount of extracted rhenium is 75% w or more of the total quantity of rhenium initially present on the donor.
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