IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0754812
(2001-01-04)
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발명자
/ 주소 |
- Janssen, Marcel J. G.
- Van Oorschot, Cornelis W. M.
- Clem, Kenneth R.
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출원인 / 주소 |
- ExxonMobil Chemical Patents, Inc.
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인용정보 |
피인용 횟수 :
3 인용 특허 :
5 |
초록
▼
The method includes freeze drying a molecular sieve having a methanol conversion ratio of less than 1, or a catalyst containing molecular sieve and a binder having a methanol conversion ratio of less than 1. The rejuvenated molecular sieve or catalyst is used to make an olefin product from an oxygen
The method includes freeze drying a molecular sieve having a methanol conversion ratio of less than 1, or a catalyst containing molecular sieve and a binder having a methanol conversion ratio of less than 1. The rejuvenated molecular sieve or catalyst is used to make an olefin product from an oxygenate. The olefin product containing ethylene and propylene can then be used to make polyethylene and polypropylene, respectively.
대표청구항
▼
1. A method for rejuvenating molecular sieve comprising: providing molecular sieve having a methanol uptake index of less than 1; and freeze drying the molecular sieve until the methanol uptake index is increased by at least 10%. 2. The method of claim 1, wherein the methanol uptake index is i
1. A method for rejuvenating molecular sieve comprising: providing molecular sieve having a methanol uptake index of less than 1; and freeze drying the molecular sieve until the methanol uptake index is increased by at least 10%. 2. The method of claim 1, wherein the methanol uptake index is increased by at least 50%. 3. The method of claim 2, wherein the methanol uptake index is increased by at least 100%. 4. The method of claim 3, wherein the methanol uptake index is increased by at least 500%. 5. The method of claim 1, wherein the molecular sieve is provided having a methanol uptake index of less than 0.5. 6. The method of claim 1, wherein the molecular sieve is selected from the group consisting of SAPO-5, SAPO-8, SAPO-11, SAPO-16, SAPO-17, SAPO-18, SAPO-20, SAPO-31, SAPO-34, SAPO-35, SAPO-36, SAPO-37, SAPO-40, SAPO-41, SAPO-42, SAP044, SAPO-47, SAPO-56, ALPO-5, ALPO-11, ALPO-18, ALPO-3 1, ALPO-34, ALPO-36, ALPO-37, ALPO-46, the metal containing forms of each thereof, and mixtures thereof. 7. The method of claim 6, wherein the molecular sieve is selected from the group consisting of SAPO-17, SAPO-18, SAPO-34, SAPO-35, SAPO44, SAPO-47, the metal containing forms of each thereof, and mixtures thereof. 8. The method of claim 1, wherein freeze drying is carried out at a pressure of 0.001 mtorr to 700 torr and a temperature of -200° C. to 0° C. 9. A method for rejuvenating molecular sieve containing catalyst comprising: providing molecular sieve containing catalyst having a methanol uptake index of less than 1; and freeze drying the molecular sieve containing catalyst until the methanol uptake index is increased by at least 10%. 10. The method of claim 9, wherein the methanol uptake index is increased by at least 50%. 11. The method of claim 10, wherein the methanol uptake index is increased by at least 100%. 12. The method of claim 11, wherein the methanol uptake index is increased by at least 500%. 13. The method of claim 9, wherein the molecular sieve containing catalyst is provided having a methanol uptake index of less than 0.5. 14. The method of claim 9, wherein the molecular sieve in the molecular sieve containing catalyst is selected from the group consisting of SAPO-5, SAPO-8, SAPO-11, SAPO-16, SAPO-17, SAPO-18, SAPO-20, SAPO-31, SAPO-34, SAPO-35, SAPO-36, SAPO-37, SAPO-40, SAPO41, SAPO-42, SAPO-44, SAPO47, SAPO-56, ALPO-5, ALPO-11, ALPO-18, ALPO-31, ALPO-34, ALPO-36, ALPO-37, ALPO-46, the metal containing forms of each thereof, and mixtures thereof. 15. The method of claim 14, wherein the molecular sieve in the molecular sieve containing catalyst is selected from the group consisting of SAPO-17, SAPO-18, SAPO-34, SAPO-35, SAPO44, SAPO-47, the metal containing forms of each thereof, and mixtures thereof. 16. The method of claim 9, wherein freeze drying is carried out at a pressure of 0.001 mtorr to 700 torr and a temperature of -200° C. to 0° C.
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