Process for treating a carrier, a process for preparing a catalyst, the catalyst, and use of the catalyst
US-8999882-B2 · Apr 7, 2015 · US
US10532989B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10532989-B2 |
| Application number | US-11690508-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 7, 2008 |
| Priority date | May 9, 2007 |
| Publication date | Jan 14, 2020 |
| Grant date | Jan 14, 2020 |
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a process for preparing the catalyst; a process for preparing an olefin oxide by reacting a feed comprising an olefin and oxygen in the presence of the catalyst; and a process for preparing a 1,2-diol, a 1,2-diol ether, a 1,2-carbonate, or an alkanolamine.
Opening claim text (preview).
What is claimed is: 1. A catalyst for the epoxidation of an olefin comprising a carrier and, deposited on the carrier, silver, a rhenium promoter, a first co-promoter, and a second co-promoter; wherein the quantity of the rhenium promoter deposited on the carrier is at least 2 mmole/kg, relative to the weight of the catalyst; the first co-promoter is selected from the group consisting of sulfur, phosphorus, boron, and mixtures thereof; the second co-promoter is selected from the group consisting of tungsten, molybdenum, chromium, and mixtures thereof; and the total quantity of the first co-promoter and the second co-promoter deposited on the carrier is at most 3.8 mmole/kg, relative to the weight of the catalyst. 2. The catalyst as claimed in claim 1 , wherein the quantity of the rhenium promoter is from 2 to 10 mmole/kg, relative to the weight of the catalyst. 3. The catalyst as claimed in claim 1 , wherein the total quantity of the first co-promoter and the second co-promoter is at most 3.5 mmole/kg, relative to the weight of the catalyst. 4. The catalyst as claimed in claim 1 , wherein the total quantity of the first co-promoter and the second co-promoter is at least 0.5 mmole/kg, relative to the weight of the catalyst. 5. The catalyst as claimed in claim 1 , wherein the second co-promoter comprises tungsten. 6. The catalyst as claimed in claim 1 , wherein the second co-promoter comprises molybdenum. 7. The catalyst as claimed in claim 1 , wherein the first co-promoter comprises sulfur. 8. The catalyst as claimed in claim 1 , wherein the catalyst further comprises a further element selected from the group consisting of nitrogen, fluorine, alkali metals, alkaline earth metals, titanium, hafnium, zirconium, vanadium, thallium, thorium, tantalum, niobium, gallium and germanium and mixtures thereof. 9. The catalyst as claimed in claim 8 , wherein the alkali metals are selected from the group consisting of lithium, sodium, and cesium. 10. The catalyst as claimed in claim 1 , wherein the catalyst further comprises deposited on the carrier a potassium promoter in a quantity of at least 0.5 mmole/kg, relative to the weight of the catalyst. 11. The catalyst as claimed in claim 1 , wherein the catalyst further comprises deposited on the carrier a potassium promoter in a quantity of at least 1.5 mmole/kg, relative to the weight of the catalyst. 12. The catalyst as claimed in claim 1 , wherein the catalyst has a water extractable quantity of potassium in the range of from 1.25 to 10 mmole/kg, relative to the weight of the catalyst. 13. The catalyst as claimed in claim 1 , wherein the catalyst has a water extractable quantity of potassium in the range of from 1.5 to 7.5 mmole/kg, relative to the weight of the catalyst. 14. The catalyst as claimed in claim 1 , wherein silver is present in a quantity in the range of 10 to 500 g/kg, relative to the weight of the catalyst. 15. The catalyst as claimed in claim 1 , wherein silver is present in a quantity in the range of 50 to 450 g/kg, relative to the weight of the catalyst. 16. The catalyst as claimed in claim 1 , wherein the molar ratio of the first co-promoter to the second co-promoter is greater than 2. 17. The catalyst as claimed in claim 1 , wherein the molar ratio of the first co-promoter to the second co-promoter is greater than 2 and at most 20.
with catalysts containing silver or gold · CPC title
by reaction of ammonia or amines with olefin oxides or halohydrins · CPC title
with alkali metals, copper, gold or silver · CPC title
with manganese, technetium or rhenium · CPC title
from carbon dioxide or inorganic carbonates · CPC title
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