Method for manufacturing catalytic cracking catalyst for hydrocarbon oil
US-2016008796-A1 · Jan 14, 2016 · US
US10647922B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10647922-B2 |
| Application number | US-201616062723-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 15, 2016 |
| Priority date | Dec 18, 2015 |
| Publication date | May 12, 2020 |
| Grant date | May 12, 2020 |
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Use of a catalyst composition comprising A) a first component containing oxidic compounds comprising aluminum and silicon with a molar ratio of silicon to aluminum of more than 1) B) a second component containing an oxidic compound of silicon wherein the ratio of the number of acidic sites of component A, determined by temperature programmed desorption with ammonia as a base, to the number of acidic sites of component B, determined under the same conditions, is at least 3: in a process for the catalytic depolymerization of plastics waste.
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The invention claimed is: 1. A process comprising catalytic depolymerization of plastics waste using a catalyst composition comprising A) a first component containing oxidic compounds comprising aluminum and silicon with a molar ratio of silicon to aluminum of more than 1, and B) a second component containing an oxidic compound of silicon; wherein the ratio of the number of acidic sites of component A, determined by temperature programmed desorption with ammonia as a base, to the number of acidic sites of component B, determined under the same conditions, is at least 3:1; and wherein the catalyst composition contains at least 50 wt %, based on the combined weight of components A and B, of component B. 2. The process of claim 1 wherein component A comprises supported or unsupported zeolites. 3. The process of claim 1 wherein component A) is a fresh fluid catalytic cracking catalyst, an equilibrium fluid catalytic cracking catalyst or a mixture thereof. 4. The process of claim 1 wherein the plastics waste is selected from the group consisting of post consumer waste plastics, off-spec plastics, and industrial scrap plastic. 5. The process of claim 1 wherein the plastics waste comprises at least 50 wt % of polyolefins, styrene polymers or mixtures thereof. 6. The process of claim 1 wherein the plastics waste is essentially free of thermosetting polymers. 7. The process according to claim 1 , wherein the catalyst composition contains at least 55 wt %, based on the combined weight of components A and B, of component B. 8. The process according to claim 7 , wherein the catalyst composition contains at greater than 60 wt %, based on the combined weight of components A and B, of component B. 9. A catalytic composition, comprising A) a first component containing oxidic compounds comprising aluminum and silicon with a molar ratio of silicon to aluminum of more than 1 and B) a second component containing an oxidic compound of silicon, wherein the ratio of the number of acidic sites of component A, determined by temperature programmed desorption with ammonia as a base, to the number of acidic sites of component B, determined under the same conditions, is at least 3:1, and wherein the catalyst composition contains at least 50 wt %, based on the combined weight of components A and B, of component B. 10. The catalytic composition in accordance with claim 9 wherein component A) comprises supported or unsupported zeolites. 11. The catalytic composition in accordance with claim 9 wherein component A) is a fresh fluid catalytic cracking catalyst, an equilibrium fluid catalytic cracking catalyst or a mixture thereof. 12. The catalytic composition in accordance with claim 9 wherein the ratio of the number of acidic sites of component A to the number of acidic sites of component B, determined under the same conditions, is at least 5:1. 13. A process for the catalytic depolymerization of plastic waste, the process comprising a) in a first step, introducing plastics waste into a reactor, melting the plastics waste, and thereafter increasing the temperature to a temperature in the range of from 350 to 600° C., b) thereafter adding, to the molten plastics, a catalytic composition comprising as component A) a fluid catalytic cracking (FCC) catalyst and as component B) a compound based on oxidic compounds of silicon, wherein the ratio of the number of acidic sites of component A to the number of acidic sites of component B is at least 3:1, and wherein the catalyst composition contains at least 50 wt %, based on the combined weight of components A and B, of component B, c) carrying out the catalytic depolymerization at a temperature of from 350 to 600° C., and d) recovering the product fractions formed. 14. The process in accordance with claim 13 wherein component A) is a fresh fluid catalytic cracking catalyst, an equilibrium fluid catalytic cracking catalyst or a mixture thereof. 15. The process of claim 13 wherein the plastic waste comprises at least 50 wt % of polyolefins, styrene polymers or mixtures thereof. 16. The process of claim 13 wherein the plastics waste is selected from the group consisting of post consumer waste plastics, off-spec plastics, and industrial scrap plastic.
not modified by chemical after treatment · CPC title
by treatment with inorganic material (C08J11/14 takes precedence) · CPC title
Polyethene · CPC title
Characterised by the catalyst used · CPC title
Homopolymers or copolymers of propene · CPC title
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