Method of Reducing Impurities in Pyrolysis Oil
US-2024400918-A1 · Dec 5, 2024 · US
US2018371326A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018371326-A1 |
| Application number | US-201616062723-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 15, 2016 |
| Priority date | Dec 18, 2015 |
| Publication date | Dec 27, 2018 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
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.
Opening claim text (preview).
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. 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 catalyst composition contains at least 50 wt %, based on the combined weight of components A and B, of component B. 5 . 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. 6 . The process of claim 1 wherein the plastics waste comprises at least 50 wt % of polyolefins, styrene polymers or mixtures thereof. 7 . The process of claim 1 wherein the plastics waste is essentially free of thermosetting polymers. 8 . 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. 9 . The catalytic composition in accordance with claim 8 wherein component A) comprises supported or unsupported zeolites. 10 . The catalytic composition in accordance with claim 8 wherein component A) is a fresh fluid catalytic cracking catalyst, an equilibrium fluid catalytic cracking catalyst or a mixture thereof. 11 . The catalytic composition in accordance with claim 8 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. 12 . A process for the catalytic depolymerization of plastic waste wherein a) in a first step plastics waste is introduced into a reactor and melted and thereafter the temperature is increased to a temperature in the range of from 350 to 600° C., b) thereafter 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, is added to the molten plastics, c) the catalytic depolymerization is carried out at a temperature of from 350 to 600° C., and d) the product fractions are recovered. 13 . The process in accordance with claim 12 wherein component A) is a fresh fluid catalytic cracking catalyst, an equilibrium fluid catalytic cracking catalyst or a mixture thereof. 14 . The process of claim 12 wherein the plastic waste comprises at least 50 wt % of polyolefins, styrene polymers or mixtures thereof. 15 . The process of claim 12 wherein the plastics waste is selected from the group consisting of post consumer waste plastics, off-spec plastics, and industrial scrap plastic.
Gasoline · CPC title
from rubber or rubber waste · CPC title
Diesel oil · CPC title
Polyethene · CPC title
by treatment with inorganic material (C08J11/14 takes precedence) · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.