Method for processing plastic waste pyrolysis gas
The present disclosure relates to methods for processing plastic waste pyrolysis gas, such as methods wherein clogging of the systems used in the method is avoided or at least alleviated.
1. A method for processing plastic waste pyrolysis gas, the method comprising:
a) providing:
a plastic waste pyrolysis gas stream wherein a temperature of the plastic waste pyrolysis gas stream is 300-650° C.; and
a hydrocarbonaceous liquid stream wherein a temperature of the hydrocarbonaceous liquid stream is below temperature of the plastic waste pyrolysis gas stream;
b) admixing in an ejecting means the plastic waste pyrolysis gas stream and the hydrocarbonaceous liquid stream to form an admixture;
c) spraying the admixture to a separation chamber to produce a condensed fraction and a gaseous fraction; and
d) separating the gaseous fraction and the condensed fraction to yield a first liquid product stream and a gaseous product stream.
2. The method according to claim 1 , wherein a temperature of the hydrocarbonaceous liquid stream of step a) is 100-300° C.
3. The method according to claim 1 , wherein a mass ratio of the hydrocarbonaceous liquid stream and the plastic waste pyrolysis gas stream in the admixture is 1-100.
4. The method according to claim 1 , comprising:
recycling a first part of first liquid product stream to the hydrocarbonaceous liquid stream of step a) and collecting a second part of the first liquid product stream.
5. The method according to claim 4 , wherein a temperature of the first part of first liquid product stream is above 100° C.
6. The method according to claim 4 , wherein the hydrocarbonaceous liquid stream of step a) contains the first part of first liquid product stream.
7. The method according to claim 1 , comprising:
cooling the gaseous product stream of step d) to 10-50° C. to yield a second liquid product stream and a gaseous stream.
8. The method according to claim 7 , comprising:
separating the second liquid product stream and the gaseous stream.
9. The method according to claim 1 , comprising:
providing:
a plastic waste pyrolysis gas stream wherein a temperature of the plastic waste pyrolysis gas stream is 450-500° C.
10. The method according to claim 9 , wherein a temperature of the hydrocarbonaceous liquid stream of step a) is 175-225° C.
11. The method according to claim 10 , wherein a mass ratio of the hydrocarbonaceous liquid stream and the plastic waste pyrolysis gas stream in the admixture is 5-25.
12. The method according to claim 11 , wherein a temperature of the first part of first liquid product stream is between 150-250° C.
13. The method according to claim 12 , comprising:
cooling the gaseous product stream of step d) to 20-40° C. to yield the second liquid product stream and the gaseous stream.
14. The method according to claim 2 wherein a mass ratio of the hydrocarbonaceous liquid stream and the plastic waste pyrolysis gas stream in the admixture is 1-100.
15. The method according to claim 14 , comprising:
recycling a first part of first liquid product stream to the hydrocarbonaceous liquid stream of step a) and collecting a second part of the first liquid product stream.
16. The method according to claim 15 , wherein the hydrocarbonaceous liquid stream of step a) contains the first part of first liquid product stream.
17. The method according to claim 16 , comprising:
cooling the gaseous product stream of step d) to 10-50° C. to yield the second liquid product stream and the gaseous stream.
18. The method according to claim 17 , comprising:
separating the second liquid product stream and the gaseous stream.