Catalyst column and thermal cracking system
According to one aspect of the invention, a catalyst tower is provided, which comprises a gas inlet and a catalyst holding plate set therein. The gas inlet is the opening where the catalyst tower and the upstream piping connects with one another. The distance between the gas inlet and the catalyst holding plate is directly proportional to the difference in diameter between the catalyst tower and the upstream piping.
1. An apparatus, comprising:
a tower with an opening, wherein said tower receives a gas stream via said opening;
a plate for holding a bed of chemicals, wherein said plate is set in said tower, and said bed of chemicals is used for treating said gas stream; and
a reactor for generating said gas stream from a reactant selected from a group consisting of the following, or combinations thereof: waste plastic, waste tire, and waste oil;
wherein said tower has a first diameter, said opening has a second diameter, and said first diameter is equal to or greater than 4.5 times of said second diameter.
2. The apparatus according to claim 1 , wherein said plate is apart from said opening by a distance, a ratio of said distance to said first diameter of said tower is equal to or greater than 0.4.
3. The apparatus according to claim 1 , wherein said bed of chemical provides reformation or purification to said gas stream.
4. The apparatus according to claim 1 , wherein a capacity ratio of said tower to said reactor is between 1/15 and ⅛.
5. The apparatus according to claim 4 , wherein said reactor is a rotary reactor.
6. The apparatus according to claim 1 , wherein a diameter ratio of said tower to said reactor is between ⅓ and 1.
7. The apparatus according to claim 6 , wherein said reactor is a rotary reactor.
8. A method for thermal cracking a feed material selected from a group consisting of the following or combinations thereof: waste plastic, waste tire, and waste oil, comprising:
subjecting said feed material to a thermal cracking reaction thereby generating a gas stream; and
sending said gas stream to a first tower, wherein said first tower includes an opening for receiving said gas stream and a bed of chemicals therein for treating said gas stream, said first tower has a first diameter, said opening has a second diameter, and said first diameter is equal to or greater than 4.5 times of said second diameter.
9. The method according to claim 8 , wherein said bed of chemicals is apart from said opening by a distance, a ratio of said distance to said first diameter of said first tower is equal to or greater than 0.4.
10. The method according to claim 8 , wherein said thermal cracking reaction occurs in a reactor, and a capacity ratio of said first tower to said reactor is between 1/15 and ⅛.
11. The method according to claim 8 , wherein said thermal cracking reaction occurs in a reactor, and a diameter ratio of said first tower to said reactor is between ⅓ and 1.
12. The method according to claim 8 , wherein said bed of chemicals provides reformation or purification to said gas stream.
13. The method according to claim 8 , further comprising:
sending said gas stream to a second tower; and
condensing said gas stream.
14. The method according to claim 13 , further comprising:
providing a plurality of sub-control valves for regulating said gas stream to said first tower and said second tower.
15. The method according to claim 8 , wherein said thermal cracking reaction occurs in a first reactor and a second reactor.
16. The method according to claim 15 , further comprising:
providing a plurality of sub-control valves for controlling distributing said feed material to said first reactor and said second reactor.