Separation of gases and solids using a cyclone
View Patent ↗Cyclone design comprising an inlet device having an inlet height (Hi) and an inlet width (Wi), a gas outlet pipe having a pipe diameter (Di) and a pipe penetration (P), a barrel having an upper barrel diameter (Db) and a barrel length (Lb), said barrel comprising a cylindrical volume on top of a conical volume, a solids outlet pipe (O), an inlet gas velocity (Ug, i) and an inlet gas flow (Q), characterised in that the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is higher than 0.5, preferably higher than 0.7, and lower than 1.5, preferably lower than 1.2 (m/s) and in that the barrel length to diameter ratio (Lb/Db) is higher than 3, preferably higher than 3.5, and lower than 6, preferably lower than 4.5.
1. A cyclone comprising an inlet device having an inlet height (Hi) and an inlet width (Wi), a gas outlet pipe having a pipe diameter (Di) and a pipe penetration (P), a barrel having an upper barrel diameter (Db) and a barrel length (Lb), said barrel comprising a cylindrical volume on top of a conical volume, a solids outlet pipe (O), an inlet gas velocity (Ug,i) and an inlet gas flow (Q), wherein the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is higher than 0.5 and lower than 1.5 and the barrel length to diameter ratio (Lb/Db) is higher than 3 and lower than 6.
2. The cyclone according to claim 1 , wherein the inlet gas velocity is higher than 6 m/s.
3. The cyclone according to claim 1 , wherein the cyclone inlet height (Hi) and the gas outlet pipe penetration (P) are such that the ratio P/Hi is higher than 0.62 and lower than 1.25.
4. The cyclone according to claim 1 , wherein the cyclone does not comprise any vortex stabiliser.
5. A process comprising separating a mixture of gas and solids using the cyclone of any one of claims 1 - 4 .
6. A process comprising separating catalyst and polymer particles from a mixture of gas and solids exiting a gas phase polymerisation fluidised bed reactor using the cyclone of any one of claims 1 - 4 .
7. The process of claim 6 , wherein the gas phase polymerisation fluidised bed reactor is operated at an absolute pressure of between 0.5 and 6 MPa.
8. The cyclone according to claim 1 , wherein the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is higher than 0.7.
9. The cyclone according to claim 1 , wherein the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is lower than 1.2.
10. The cyclone according to claim 1 , wherein the barrel length to diameter ratio (Lb/Db) is higher than 3.5.
11. The cyclone according to claim 1 , wherein the barrel length to diameter ratio (Lb/Db) is lower than 4.5.
12. The process according to claim 5 , wherein the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is higher than 0.7.
13. The process according to claim 5 , wherein the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is lower than 1.2.
14. The process according to claim 6 , wherein the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is higher than 0.7.
15. The process according to claim 6 , wherein the ratio of the inlet gas flow to the square of the upper barrel diameter (Q/Db 2 ) is lower than 1.2.