DISPERSION NOZZLE, FLOTATION MACHINE EQUIPPED THEREWITH, AND METHOD FOR OPERATING SAME
A dispersion nozzle for dispersing a liquid with a gas, has a gas feed nozzle and a tubular mixing arrangement which has an inlet zone for the gas and the liquid and an outlet zone for a gas/liquid mixture. The mixing arrangement adjoins the gas feed nozzle. The gas feed nozzle is tapered in the direction of the mixing arrangement and opens into the inlet zone. The mixing arrangement has at least one liquid intake opening in the inlet zone. In the inlet zone a ratio of a diameter DG of a gas outlet opening of the gas feed nozzle and an internal diameter DM of the mixing arrangement is in the range from 1:3 to 1:5. A gas regulating valve meters a quantity of the gas being supplied with the gas feed nozzle. The dispersion nozzle may be used in a flotation machine.
1 - 19 . (canceled)
20 . A dispersion nozzle for dispersing a liquid with a gas, the dispersion nozzle extending about a longitudinal center axis, the dispersion nozzle comprising:
a tubular mixing arrangement which has a common inlet region for the gas and the liquid and an outlet region for a gas/liquid mixture formed from the gas and the liquid, the inlet region having an internal diameter D M , the mixing arrangement having at least 3 intake openings in the inlet region, for the liquid, the intake openings being disposed at an angle to the longitudinal center axis of the dispersion nozzle;
a gas feed nozzle adjoining the mixing arrangement, the gas feed nozzle tapering toward the mixing arrangement and having a gas outlet opening that opens into the inlet region of the mixing arrangement, the gas outlet opening having a diameter D G , a ratio of the diameter D G of the gas outlet opening to the internal diameter D M of the inlet region of the mixing arrangement being from 1:3 to 1:5; and
a gas regulating valve to meter a quantity of the gas fed into the liquid via the gas feed nozzle.
21 . The dispersion nozzle as claimed in claim 20 , wherein
the mixing arrangement is divided into a mixing chamber, a mixing tube and a diffuser,
the inlet region is provided in the mixing chamber,
the outlet region is provided in the diffuser,
the mixing tube is provided between the mixing chamber and the diffuser, and
the diffuser has a diameter which increases from the mixing tube to the outlet region.
22 . The dispersion nozzle as claimed in claim 21 , wherein
the mixing tube has an inlet opening with a diameter D MR ,
the mixing tube has a length L MR , and
a ratio of the diameter D MR of the mixing tube inlet opening to the length L MR of the mixing tube being from 1:3 to 1:8.
23 . The dispersion nozzle as claimed in claim 21 , wherein the diffuser is curved.
24 . The dispersion nozzle as claimed in claim 20 , wherein
the mixing arrangement is divided into a mixing tube and a diffuser,
the inlet region is provided in the mixing tube,
the outlet region is provided in the diffuser, and
the diffuser has a diameter which increases from the mixing tube to the outlet region.
25 . The dispersion nozzle as claimed in claim 24 , wherein
the mixing tube has an inlet opening with a diameter D MR ,
the mixing tube has a length L MR , and
a ratio of the diameter D MR of the mixing tube inlet opening to the length L MR of the mixing tube being from 1:3 to 1:8.
26 . The dispersion nozzle as claimed in claim 24 , wherein the diffuser is curved.
27 . The dispersion nozzle as claimed in claim 20 , wherein at least 8 intake openings are provided in the inlet region.
28 . The dispersion nozzle as claimed in claim 20 , wherein
the intake openings are disposed at a regular distance from one another on at least one circular path centered around the longitudinal center axis of the dispersion nozzle.
29 . The dispersion nozzle as claimed in claim 20 , wherein
the gas feed nozzle has an internal wall, which is aligned at an angle α of from 3° to 15° to the longitudinal center axis of the dispersion nozzle.
30 . The dispersion nozzle as claimed in claim 20 , wherein
the gas feed nozzle has an internal wall, which is aligned at an angle α of from 4° to 6° to the longitudinal center axis of the dispersion nozzle.
31 . The dispersion nozzle as claimed in claim 20 , wherein the intake openings are round.
32 . The dispersion nozzle as claimed in claim 31 , wherein the intake openings have a hole diameter greater than or equal to a wall thickness of the mixing arrangement.
33 . The dispersion nozzle as claimed in claim 20 , wherein the intake openings are disposed perpendicular to the longitudinal center axis of the dispersion nozzle.
34 . A method for operating a dispersion nozzle for dispersing a liquid with a gas, the dispersion nozzle extending about a longitudinal center axis, the dispersion nozzle comprising:
a tubular mixing arrangement which has a common inlet region for the gas and the liquid and an outlet region for a gas/liquid mixture formed from the gas and the liquid, the inlet region having an internal diameter D M , the mixing arrangement having at least 3 intake openings in the inlet region, for the liquid, the intake openings being disposed at an angle to the longitudinal center axis of the dispersion nozzle;
a gas feed nozzle adjoining the mixing arrangement, the gas feed nozzle tapering toward the mixing arrangement and having a gas outlet opening that opens into the inlet region of the mixing arrangement, the gas outlet opening having a diameter D G , a ratio of the diameter D G of the gas outlet opening to the internal diameter D M of the inlet region of the mixing arrangement being from 1:3 to 1:5; and
a gas regulating valve to meter a quantity of the gas fed into the liquid via the gas feed nozzle, the method comprising:
conducting the gas into the mixing arrangement by way of the gas feed nozzle, the gas being fed in such a manner that the gas is present at the gas outlet opening with a pulsed flow density in a range of from 5*10 3 to 5*10 4 kg/(m*s 2 );
sucking the liquid into the mixing arrangement by way of the intake openings; and
forming a gas/liquid mixture in the mixing arrangement.
35 . The method as claimed in claim 34 , wherein the pulsed flow density is in a range of from 1*10 4 to 5*10 4 kg/(m*s 2 ).
36 . The method as claimed in claim 35 , wherein the pulsed flow density is in a range of from 3*10 4 to 5*10 4 kg/(m*s 2 ).
37 . The method as claimed in claim 34 , wherein
the mixing arrangement has a mixing tube having a mixing tube outlet opening, and
a shear rate of from 500 to 5000 l/s is present for the gas/liquid mixture at the mixing tube outlet opening.
38 . The method as claimed in claim 34 , wherein
the mixing arrangement has a mixing tube having a mixing tube outlet opening, and
a shear rate of from 1000 to 1500 l/s is present for the gas/liquid mixture at the mixing tube outlet opening.
39 . A flotation machine comprising at least one dispersion nozzle as claimed in claim 20 .
40 . The flotation machine as claimed in claim 39 , wherein
the flotation machine has a housing with a flotation chamber, and
the at least one dispersion nozzle opens into the flotation chamber.
41 . The flotation machine as claimed in claim 40 , wherein the mixing arrangement, including the intake openings, is disposed in the flotation chamber.
42 . The flotation machine as claimed in claim 40 , wherein the longitudinal center axis of each dispersion nozzle is aligned horizontally with respect to a vertically extending flotation chamber.
43 . A method for operating a flotation machine comprising a housing with a flotation chamber and at least one dispersion nozzle opening into the flotation chamber for dispersing a liquid with a gas, each dispersion nozzle extending about a longitudinal center axis, each dispersion nozzle comprising:
a tubular mixing arrangement which has a common inlet region for the gas and the liquid and an outlet region for a gas/liquid mixture formed from the gas and the liquid, the inlet region having an internal diameter D M , the mixing arrangement having at least 3 intake openings in the inlet region, for the liquid, the intake openings being disposed at an angle to the longitudinal center axis of the dispersion nozzle;
a gas feed nozzle adjoining the mixing arrangement, the gas feed nozzle tapering toward the mixing arrangement and having a gas outlet opening that opens into the inlet region of the mixing arrangement, the gas outlet opening having a diameter D G , a ratio of the diameter D G of the gas outlet opening to the internal diameter D M of the inlet region of the mixing arrangement being from 1:3 to 1:5; and
a gas regulating valve to meter a quantity of the gas fed into the liquid via the gas feed nozzle, the method comprising:
filling the flotation chamber with liquid or a solid-liquid suspension, in such a manner that the intake openings of the at least one dispersion nozzle are below a surface formed by the liquid or the solid-liquid suspension.
44 . The method as claimed in claim 43 , further comprising feeding the gas by way of the gas feed nozzle such that the gas is present at the gas outlet opening with a pulsed flow density in a range of from 5*10 3 to 5*10 4 kg/(m*s 2 ).
45 . The method as claimed in claim 43 , wherein
the flotation chamber is filled with the solid-liquid suspension, and
the solid-liquid suspension has a solid material content of from 30 to 60%.
46 . The method as claimed in claim 45 , further comprising separating suspended ore from gangue.