Apparatus for simultaneous grinding and froth flotation

Patent metadata

Field	Value
Publication number	US-11413622-B2
Application number	US-201515526059-A
Country	US
Kind code	B2
Filing date	Nov 24, 2015
Priority date	Nov 28, 2014
Publication date	Aug 16, 2022
Grant date	Aug 16, 2022

Abstract

The present invention relates to apparatus for simultaneous grinding and froth flotation of at least one crude mineral and/or pigment, a process carried out in the apparatus for manufacturing at least one ground mineral and/or pigment, use of the ground mineral and/or pigment bearing phase obtainable by the process in paper applications as well as in paper, plastics, paints, coatings, adhesives, sealants, food, feed, pharma, concrete, cement, cosmetic, water treatment and/or agriculture applications, preferably in a wet end process of paper machine, in cigarette paper, board, and/or coating applications, or as support for rotogravure and/or offset and/or ink jet printing and/or continuous ink jet printing and/or flexography and/or electrophotography and/or decoration surfaces and the ground mineral and/or pigment bearing phase or ground mineral and/or pigment obtainable by the process.

First claim

The invention claimed is:

1. An apparatusfor simultaneous grinding and froth flotation of at least one crude mineral and/or pigment, comprising
a) a vessel ( 1 ) suitable for containing grinding media ( 2 ), a flotation gas, a collector agent and at least one crude mineral and/or pigment;
b) an agitation unit ( 3 ) rotatably mounted in vessel ( 1 );
c) drive means ( 4 ) connected to agitation unit ( 3 ) for agitating the grinding media ( 2 ) and the at least one crude mineral and/or pigment to grind the at least one crude mineral and/or pigment into at least one ground mineral and/or pigment;
d) a charge system ( 5 ) connected to vessel ( 1 ) comprising
i. a crude mineral and/or pigment feed ( 5 a ),
ii. a collector agent feed ( 5 b ), and
iii. a flotation gas inlet ( 5 c );

e) a discharge system ( 6 ) connected to vessel ( 1 ) comprising
i. a sieve ( 6 a ) suitable for separating froth from the ground mineral and/or pigment, and suitable for preventing the grinding media from being discharged with the ground mineral and/or pigment,
ii. a product collecting zone ( 6 b ) suitable for collecting the ground mineral and/or pigment,
iii. a froth collecting zone ( 6 c ) and
iv. a froth redirecting element ( 6 d ) having a conical structure affixed to and around a circumference of the stirring shaft of the agitation unit, wherein said froth redirecting element is arranged above the sieve ( 6 a ).

2. The apparatus according to claim 1 , characterized in that the froth collecting zone ( 6 c ) comprises spraying nozzles ( 6 c 1 ) and/or the discharge system ( 6 ) comprises a discharge control valve ( 6 e ) or a bypass with overflow ( 6 f ) and/or the productcollecting zone ( 6 b ) is ring-shaped and/or the froth collecting zone ( 6 c ) is ring- shaped and/or the froth redirecting element ( 6 d ) is ring-shaped.

3. The apparatus according to claim 1 , characterized in that the mineral and/or pigment feed ( 5 a ) is connected to the bottom ( 7 ) of vessel ( 1 ), and/or the crude mineral and/or pigment feed ( 5 a ), the collector agent feed ( 5 b ) and the flotation gas inlet ( 5 c ) of the charge system ( 5 ) are connected to each other such that the flotation gas and the collector agent are fed together with the at least one crude mineral and/or pigment in vessel ( 1 ).

4. The apparatus according to claim 1 , characterized in that the at least one crude mineral and/or pigment has/have a weight median particle diameter d 50 in the range from 20 to 500 μm and the grinding media ( 2 ) have a bulk density in the range from 1.5 to 6.0 kg/dm 3 ; and/or the grinding media ( 2 ) have a weight median particle diameter d 50 in the range from 0.2 to 5.0 mm; and/or the at least one crude mineral and/or pigment has/have a weight median particle diameter d 50 in the range from 0.5 to 20 μm and the grinding media ( 2 ) have a bulk density in the range from 1.5 to 6.0 kg/dm 3 ; and/or the grinding media ( 2 ) have a weight median particle diameter d 50 in the range from 0.2 to 5 mm.

5. A process carried out in an apparatus according to claim 1 for manufacturing at least one ground mineral and/or pigment comprising the steps
I. providing at least one crude mineral and/or pigment, grinding media ( 2 ) and at least one collector agent in vessel ( 1 );
II. mixing the at least one crude mineral and/or pigment, the grinding media ( 2 ) and the at least one collector agent as provided in step I. with water to form an aqueous suspension;
Ill. passing a flotation gas through flotation gas inlet ( 5 c ) into the aqueous suspension formed in step II. and agitating the obtained aqueous suspension by using agitation unit ( 3 ) to transform the at least one crude mineral and/or pigment into at least one ground mineral and/or pigment and obtaining thereby a ground mineral and/or pigment bearing phase and a froth;
IV. recovering the at least one ground mineral and/or pigment by removing the ground mineral and/or pigment bearing phase from the froth obtained in step III.

6. The process according to claim 5 , characterized in that the process involves a direct or an indirect flotation step leading to the formation of a froth containing the floated phase and a slurry bearing phase with the remaining ground mineral and/or pigment.

7. The process according to claim 5 , characterized in that at least one dispersing agent is added before or during step III. and/or the at least one crude mineral and/or pigment comprises at least one dispersing agent.

8. The process according to claims 5 , characterized in that the at least one dispersing agent is selected from the group consisting of sodium, potassium, calcium, magnesium, lithium, strontium, primary amine, secondary amine, tertiaryamine and/or ammonium salts, whereby the amine salts are linear or cyclic, of at least partly neutralized homopolymers or copolymers of (meth)acrylic acid, maleic acid, fumaric acid, itaconic acid and derivatives of these acids; and/or
the at least one collector agent is selected from the group consisting of surface active and hydrophobic tensides and/or mixtures thereof; and/or
the content of the at least one dispersing agent is in the range from 0.1 to 1.0 wt.-% based on the total weight of the at least one crude mineral and/or pigment in the aqueous suspension; and/or
the content of the at least one collector agent is in the range from 0.001 to 5.0 wt.-% based on the total weight of the at least one crude mineral and/or pigment in the aqueous suspension as provided in step II.

9. The process according to claim 5 , characterized in that the mill diameter is in a range from 200 to 750 mm and the agitation unit is adjusted to a shaft speed of 150 to 400 rpm or the mill diameter is in the range from 751 to 1 250 mm and the agitation unit is adjusted to a shaft speed of 125 to 350 rpm or the mill diameter is in the range from 1 251 to 1 750 mm and the agitation unit is adjusted to a shaft speed of 100 to 300 rpm.

10. The process according to claim 5 , characterized in that the solid content of the aqueous suspension is between 5.0 and 80.0 wt.-% based on the total weight of the at least one crude mineral and/or pigment in the aqueous suspension as provided in step II.

11. The process according to claim 5 , characterized in that the at least one crude mineral and/or pigment provided in step I. is a crude white pigment containing material.

12. The process according to claim 11 , characterized in that the crude white pigment containing material comprises impurities selected from the group consisting of iron sulphides; iron oxides; silicates; graphite and mixtures thereof, and/or the weight ratio of white pigment to impurities in the crude white pigment containing material (white pigment:impurities) is from 0.1:99.9 to 99.9:0.1, based on the dry weight.

13. The process according to claim 5 , characterized in that one or more additives selected from the group consisting of pH-adjusting agents, frothers, depressing agents, solvents, and/or polyelectrolytes are added before step IV.

14. The process according to claim 5 , characterized in that the process further comprises the steps of
V. dewatering and optionally drying the ground mineral and/or pigment bearing phase obtained in step IV. to remove at least a portion of water to obtain a partially dewatered ground mineral and/or pigment or to obtain a dried ground mineral and/or pigment;
VI. treating the partially dewatered and/or dried ground mineral and/or pigment obtained after dewatering step V. with at least one dispersing agent and re-dilute it to obtain an aqueous suspension comprising a dispersed grou

Assignees

• Omya Int Ag

Inventors

• Steinwender Michael
• Sötemann Jörg

Classifications

• B02C23/30

  the applied gas acting to effect material separation (B02C23/34 takes precedence) · CPC title

• B03D1/1462

  Discharge mechanisms for the froth · CPC title

• B03D1/082

  of the froth product, e.g. washing · CPC title

• B03D1/028 Primary

  Control and monitoring of flotation processes; computer models therefor · CPC title

• B02C17/185

  with more than one separator · CPC title