Claims
- 1. A process in which mineral ore pellets are made by adding binder comprising organic polymer to particulate iron ore having substantially all particles below 250 .mu.m and stirring in the presence of 5 to 15% by weight water (based on total mix) to form a substantially homogeneous moist mixture and pelleting the moist mixture, and in which the binder comprises about 0.002% to about 0.5% by weight, based on total mix, of a water soluble synthetic polymer and that is added to the ore as dry, free flowing beads that are substantially all above 20 .mu.m and below 300 .mu.m and that are made by reverse phase bead polymerisation from a water soluble ethylenically unsaturated monomer or blend of monomers.
- 2. A process according to claim 1 in which the binder gives a surface tension of above 70 dynes/cm at a concentration in water at 20.degree. C. of 0.075%.
- 3. A process according to claim 1 in which at least 70% by weight of the iron ore has a particle size below 50 .mu.m.
- 4. A process according to claim 1 in which substantially all the polymer beads are below 150 .mu.m.
- 5. A process according to claim 1 in which substantially all the polymer beads are below 200 .mu.m and at least 50% by weight are below 100 .mu.m.
- 6. A process according to claim 1 in which the ore is an iron ore that gives a pH in water of above 8 and the soluble polymer is an anionic polymer that has intrinsic viscosity of from 3 to 16 dl/g.
- 7. A process according to claim 1 in which the ore gives a pH in water of below 8 and the soluble polymer is a cationic polymer.
- 8. A process according to claim 1 in which the binder consists essentially of the soluble polymer beads and other additives selected from cross linked polymers and monomeric compounds, and in which the said other additives are present as beads of below 300 .mu.m size.
- 9. A process in which mineral ore pellets are made by adding binder comprising organic polymer to particulate iron ore having substantially all particles below 250 .mu.m and stirring in the presence of 5 to 15% by weight water (based on total mix) to form a substantially homogeneous moist mixture and pelletising the moist mixture, and in which the binder comprises about 0.002% to about 0.5% by weight, based on total mix, of a water soluble synthetic polymer that is cationic and the ore gives a pH in water of below 8.
- 10. A process according to claim 9 in which the cationic polymer is selected from polymers that have intrinsic viscosity 0.4 to 5dl/g and that are formed from monomers of which at least 70% by weight are cationic, and polymers that have intrinsic viscosity of 3 to 20 dl/g and that are formed by copolymerisation of 20 to 75 weight percent cationic monomer with 80 to 25 weight percent non-ionic monomer.
- 11. A process according to claim 9 in which the cationic polymer is substantially a homopolymer having intrinsic viscosity 0.4 to 2 dl/g.
- 12. A process accroding to claim 9 in which the cationic polymer is a copolymer of 25 to 60 weight percent cationic monomer with 75 to 40 weight percent acrylamide and has IV 3 to 12.
- 13. A process according to claim 9 in which the cationic polymer is a substantial homopolymer of monomers selected from diallyl dimethyl ammonium chloride and quaternised dialkylaminoalkyl (meth) acrylates and quaternised dialkylaminoalkyl (meth) acrylamides and has intrinsic viscosity 0.4 to 2 dl/g.
- 14. A process according to claim 9 in which the cationic polymer is a copolymer of about 20 to about 60% acrylamide with about 80 to about 40% by weight of a quaternised monomer selected from dialkylaminoalkyl (meth) acrylates and dialkylaminoalkyl (meth) acrylamides and has intrinsic viscosity of from 3 to 12 dl/g.
- 15. A process according to claim 9 in which the ore is iron ore which gives a pH in water of below 7.
- 16. A process according to claim 9 in which the polymer is added to the ore as dry free flowing powder having substantially all particles above 20 .mu.m and below 300 .mu.m.
- 17. A process according to claim 9 in which the polymer is added in the form of beads made by reverse phase suspension polymerisation and that are substantially all above 20 .mu.m and below 300 .mu.m.
- 18. A process according to claim 17 in which the binder gives a surface tension of above 70 dynes/cm at a concentration in water at 20.degree. C. of 0.075% by weight.
- 19. A process according to claim 9 in which the amount of polymer is from 0.01 to 0.05% by weight.
- 20. A process according to claim 9 in which at least 70% by weight of the iron ore has a particle size below 50 .mu.m.
- 21. A process according to claim 17 in which substantially all the polymer particles are below 150 .mu.m.
- 22. A process according to claim 17 in which substantially 100% of the polymer particles are below 200 .mu.m and at least 50% are below 100 .mu.m.
Priority Claims (2)
Number |
Date |
Country |
Kind |
8529418 |
Nov 1985 |
GBX |
|
8706932 |
Mar 1987 |
GBX |
|
Parent Case Info
This application is a continuation-in-part of application Ser. No. 935,006 filed Nov. 26, 1986, now U.S. Pat. No. 4,684,549, patented Aug. 4, 1987.
US Referenced Citations (4)
Number |
Name |
Date |
Kind |
4050962 |
Koester et al. |
Sep 1977 |
|
4248907 |
Uehori et al. |
Feb 1981 |
|
4470844 |
Rademachers |
Sep 1984 |
|
4543208 |
Horie et al. |
Sep 1985 |
|
Continuation in Parts (1)
|
Number |
Date |
Country |
Parent |
935006 |
Nov 1986 |
|