Oolitic hematite flocculant and oolitic hematite selective dispersing and agglomeration separation method
A technology of oolitic hematite and flocculant, which is applied in the field of selective dispersion and agglomeration separation of flocculant and oolitic hematite, to achieve the effects of excellent recovery rate and grade of total iron, stable product quality and easy control of conditions
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Publication Date
- 2014-06-04
- Estimated Expiration
- Not applicable · inactive patent
Abstract
Description
technical field
[0001] The invention relates to sorting of hematite, in particular to a flocculant for beneficiation of oolitic hematite and a method for selectively dispersing and agglomerating the oolitic hematite. Background technique
[0002] One-ninth of my country's iron ore reserves is oolitic hematite, accounting for 30% of my country's hematite reserves. This type of oolitic hematite often forms large mines, such as the Xuanlong iron mine in the north and the Ningxiang iron mine in the south. Oolitic hematite is extremely finely distributed and often coexists or wraps with siderite, oolitic chlorite and phosphorus-containing minerals, so it is currently recognized as the most difficult type of iron ore at home and abroad. Because oolitic hematite has extremely fine particle size and its layer-by-layer wrapping structure, it is not conducive to the dissociation of ore monomers, and the ore is particularly easy to form fine particles after crushing and grinding, with...
Examples
Embodiment 1
[0053] Prepare flocculant according to the above steps, wherein:
[0054] The amount of each component in step a is 10% by weight of carboxymethyl starch, 50% of acrylic acid, 0.5% of initiator, 0.01% of crosslinking agent, and 39.49% of deionized water; in step b, the temperature of the mixed material is raised to 70 ℃, heat preservation for 3 hours; during Soxhlet extraction in step d, the weight ratio of the crude product to methanol is 2.5, the extraction time is 24 h, and finally the flocculant product is obtained.
[0055] Calculate the graft rate of the product to be 75.25%, and the molecular weight of the graft copolymer is 6.45×10 5 .
Embodiment 2
[0057] Carry out operation according to embodiment 1 step, difference is: mixed material is mixed evenly by the weight percentage of carboxymethyl starch 30%, acrylic acid 40%, initiator 1.0%, crosslinking agent 0.05% and surplus is deionized water 29.15%, Raise the temperature of the mixed material to 80°C and keep it warm for 4 hours.
[0058] Finally, the grafting rate of the product calculated was 84.30%, and the molecular weight of the grafted copolymer was 1.749×10 6 .
Embodiment 3
[0060] Carry out operation according to embodiment 1 step, difference is: mixed material is by carboxymethyl starch 35%, acrylic acid 40%, initiator 2.0%, crosslinking agent 0.1% and surplus are the weight percent of deionized water 22.90% and mix homogeneously, Raise the temperature of the mixed material to 90°C and keep it warm for 6 hours.
[0061] Calculated by formula (1), the grafting ratio of the product is 92.45%, and calculated by formula (2), the molecular weight of the graft copolymer is 2.639 × 10 6 .
[0062] 2. Selective dispersion and agglomeration of oolitic hematite: