Acrylamide diallyl dimethyl ammonium chloride copolymers as improved dewatering acids for mineral processing

Information

  • Patent Grant
  • 4673511
  • Patent Number
    4,673,511
  • Date Filed
    Monday, September 30, 1985
    39 years ago
  • Date Issued
    Tuesday, June 16, 1987
    37 years ago
Abstract
An improved method of dewatering mineral slurries which comprises treating said slurries with a dewatering amount of a copolymer of acrylamide and DADMAC, which polymers are characterized as containing from 3-50 mole percent of acrylamide and having a Reduced Specific Viscosity of at least 2.
Description

INTRODUCTION
The most commonly used coagulant in mining and mineral processing for solids removal and dewatering (hereafter collectively referred to as "dewatering") is the homopolymer of diallyl dimethyl ammonium chloride (DADMAC). DADMAC polymers have been used to treat a variety of mineral slurries including but not limited to coal, taconite, trona, sand and gravel slurries, and titania.
Conventionally the DADMAC polymers used in the above dewatering operations have a Reduced Specific Viscosity (RSV) less than 1. Typically DADMAC polymers used to dewater slurries of the above type have a RSV within the range of about 0.3-1.0.
If it were possible to find an improved cationic dewatering aid for slurries of the above type, an advance in the art would be made.
THE INVENTION
An improved method of dewatering mineral slurries which comprises treating said slurries with a dewatering amount of a copolymer of acrylamide and DADMAC, which polymers are characterized as containing from 3-50 mole percent of acrylamide and having a Reduced Specific Viscosity of at least 2. The RSV's reported herein were measured on 0.05% polymer solutions in 1N sodium nitrate at a pH of 4.
The acrylamide DADMAC polymers, as indicated above, have an RSV of at least 2. Typically, the RSV is within the range of 2-6 although copolymers having higher RSV's give improved performances over copolymers having lower RSV's.
Preparation of 75/25 mole % DADMAC/AcAm
Aqueous:
75% DADMAC--523.3 grams
46.4% AcAm.sup.1 --124.0 grams
DI H.sub.2 O--71.6 grams
Versene--0.2 grams
Sodium Formate--0.2 grams
Oil:
LOPS--260.0 grams
Sorbitan monooleate--7.0 grams
Sorbitan monostearate reacted with 4 moles EO--7.0 grams
Substituted oxazoline surfactant--6.0 grams
Initiator:
Free radical catalyst--1.0 grams
Temperature:
50.degree. C. for 1 hour
60.degree. C. for 2 hours
75.degree. C. for 5 hours
45% initial solids
pH-5
39.1% solids
10 ppm AcAm in 2% solution
99.1% reacted
.sup.1 AcAm=Acrylamide
The amount of copolymer used to treat the slurries will vary based upon the nature of the slurry, the RSV of the copolymer, and other conditions. As a general rule, however, the dosage of active polymer will vary between 0.01-50 ppm based on the weight of the slurry treated with a preferred dosage level being 0.1-25 ppm.
In order to illustrate the advantages of the invention, the following examples are presented:





EXAMPLE 1
Coal Refuse
A series of DADMAC/Acrylamide copolymers were investigated as possible coagulants for coal refuse slurries obtained from commercial sources. The characteristics of the polymers tested are listed in Table I. The results of cylinder tests are given in Table II. FIG. 1 shows typical turbidity dosage curves obtained from cylinder tests for three of the copolymers and homopolymer DADMAC. Clearly, all the copolymers produce clearer water at dosages less than that required of homopolymer DADMAC. In addition, the copolymers provide the benefit of faster settling rates. This is illustrated in FIG. 2 which shows the settling rate versus dose for the same experiments used to generate FIG. 1.
At dosages given comparable clarity, settling rates were significantly faster with the copolymers as compared to homopolymer DADMAC.
Cylinder Test
The slurry is split into 500 cc glass mixing cylinders. The cyclinders are inverted several times to mix the slurry. The coagulant is added and the cylinder inverted four times. For coal refuse, flocculant is then added and the cylinder inverted an additional four times. The distance the solids setttle is noted at regular intervals. The clarity of the resulting supernatant is measured five minutes after the start of the test.
TABLE I______________________________________CHARACTERISTICS OF COAGULANTS TESTEDSample Mol. % DADMAC RSV______________________________________Comp. 1 100.0 0.7Comp. 2 93.4 2.3Comp. 3 83.5 3.3Comp. 4 80.0 6.5Comp. 5 71.4 5.2Comp. 6 61.6 6.6______________________________________
TABLE II______________________________________RESULTS OF CYLINDER TESTS USINGEXPERIMENTAL COAGULANTS ON COMMERCIALCOAL REFUSE SLURRIES Replacement Ratio*Sample Slurry 1 Slurry 2 Slurry 3______________________________________Comp. 1 1.00 1.00 1.00Comp. 2 0.76 0.79 0.82Comp. 3 0.74 0.81 0.78Comp. 4 0.77 0.85 0.51Comp. 5 0.65 0.54 0.37Comp. 6 0.59 0.46 0.37______________________________________ ##STR1## (Nelson Turbidity Units). The smaller the replacement ratio value, the more active the polymer tested. All replacement ratios were calculated on an actives (polymer) basis.
EXAMPLE 2
Coal Refuse
A series of copolymers were synthesized further varying the amount of DADMAC in the polymer. These polymers were then tested on two commercial coal refuse slurries. The characteristics of these polymers and the results obtained from cylinder tests are given in Table III. As these data show, the DADMAC/Acrylamide copolymers show good activity over a wide range of compositions, although as the amount of DADMAC decreases to 35%, activity starts to decrease.
TABLE III______________________________________CHARACTERISTICS AND RELATIVE ACTIVITYOF DADMAC/ACRYLAMIDE COPOLYMERS Replacement RatioSample Mol. % DADMAC RSV Slurry 4 Slurry 5______________________________________Comp. 1 100 0.7 1.00 1.00Comp. 7 76.9 4.4 0.78 0.31Comp. 8 65.5 5.2 -- 0.51Comp. 9 54.3 5.6 0.59 -- Comp. 10 34.6 9.2 0.75 0.86______________________________________
EXAMPLE 3
Taconite Tails
Two DADMAC/Acrylamide copolymers were tested on taconite tails from commercial sources. In addition, a mixture of homopolymer DADMAC with homopolymer acrylamide acrylamide was tested. The characteristics of the polymers tested are given in Table IV. The turbidities obtained from cylinder tests are plotted versus dose in FIG. 3. The copolymers are more active than either homopolymer DADMAC or the blend of acrylamide and DADMAC. The results obtained from cylinder tests on the slurries are presented in Table V. Note that the copolymers result in significantly faster settling rates at equivalent dosages.
TABLE IV______________________________________CHARACTERISTICS OF POLYMERSTESTED ON TACONITE TAILSSample Mol. % DADMAC RSV______________________________________Comp. 1 100 0.7Comp. 11 80 2.9Comp. 12 80 5.0Comp. 13 80* --______________________________________ *Mixture, not a copolymer.
TABLE V______________________________________RESULTS OF CYLINDER TESTS USINGEXPERIMENTAL COAGULANTS ON TACONITE TAILS Dosage Settling Rate Turbidity ReplacementSample (ppm) (in/min.) (JTU) Ratio*______________________________________Comp. 1 2 8 1600 1.0Comp. 1 5 8.6 675Comp. 1 10 11.4 155Comp. 1 15 12.4 66Comp. 13 2 9.8 1800 1.0Comp. 13 5 9.4 690Comp. 13 10 11.2 150Comp. 13 15 11.5 75.5Comp. 12 2 10.7 760 0.54Comp. 12 5 12.5 209Comp. 12 10 17.0 100Comp. 12 15 21 89Comp. 11 2 10 900 0.63Comp. 11 5 11.6 243Comp. 11 10 16 74Comp. 11 15 18.9 80______________________________________ *Calculated at 200 NTU (Nelson Turbidity Units) using Comp. 1 as a standard. The smaller the replacement ratio value, the more active the polymer tested.
Claims
  • 1. An improved method of dewatering mineral slurries which comprises treating said slurries with a dewatering amount of a copolymer of acrylamide and DADMAC, which polymers are characterized as containing from 3-50 mole percent of acrylamide and having a Reduced Specific Viscosity of at least 2.
  • 2. The method of claim 1 where the mineral slurry is a taconite slurry.
  • 3. The method of claim 1 where the mineral slurry is a coal slurry.
US Referenced Citations (7)
Number Name Date Kind
3171805 Suen et al. Mar 1965
3288770 Butler Nov 1966
3409547 Dajani Nov 1968
3461163 Boothe Aug 1969
4077930 Lim et al. Mar 1978
4141691 Antonetti et al. Feb 1979
4439580 Schaper Mar 1984