专利摘要:
A process for separating molybdenite from copper sulphide and other metal sulphide minerals with which it is associated in a metallurgical concentrate through use of a copper sulphide depressant which is a compound having at least one nitrogen atom, at least one thio group and at least one hydrophilic group. Some examples are 2-thiouracil, pseudothio-hydantoin, and 2-imino-4-oxo-5-thiazolidineacetic acid.
公开号:SU837310A3
申请号:SU782610800
申请日:1978-04-21
公开日:1981-06-07
发明作者:Джон Ганнон Дэвид
申请人:Си-Ай-Эл Инк (Фирма);
IPC主号:
专利说明:

6-Methyl-2-thiouracil
2-Gi®barbituric acid
V
about
Tioorougov acid
M Noos
Group II. Five-membered heterocyclic nuclei containing at least one nitrogen atom, sulfur and oxygen in the molecule: 2-hyohydrantoium
&
$.
.NH
L

CHN
 -. .
2-Imino-4-oxo-5-thiaerolidine-acetic acid
noos n with
 jfPv
about
Rodanin-N-acetic acid
 four
Cr.
J -CHgM-Aminorodanin
Tioparabanova
-four
ABOUT
Group ill. Derivatives of the thiomoquine adduct of D -glucose with thiourea, which is a mixture of I-B-fi-glucopyranosylthresholds
n D-V-W) G1pkzh1Sh1yranosylthiol and III
n
x
  NH,
- n he
oioacetic acid "sN
;; c - $ - CH2- (ioo
Hgn
oethoethanesulfa lot
Hgh
C-S- (CH2) 2-S03
Hotf
Dithiooxamide
H2N-C- J-Nll2 S $
Group IV. Thioamino.cysteine CH2 (SH) -CltfNH) COOH
Methionium (CHj) j-CH (
Group U, 1,3,5-Triaeny containing the SH group or it in positions 2, 4, 6. Tritiocyanuric acid
LN
n $. . $ and
n ii
0
Solubilized pseudothiocyan: mixture of type compounds

X,
X
Jj

1 „1, 0.
Ya.-A:
where X, Х2ХАХй- $ Н or ОН.
Group IV No. Captopyridinols
The method is carried out as follows.
Copper-molybdenum product, which is a rough concentrate of collective flotation or concentrate from the cleaning of the rough concentrate, pulping to a content of 15-50%
solid By adding an alkaline agent: lime, sodium hydroxide, or another, the pH of the pulp is adjusted to 8-12. Then one of the listed compounds is introduced into the pulp and conditioned with stirring for 1–20 minutes.
The consumption of modifiers is 0.045-0.45 kg per ton of concentrate. Into the prepared pulp is injected
collector: hydrocarbon oil and
blowing agent: 4-methyl-2-pentanol and float molybdenite.
The consumption of the collector, for example kerosene, with the addition of fuel oil - 0.092, 27 kg / t, foaming agent - 0.14 kg / t. Flotation time 2-10 min.
Modifiers can be introduced into the pulp in the form of solid particles, but it is preferable to use them in the form of aqueous solutions in which alkali or acid can be added to increase the solubility of the compounds.
Example 1. Modifiers tested in the flotation of a rough concentrate containing 26% copper and 2.7% molybdenum. The pH of the suspension was adjusted by adding lime and adjusted to 10. Conditioning with modifiers was carried out for 20 minutes. Collector: kerosene - 0.9 kg / t.
As a result of the process installed.
Extraction of molybdenum in concentrate with the use of acidic sulfurous sodium (known modifier) was 89%. Its consumption at the same time 45, 4 kg / t.
The use of these modifiers, depending on their particular type, allows for the extraction of 8492% molybdenum. Their required consumption was 6.8-13.6 kg / t, i.e. with almost identical process indicators, it was more than 3 times lower
Example 2. Floated concentrate with a copper content of 10%, moliden 0.4%. The use of acidic sulphurous sodium allows to extract 84-87% of molybdenum, these compounds - 75-89% with a reduction in consumption of 10-40 times.
Example 3. The concentrate, flotation flotation, contained 27% copper and 1.7% molybdenum. The natural pH of the suspension was 10, so the alkaline agent was not added.
The flotation results show that acidic sodium sulphide contributes to recovery of up to 91% in the concentrate. Using the recommended modifiers allows you to extract 80-94% molybdenum while reducing consumption by 3 times.
- As such, the consumption of these modifiers is significantly lower than the known. In this case, a number of them, namely, thiobarbituric acid, 2-t iouracid, 2-methyl-2-thiouracil, thioorotic acid, thiogidantoin, allow to increase the recovery of molybdenum in the concentrate by 1-3%. This is the main advantage of this invention.
ten
权利要求:
Claims (3)
[1]
Invention Formula
A method of separating sulfide copper-molybdenum products, concluded in conditioning products in the form of pulp with a copper-containing and other sulfide depressant, injecting hydrocarbon oil and a frother, and molybdenite flotation, characterized in that selected from the series: 2-thiouracil,
6-amino, 2-thiouracil, 6-methyl-2-thiouracil, 2-thiobarbituric acid; , cysteine, methionine, amidinothioacetic acid, amidino-thioethane-sulfonic acid, 2-mercapto-3-pyridinol, 3-thiocyanuric acid, dithiooxamcd. rhodang -H-acetic acid fN -at. Shkorodakin, tisparabanovy acid,
[2]
2. The method according to claim 1, wherein the compound; used in the form of potassium salts, sodium
or ammonium.
[3]
3 .. The method according to claim 1, characterized by the fact that the compounds are used in the form of salts of hydrochloric, sulfuric or nitric acids.
Information sources,
taken into account in the examination
1.Fishman M.A. and others. The practice of enrichment of ores of non-ferrous and rare metals. M., Gosgortehizdat, - 1963, p. 21-22 (prototype) ..
类似技术:
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同族专利:
公开号 | 公开日
AR214784A1|1979-07-31|
US4196073A|1980-04-01|
PH12924A|1979-10-10|
CA1071336A|1980-02-05|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题
CN105665148A|2016-01-15|2016-06-15|中南大学|Isothiocyanate derivative and preparation method and application thereof|US1364308A|1919-03-25|1921-01-04|Metals Recovery Co|Flotation of minerals|
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GB314822A|1928-03-03|1929-07-03|Reginald John Lemmon|Improvements in froth flotation|
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US1960459A|1932-08-23|1934-05-29|Ruth Company|Method of ore separation|
US2449984A|1944-04-10|1948-09-28|Harold L Gibbs|Differential froth flotation of sulfide ores|
GB617944A|1946-03-15|1949-02-14|Koppers Co Inc|Improvements in froth flotation processes|
US3329266A|1964-04-17|1967-07-04|Kennecott Copper Corp|Flotation process involving depression of sulfide minerals previously activated|
US3400817A|1966-03-10|1968-09-10|Miami Copper Company|Process and reagent for recovery of molybdenite from copper sulfide-molybdenite flotation concentrates|
US3788467A|1972-04-27|1974-01-29|American Cyanamid Co|Flotation process for recovering molybdenum|US4329223A|1980-01-11|1982-05-11|United States Borax & Chemical Corporation|Flotation of molybdenite|
US4295962A|1980-04-30|1981-10-20|Phillips Petroleum Company|Recovering copper by flotation using N-mercaptoalkyl amide depressant|
US4425230A|1982-02-16|1984-01-10|Oreprep Chemicals, Inc.|Separation of molybdenite from its mixture with other sulfide ores|
PH17957A|1982-05-28|1985-02-20|Phillips Petroleum Co|Ore flotation process|
US5089116A|1990-12-31|1992-02-18|Establecimientos Industriales Quimicos Oxiquim S.A.|Process of froth floatation using a 5-alkyl, 5-alkenyl, or 5-aryl-1,3,5,-dithiazine as a collector reagent|
EA039011B1|2016-10-07|2021-11-22|Сайтек Индастриз Инк.|Depressant compositions and methods for depressing the gangue sulfide minerals during the flotation of sulfide ores|
SG10202103970YA|2016-10-20|2021-06-29|Newsouth Innovations Pty Ltd|Method for removing heavy metals from an aqueous solution|
CN107138286A|2017-06-22|2017-09-08|刘秀云|The application of L cysteines and its salt in metal sulfide ore FLOTATION SEPARATION|
CN108588417B|2018-01-26|2019-09-27|中南大学|A method of the extraction and separation molybdenum from tungstate solution|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
CA276,821A|CA1071336A|1977-04-22|1977-04-22|Hydrophilic thio compounds as selective depressants in the flotation separation of copper and molybdenum|
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