专利摘要:
In a method for the flotation of oxidic tin ores, fine-ground tin ore is converted into a suspension which is floated in the presence of a collecting and/or controlling and/or foaming agent, wherein the collecting agent is either (7) a biolipid extract and 2- phenylethylene-phosphonic acid or (2) a biolipid extract, a sodium soap of a biolipid extract and 2-phenylethylene- phosphonic acid or (3) biolipid extract fractions enriched with phosphatide or free fatty acid and 2-phenylethylene- phosphonic acid.
公开号:SU1457939A1
申请号:SU827772615
申请日:1982-09-01
公开日:1989-02-15
发明作者:Мартин Беккер;Христиан Неубер;Александер Росенбаум;Гейнц Сейдел;Беате Войгт;Карл Леманн;Клаус Пюхнер;Эккегарт Мош
申请人:Феб Бергбау-У Хюттенкомбинат "Альберт Функ" (Инопредприятие);
IPC主号:
专利说明:

one
The invention relates to the enrichment of minerals, and in particular to the method of flotation of oxidized tin
RUD
There is a method of flotation of oxidized tin ores, involving the addition of 2-phenylethylene phosphonic acid to the suspension of crushed ore as a collector, control reagents and blowing agents.
The purpose of the invention is to increase the degree of extraction of tin.
The method is carried out as follows.
The tin ore is ground to a particle size of less than 0.1 mm, suspended in a hearth, to which is added to clean the surface. Then, wasp flotation in the presence of a blowing agent using a collector mixture consisting of 2-phenylethylene phosphonic acid and a biolipid extract obtained from the yeast Lodderomyces elongisporus grown on hydrocarbon oil. The ratio of 2-phenylethylene phosphonic acid and biolead extract is 1: (0.25-1.5). It is advisable to use the collector mixture in the form of an aqueous emulsion. Partial application of the biolipid extract in the form of sodium soap contributes to emulsification, and the saponification depth is 35-70%,
The table presents the data of grinding of tin by fraction 1 p m.
Using a mixture of 2-phsnylethylene phosphonic acid and biolipid
cl
with so
the extract increases the size of the particles of the material undergoing flotation, which increases the degree of extraction of tin (table).
Example 1. A biolipid extract is obtained as a by-product after the extraction purification of the yeast Lodderomyces elongispori s JMET H128, boosted on distillate oil with a boiling point of 237-377 ° C. 1 mm, suspended in water to obtain a suspension with a density of 1.7 kg / l. 250 g / t is added to the slurry to clean the surface of the tin ore. After a partial change of water, the tin contained in the pulp is floated using 200 g / t of collector mixture consisting of 50% 2-phenylethylene phosphonic acid and 50% of the biolipid extract previously saponified to a depth of 70%.
Biolipid extract has the following composition,%:
Phosphatides 38.5 Glycerides and free fatty acids19.0
Biogenic components2, 5, Hydrocarbons 40.0 Octanediol is used as foaming agent. The degree of enrichment is 6.37, and the extraction of tin is 80.2%. When using as a collector only 2-phenylethylene phosphonic acid, the degree of enrichment is 8.37, and the increase in tin is 76.3%.
Example 2: The method is carried out according to Example 1, but nonylphenol is used as the blowing agent. The degree of enrichment of 7.37, the extraction of tin 83.1%. When using only 2-phenylethylene phosphonic acid as a collector, the same degree of enrichment is achieved, and the extraction of tin is 82.2%.
thirty
40
35
Example 5 The method is carried out according to example 4, but the ratio of 2-phenylethylene phosphonic acid and biolipid extract is 1: 1.5. The degree of enrichment is 6.07, the extraction of tin is 78.9%.
Thus, the proposed method of flotation of oxidized tin ores allows to increase the extraction of tin from the ore.
权利要求:
Claims (1)
[1]
Invention Formula
The method of flotation of oxidized tin ores, which involves adding 2-phenylethylenephosphonic acid to the crushed ore as a collector, control reagents and blowing agents, characterized in that, in order to increase the degree of tin recovery, a biolipid yeast extract is added to the suspension, hydrocarbon-grown petroleum at a ratio of 2-phenylethylene phosphonic acid and biol | fatty extract 1: (0.25-1.5), with a bioPerimer 3. The method is carried out 50 yeast lipid extract 1 but Use Tel'nykh saponified to a depth of 35-70%.
g
biolipid extract having the following composition,%:
Phosphatides 55 Glycerides and free fatty acids 32 Other biogenic components
0
five
0
Hydrocarbons
2 11
five
The ratio of 2-phenylethylene phosphonic acid and biolipid extract is 3: 1. The share of the saponified product is 35%.
The degree of enrichment is 6.06, the extraction of tin is 79.2%.
Example 4: The method is carried out according to Example 1, but using a biolipid extract containing 50% glycerides and free fatty acids. The ratio of 2-phenylethylene phosphonic acid and biolipid extract is 1: 0.25. The degree of enrichment is 7.11, the extraction of tin is 84.0%.
EXAMPLE 5 The method is carried out according to Example 4, but the ratio of 2-phenylethylene phosphonic acid and biolipid extract is 1: 1.5. The degree of enrichment is 6.07, the extraction of tin is 78.9%.
Thus, the proposed method of flotation of oxidized tin ores makes it possible to increase the recovery of tin from the ore.
Invention Formula
The method of flotation of oxidized tin ores, which involves adding 2-phenylethylenephosphonic acid to crushed ore as a collector, control reagents and blowing agents, characterized in that, in order to increase the degree of tin recovery, a biolipid extract of yeast grown on petroleum hydrocarbons with a ratio of 2-phenylethylene phosphonic acid and biol | fi xy extract 1: (0.25-1.5), while the bio100% 2-phenylethylene phosphone
acid95.1 83.3 50.5 10.5 5.3 76.9
A mixture of biolipid extract and 2-phenylethylene phosphonic acid (50:50) 94.8 84.0 51.7 17.8 8.6 80.6
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同族专利:
公开号 | 公开日
CS638982A1|1985-04-16|
DD221333A3|1985-04-17|
AU557734B2|1987-01-08|
GB2108870B|1985-08-14|
GB2108870A|1983-05-25|
AU8854782A|1983-05-12|
CS251219B1|1987-06-11|
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法律状态:
优先权:
申请号 | 申请日 | 专利标题
DD81234613A|DD221333A3|1981-11-04|1981-11-04|PROCESS FOR FLOTING OXIDIZED ZINNERZEZE|
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