US1904462A

US1904462A - Flotation of minerals

Info

Publication number: US1904462A
Application number: US193052A
Authority: US
Inventors: Raymond W Hess; Joseph M F Leaper
Original assignee: Barrett Co Inc
Current assignee: Barrett Co Inc
Priority date: 1927-05-20
Filing date: 1927-05-20
Publication date: 1933-04-18
Anticipated expiration: 1950-04-18

Description

Patented Apr. 18, 1933 UNITED STATES PATENT OFFICE BAYIOND w. HESS AND JOSEPH I. LEAPEB, OF BUFFALO, NEW YORK, ASSIGNOBS TO THE BARBIE! COMPANY, OF NEW YORK, N. Y A. CORPORATION OF NEW JERSEY manor: or

lo'nrawinz.

This invention relates to the separation of minerals and the concentration of ores by flotation rocesses, and is particularly directed to sue separation and concentration carried out with the utilization of a mixture of substances containing certain organic sulfur compounds.

Accordin to the present invention, improved res ts can be obtained in the separation of minerals and concentration of ores by carrying out the flotation operation with the addition to the mineral pulp or ore of the resultant organic roduct or composition of matter obtained y the hydrolytic decomposition in the presence of an acid of a metal salt of an aralkyl ester of thiosulfuric acid represented by the formula RS O,M where R denotes an aralkyl group such as CJLCH etc., and M signifies a metal, particularly an alkali metal.

The flotation agent particularly employed in the present invention can be prepared by reacting benzyl chloride with sodium thicsulfate in substantially equal molecular proportions in the presence of water, and subseguently subjecting the sodium benzyl thiosulate thus produced, and without isolation from the reaction mixture containing it, to hydrolytic decomposition by adding an acid thereto, such as hydrochloric or sulfuric acid, and heating the mixture, preferably to or near the boiling temperature as described in our co-pending application filed of even date herewith, which has matured into Patent No. 1,729,615, granted October 1, 1929. When the reaction is complete, two liquid layers are produced, an oily layer and an aqueous layer.

The oily layer, which comdprises the flotation agent particularly utilize in the present invention, is separated in any suitable manner. The flotation or modifying agent thus obtained is relatively insoluble in water but is soluble in alcohol, benzene, aniline, xylidine, cresol. pine oil, carbon tetrachloride and other organic solvents. It is comprised chiefly of benzyl mercaptan (about to 75 percent) associated with dibenzyl disulfide (about 20 to 35 percent), together withrelatively small amounts of other hydrolytic decomposition products of sodium benzyl thiosnlfate.

Application filed Kay. 80, 1987. Serial Il'o. 198,058.

Analogous products can be obtained in asimilar manner b the decomposition in an acid medium of t e metal salts of other aralkyl thiosulfates obtained by the action of aralkyl halides on sodium thiosulfate. It will be understood, however, that the use in flotation operations of mixtures comprising an aralkyl mercaptan and a diaralkyl disulfide, whether said mixtures are prepared by mechanical or by chemical recesses, are included within the scope of t e present invention.

In carrying out the flotation process, the flotation a ent comprising the product obtained by ecomposmg the metal salt of an aralkyl ester of thiosulfuric acid, such as sodium benzyl thiosulfate, in acid ueous solution may be incorporated with t e ore or mineral pulp in any suitable manner and at any suitable time which will insure a satis factory flotation o eration. For example, it may be introduce in the free state or it may be dissolved, suspended or dispersed in any suitable solvent or dispersing agent such as, for example, water, caustic alkali, or one or more of the usual flotation oils or oil mixtures, or in any suitable organic solvent or medium such as, for example, an aromatic h drocarbon or an aromatic amine or a bone and incorporating the resulting so ution, suspension or dispersion with the ore or ore ulp. While the present flotation agent shows marked action as a flotation or collecting agent in ore concentration, it generally exhibits. weak and usually insuflicient frothing qualities and, therefore, is ordinarily used to advantage in conjunction with any suitable and -well-known frothing agent, a. pine oil, crude turpentine, tar acids, etc. t may he sometimes used with advantage'in conjunction with other flotation agents.

The process of the present invention may be carried out in any suitable apparatus, for example, those of the pneumatic type such as the Callow cell, or those where the air is incorporated with the mixture by mechanical agitation such as the Janney apparatus, or the like.

It is of advantage in many cases, such as with certain co per ores, to submit the pulp to'the action 0 an amount of alkali to give as j ,i so

it a distinctly alkaline reaction before subjecting it to the flotation operation with the aid of the flotation agent of the present invention. The alkali may be caustic alkali such as caustic soda, or an alkaline salt such as soda ash, or it may be calcium oxide or hydrate.

In the diflerential separation of various minerals, such as zinc blende from associated minerals, the presence of an alkali metal cyanide, or of copper sulfate or other salts, is sometimes advantageous.

The amount of flotation agent required to be used in the flotation operation will vary, it depending partly on the character and composition of the ore, and partly on other factors. Ordinarily. about one-sixth to onefourth pound of the flotation agent per ton of ore will be sufficient; while in other cases larger or smaller amounts than this may be required.

The invention will be further illustrated by the following Specific examples, but it will be understood that the invention is not limited thereto. The parts are by weight.

Example 1.500parts of a copper sulfide ore (from Butte. Montanalassaying 1.51

percent of copperwas ground in a ball mill 4 with 210 parts of water and 0.75 parts of hydratedlime (equivalent to 3 pounds per ton of. ore) until practically all of the mixture was sufliciently fine to pass a 40-mesh screen. The ground pulp was diluted with water to give about 16 percent solids and subjected to flotation in a Janney flotation apparatus with the addition in the free state of 0.042 parts (equivalent to one-sixth pound per ton of ore) of the flotation agent pre pared by the hydrolytic decomposition of sodium benzyl thiosulfate as herein described. The mixture was agitated for 20 minutes during which time 0.04 parts of'pine oil was introduced. 47.1 parts of a concentrate assaying 15.8 percent of copper was obtained which is a recoverv in the concentrate of 96.5 percent of the copper. The tailings assayed 0.06 percent copper. It may be remarked that in this test 31.2 parts of a concentrate assaving 22.5 percent copper was obtained at the end of the first 10 minutes of agitation. During the next '10 minutes of agitation.'15.9 parts of a concentrate assaying 2.92 percent copper was obtained.

Example 2.-500 parts of a copper sulfide ore (from Butte, Montana) assaying 1.51 percent copper was treated as in Example 1 I except 0.0625 parts (equivalent to one-fourth pound per ton of ore) of said flotation agent dissolved in a small amount of one-tenth normal caustic soda solution was used in place of the 0.042 parts of the agent in the free or undissolved state. 43.2 parts of con- I centrate assaying 16.165 percent co per was obtained, which is a recovery of 95. percent als, the process which comprises subjecting a of the copper. percent copper.

It will thus be'hoted that the present invention contemplates the utilization as a flotation agent of the product obtained by the hydrolytic decomposition of a metal salt of an aralkyl ester of thiosulfuric acid, particularly sodium benzyl thiosulfate, in acid solution; that the flotation agent may be incorporated with thc'ore or mineral pulp in any well-known or suitable manner; that it may be used in the free state or in solution, suspension or dispersion in any suitable solvent or medium; that it may be used in the diflerential separation of minerals; and that it may be. used in conjunction with afrothing agent or with other flotation agents, or both.

It may be understood that the present in vention is applicable to the treatment of The tailings assayed 0.07

various kinds of mineral mixtures, both natural apd artificial, which are amenable to concentration by flotation processes.

We claim: 7 y

1. In eflecting the concentration of minerals, the process which comprises adding to the mineral pulp a flotation agent comprising the product relatively insoluble in water obtainable by the decomposition of a. metal salt of benzyl thiosulfuric acid in the presence of water and an acid, and subjecting the mixture to a froth flotation operation;

2. In effecting the concentration of minermineral pulp to a froth flotation operation in the presence of the product relatively insoluble in water obtainable by the hydrolytic decomposition of sodium benz'yl thiosulfate in the presence of water and an acid.

3. In effecting the concentration of minerals, the process which comprises incorporating with a mineral pulp an aralkyl mercaptan associated with a diaralkyl disulfide, and subjecting the mixture to a froth flotation operation. I no 4. In efl'ecting the concentration of minerals, the process which comprises subjecting a mineral pulp to a froth flotation operation in the presence of an aralkyl mercaptan, a diaralkyl disulfide, and other organic products resulting from the hydrolytic decomposition of an aralkyl thiosulfuric acid.

In effecting the concentration of minerals, the process which comprises subjecting a n mineral pulp to a froth flotation operation in the presence of benzyl mercaptan, dibenzyl disulfide, and other organic products result ing from the decomposition of sodium benzyl thiosulfate in the presence of an acid.

6. In effecting the concentration of minerals, the process which comprises incorporating with a mineral pulp a composition containing about 60 to 75 percent benzyl mercaptain and 20 to 35 percent dibenzyl disul- I30 I "tide; and subjecting the mixture to a froth flotation 0 eration.

7. In e ecting the concentration of mineral s,- the process which comprises subjecting an ore pulp to a froth flotation operation in the presence of the product relatively insoluble in water obtainable by decomposing sodium benzyl thiosulfate in aqueous solution in the presence of sulfuric acid.

8. In effecting the concentration of minerals, the process which comprises subjecting an ore pulp to a froth flotation operation in the presence of the product relatively insol-- uble in water which can be obtained by first reacting benzyl chloride with sodium thiosulfate in the presence of water with formation of a reaction mixture containing sodium benzyl thiosulfate and subsequently heating said i reaction mixture in the presence of sulfuric acid.-

9. In efi'ecting the concentration of minerals, the process which comprises subjecting an ore pulp to a froth flotation operation in the presence of a mixed product containing benzyl mercaptan, said product being relatively insoluble in water and obtainable by heating sodium benzyl thiosulfate in aqueous solution in the presence of an acid added thereto.

10. In eflecting the concentration of minerals, the process which comprises subjecting an ore pulp to a froth flotation operation in the presence of benzyl mercaptan associated with dibenzyl disulfide.

11. In efl'ecting the concentration of a copper sulfide ore, the process which comprises subjecting an alkahnepulp of the ore to a froth flotation operation in the presence of the product relatively insoluble in water which can be obtained b the decomposition of a metal salt of an aralli yl thiosulfuric acid in the presence of water and an acid.

12. In effecting the concentration of a cop per sulfide ore, the process which comprises subjecting an alkaline pulp of the ore to a froth flotation operation in the presence of the product relatively insoluble in water which can be obtained by the decomposition of sodium benz l thiosulfate in the presence of water and 0 an acid.

13. In effecting the concentration of a copper sulfide ore, the process which comprises subjecting an alkaline pulp of the ore to a froth flotation operation in the presence of an aralkyl mcrcaptan and a diaralkyl disulfide.

14. In effecting the concentration of a copper sulfide ore, the process which comprises subjecting an alkaline pulp of the ore to a froth flotation operation in the resence of benzyl mercaptan and dibenzyl isulfide.

In testimony whereof we aflix our signatures.

RAYMOND W. HESS. JOSEPH M. F. LEAPER.