US2125852A

US2125852A - Process of concentrating ores and flotation agents therefor

Info

Publication number: US2125852A
Application number: US141874A
Authority: US
Inventors: Anderson W Ralston; William O Pool
Original assignee: Armour and Co
Current assignee: Armour and Co
Priority date: 1937-05-10
Filing date: 1937-05-10
Publication date: 1938-08-02
Anticipated expiration: 1955-08-02

Description

Patented Aug. 2, 1938 UNITED STATES PATENT OFFICE PROCESS OF CONCENTRATING ORES AND FLOTATION AGENTS THEREFOR No Drawing. Application May 10, 1931. Serial No.

6 Claims.

This invention relates. to processes of concentrating ores and flotation agents thereof, and it comprises processes wherein an aqueous pulp of the ore, the mineral values of which are to be separated from the gangue, are subjected to flotation processes in the presence of a flotation agent comprising mixtures of saturated and unsaturated aliphatic carboxyllc acids containing from about five to ten carbon atoms associatedwith 10 low molecular weight straight-chain saturated and unsaturated aliphatic hydrocarbons, said flotation agent advantageously being prepared by subjecting mixtures of aliphatic nitriles and such hydrocarbons to hydrolysis and the recovery of i5 mixtures of such aliphatic carboxylic acids dissolved in said hydrocarbons.

Flotation agents are used in great quantities in the concentration of. ores by flotation methods. These agents modify the surface of the desired values in the ore in such a way that the values are floated, leaving the gangue behind. Thus, for example, in thefroth flotation of ores an aqueous pulp of the ore is first prepared, flotation agents are added thereto, and the mixture is aerated whereby metalliferous values in the ore collect as a froth which can be readily skimmed off and the metal values therein recovered. Similarly, nonmetalliferous values, such as phosphate rock, can

be separated from the siliceous gangue.

Oleic acid was one of the first flotation agents used in the froth flotation of ore, and many other flotation agents have since been proposed. Flotation methods require that the surface of the ore values to be floated should be modified with respect to its interfacial tension towards water so that the surface is preferentially wetted by water. When froth flotation is employed a frothing agent must also be present to assist in the formation of a relatively stable froth during the aeration. The minute bubbles formed adhere to the surface-modified ore value causing them to rise as a froth.

Oleic acid, fuel oil and other hydrocarbon oils are frequently used as collectors.

substances which appear to have a selective action on the values in the ore it is desired to float so that they modify the interfacial tension thereof with respect to water. The frothing substance is commonly a soap. Frequently the flotation agents used are mixtures, the constituents of which perform the two functions just stated; and

sometimes a single substance will perform both functions.

There have been many different flotation agents proposed, and of late most of these agents These are.

are synthetically-prepared chemicals such as xanthates. Synthetic flotation agents are quite expensive, and the art has desired more efficient flotation agents which could be prepared at little cost and which would function as flotation agents 5 with most of the ores commercially subjected to this type of concentrating process. Many oxide and carbonate ores, for example, are not readily floated by flotation agents hitherto proposed without some special treatment of the ore prior 10 to concentration.

In the Ralston, Pool and Harwood Patents 2,033,536 and 2,033,537 there are described methods of pyrolytically decomposing high molecular weight nitriles, such as stearo-nitrlle, palmitol6 nitrile, lard fatty acid nitriles and the like, whereby distillates containing mixtures of lower molecular weight nitriles and hydrocarbons are obtained. Thus, for example, from stearonitrile there can be obtained a condensate boiling from 20 40 C. toabout 275 C. which can be fractionated to give distillates having any desired boiling point range within the above upper and lower limits, and by fractionation of the said condensate fractions or cuts containing two or more nitriles hav- 25 ing from three to ten carbon atoms can be readily obtained.

For example, when stearonitrlle is heated at a cracking temperature under pressure the condensate is a pale yellow liquid containing a mix- 30 ture of saturated and unsaturated nitriles associated with liquid hydrocarbons. This condensate, when fractionated, yields the following fractions, assuming the starting mixture is parts of condensate. 35

25 parts fraction 1 boiling range 40 C.- C.

25 parts fraction 2 boiling range 110 C.- C.

25 parts fraction 3 boiling range 175 C.-220 C.

20 parts fraction 4 boiling range 220 C.-275 C. 40

5 parts residue boiling range above 275 C.

Fraction 1 is mostly capronitrile and low boiling hydrocarbons. Fraction 2 is mostly enanthonitrile and capronitrile together with saturated and unsaturated hydrocarbons. Fraction 3 is 45 mostly pelargononitrile, caprylonitrile, enanthonitrile, saturated and unsaturated hydrocarbons. Fraction 4 is mostly lauronitrile, undecylonitrile, caprinitrile, pelargonitrile, saturated and unsatu rated hydrocarbons. Each fraction contains an 50 amount of unsaturated nitriles equivalent to the saturated nitriles present and an amount of unsaturated hydrocarbons equivalent to the saturated. In other words, they contain approxi-' mately fifty percent unsaturated compounds. 65

There may also be present small amounts of propionitrile, butyronitrile and valeronitrlle.

When the starting material is an unsaturated nitrile the condensate will be higher in. unsaturated nitriles and hydrocarbons than when the starting material is a saturated nitrile.

We have now discovered that when mixtures containing aliphatic nitriles of fromthree to ten carbon atoms, together with aliphatic hydrocarbons are subjected to hydrolysis, and the hydrolyzate is treated with a mineral acid we can obtain a hydrocarbon solution of aliphatic carboxylic acids corresponding to the nitriles in the starting mixture, and that such mixture of acids and hydrocarbons is a markedly suitable flotation agent for concentrating many ores.

Thus, for example, when we wish to make our flotation agent from the mixture of nitriles and hydrocarbons we prepare a mixture of caustic soda solution, about 20 percent strength, and the hydrocarbon solution of nitriles and subject the entire mixture to an elevated temperature in an autoclave or bomb. Thus we first isolate a nitrilehydrocarbon mixture having a boiling point range of 100 C. to 200 C. 2,500 parts by weight of this nitrile-hydrocarbon mixture is mixed with 2,000 parts by weight of a 20 percent solution of sodium hydroxide. The mixture is heated at about 200 C. in a closed vessel, such as autoclave or bomb, until all of the nitriles therein are converted to sodium salts of aliphatic acids corresponding to the nitriles present. Thus, for example, valeronitrile is converted to sodium pentanoate. Caprylonitrile is converted to sodium octanoate. The reaction mixture withdrawn from the autoclave is, therefore, a mixture of the hydrocarbons in the original nitrile starting mixture and an aqueous solution of sodium salts of aliphatic carboxylic acids. To this reaction mixture we add a mineral acid, such as sulfuric or hydrochloric acid, to liberate free aliphatic carboxylic acids from their sodium salts. These aliphatic carboxylic acids are highly soluble in the hydrocarbons present in the mixture and readily dissolve therein. In a sense the hydrocarbons present can be looked upon as an extraction agent for the aliphatic carboxylic acids. We then shake or otherwise agitate the mixture of aliphatic acids, water solution, and hydrocarbons so that solution of the aliphatic acids in the hydrocarbon layer is facilitated, and thereafter we allow the hydrocarbon layer to stratify and decant a hydrocarbon solution of aliphatic carboxylic acids. It is this product which we use as a flotation agent in our process.

The composition of the carboxylic acid-hydrocarbon mixture can vary over wide limits depending largely upon the boiling point range of the nitrile-hydrocarbon mixture subjected to hydrolysis. By appropriate fractionation of the reaction products obtained from cracking higher aliphatic nitriles, namely those containing eighteen carbon atoms on the average, it will be apparent that we can obtain mixtures of nitriles and hydrocarbons wherein the predominating nitriles contain from three to ten carbon atoms, and the hydrocarbons contain from five to ten carbon atoms. Approximately flfty percent of the nitriles and hydrocarbons present will contain one double bond and we believe that the double bond is in a terminal position.

Thus, by condensing various fractions of nitrilehydrocarbon mixtures and subjecting these to hydrolysis we are able to obtain flnal reaction products consisting of at least one aliphatic caramass:

boxylic acid having from three to ten carbon atoms dissolved in an aliphatic straight-chain hydrocarbon containing from flve to fourteen carbon atoms. Our flotation agents will contain two or more saturated or unsaturated aliphatic corboxylic acids dissolved in a mixture of hydrocarbons. This is because the nitrile mixtures which we hydrolyze will almost always contain at least two nitriles because it is very diflicult to separate, by distillation, a saturated nitrile from an unsaturated nitrile containing the same number of carbon atoms.

Thus, in broad aspects, our flotation agents comprise hydrocarbon solutions of at least two aliphatic carboxylic acids containing from three to ten carbon atoms, at least one of said acids being unsaturated.

The flotation agents of the present invention can be used to concentrate by froth flotation methods any of the following minerals from ores containing the same.

Pyrolusite Franklinite Malachite Apatite Chalcopyrlte Ilmenite Chalcocite Zincite Galena Magnetite Rutile Pyrite When using our flotation agents we proceed in the accepted ways of this art. Namely, we first prepare a ground-up mixture of the ore, avoiding the presence of large quantities of slime. Ordinarily the ore is ground to a mesh of about 40 to and then admixed with water to form a pulp in the usual way. To this pulp we add our flotation agents in proportions of about to 300 parts by weight of flotation agent to one million parts by weight of the water. The mixture is then subjected to froth flotation in the usual way and a mineral concentrate skimmed oil! as a froth.

Thus, for example, we prepare our flotation agent by hydrolyzing a nitrile hydrocarbon mixture having a boiling point range of from 100 C. to 200 C., acidify the hydrolyzate, and separate off a hydrocarbon solution containing saturated and unsaturated aliphatic carboxylic acids having three to eight carbon atoms. As a general rule, about equal quantities of aliphatic acids containing three, four, flve, six, seven and eight carbon atoms and their unsaturated analogues will be present. In other words, these acids will contain about equal quantities of propionic acid and other acids in the series up to and including capryllc (octanoic). The hydrocarbons present will have flve to ten carbon atoms. We add about 300 parts per million of such a mixture to the ground aqueous pulp of pyrolusite, aerate the pulp in the usual way and skim off the froth of concentrated pyrolusite.

So far as we are aware we are the first to describe mixtures of saturated and unsaturated aliphatic carboxylic acids having from three to ten carbon atoms dissolved in straight-chain saturated and unsaturated hydrocarbons, and we broadly claim our invention with respect thereto. This mixture is superior for the flotation of both metallic and non-metallic ores because of the presence of both saturated and unsaturated straight-chain acids. In the presence of the oleflns and paraflins the mixture performs the double function of preferentially wetting minerals to be floated whereby its surface tension with respect to water is so changed that the mineral will float, together with imparting frothing amass:

our invention is not to be construed so narrowly as to exclude the addition of further floating agents and irothing agents should such be desired.

Having thus described our invention, what we claim is:

1. The process of concentrating ores which comprises subjecting the ore to froth flotation separation in the presence of a mixture of saturated and unsaturated aliphatic carboxylic acids having from three to ten carbon atoms and saturated and unsaturated aliphatic straight-chain hydrocarbons.

2.'The process of concentrating ores, which comprises subjecting the ore to froth flotation separation in the presence oi a mixture of saturated and unsaturated aliphatic carboxylic acids having from three to ten carbon atoms and saturated and unsaturated aliphatic straight-chain hydrocarbons, said mixture being derived from a mixture of aliphatic nitriles and hydrocarbons resulting from the pyrolytic decomposition of aliphatic nitriies having eighteen carbon atoms.

3. In the froth flotation of ores the step comprising subjecting an aqueous pulp of the ore to froth flotation in the presence oi a flotation agent comprising an admixture of at least one unsaturated aliphatic carboxylic acid having from three to ten carbon atoms and saturated and unsaturated straight-chain aliphatic hydrocarbons having from live to iourten carbon atoms.

4. In the i'roth flotation oi ores the step which comprises subjecting an aqueous pulp of the ore to froth flotation in the presence or a flotation agent comprising the product of hydrolyzing a mixture of aliphatic nitriles containing from three to ten carbon atoms and straight-chain aliphatic hydrocarbons.

5. A flotation agent comprising an aliphatic hydrocarbon solution of saturated and unsaturated aliphatic carboxylic acids having from three to ten carbon atoms.

6. A flotation agent comprising an aliphatic hydrocarbon solution or at least one unsaturated