US755951A - Process of treating ores. - Google Patents

Process of treating ores. Download PDF

Info

Publication number
US755951A
US755951A US16600803A US1903166008A US755951A US 755951 A US755951 A US 755951A US 16600803 A US16600803 A US 16600803A US 1903166008 A US1903166008 A US 1903166008A US 755951 A US755951 A US 755951A
Authority
US
United States
Prior art keywords
cyanid
treatment
oxid
sulfids
ferrous
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US16600803A
Inventor
Joseph Smith
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US16600803A priority Critical patent/US755951A/en
Application granted granted Critical
Publication of US755951A publication Critical patent/US755951A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • C22B11/08Obtaining noble metals by cyaniding

Definitions

  • FeSO4 ferrous sulfate
  • H2SO4 some free sulfuric acid
  • FeO ferrous oxid
  • the ferrous sulfate and the free sulfuric acid can be easily neutralized in the usual way with a caustic lime or other alkaline treatment; but the ferrous oxid (FeO) cannot be neutralized or made inactive by lime or by any alkaline treatment, and its presence is productive of an abnormal and excessive consumption of cyanid in the after treatment, the quantity actuallyconsumed beingonly limited by the pro-
  • FeO ferrous oxid
  • the procedure has been to admit the cyanid solution to them directly after the crushing or grinding and while they were yet in a moist condition.

Description

portion of the ferrous oxid present.
UNITED, STATES Patented March 29, 1904:.
PATENT OFFICE.
PROCESS OF TREATING ORES.
SPECIFICATION forming part of Letters Patent No. 55,951, dated March 29, 1904.
Application filed July 17, 1903. Serial No. 166,008. (No specimens.)
T0 aZl whom, it may concern:
Be it known that I, J OSEPH SMITH, a citizen ofthe United States,residing at San Francisco, in the county of San Francisco and State of California, have invented certain new and useful Improvements in Processes of Treating Ores, of which the following is a specification.
In the modern treatment of gold and silver bearing iron sulfids by the cyanid process it has been found desirable to first reduce the sulfids by grinding or crushing from the coarse grains in which they leave the concentratingtables,so that they will pass a fine-mesh screen, the degree of fineness varying in different cases to suit the working of different sulfids. For economic reasons it is not practicable to crush them in the dry state, and to obtain a speedy and inexpensive operation it is necessary to crush or grind them with water. In the course of this grinding or crushing a certain decomposition occurs, producing ferrous sulfate, (FeSO4,) some free sulfuric acid, (H2SO4,) and ferrous oxid, (FeO,) a partiallyoxidized iron set free from the pyrites. The ferrous sulfate and the free sulfuric acid can be easily neutralized in the usual way with a caustic lime or other alkaline treatment; but the ferrous oxid (FeO) cannot be neutralized or made inactive by lime or by any alkaline treatment, and its presence is productive of an abnormal and excessive consumption of cyanid in the after treatment, the quantity actuallyconsumed beingonly limited by the pro- When attempts have heretofore been made to treat gold and silver bearing iron sulfids, the procedure has been to admit the cyanid solution to them directly after the crushing or grinding and while they were yet in a moist condition. The result'has been that the consumption of cyanid was always high, (in many cases so high as to render the treatment commercially impossible,) the extraction of the precious metals in many cases was very low, and the cyanid solution itself, which should be kept free of the base metals, was rendered foul by the large quantities of ferrous oxid which it was continuously taking into solution. To render this ferrous oxid insoluble in cyanid solutions, thereby preventing such solution.
lutions from becoming charged with base mat ter, to render more effective the extraction of the precious metals, to prevent the destruction of unnecessarily large quantities of the cyanide used as solvents, and to reduce to a minimum the cost of treatment are the objects of the process which constitutes my invention. Under the proper conditions this ferrous oxid is very susceptible of complete oxidation, so as to become a ferric oxid. As ferrous oxid it destroys potassium cyanid by the following formula:
but if oxidized to the ferric-oxid statesviz. E6203 and Fe3O4it becomes insoluble in cyanid solutions, and hence the salt is not affected by the iron during treatment. To secure said oxidation, I proceed in the following way: The sulfids crushed or ground to pass the desired-mesh screen are drained of the water used in crushing, given an alkaline treatment in the usual way, and the whole mass previous to cyaniding is subjected to a drying process with the free access of air, The drying may be performed by a low-fire heat, but preferably by steam heat, no danger of sparking the sulfids attending the latter method. If fire-drying is employed, care must be exercised that no roasting occur, which might produce a decomposition of the unaltered sulfids, and more acid. In all cases the drying should be completed in a moderate length of time, no chance being given the material for further weathering. By this treatment the partial oxidation or rusting of the iron, which commenced during the grinding period, is completed, and the whole of the soluble iron is rendered insoluble and inert in cyanid solutions. The result is that in the after cyanid treatment the cyanid consumption is low, the solution is not contaminated, and the extrac tion of the precious metals is good.
The above-stated facts in relation to the iron can be demonstrated in the following way: When cyanid in solution is destroyed, some metal, base or otherwise, has combined with it chemically and has been taken into so- In cyaniding in the old way without preliminary drying the base entering into ferrous oxid contained in a mass of moist crushed ore, which method consists in applying heat to said mass in the presence of air, previous to its treatment by the cyanid solution.
In testimony whereof Ihave aflixed my signature, in presence of two witnesses, this 7th day of July, 1903.
JOSEPH SMITH.
Witnesses:
F. M. BURT, LI W. SEELY.
US16600803A 1903-07-17 1903-07-17 Process of treating ores. Expired - Lifetime US755951A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US16600803A US755951A (en) 1903-07-17 1903-07-17 Process of treating ores.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US16600803A US755951A (en) 1903-07-17 1903-07-17 Process of treating ores.

Publications (1)

Publication Number Publication Date
US755951A true US755951A (en) 1904-03-29

Family

ID=2824443

Family Applications (1)

Application Number Title Priority Date Filing Date
US16600803A Expired - Lifetime US755951A (en) 1903-07-17 1903-07-17 Process of treating ores.

Country Status (1)

Country Link
US (1) US755951A (en)

Similar Documents

Publication Publication Date Title
US755951A (en) Process of treating ores.
US1461807A (en) Process of treating ores
US702047A (en) Process of rendering metallic sulfids soluble.
US2890933A (en) Recovery of uranium values from uranium bearing raw materials
US732641A (en) Metal-leaching process.
US1044316A (en) Process of extracting nickel.
US824699A (en) Process of treating refractory ores containing iron sulfids.
US138500A (en) Improvement in treating gold and silver ores
US483639A (en) Jules strap
US2127240A (en) Chloridizing-cyanide process for extracting values from ores
US635056A (en) Process of treating ore.
US1185817A (en) Process of treating metal and mineral bearing materials.
US731590A (en) Process of leaching ores or tailings with solutions of alkaline cyanids.
US962383A (en) Process of treating ores.
US2454336A (en) Process for the treatment of goldand silver-bearing ores, residues, and other products
US52834A (en) Improved process for separating gold and silver from ores
US659340A (en) Process of extracting zinc and copper from their ores.
US780293A (en) Metal-leaching process.
US814452A (en) Metal-leaching process.
US659338A (en) Process of extracting zinc and copper from their ores.
US769254A (en) Method of extracting precious metals from their ores.
US223913A (en) Ottokae
US1407045A (en) Treatment of ores containing oxides of copper
US870786A (en) Process of obtaining pure copper.
US801470A (en) Process of treating precious-metal-bearing materials.