[go: up one dir, main page]

US1678311A - Flotation method - Google Patents

Flotation method Download PDF

Info

Publication number
US1678311A
US1678311A US689584A US68958424A US1678311A US 1678311 A US1678311 A US 1678311A US 689584 A US689584 A US 689584A US 68958424 A US68958424 A US 68958424A US 1678311 A US1678311 A US 1678311A
Authority
US
United States
Prior art keywords
water
residuum
flotation
froth
sulfated
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
US689584A
Inventor
Gale L Adams
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
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 Standard Oil Development Co filed Critical Standard Oil Development Co
Priority to US689584A priority Critical patent/US1678311A/en
Priority to US209189A priority patent/US1678312A/en
Application granted granted Critical
Publication of US1678311A publication Critical patent/US1678311A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/012Organic compounds containing sulfur
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/016Macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2203/00Specified materials treated by the flotation agents; Specified applications
    • B03D2203/02Ores
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S209/00Classifying, separating, and assorting solids
    • Y10S209/901Froth flotation; copper

Definitions

  • This invention relates to flotation methods such as are used in concentrating ores.
  • flotation methods such as are used in concentrating ores.
  • the finely ground ore is agitated with water 6 and a small proportion of an oily material.
  • the widely used flotation oils have comprised creosote oils, particularly those derived from Wood distillation and pine oils. With the gradual decrease in 10 sources of raw materials for such. oils, it is becoming increasingly desirable to provide other agents which will be equally or more satisfactory.
  • This latter is to be had as a byproduct in the manufacture of alcohols from olefines
  • olefine gases are absorbed in sulfuric acid under sulfating conditions while largely and preferably entirely avoiding the formation of tarry and resinoussulfonated material and similar products and sludges.
  • This is accomplished by contacting the olefine material with acid for a comparatively short period of time while emtreatment of petroleum fractions.
  • the sulfated products are hydrolyzed by addition of Water and the alcohol-containing layer separated off.
  • the oily layer or residuum contains polymerized hydrocarbons and small quantities of higher alcohols.
  • such a sodium sulfonate contains about 40% of moisture, and in making up compositions with this as an ingredient I prefer ordinarily to employ from .1% to 5% of such sulfonate.
  • Usually such sulfonate carries also some free alkali, suflicient to impart an alkaline reaction, and this is generally of advantage. In some instances it is desirable also to add alkali. In instances where an alkaline reaction is not wanted, it can be readily obviated by addition of an acid.
  • the amount of flotation oil used will vary in different cases within considerable limits, in general for instance between about 0.05 and 1%, and with different ores the proportions of ingredients will necessarily be somewhat varied and, as already indicated, in some instances the sulfonate, or both sulfonate and residuum from the hydrolysis of sulfated olefines may be omitted with sufficiently satlsfactory results.
  • a process of concentrating ores which comprises agitating the finely divided ore with water and a small quantity of a mixture containing 80% of pressure still tar, about 19% of residuum from hydrolysis of sulfated olefines, and about 1% of a water- 3 soluble sodium sulfonate of petroleum hydrocarbons. aerating to form a froth and separating the froth.
  • a process of concentrating ores which comprises agitating the finely dividedv ore with Water and a small quantity of pressure still tar, residuum from hydrolysis of sulfated gaseous olefines, and a Water-soluble sodium sulfonate of petroleum hydrocarbons, aerating to form a froth and separating the froth;
  • a process of concentrating ores which comprises agitating the finely divided ore with Water and a small quantity of pressure still tar and residuum from hydrolysis of sulfated olefines substantially free from sulfonio compounds, aerating to form a froth and separating the froth.
  • a process of concentrating ores which comprises agitating the finely divided ore with water and a small quantity of residuum from the cracking of petroleum hydrocarbons and a reinforcing agent substantially comprised of polymerized hydrocarbons, aerating to form a froth and separating the froth. 5.
  • a process of concentrating ores which comprises agitating the finely divided ore with Water and a small quantity of hydrocarbon residuum from the cracking of petroleum hydrocarbons.

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

Patented July 24, 1928.
UNITED STATES PATENT orrics.
GALE L. ADAMS, OF ELIZABETH, NEW JERSEY, ASSIGNOR T STANDARD OIL DEVEL- OIPMENT COMPANY, A CORPORATION OF DELAWARE.
FLOTATION METHOD.
No Drawing.
This invention relates to flotation methods such as are used in concentrating ores. In the present day flotation methods the finely ground ore is agitated with water 6 and a small proportion of an oily material. Heretofore the widely used flotation oils have comprised creosote oils, particularly those derived from Wood distillation and pine oils. With the gradual decrease in 10 sources of raw materials for such. oils, it is becoming increasingly desirable to provide other agents which will be equally or more satisfactory.
I have now found that the residuums from cracking mineral hydrocarbons, particularly residues from cracking petroleum where the cracking operation has been carried out under pressure, furnish very desirable flotation material. In some instances this may bereinforced with other'agents as, for instance, a minor proportion of pine oil, say 15%; but I find that a material which is yet superior to the pine oil is had in the residuum from the hydrolysis of sulfated olefines. This latter is to be had as a byproduct in the manufacture of alcohols from olefines Where olefine gases are absorbed in sulfuric acid under sulfating conditions while largely and preferably entirely avoiding the formation of tarry and resinoussulfonated material and similar products and sludges. This is accomplished by contacting the olefine material with acid for a comparatively short period of time while emtreatment of petroleum fractions. The sulfated products are hydrolyzed by addition of Water and the alcohol-containing layer separated off. The oily layer or residuum contains polymerized hydrocarbons and small quantities of higher alcohols. In compounding flotation oil, where this material is used I prefer ordinarily to use from 5% to 30%, the balance up to 100% being made 5 up, as above indicated, of the residuum from ploying weaker acid than is used in the acid Application filed January 30, 1924. Serial No. 689,584.
ing oils with fuming or concentrated sulfurie acid and preparing a sodium salt or alkaline metal salt of the sulfonic acid. As customarily prepared, such a sodium sulfonate contains about 40% of moisture, and in making up compositions with this as an ingredient I prefer ordinarily to employ from .1% to 5% of such sulfonate. Usuallysuch sulfonate carries also some free alkali, suflicient to impart an alkaline reaction, and this is generally of advantage. In some instances it is desirable also to add alkali. In instances where an alkaline reaction is not wanted, it can be readily obviated by addition of an acid.
i As an illustration of the practice of the invention the following example may be noted: An ore containing 1.9% copper as chalcocite and chalcopyrite, was ground as usual and agitatedwith water in a flotation machine, using 1.4 lbs. of flotation oil per ton of ore, the oil being a compound of 80% pressure still tar, 19.1% of residuum from hydrolysis of sulfated olefines and .9% of water-soluble sodium sulfonate of petroleum hydrocarbons, the sulfonate having been preliminarily stabilized by long heating on a water bath.
It will be understood that the amount of flotation oil used will vary in different cases within considerable limits, in general for instance between about 0.05 and 1%, and with different ores the proportions of ingredients will necessarily be somewhat varied and, as already indicated, in some instances the sulfonate, or both sulfonate and residuum from the hydrolysis of sulfated olefines may be omitted with sufficiently satlsfactory results.
"What- I claimis:
1. A process of concentrating ores, which comprises agitating the finely divided ore with water and a small quantity of a mixture containing 80% of pressure still tar, about 19% of residuum from hydrolysis of sulfated olefines, and about 1% of a water- 3 soluble sodium sulfonate of petroleum hydrocarbons. aerating to form a froth and separating the froth.
2. A process of concentrating ores, which comprises agitating the finely dividedv ore with Water and a small quantity of pressure still tar, residuum from hydrolysis of sulfated gaseous olefines, and a Water-soluble sodium sulfonate of petroleum hydrocarbons, aerating to form a froth and separating the froth;
3. A process of concentrating ores, which comprises agitating the finely divided ore with Water and a small quantity of pressure still tar and residuum from hydrolysis of sulfated olefines substantially free from sulfonio compounds, aerating to form a froth and separating the froth. v
4. A process of concentrating ores, which comprises agitating the finely divided ore with water and a small quantity of residuum from the cracking of petroleum hydrocarbons and a reinforcing agent substantially comprised of polymerized hydrocarbons, aerating to form a froth and separating the froth. 5. A process of concentrating ores, which comprises agitating the finely divided ore with Water and a small quantity of hydrocarbon residuum from the cracking of petroleum hydrocarbons.
- GALE L. ADAMS.
US689584A 1924-01-30 1924-01-30 Flotation method Expired - Lifetime US1678311A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US689584A US1678311A (en) 1924-01-30 1924-01-30 Flotation method
US209189A US1678312A (en) 1924-01-30 1927-07-28 Flotation oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US689584A US1678311A (en) 1924-01-30 1924-01-30 Flotation method

Publications (1)

Publication Number Publication Date
US1678311A true US1678311A (en) 1928-07-24

Family

ID=24769076

Family Applications (1)

Application Number Title Priority Date Filing Date
US689584A Expired - Lifetime US1678311A (en) 1924-01-30 1924-01-30 Flotation method

Country Status (1)

Country Link
US (1) US1678311A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2446207A (en) * 1945-04-11 1948-08-03 Hercules Powder Co Ltd Froth flotation of ores employing a water-soluble salt of a cymene sulfonic acid
US2698088A (en) * 1952-03-11 1954-12-28 Pryor Edmund James Separation of minerals by froth flotation
US3890222A (en) * 1974-06-12 1975-06-17 Vojislav Petrovich Froth flotation method for recovery of minerals by means of alkali or ammonium alkyl alkylaryl, and aryl sulfinates as froth flotation reagents
US20210016231A1 (en) * 2018-03-29 2021-01-21 Compact Membrane Systems Inc. Carbon dioxide separation membranes and process

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2446207A (en) * 1945-04-11 1948-08-03 Hercules Powder Co Ltd Froth flotation of ores employing a water-soluble salt of a cymene sulfonic acid
US2698088A (en) * 1952-03-11 1954-12-28 Pryor Edmund James Separation of minerals by froth flotation
US3890222A (en) * 1974-06-12 1975-06-17 Vojislav Petrovich Froth flotation method for recovery of minerals by means of alkali or ammonium alkyl alkylaryl, and aryl sulfinates as froth flotation reagents
US20210016231A1 (en) * 2018-03-29 2021-01-21 Compact Membrane Systems Inc. Carbon dioxide separation membranes and process
US12370502B2 (en) * 2018-03-29 2025-07-29 Compact Membrane Systems, Inc. Carbon dioxide separation membranes and process

Similar Documents

Publication Publication Date Title
US2653970A (en) Olefin sulfitation process
US1678311A (en) Flotation method
US4925976A (en) Olefin sulfonation method
US2112362A (en) Flotation process
US1667277A (en) Treatment of fine coal
US1678312A (en) Flotation oil
US1772386A (en) Froth-flotation process and product for effecting same
US2256886A (en) Emulsion and method of preparing the same
US2343791A (en) Recovery of alkylation acids
US1530496A (en) Flotation oil
US1981506A (en) Froth production and frothproducing reagent
US2252138A (en) Process for production of thioethers
US1875001A (en) Emulsifiable oil and method of producing same
US1412233A (en) Fuel and process of making same
US2705681A (en) Bituminous composition and process of making it
US1573226A (en) Process for the concentration of oxidized ores
US2446159A (en) Distillation of alcohol from hydrolyzed mixtures of alkyl sulfates and sulfuric acid
US2426648A (en) Manufacture of sulfur compounds
US1915820A (en) Production of alkyl acid esters of polybasic inorganic acids
US1703838A (en) And warren t
US3148137A (en) Treating hydrocarbon distillates
US1718335A (en) Soaps from sulphonated mineral-oil acid sludge and method of making same
US1196274A (en) Product and process of manufacturing a product having the properties of soap.
US2768130A (en) Addition of oxo bottoms to an acid sludge for stabilization and pumping ease
US2058821A (en) Waterproofing composition