US1678311A - Flotation method - Google Patents
Flotation method Download PDFInfo
- 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
Links
- 238000005188 flotation Methods 0.000 title description 10
- 238000000034 method Methods 0.000 title description 9
- 229930195733 hydrocarbon Natural products 0.000 description 9
- 150000002430 hydrocarbons Chemical class 0.000 description 9
- 239000003921 oil Substances 0.000 description 9
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000003208 petroleum Substances 0.000 description 7
- 230000007062 hydrolysis Effects 0.000 description 6
- 238000006460 hydrolysis reaction Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 238000005336 cracking Methods 0.000 description 5
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 239000010665 pine oil Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- WHRZCXAVMTUTDD-UHFFFAOYSA-N 1h-furo[2,3-d]pyrimidin-2-one Chemical compound N1C(=O)N=C2OC=CC2=C1 WHRZCXAVMTUTDD-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 235000006173 Larrea tridentata Nutrition 0.000 description 1
- 244000073231 Larrea tridentata Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052947 chalcocite Inorganic materials 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229960002126 creosote Drugs 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 230000001180 sulfating effect Effects 0.000 description 1
- -1 sulfonio compounds Chemical class 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/012—Organic compounds containing sulfur
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/016—Macromolecular compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S209/00—Classifying, separating, and assorting solids
- Y10S209/901—Froth 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.
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)
| 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 |
-
1924
- 1924-01-30 US US689584A patent/US1678311A/en not_active Expired - Lifetime
Cited By (5)
| 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 |
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