Patent US4726896A successfully refreshed from Google Patents.
US4726896A
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Method and apparatus for on-stream analysis of slurried ore
Assignee: IMC Fertilizer Inc
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Filing: 1987-03-09
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Granted: 1988-02-23
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Expires: 2007-03-09
Abstract
Abstract An on-stream method and apparatus for measuring the content of a mineral constituent in a flowing slurried ore on a dry weight basis, is provided. The slurry density and flow rate, and optionally temperature, are measured to calculate a period of time during which the flowing slurry is diverted into a vessel in order to collect a target mass of ore solids therein. The time period is preferably calculated according to the following formula: ##EQU1## wherein: t is the period of time (sec); M solid is the selected target mass of the ore (g); Q slurry is the measured mass flow rate of the slurry (g/sec); p water is the density of water (g/cm 3 ); p slurry is the measured density of the slurry (g/cm 3 ); and p solid is the known density of the ore solids contained in the slurry (g/cm 3 ). The slurry flow is then diverted into the vessel for the duration of the calculated time period. During the diverting, the slurry density, flow rate, and optionally temperature are remeasured to calculate the actual mass of ore solids diverted into the vessel. The mineral constituent of the ore solids is then analyzed and determined as a percentage of the diverted slurry solids. The measurement method has particular utility in controlling froth flotation beneficiation processes.
Inventors
- 👤 Richard D. Grove
- 👤 Ronald L. Wiegel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 15:08
CPC Classifications
B; B03; B03B; B03B13/00; B03D; B03D1/00; B03D1/02; B03D1/028; B03D1/14; B03D1/24; B03D1/247; G; G01; G01F; G01F1/00; G01F1/74; Y; Y10; Y10T; Y10T137/00; Y10T137/0318; Y10T137/0324; Y10T137/0329; Y10T137/0335; Y10T137/2496; Y10T137/2499; Y10T137/2504; Y10T436/00; Y10T436/12
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
139 words
An on-stream method of measuring the content of a mineral constituent in an ore on a dry weight basis, the ore being in a flowing aqueous slurry, comprising: (a) selecting a target mass of ore solids to be collected and analyzed; (b) measuring the flow rate and density of the flowing slurry and calculating the time period necessary to collect the target mass of ore solids by diverting the flowing slurry into a vessel; (c) diverting the slurry flow into the vessel for the calculated time period; (d) measuring the flow rate and density of the diverted slurry and calculate the mass of ore solids actually collected in the vessel; (e) analyzing the content of the mineral constituent in the collected ore solids; and (f) determining the constituent content as a percentage of the collected mass of ore solids.
Claim 2
Dependent Claim
139 words
An on-stream method of measuring the content of a mineral constituent in an ore on a dry weight basis, the ore being in a flowing aqueous slurry, comprising: (a) selecting a target mass of ore solids to be collected and analyzed; (b) measuring the flow rate and density of the flowing slurry and calculating the time period necessary to collect the target mass of ore solids by diverting the flowing slurry into a vessel; (c) diverting the slurry flow into the vessel for the calculated time period; (d) measuring the flow rate and density of the diverted slurry and calculate the mass of ore solids actually collected in the vessel; (e) analyzing the content of the mineral constituent in the collected ore solids; and (f) determining the constituent content as a percentage of the collected mass of ore solids.
Claim 3
Dependent Claim
85 words
The method of claim 1, wherein said calculated time period is calculated according to the following formula: ##EQU11## wherein: M solid is the selected target mass of ore solids (g); Q slurry is the measured mass flow rate of the slurry (g/sec); P water is the density of water (g/cm 3 ); P slurry is the measured density of the slurry (g/cm 3 ); P solid is the known density of the ore solids (g/cm 3 ); and t is the period of time (sec).
Claim 4
Dependent Claim
13 words
The method of claim 1, wherein the mineral constituent is a phosphate mineral.
Claim 5
Dependent Claim
12 words
The method of claim 3, wherein the ore comprises a phosphate ore.
Claim 6
Independent Claim
188 words
A method of controlling the beneficiation of an ore in the froth flotation of an aqueous pulp containing the ore using a flotation reagent, by on-stream measurement of the content of a mineral constituent in a selected target mass of ore on a dry weight basis, the ore being in an aqueous slurry flowing from the froth flotation, comprising: (a) selecting a target mass of ore solids to be collected and analyzed; (b) measuring the flow rate and density of the flowing surry and calculating the time period necessary to collect the target mass of ore solids by diverting the flowing slurry into a vessel; (c) diverting the slurry flow into the vessel for the calculated time period; (d) measuring the flow rate and density of the diverted slurry and calculating the mass of ore solids actually collected in the vessel; (e) analyzing the content of the mineral constituent in the collected ore solids; (f) determining the constituent content as a percentage of the collected mass of ore solids; and (g) adjusting the amount of flotation reagent added to the aqueous pulp in response to the determined percent.
Claim 7
Independent Claim
188 words
A method of controlling the beneficiation of an ore in the froth flotation of an aqueous pulp containing the ore using a flotation reagent, by on-stream measurement of the content of a mineral constituent in a selected target mass of ore on a dry weight basis, the ore being in an aqueous slurry flowing from the froth flotation, comprising: (a) selecting a target mass of ore solids to be collected and analyzed; (b) measuring the flow rate and density of the flowing surry and calculating the time period necessary to collect the target mass of ore solids by diverting the flowing slurry into a vessel; (c) diverting the slurry flow into the vessel for the calculated time period; (d) measuring the flow rate and density of the diverted slurry and calculating the mass of ore solids actually collected in the vessel; (e) analyzing the content of the mineral constituent in the collected ore solids; (f) determining the constituent content as a percentage of the collected mass of ore solids; and (g) adjusting the amount of flotation reagent added to the aqueous pulp in response to the determined percent.
Claim 8
Dependent Claim
86 words
The method of claim 5, wherein said calculated time period is calculated according to the following formula: ##EQU12## wherein: t is the period of time (sec); M solid is the selected target mass of the ore (g); Q slurry is the mass flow rate of the slurry (g/sec); P water is the density of water (g/cm 3 ); P slurry is the density of the slurry (g/cm 3 ); p solid is the known density of the ore solids contained in the slurry (g/cm 3 ).
Claim 9
Dependent Claim
13 words
The method of claim 5 wherein the mineral constituent comprises a phosphate mineral.
Claim 10
Dependent Claim
12 words
The method of claim 5 wherein the ore comprises a phosphate ore.
Claim 11
Dependent Claim
30 words
The method of claim 5, wherein the aqueous slurry flowing from the froth flotation represents an average slurry composition obtained by periodically sampling a froth flotation exit stream over time.
Claim 12
Dependent Claim
16 words
The method of claim 1 or 5, wherein the analyzing step comprises a flow injection analysis.
Claim 13
Dependent Claim
162 words
Apparatus for on-stream measurement of a mineral constituent in an ore on a dry weight basis, the ore being in a flowing aqueous slurry, comprising: (a) means for measuring the flow rate and density of the flowing slurry and for calculating a period of time necessary to collect a selected target mass of ore solids in a vessel; (b) valve means for deverting the flowing slurry into said vessel, the vessel having sufficient capacity to contain the amount of slurry diverted over said period of time; (c) said means for measuring the flow rate and density of the flowing slurry further measures the flow rate and density of the diverted slurry; (d) means to calculate the mass of the ore solids actually collected in said vessel; (e) means for analyzing the content of the mineral constituent content in the ore solids collected in the vessel; (f) means to determine the constituent content as a percentage of the collected mass of ore solids.
Claim 14
Dependent Claim
162 words
Apparatus for on-stream measurement of a mineral constituent in an ore on a dry weight basis, the ore being in a flowing aqueous slurry, comprising: (a) means for measuring the flow rate and density of the flowing slurry and for calculating a period of time necessary to collect a selected target mass of ore solids in a vessel; (b) valve means for deverting the flowing slurry into said vessel, the vessel having sufficient capacity to contain the amount of slurry diverted over said period of time; (c) said means for measuring the flow rate and density of the flowing slurry further measures the flow rate and density of the diverted slurry; (d) means to calculate the mass of the ore solids actually collected in said vessel; (e) means for analyzing the content of the mineral constituent content in the ore solids collected in the vessel; (f) means to determine the constituent content as a percentage of the collected mass of ore solids.
Claim 15
Dependent Claim
216 words
Apparatus for controlling the beneficiation of an ore in the froth flotation of an aqueous pulp containing the ore using a flotation reagent, by on-stream measurement of the content of a mineral constituent in a selected target mass of ore on a dry weight basis, the ore being in an aqueous slurry flowing from the froth flotation, comprising: (a) means for measuring the flow rate and density of the flowing slurry and for calculating a period of time necessary to collect a selected target mass of ore solids in a vessel; (b) valve means for diverting the flowing slurry into said vessel, the vessel having sufficient capacity to contain the amount of slurry diverted over said period of time; (c) said means for measuring the flow rate and density of the flowing slurry further measures the flow rate and density of the diverted slurry; (d) means to calculate the mass of the ore solids acturally collected in said vessel; (e) means for analyzing the content of the mineral constituent content in the ore solids collected in the vessel; and (f) means to determine the constituent content as a percentage of the collected mass of ore solids; (g) means for adjusting the amount of flotation reagent added to the aqueous pulp in response to the determined percentage.
Claim 16
Dependent Claim
216 words
Apparatus for controlling the beneficiation of an ore in the froth flotation of an aqueous pulp containing the ore using a flotation reagent, by on-stream measurement of the content of a mineral constituent in a selected target mass of ore on a dry weight basis, the ore being in an aqueous slurry flowing from the froth flotation, comprising: (a) means for measuring the flow rate and density of the flowing slurry and for calculating a period of time necessary to collect a selected target mass of ore solids in a vessel; (b) valve means for diverting the flowing slurry into said vessel, the vessel having sufficient capacity to contain the amount of slurry diverted over said period of time; (c) said means for measuring the flow rate and density of the flowing slurry further measures the flow rate and density of the diverted slurry; (d) means to calculate the mass of the ore solids acturally collected in said vessel; (e) means for analyzing the content of the mineral constituent content in the ore solids collected in the vessel; and (f) means to determine the constituent content as a percentage of the collected mass of ore solids; (g) means for adjusting the amount of flotation reagent added to the aqueous pulp in response to the determined percentage.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-02-22 | 1991-08-24 | 1992-02-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-02-22 | 1995-08-24 | 1996-02-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-02-22 | 1999-08-24 | 2000-02-23 | $7700.00 | Window Closed / Lapsed |