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US3867285A Expired / Lapsed US ⏱️ 0.0 years remaining

Oil-water separation process

Assignee: Individual
•
Filing: 1973-10-15
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Granted: 1975-02-18
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Expires: 1993-10-15
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Abstract

Abstract A fluid system containing oil having an API Gravity value from about 11 to about 70, water and particulate solids is filtered through a finely divided oil and water insoluble filter media to retain particulate solids and oil within the filter media and pass an effluent of either clarified water or a mixture of solids-free oil and water which separates into defined layers of solids-free oil and clarified water, with the mixture being attained when the oil content of the fluid system is in excess of about 1 percent by weight. The filter media has minimum and maximum particle mesh sizes which are a function of flow rate and solids retention, a median particle mesh size, by weight, which is a function of the API Gravity of the oil in the feed fluid, and a particle size distribution pattern which uniformly and progressively increases, by weight, from the minimum particle mesh size to the median particle mesh size and from the maximum particle mesh size to the median particle mesh size. In the event that the fluid system contains acid insolubilizing, water soluble, organic material, a non-toxic acid is added to the fluid system prior to the filtration step to convert the organic material to a water insoluble, adsorbable oil. Oil-water systems which contain no significant quantity of particulate solids can be treated by the foregoing method to produce clarified water and oil. The steps of the method are the same except that no significant quantity of particulate solids is retained by the filter media and, thus, no significant quantity of particulate solids is removed from the filter media during the backwashing step.

Inventors

  • 👤 Jr Howard F Keller

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 15:53
CPC Classifications
B; B01; B01D; B01D17/00; B01D17/02; B01D17/0202; B01D17/04; B01D17/045; B01D17/047; B01D17/08

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 459 words
A METHOD FOR TREATING A FLUID SYSTEM CONTAINING OIL HAVING AN API GRAVITY VALUE FROM ABOUT 11 TO ABOUT 70, WATER AND PARTICULATE SOLIDS TO PRODUCE CLARIFIED WATER, SOLIDS-FREE OIL AN OIL-FREE SOLIDS WHICH COMPRISES: A. FILTERING SAID FLUID SYSTEM THROUGH A FINELY DIVIDED OIL AND WATER INSOLUBLE FILTER MEDIA CONTAINING FROM ABOUT 2 TO ABOUT 8 CUBIC FEET OF FILTER MATERIAL FOR EACH SQUARE FOOT OF FILTER MEDIA SURFACE AREA, AT A FLOW RATE FROM ABOUT 10 TO ABOUT 35 GALLONS PER MINUTE PER SQUARE FOOT OF FILTER MEDIA SURFACE AREA TO RETAIN PARTICULATE SOLIDS AND OIL WITHIN THE FILTER MEDIA AND PASS AN EFFLUENT SELECTED FROM THE GROUP CONSISTING OF: CLARIFIED WATER AND A MIXTURE OF SOLIDS-FREE OIL AND WATER WHICH SEPARATES INTO DEFINED LAYERS OF SOLIDS-FREE OIL AND CLARIFIED WATER, SAID MIXTURE BEING ATTAINED WHEN THE OIL CONTENT OF THE FLUID SYSTEM IS IN EXCESS OF ABOUT 1% BY WEIGHT, SAID FILTER MEDIA HAVING: I. A MININUM PARTICLE MESH SIZE WITHIN THE RANGE FROM ABOUT 3 TO ABOUT 30 AND A MAXIMUM PARTICLE MESH SIZE WITHIN THE RANGE FROM ABOUT 30 TO ABOUT 100 WITH THE RANGE BETWEEN SAID MINIMUM AND MAXIMUM PARTICLE MESH SIZES BEING AT LEAST 20 MESH, II. A MEDIAN PARTICLE MESH SIZE, BY WEIGHT, WHICH IS A FUNCTION OF THE API GRAVITY VALUE OF THE OIL, SAID MEDIAN PARTICLE MESH SIZE FALLING WITHIN THE RANGE DEFINED BY MAXIMUM AND MINIMUM LINEAR VALUE VARYING FROM DIRECTLY WITH THE LINEAR VALUE OF SAID API GRAVITY, SAID MEDIAN MESH SIZE MAXIMUM LINEAR VALUE VARYING FROM ABOUT 18 TO 62 AND SAID MEDIAN MESH SIZE MINIMUM LINERAR VALUE VARYING FROM ABOUT 10 TO 54 AS SAID API GRAVITY VALUE VARIES FROM ABOUT 11 TO 70, AND III. A PARTICLE SIZE DISTRUBUTION PATTERN EXTENDING FROM THE MINIMUM PARTICLE MESH SIZE TO THE MAXIMUM PARTICLE MESH SIZE CHARACTERIZED IN THAT THE WEIGHT OF THE FILTER MEDIA SUBSTANTIALLY UNIFORMLY AND PROGRESSIVELY INCREASES FROM: A. ABOUT 0 TO 50 PERCENT AS THE FILTER MEDIA PARTICLE MESH SIZE VARIES FROM THE MINIMUM PARTICLE MESH SIZE TO THE MEDIAN PARTICLE MESH SIZE, AND B. ABOUT 0S TO 50 WEIGHT PRECENT AS THE FILTER MEDIA PARTICLE MESH SIZE VARIES FROM THE MAXIMUM PARTICLE MESH SIZE TO THE MEDIAN PARTICLE MESH SIZE, AND B. PERIODICALLY REGENERATING THE FILTER MEDIA BY: PASSING AN OIL STRIPPING COMPOSITION THROUGH SAID FILTER MEDIA IN THE SAME DIRECTION OF FLOW AS THAT OF THE FLUID SYSTEM TOREMOVE SOLIDS-FREE OIL FROM SAID FILTER MEDIA, AND THEREAFTER BACKWASHING SAID FILTER MEDIA IN A DIRECTION COUNTERCURRENT TO THE FLOW OF SAID FLUID SYSTEM AT A RATE FROM ABOUT 10 TO ABOUT 55 GALLONS PER MINUTE PER SQUARE FOOT OF FILTER MEDIA SURFACE AREA TO REMOVE OILFREE PARTICULATE SOLIDS FROM SAID FILTER MEDIA.
Claim 2
Independent Claim 459 words
A METHOD FOR TREATING A FLUID SYSTEM CONTAINING OIL HAVING AN API GRAVITY VALUE FROM ABOUT 11 TO ABOUT 70, WATER AND PARTICULATE SOLIDS TO PRODUCE CLARIFIED WATER, SOLIDS-FREE OIL AN OIL-FREE SOLIDS WHICH COMPRISES: A. FILTERING SAID FLUID SYSTEM THROUGH A FINELY DIVIDED OIL AND WATER INSOLUBLE FILTER MEDIA CONTAINING FROM ABOUT 2 TO ABOUT 8 CUBIC FEET OF FILTER MATERIAL FOR EACH SQUARE FOOT OF FILTER MEDIA SURFACE AREA, AT A FLOW RATE FROM ABOUT 10 TO ABOUT 35 GALLONS PER MINUTE PER SQUARE FOOT OF FILTER MEDIA SURFACE AREA TO RETAIN PARTICULATE SOLIDS AND OIL WITHIN THE FILTER MEDIA AND PASS AN EFFLUENT SELECTED FROM THE GROUP CONSISTING OF: CLARIFIED WATER AND A MIXTURE OF SOLIDS-FREE OIL AND WATER WHICH SEPARATES INTO DEFINED LAYERS OF SOLIDS-FREE OIL AND CLARIFIED WATER, SAID MIXTURE BEING ATTAINED WHEN THE OIL CONTENT OF THE FLUID SYSTEM IS IN EXCESS OF ABOUT 1% BY WEIGHT, SAID FILTER MEDIA HAVING: I. A MININUM PARTICLE MESH SIZE WITHIN THE RANGE FROM ABOUT 3 TO ABOUT 30 AND A MAXIMUM PARTICLE MESH SIZE WITHIN THE RANGE FROM ABOUT 30 TO ABOUT 100 WITH THE RANGE BETWEEN SAID MINIMUM AND MAXIMUM PARTICLE MESH SIZES BEING AT LEAST 20 MESH, II. A MEDIAN PARTICLE MESH SIZE, BY WEIGHT, WHICH IS A FUNCTION OF THE API GRAVITY VALUE OF THE OIL, SAID MEDIAN PARTICLE MESH SIZE FALLING WITHIN THE RANGE DEFINED BY MAXIMUM AND MINIMUM LINEAR VALUE VARYING FROM DIRECTLY WITH THE LINEAR VALUE OF SAID API GRAVITY, SAID MEDIAN MESH SIZE MAXIMUM LINEAR VALUE VARYING FROM ABOUT 18 TO 62 AND SAID MEDIAN MESH SIZE MINIMUM LINERAR VALUE VARYING FROM ABOUT 10 TO 54 AS SAID API GRAVITY VALUE VARIES FROM ABOUT 11 TO 70, AND III. A PARTICLE SIZE DISTRUBUTION PATTERN EXTENDING FROM THE MINIMUM PARTICLE MESH SIZE TO THE MAXIMUM PARTICLE MESH SIZE CHARACTERIZED IN THAT THE WEIGHT OF THE FILTER MEDIA SUBSTANTIALLY UNIFORMLY AND PROGRESSIVELY INCREASES FROM: A. ABOUT 0 TO 50 PERCENT AS THE FILTER MEDIA PARTICLE MESH SIZE VARIES FROM THE MINIMUM PARTICLE MESH SIZE TO THE MEDIAN PARTICLE MESH SIZE, AND B. ABOUT 0S TO 50 WEIGHT PRECENT AS THE FILTER MEDIA PARTICLE MESH SIZE VARIES FROM THE MAXIMUM PARTICLE MESH SIZE TO THE MEDIAN PARTICLE MESH SIZE, AND B. PERIODICALLY REGENERATING THE FILTER MEDIA BY: PASSING AN OIL STRIPPING COMPOSITION THROUGH SAID FILTER MEDIA IN THE SAME DIRECTION OF FLOW AS THAT OF THE FLUID SYSTEM TOREMOVE SOLIDS-FREE OIL FROM SAID FILTER MEDIA, AND THEREAFTER BACKWASHING SAID FILTER MEDIA IN A DIRECTION COUNTERCURRENT TO THE FLOW OF SAID FLUID SYSTEM AT A RATE FROM ABOUT 10 TO ABOUT 55 GALLONS PER MINUTE PER SQUARE FOOT OF FILTER MEDIA SURFACE AREA TO REMOVE OILFREE PARTICULATE SOLIDS FROM SAID FILTER MEDIA.
Claim 3
Dependent Claim 27 words
A method according to claim 1 wherein the range between the minimum and maximum particle mesh sizes of the filter media is at least about 30 mesh.
Claim 4
Dependent Claim 12 words
A method according to claim 1 wherein the filter media is garnet.
Claim 5
Dependent Claim 13 words
A method according to claim 1 wherein the filter media is aluminum oxide.
Claim 6
Dependent Claim 13 words
A method according to claim 1 wherein the filter media is ground slag.
Claim 7
Dependent Claim 13 words
A method according to claim 1 wherein the filter media is volcanic tuff.
Claim 8
Dependent Claim 26 words
A method according to claim 1 wherein the oil stripping composition is initially a mixture of steam and low viscosity refined oil and thereafter steam alone.
Claim 9
Dependent Claim 53 words
A method according to claim 1 wherein the fluid system contains, additionally, acid insolubilizing, water soluble, organic material and, prior to filtration, a non-toxic acid is added to said fluid system in an amount to adjust the pH thereof below about 4.8 to convert said organic material to a water insoluble, adsorbable oil.
Claim 10
Dependent Claim 35 words
A method according to claim 1 wherein the median particle mesh size, by weight, varies linearly from about 14 to about 58 as the API Gravity value varies linearly from about 11 to about 70.
Claim 11
Dependent Claim 35 words
A method according to claim 1 wherein the flow rate of fluid system through the filter media is from about 15 to about 30 gallons per minute per square foot of filter media surface area.
Claim 12
Dependent Claim 34 words
A method according to claim 10 wherein the backwashing step is carried out at a flow rate from about 10 to about 20 gallons per minute per square foot of filter media surface area.
Claim 13
Independent Claim 431 words
A method for treating a fluid system containing oil and water to produce clarified water and oil which comprises: A. filtering said fluid system through a finely divided oil and water insoluble filter media containing from about 2 to about 8 cubic feet of filter material for each square foot of filter media surface area, at a flow rate from about 10 to about 35 gallons per minute per square foot of filter media surface area to retain oil within the filter media and pass an effluent selected from the group consisting of: clarified water and a mixture of oil and water which separates into defined layers of oil and clarified water, said mixture being attained when the oil content of the fluid system is in excess of about 1% by weight, said filter media having: i. a minimum particle mesh size within the range from about 3 to about 30 and a maximum particle mesh size within the range from about 30 to about 100 with the range between said minimum and maximum particle mesh sizes being at least about 20 mesh, ii. a median particle mesh size, by weight, which is a function of the API Gravity value of the oil, said median particle mesh size falling within the range defined by maximum and minimum linear values which vary directly with the linear value of said API Gravity, said median mesh size maximum linear value varying from about 18 to 62 and said median mesh size minimum linear value varying from about 10 to 54 as said API Gravity value varies from about 11 to 70, and iii. a particle size distribution pattern extending from the minimum particle mesh size to the maximum particle mesh size characterized in that the weight of the filter media substantially uniformly and progressively increases from: a. about 0 to 50 weight percent as the filter media particle mesh size varies from the minimum particle mesh size to the median particle mesh size, and b. about 0 to 50 weight percent as the filter media particle mesh size varies from the maximum particle mesh size to the median particle mesh size; and B. periodically regenerating the filter media by: passing an oil stripping composition through said filter media in the same direction of flow as that of the fluid system to remove oil from the filter media, and thereafter backwashing said filter media in a direction countercurrent to the flow of said fluid system at a rate from about 10 to about 35 gallons per minute per square foot of filter media surface area.
Claim 14
Independent Claim 431 words
A method for treating a fluid system containing oil and water to produce clarified water and oil which comprises: A. filtering said fluid system through a finely divided oil and water insoluble filter media containing from about 2 to about 8 cubic feet of filter material for each square foot of filter media surface area, at a flow rate from about 10 to about 35 gallons per minute per square foot of filter media surface area to retain oil within the filter media and pass an effluent selected from the group consisting of: clarified water and a mixture of oil and water which separates into defined layers of oil and clarified water, said mixture being attained when the oil content of the fluid system is in excess of about 1% by weight, said filter media having: i. a minimum particle mesh size within the range from about 3 to about 30 and a maximum particle mesh size within the range from about 30 to about 100 with the range between said minimum and maximum particle mesh sizes being at least about 20 mesh, ii. a median particle mesh size, by weight, which is a function of the API Gravity value of the oil, said median particle mesh size falling within the range defined by maximum and minimum linear values which vary directly with the linear value of said API Gravity, said median mesh size maximum linear value varying from about 18 to 62 and said median mesh size minimum linear value varying from about 10 to 54 as said API Gravity value varies from about 11 to 70, and iii. a particle size distribution pattern extending from the minimum particle mesh size to the maximum particle mesh size characterized in that the weight of the filter media substantially uniformly and progressively increases from: a. about 0 to 50 weight percent as the filter media particle mesh size varies from the minimum particle mesh size to the median particle mesh size, and b. about 0 to 50 weight percent as the filter media particle mesh size varies from the maximum particle mesh size to the median particle mesh size; and B. periodically regenerating the filter media by: passing an oil stripping composition through said filter media in the same direction of flow as that of the fluid system to remove oil from the filter media, and thereafter backwashing said filter media in a direction countercurrent to the flow of said fluid system at a rate from about 10 to about 35 gallons per minute per square foot of filter media surface area.

References Cited (Backward Citations)

US3574329A Cited
US3718457A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-02-17 1978-08-19 1979-02-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-02-17 1982-08-19 1983-02-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-02-17 1986-08-19 1987-02-18 $7700.00 Window Closed / Lapsed

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