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US4521313A Expired / Lapsed US ⏱️ 0.0 years remaining

Fluid purification system

Assignee: Donaldson Co Inc
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Filing: 1984-04-25
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Granted: 1985-06-04
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Expires: 2004-04-25
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Abstract

Abstract The present invention is a process for purifying a fluid, particularly an industrial coolant fluid, contained within a contaminated mixture which includes mechanically emulsified as well as free or floating oil and various solid matter including metal fines. The process includes several steps for separating and recovering the coolant fluid from the mixture generally by fluid displacement and centrifugal separation. Recovered coolant fluid is regenerated with freshly made coolant fluid and any stored, recovered coolant fluid not immediately reused is recycled through a portion of the system to prevent any degradation of the stored fluid.

Inventors

  • 👤 Girma Wolde-Michael

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 00:12
CPC Classifications
B; B01; B01D; B01D17/00; B01D17/12; B01D17/02; B01D17/0208; B01D17/0214; B01D17/0217

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 335 words
A process for separating apart from each other a heavier fluid, a lighter fluid, and particulate matter contained in a contaminated mixture, said process comprising the steps of: (a) partially purifying the contaminated mixture by separating relatively heavy particulate matter from the mixture through gravitational settling in a first container and idling the process a pre-determined length of time allowing separable lighter fluid to separate from the mixture and form a layer at the surface of the mixture in the first container; (b) transferring from a second container, a volume of substantially uncontaminated heavier fluid into the first container in a manner leaving the layer of separated lighter fluid at the mixture surface undisturbed and in sufficient quantity to raise the fluid surface in the first container to a preselected level; (c) after the pre-selected level is reached, skimming the mixture surface by overflowing a portion of the mixture within the first container into a third container; (d) concentrating the skimmed fluid in the third container; (e) subsequent to step (c), transferring a portion of the partially purified contaminated mixture in the first container to a centrifuge; (f) separating in a single pass through the centrifuge the lighter fluid, the heavier fluid and the suspended particulate matter apart from each other within the centrifuge; (g) transferring from the centrifuge the lighter liquid to the third container, and the heavier fluid to the second container; (h) replenishing the heavier fluid contained in the second container by introducing fresh heavier fluid into the second container in sufficient amounts to achieve a pre-selected level of fluid within the second container; (i) after step (h), skimming the surface of the replenished heavier fluid in the second container by overflowing a portion of the fluid into the first container; and (j) after a pre-determined interval of time has elapsed following step (i), refreshing the fluid within the second container by circulating fluid from the first container through the centrifuge, and transferring recovered fluid from the centrifuge to the second container.
Claim 2
Dependent Claim 335 words
A process for separating apart from each other a heavier fluid, a lighter fluid, and particulate matter contained in a contaminated mixture, said process comprising the steps of: (a) partially purifying the contaminated mixture by separating relatively heavy particulate matter from the mixture through gravitational settling in a first container and idling the process a pre-determined length of time allowing separable lighter fluid to separate from the mixture and form a layer at the surface of the mixture in the first container; (b) transferring from a second container, a volume of substantially uncontaminated heavier fluid into the first container in a manner leaving the layer of separated lighter fluid at the mixture surface undisturbed and in sufficient quantity to raise the fluid surface in the first container to a preselected level; (c) after the pre-selected level is reached, skimming the mixture surface by overflowing a portion of the mixture within the first container into a third container; (d) concentrating the skimmed fluid in the third container; (e) subsequent to step (c), transferring a portion of the partially purified contaminated mixture in the first container to a centrifuge; (f) separating in a single pass through the centrifuge the lighter fluid, the heavier fluid and the suspended particulate matter apart from each other within the centrifuge; (g) transferring from the centrifuge the lighter liquid to the third container, and the heavier fluid to the second container; (h) replenishing the heavier fluid contained in the second container by introducing fresh heavier fluid into the second container in sufficient amounts to achieve a pre-selected level of fluid within the second container; (i) after step (h), skimming the surface of the replenished heavier fluid in the second container by overflowing a portion of the fluid into the first container; and (j) after a pre-determined interval of time has elapsed following step (i), refreshing the fluid within the second container by circulating fluid from the first container through the centrifuge, and transferring recovered fluid from the centrifuge to the second container.
Claim 3
Dependent Claim 352 words
A process for recovering an industrial coolant fluid from a contaminated mixture containing solid matter and a separable waste oil, the process including the steps of: (a) first, separating by gravitational forces within a first container a portion of the solid matter from the contaminated mixture and removing the separated solid matter to a remote location then idling the process a pre-determined length of time allowing separable waste oil to separate from the mixture and form a layer at the surface of the mixture; (b) transferring from a second container containing previously recovered coolant fluid, a sufficient volume of the recovered coolant fluid to raise the level of fluid in the first container to a pre-selected level and in a manner leaving the layer of separated waste-oil undisturbed at the mixture surface; (c) skimming surface-carried waste oil from the first container by overflowing the oil into an oil concentrating container; (d) after skimming the oil, transferring the contaminated mixture from the first container to a centrifuge; (e) separating in a single pass through the centrifuge, the coolant fluid, waste oil and suspended solid matter apart from each other and transferring the coolant fluid to the second container and the waste oil to the oil concentrating container, and returning the solid matter to the first container; (f) adding a sufficient volume of pre-mixed fresh coolant fluid to the recovered fluid in the second container to regenerate the fluid and replenish the fluid in the second container to a pre-selected level; (g) skimming the surface of the fluid within the second container by overflowing and transferring the skimmed fluid into the first container; (h) after a pre-determined interval of time has elapsed following step (g), transferring fluid in the first container through the centrifuge and then into the second container in a manner aerating the fluid therein, thereby refreshing the recovered fluid contained in the second container; and (i) transferring any resulting overflow volume of recovered fluid from a bottom portion of the second container to the first container and scavenging the bottom of the second container during the transfer of the overflow volume.
Claim 4
Dependent Claim 352 words
A process for recovering an industrial coolant fluid from a contaminated mixture containing solid matter and a separable waste oil, the process including the steps of: (a) first, separating by gravitational forces within a first container a portion of the solid matter from the contaminated mixture and removing the separated solid matter to a remote location then idling the process a pre-determined length of time allowing separable waste oil to separate from the mixture and form a layer at the surface of the mixture; (b) transferring from a second container containing previously recovered coolant fluid, a sufficient volume of the recovered coolant fluid to raise the level of fluid in the first container to a pre-selected level and in a manner leaving the layer of separated waste-oil undisturbed at the mixture surface; (c) skimming surface-carried waste oil from the first container by overflowing the oil into an oil concentrating container; (d) after skimming the oil, transferring the contaminated mixture from the first container to a centrifuge; (e) separating in a single pass through the centrifuge, the coolant fluid, waste oil and suspended solid matter apart from each other and transferring the coolant fluid to the second container and the waste oil to the oil concentrating container, and returning the solid matter to the first container; (f) adding a sufficient volume of pre-mixed fresh coolant fluid to the recovered fluid in the second container to regenerate the fluid and replenish the fluid in the second container to a pre-selected level; (g) skimming the surface of the fluid within the second container by overflowing and transferring the skimmed fluid into the first container; (h) after a pre-determined interval of time has elapsed following step (g), transferring fluid in the first container through the centrifuge and then into the second container in a manner aerating the fluid therein, thereby refreshing the recovered fluid contained in the second container; and (i) transferring any resulting overflow volume of recovered fluid from a bottom portion of the second container to the first container and scavenging the bottom of the second container during the transfer of the overflow volume.
Claim 5
Dependent Claim 40 words
The process of claim 1 or 2 wherein the initial step of transferring a volume of recovered fluid into the volume of contaminated mixture includes the step of quietening the flow of the fluid as it enters the contaminated mixture.

References Cited (Backward Citations)

US3540588A Cited
US3456798A Cited
US3679051A Cited
US3596769A Cited
US3925204A Cited
US3897335A Cited
US4366069A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-06-03 1988-12-03 1989-06-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-06-03 1992-12-03 1993-06-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-06-03 1996-12-03 1997-06-04 $7700.00 Window Closed / Lapsed

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