Patent US5403490A successfully refreshed from Google Patents.
← Back to Patent Explorer
US5403490A Expired / Lapsed US ⏱️ 0.0 years remaining

Process and apparatus for removing solutes from solutions

Assignee: Individual
•
Filing: 1992-11-23
•
Granted: 1995-04-04
•
Expires: 2012-11-23
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract An improved process and system for treating a solution of a solute which can be concentrated by forcing a portion of the solvent through a semi-permeable membrane and converted to the solid phase by increasing the concentration of the solute in the solution. A phase conversion device receives the solution and converts a portion of the solute to the solid phase. The resulting mixture is passed through a separation device such as a filter to remove the solids from the remaining solution. A concentration device such as a reverse osmosis, electrodialysis or ultrafiltration device treats the resultant solution discharging a permeate of solvent essentially free of solute and a concentrate enriched in solute. A recycle line recycles the concentrate to the phase conversion device to advance precipitation of the solute by driving the solubility equilibrium toward precipitation.

Inventors

  • 👤 Satish DeSai

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 20:47
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/44; B; B01; B01D; B01D61/00; B01D61/02; B01D61/025; B01D61/04; B01D61/14; B01D61/145; B01D61/16; B01D61/42; B01D61/44; B01D2311/00; B01D2311/04; C02F1/441; C02F1/444

Claims Analysis

Total Claims: 29
Claim 1
Independent Claim 199 words
A process for treating a substantially continuous stream of a solution of solute and solvent which can be concentrated by passing a portion of the solvent through a semi-impermeable membrane and in which the solute can be converted to a solidified form by increasing the concentration of the solute in the solution, said process comprising the steps of providing a source of starting solution; treating a portion of said solution to convert a portion of the solute in said solution to the solid phase to produce a mixture of the solution and the solidified solute; removing the solidified solute from said mixture; subjecting the remaining solution to a semi-impermeable membrane to produce a first liquid stream comprising solvent essentially free from solute and a second liquid stream comprising a concentrated solution of solute; recycling substantially all of said first liquid stream to the source of the starting solution; converting at least a portion of the solute in substantially all of said second liquid stream to the solid phase to produce a mixture of the solution and the solidified solute; removing the solidified solute from the mixture produced from said concentrate; and returning the remaining solution to said semi-impermeable membrane.
Claim 2
Dependent Claim 199 words
A process for treating a substantially continuous stream of a solution of solute and solvent which can be concentrated by passing a portion of the solvent through a semi-impermeable membrane and in which the solute can be converted to a solidified form by increasing the concentration of the solute in the solution, said process comprising the steps of providing a source of starting solution; treating a portion of said solution to convert a portion of the solute in said solution to the solid phase to produce a mixture of the solution and the solidified solute; removing the solidified solute from said mixture; subjecting the remaining solution to a semi-impermeable membrane to produce a first liquid stream comprising solvent essentially free from solute and a second liquid stream comprising a concentrated solution of solute; recycling substantially all of said first liquid stream to the source of the starting solution; converting at least a portion of the solute in substantially all of said second liquid stream to the solid phase to produce a mixture of the solution and the solidified solute; removing the solidified solute from the mixture produced from said concentrate; and returning the remaining solution to said semi-impermeable membrane.
Claim 3
Dependent Claim 42 words
The process of claim 1 wherein said second liquid stream is recycled and mixed with the starting solution so that a portion of the solute in both said second liquid steam and the starting solution is concurrently converted to the solid phase.
Claim 4
Dependent Claim 19 words
The process of claim 1 wherein said semi-impermeable membrane is contained in a reverse osmosis, electrodialysis, or ultrafiltration unit.
Claim 5
Dependent Claim 33 words
The process of claim 1 wherein said semi-permeable membrane is contained in a reverse osmosis or ultrafiltration unit, said first liquid stream is a permeate, and said second liquid stream is a concentrate.
Claim 6
Dependent Claim 31 words
The process of claim 1 wherein said semi-permeable membrane is contained in an electrodialysis unit, said first liquid stream is a demineralized stream, and said second liquid stream is a concentrate.
Claim 7
Dependent Claim 21 words
The process of claim 1 wherein the converting of solute to the solid phase is effected by precipitation, coagulation or crystallization.
Claim 8
Dependent Claim 17 words
The process of claim 6 wherein said precipitation or crystallization is promoted by cooling, heating or agitation.
Claim 9
Dependent Claim 15 words
The process of claim 1 wherein the removing of solidified solute is effected by filtration.
Claim 10
Dependent Claim 27 words
The process of claim 1 wherein said solution is an aqueous solution of metal ions and said solid phase comprises solid metal oxides and solid metal hydroxides.
Claim 11
Dependent Claim 69 words
The process of claim 9 wherein said metal ions include at least one of Al 3+ , AlO 2 - , Cr 6+ , Cr 3+ , Cu + , Zn 2+ , Cu 2+ , Ni 2+ , Cd 2+ , Fe 3+ , Fe 2+ , Hg 2+ , Hg + , Ag + , Sn 2+ , Sn 4+ , Au + and Au 3+ .
Claim 12
Dependent Claim 28 words
The process of claim 10 wherein said metal ions include Cr 6+ ions, and which includes the step of reducing said Cr 6+ ions to Cr 3+ ions.
Claim 13
Dependent Claim 25 words
The process of claim 10 wherein said metal ions further include CN - ions, and which includes the step of oxidizing said CN - ions.
Claim 14
Dependent Claim 36 words
The process of claim 1 wherein said solute includes ions in a complex form, and which includes the step of converting said ions by oxidation, fermentation, reduction, neutralization or substitution to a form which promotes precipitation.
Claim 15
Dependent Claim 37 words
The process of claim 1 which includes the step of adding an acid or alkali solution to said solution and said concentrate in said converting step to promote the conversion of said solute to the solid phase.
Claim 16
Dependent Claim 22 words
The process of claim 1 which includes the step of passing said mixture of solution and solidified solute through a carbon filter.
Claim 17
Dependent Claim 140 words
A process for treating an aqueous solution of metal ions which can be concentrate by reverse osmosis and in which the metal ions can be precipitated by increasing the concentration of the metal ions in the solution, said process comprising the steps of providing a source of starting aqueous solution; precipitating a portion of the metal ions from the solution to form a mixture of solution and precipitate, filtering said mixture to remove the precipitate from the solution, subjecting the remaining solution to reverse osmosis to produce a permeate comprising water essentially free of metal ions and a concentrate comprising a concentrate aqueous solution of metal ions, recycling substantially all of said permeate to the source of the starting aqueous solution, and recycling substantially all of said concentrate to said precipitating step to promote the precipitation of said metal ions.
Claim 18
Dependent Claim 140 words
A process for treating an aqueous solution of metal ions which can be concentrate by reverse osmosis and in which the metal ions can be precipitated by increasing the concentration of the metal ions in the solution, said process comprising the steps of providing a source of starting aqueous solution; precipitating a portion of the metal ions from the solution to form a mixture of solution and precipitate, filtering said mixture to remove the precipitate from the solution, subjecting the remaining solution to reverse osmosis to produce a permeate comprising water essentially free of metal ions and a concentrate comprising a concentrate aqueous solution of metal ions, recycling substantially all of said permeate to the source of the starting aqueous solution, and recycling substantially all of said concentrate to said precipitating step to promote the precipitation of said metal ions.
Claim 19
Independent Claim 176 words
A system for treating a solution of solute which can be concentrated by passing a portion of the solution through an semi-impermeable membrane and in which the solute can be converted to a solidified form by increasing the concentration of the solute in the solution, said system comprising a container housing the solution, a phase conversion device for receiving said solution and converting a portion of the solute to the solid phase to produce a mixture of the solution and the solidified solute; a physical separation device for removing the solidified solute from said mixture; a concentration device for subjecting the remaining solution to semi-impermeable membrane to produce a first liquid stream comprising solvent essentially free of solute and a second liquid stream comprising a concentrated solution of solute; a recycle line for recycling substantially all of said first liquid stream to the container having the starting solution of solute; and a recycle line for recycling substantially all of said second liquid stream to said phase conversion device to increase the concentration of the solution therein.
Claim 20
Independent Claim 176 words
A system for treating a solution of solute which can be concentrated by passing a portion of the solution through an semi-impermeable membrane and in which the solute can be converted to a solidified form by increasing the concentration of the solute in the solution, said system comprising a container housing the solution, a phase conversion device for receiving said solution and converting a portion of the solute to the solid phase to produce a mixture of the solution and the solidified solute; a physical separation device for removing the solidified solute from said mixture; a concentration device for subjecting the remaining solution to semi-impermeable membrane to produce a first liquid stream comprising solvent essentially free of solute and a second liquid stream comprising a concentrated solution of solute; a recycle line for recycling substantially all of said first liquid stream to the container having the starting solution of solute; and a recycle line for recycling substantially all of said second liquid stream to said phase conversion device to increase the concentration of the solution therein.
Claim 21
Dependent Claim 26 words
The system of claim 17 which includes means for controlling the pH of the aqueous solution from which said solute is converted to the solid phase.
Claim 22
Dependent Claim 17 words
The system of claim 17 wherein said concentration device is a reverse osmosis, electrodialysis, or ultrafiltration device.
Claim 23
Dependent Claim 17 words
The system of claim 17 wherein said phase conversion device is a precipitation, crystallization or coagulation tank.
Claim 24
Dependent Claim 34 words
The system of claim 17 which includes means for supplying an agent for oxidizing, fermenting, reducing, neutralizing or substituting ions in said solution to a form which promotes precipitation in said phase conversion device.
Claim 25
Dependent Claim 14 words
The system of claim 17 wherein said physical separation device includes a carbon filter.
Claim 26
Independent Claim 162 words
A system for treating a substantially continuous stream of aqueous solution of metal ions which can be concentrated by reverse osmosis and in which the metal ions can be precipitated by increasing the concentration of the metal ions in the solution, said process comprising a container having the solution, a precipitation tank for receiving said aqueous solution and precipitating a portion of the metal ions from the solution to form a mixture of solution and precipitate, a filter for receiving said mixture and removing the precipitate from the solution, a reverse osmosis unit for receiving the filtered aqueous solution and producing a permeate comprising water essentially free of metal ions and a concentrate comprising a concentrated aqueous solution of metal ions, a recycle line for recycling substantially all of said permeate to the container having the starting aqueous solution, and a recycle line for recycling substantially all of said concentrate to said precipitation tank to promote the precipitation of said metal ions.
Claim 27
Independent Claim 162 words
A system for treating a substantially continuous stream of aqueous solution of metal ions which can be concentrated by reverse osmosis and in which the metal ions can be precipitated by increasing the concentration of the metal ions in the solution, said process comprising a container having the solution, a precipitation tank for receiving said aqueous solution and precipitating a portion of the metal ions from the solution to form a mixture of solution and precipitate, a filter for receiving said mixture and removing the precipitate from the solution, a reverse osmosis unit for receiving the filtered aqueous solution and producing a permeate comprising water essentially free of metal ions and a concentrate comprising a concentrated aqueous solution of metal ions, a recycle line for recycling substantially all of said permeate to the container having the starting aqueous solution, and a recycle line for recycling substantially all of said concentrate to said precipitation tank to promote the precipitation of said metal ions.
Claim 28
Dependent Claim 142 words
A process for treating a substantially continuous stream of water from a rinse tank in an electroplating facility in which the rinse tank water is an aqueous solution of metal ions, said process comprising the steps of delivering the rinse tank water to a precipitation tank and allowing a portion of the metal ions to precipitate from the solution as metal oxides and metal hydroxides, removing a portion of the aqueous solution and precipitate from the precipitation tank, and separating the precipitate from the aqueous solution by filtering, delivering the filtrate to a reverse osmosis unit to product a concentrate and a permeate, the permeate being essentially free of metal ions and the concentrate containing an increased concentration of metal ions, returning substantially all of the permeate to the rinse tank, and returning substantially all of the concentrate to the precipitation tank.
Claim 29
Dependent Claim 142 words
A process for treating a substantially continuous stream of water from a rinse tank in an electroplating facility in which the rinse tank water is an aqueous solution of metal ions, said process comprising the steps of delivering the rinse tank water to a precipitation tank and allowing a portion of the metal ions to precipitate from the solution as metal oxides and metal hydroxides, removing a portion of the aqueous solution and precipitate from the precipitation tank, and separating the precipitate from the aqueous solution by filtering, delivering the filtrate to a reverse osmosis unit to product a concentrate and a permeate, the permeate being essentially free of metal ions and the concentrate containing an increased concentration of metal ions, returning substantially all of the permeate to the rinse tank, and returning substantially all of the concentrate to the precipitation tank.

References Cited (Backward Citations)

US4244505A Cited
US4775480A Cited
US4758320A Cited
US4652352A Cited
US4680126A Cited
US4880511A Cited
US4885095A Cited
DE4031979A1 Cited
US5200082A Cited
US5192418A Cited
US5204001A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1998-04-03 1998-10-03 1999-04-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2002-04-03 2002-10-03 2003-04-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2006-04-03 2006-10-03 2007-04-04 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag