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US5560838A Expired / Lapsed US ⏱️ 0.0 years remaining

Process and apparatus for converting spent etchants

Assignee: Training ''N'' Tech Inc
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Filing: 1994-12-05
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Granted: 1996-10-01
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Expires: 2014-12-05
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Abstract

Abstract Cupric chloride etchant waste is converted into non-hazardous material consisting of copper oxide and salt water. The cupric chloride etchant is preheated and a stream of the etchant is combined with a stream of preheated caustic solution. A neutralization reaction occurs in the mixed stream which is directed to a mixing tank. The reaction completes in the mixing tank without addition of heat, producing fine copper oxide which is filtered out from the salt water. The entire apparatus for carrying out the process can be integrated into a single portable unit.

Inventors

  • 👤 Victoria R. Allies
  • 👤 Mark F. Lloyd
  • 👤 James M. McCarron

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 14:55
CPC Classifications
C; C01; C01G; C01G3/00; C01G3/02

Claims Analysis

Total Claims: 32
Claim 1
Independent Claim 65 words
A process for conversion of etchant into non-hazardous material comprising the steps of: adjusting the temperatures of said etchant to a first temperature; adjusting the temperatures of a caustic solution to a second temperature; combining stream of said etchant at said first predetermined temperature with a stream of said caustic at said second temperature to produce a mixed stream in which a neutralization reaction occurs.
Claim 2
Dependent Claim 65 words
A process for conversion of etchant into non-hazardous material comprising the steps of: adjusting the temperatures of said etchant to a first temperature; adjusting the temperatures of a caustic solution to a second temperature; combining stream of said etchant at said first predetermined temperature with a stream of said caustic at said second temperature to produce a mixed stream in which a neutralization reaction occurs.
Claim 3
Dependent Claim 20 words
A process in accordance with claim 1 wherein: said etchant stream and said caustic stream are of substantially equal velocity.
Claim 4
Dependent Claim 24 words
A process in accordance with claim 2 wherein: said etchant stream is at a flow rate which is in proportion to said caustic stream.
Claim 5
Dependent Claim 31 words
A process in accordance with claim 1 wherein: said combining step is carried out by directing said first and said second streams each at an angle relative to said mixed stream.
Claim 6
Dependent Claim 21 words
A process in accordance with claim 4 wherein: said angle is 45° from an imaginary axis extending through said mixed stream.
Claim 7
Dependent Claim 14 words
A process in accordance with claim 1 wherein said etchant is a cupric etchant.
Claim 8
Dependent Claim 15 words
A process in accordance with claim 6 wherein said caustic is a sodium hydroxide solution.
Claim 9
Dependent Claim 20 words
A process in accordance with claim 7 wherein: said first temperature and said second temperature each is above 100° F.
Claim 10
Dependent Claim 28 words
A process in accordance with claim 8 wherein: each of said first temperature and said second temperature is selected to be equal to or greater than 120° F.
Claim 11
Dependent Claim 32 words
A process in accordance with claim 1 including the further step of: automatically adjusting the relative flow rates of said etchant and caustic streams to control the pH in said mixed stream.
Claim 12
Dependent Claim 35 words
A process in accordance with claim 10 further comprising the step of: capturing said mixed stream in a reaction tank and allowing the reaction to continue to completion without adding heat to said reaction tank.
Claim 13
Dependent Claim 98 words
A process for converting a metal-bearing acid solution to a non-hazardous material containing metal salt comprising the steps of: heating said acid solution to a first temperature; heating a concentrated base solution to a second temperature; producing a first stream of said acid solution at said first temperature; producing a second stream of said base solution at said second temperature; impinging said first and second streams into a mixed stream in which an exothermic reaction occurs; adjusting the flow of said first and second streams relative to each other to maintain a pH level in the mixed stream.
Claim 14
Dependent Claim 98 words
A process for converting a metal-bearing acid solution to a non-hazardous material containing metal salt comprising the steps of: heating said acid solution to a first temperature; heating a concentrated base solution to a second temperature; producing a first stream of said acid solution at said first temperature; producing a second stream of said base solution at said second temperature; impinging said first and second streams into a mixed stream in which an exothermic reaction occurs; adjusting the flow of said first and second streams relative to each other to maintain a pH level in the mixed stream.
Claim 15
Dependent Claim 101 words
A process for converting cupric chloride etchant into non-hazardous material comprising the steps of: adjusting the temperature of said cupric chloride etchant to a temperature; adjusting the temperature of a sodium hydroxide solution to a second temperature; combining a stream of said cupric chloride etchant at said temperature with a stream of said sodium hydroxide at said second temperature to form a combined stream; allowing a neutralization reaction to occur in the combined stream without addition of heat whereby cupric oxide and a saline solution are produced; and separating the cupric oxide from the saline solution by means of a filter.
Claim 16
Dependent Claim 101 words
A process for converting cupric chloride etchant into non-hazardous material comprising the steps of: adjusting the temperature of said cupric chloride etchant to a temperature; adjusting the temperature of a sodium hydroxide solution to a second temperature; combining a stream of said cupric chloride etchant at said temperature with a stream of said sodium hydroxide at said second temperature to form a combined stream; allowing a neutralization reaction to occur in the combined stream without addition of heat whereby cupric oxide and a saline solution are produced; and separating the cupric oxide from the saline solution by means of a filter.
Claim 17
Dependent Claim 19 words
A process in accordance with claim 13 wherein: said temperature and said second temperature are each over 100° F.
Claim 18
Dependent Claim 23 words
A process in accordance with claim 14 wherein: said temperature and said second temperature are both equal to or greater than 120° F.
Claim 19
Dependent Claim 33 words
A process in accordance with claim 13 wherein: said sodium hydroxide stream and said cupric chloride etchant stream are each directed at an angle of 45° from the axis of the mixed stream.
Claim 20
Dependent Claim 39 words
A process in accordance with claim 13 comprising the further step prior to said separating step of: receiving said combined stream in a tank and allowing said neutralization reaction to carry on to completion without the addition of heat.
Claim 21
Dependent Claim 43 words
A process in accordance with claim 13 comprising: monitoring the pH of the solution in said tank and adjusting the flow of at least one of said sodium hydroxide stream and said cupric chloride etchant stream to maintain said pH within a range.
Claim 22
Dependent Claim 11 words
Cupric oxide produced in accordance with the process of claim 13.
Claim 23
Dependent Claim 154 words
Apparatus for automatically converting cupric chloride etchant into non-hazardous material comprising: a first heater for heating said etchant to a first temperature to produce heated etchant; a second heater for heating a sodium hydroxide solution to a second temperature to produce heated caustic; a first pump for producing a first stream of heated etchant; a second pump for producing a second stream of heated caustic; a mixing "y" for combining said stream of heated etchant and said stream of heated caustic into a mixed stream, wherein a neutralization reaction is initiated; a static mixer coupled to said mixing "y" in which said neutralization reaction occurs without added heat; a mixing tank receiving the output of said static mixer; said neutralization reaction being allowed to continue to completion in said mixing tank without added heat to produce copper oxide and a saline solution; and a separator for separating said copper oxide from said saline solution.
Claim 24
Dependent Claim 154 words
Apparatus for automatically converting cupric chloride etchant into non-hazardous material comprising: a first heater for heating said etchant to a first temperature to produce heated etchant; a second heater for heating a sodium hydroxide solution to a second temperature to produce heated caustic; a first pump for producing a first stream of heated etchant; a second pump for producing a second stream of heated caustic; a mixing "y" for combining said stream of heated etchant and said stream of heated caustic into a mixed stream, wherein a neutralization reaction is initiated; a static mixer coupled to said mixing "y" in which said neutralization reaction occurs without added heat; a mixing tank receiving the output of said static mixer; said neutralization reaction being allowed to continue to completion in said mixing tank without added heat to produce copper oxide and a saline solution; and a separator for separating said copper oxide from said saline solution.
Claim 25
Dependent Claim 26 words
Apparatus in accordance with claim 20 comprising: a controller for automatically controlling the operation of said first and second heaters and said first and second pumps.
Claim 26
Dependent Claim 17 words
Apparatus in accordance with claim 21 wherein: said first and second temperatures are greater than 100° F.
Claim 27
Dependent Claim 18 words
Apparatus in accordance with claim 22 wherein: said first and second temperatures are preferably 120° F. or greater.
Claim 28
Dependent Claim 53 words
Apparatus in accordance with claim 21 comprising: a first pH sensor monitoring the pH below or downstream from said static mixer; and wherein said controller adjusts the flow of at least one of said heated etchant and said heated caustic to automatically maintain a pH level below or downstream from said static mixer.
Claim 29
Dependent Claim 48 words
Apparatus in accordance with claim 21 comprising: a second pH sensor for monitoring the pH in said mixing tank; and wherein said controller adjusts the flow of at least one of said heated etchant and said heated caustic to automatically maintain a pH level in said mixing tank.
Claim 30
Dependent Claim 15 words
Apparatus in accordance with claim 20 wherein: said apparatus is portable as an integrated unit.
Claim 31
Dependent Claim 79 words
Apparatus in accordance with claim 20 comprising: a controller; said controller controlling the operating of said first and second pumps; a first recirculation loop for recirculating said heated etchant through said first pump; a second recirculation loop for recirculating said heated caustic through said second pump; and whereby said controller causes said first pump to recirculate said heated etchant through said first recirculation loop and said second pump to recirculate heated caustic through said second recirculation loop at times.
Claim 32
Dependent Claim 48 words
Apparatus in accordance with claim 24 comprising: a second pH sensor for monitoring the pH in said mixing tank; and wherein said controller adjusts the flow of at least one of said heated caustic and said heated etchant to automatically maintain a pH level in said mixing tank.

References Cited (Backward Citations)

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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) 1999-10-01 2000-04-01 2000-10-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2003-10-01 2004-04-01 2004-10-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2007-10-01 2008-04-01 2008-10-01 $7700.00 Window Closed / Lapsed

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