In situ remediation of underground organic pollution

• US 5,954,452 A
• Filed: 07/11/1997
• Issued: 09/21/1999
• Est. Priority Date: 07/11/1997
• Status: Expired due to Fees

• Current Assignee: GA Technologies Incorporated
• Original Assignee: GA Technologies Incorporated
• Inventors: Goldstein, Michel
• Primary Examiner(s): SUCHFIELD, GEORGE A
• Application Number:
  US08/893,748
• Time in Patent Office: 802 Days
• Field of Search: 166/52, 166/53, 166/64, 166/66, 166/250.1, 166/303, 210/170, 210/747, 210/759, 210/761, 405/128, 405/131
• US Class Current: 405/128.55
• CPC Class Codes: B01F 25/31243 Eductor or eductor-type venturi, i.e. the main flow being injected through the venturi with high speed in the form of a jet
• CPC Class Codes: B09C 1/08 chemically
• CPC Class Codes: B09C 2101/00 In situ
• CPC Class Codes: E21B 36/00 Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones

Abstract

Heated hydrogen peroxide reagent under pressure is supplied to a well for underground remediation of pollution; the reaction with the pollutant is exothermic so that the high temperature of the reagent when injected is maintained as the reagent spreads. The remediation reaction is monitored by sensors, to regulate the supply of reagent and to shut off the supply automatically when the pollutant has been reduced to an acceptable level.

Claims

1. Apparatus for in situ remediation of underground organic pollution, including an injection well extending to a subterranean injection site, means for supplying a reagent of hydrogen peroxide in water to the top of the well at a pressure substantially above ambient, for in situ reaction with organic pollutant, said reagent-supplying means including means for heating the reagent to a temperature substantially above ambient.

2. Apparatus as in claim 1, wherein said reagent-supplying means comprises a boiler and means for supplying fluid to said boiler, said means for supplying fluid including means providing a supply of aqueous hydrogen peroxide solution and a supply of water, the boiler, when in operation, providing said reagent at a temperature substantially above ambient and at a pressure substantially above ambient.

3. Apparatus as in claim 1, wherein said reagent-supplying means includes a boiler for supplying steam at a pressure substantially above ambient and means for providing an aqueous solution of hydrogen peroxide, and a device for combining said steam and said aqueous solution to yield a flow of a two-phase fluid, said device having means for accelerating the flow of said two-phase fluid at least to its supersonic velocity and having means for developing a shock front in the flow of the two-phase fluid so as to result in pressure of the fluid downstream of the shock front greatly exceeding the ambient pressure.

4. Apparatus as in claim 1, further including means for monitoring the conditions of the in situ reaction, and means responsive to the monitoring means for regulating the reagent supplied to the well.

5. Apparatus as in claim 1, including means for sensing the effects of chemical reaction of the reagent with pollutant in situ, means for detecting an increase in reaction effects followed by a decrease in the reaction effects, means for detecting a low level of reaction effects at which the remediation may be considered complete, and means responsive to both said detecting means for shutting off further operation of said remediation apparatus.

6. A method of in situ remediation of underground organic pollution, including the step of heating a reagent of hydrogen peroxide in water to a temperature substantially above ambient, and supplying a flow of the heated reagent under pressure substantially above ambient to a well having a subterranean injection site for injection of the reagent into the subsoil and reaction with organic pollutant in situ.

7. A method as in claim 6, wherein the step of heating said reagent comprises converting the reagent to steam at a temperature substantially above ambient and at a pressure substantially above ambient.

8. A method as in claim 6, including the step of combining an aqueous solution of hydrogen peroxide with steam to provide a combined flow of said solution and steam and accelerating said combined flow at least to its supersonic velocity, including the further step of causing the accelerated flow to develop a shock front wherein the pressure of the fluid downstream of the shock front greatly exceeds the ambient pressure, said downstream flow being supplied to the well.

9. A method as in claim 6, including the further step of sensing the conditions of the in situ reaction, and regulating the supply of hydrogen peroxide to the well in dependence on the sensed conditions.

10. A method as in claim 6, including the further step of detecting increasing intensity of the chemical reaction to a peak and subsequent decline from the peak, and detecting attainment of a low level of reaction representing completion of the remediation, and discontinuing the remediation treatment after detection of said increase and decline of the reaction intensity upon subsequent detection of the reaction attaining said low level.

11. A method of remediating soil containing organic pollutant, including the steps of injecting said remediation fluid into a subterranean treatment site, monitoring the chemical reaction between the injected fluid and the pollutant, and controlling the injection of the remediation fluid in dependence on the result of the monitoring step, and said remediation fluid is steam and aqueous hydrogen peroxide combined, and said monitoring step is performed by regulating the concentration of the hydrogen peroxide in said remediation fluid.

12. A method as in claim 11, wherein said monitoring step includes storing a value that represents an effect of the chemical reaction when the pollution has been reduced to a low level considered acceptable and making comparisons of the values of that effect of ongoing chemical reactions with said stored value, and wherein said control of the injection of remediation fluid is performed by terminating the injection of such fluid.