Methods for the formation and operation of an in situ process reactor

• US 5,348,422 A
• Filed: 02/25/1993
• Issued: 09/20/1994
• Est. Priority Date: 02/25/1993
• Status: Expired due to Fees

• Current Assignee: Terranalysis Corporation
• Original Assignee: Terranalysis Corporation
• Inventors: Manchak, Peter J., Manchak, Michael E., Manchak, Frank E. III
• Primary Examiner(s): Taylor, Dennis L.
• Application Number:
  US08/022,189
• Time in Patent Office: 572 Days
• Field of Search: 405/128, 405/129, 405/131, 405/38, 405/303, 405/267, 37/142.5, 37/464, 37/359, 37/189, 210/751, 210/747, 210/739
• US Class Current: 405/128.35
• CPC Class Codes: B09C 1/00 Reclamation of contaminated soil
• CPC Class Codes: B09C 1/02 Extraction using liquids, e.g. washing, leaching , flotation
• CPC Class Codes: B09C 1/062 by using electrode or resistance heating elements
• CPC Class Codes: B09C 1/08 chemically
• CPC Class Codes: B09C 1/10 microbiologically, biologically or by using enzymes
• CPC Class Codes: B09C 2101/00 In situ
• CPC Class Codes: E02F 7/06 Delivery chutes or screening plants or mixing plants mounted on dredgers or excavators for back-filling E02F5/226 takes precedence; separating equipment in general B03; delivery chutes in general B65G

Abstract

A hazardous waste site remediation process for decontamination of petrochemical and other toxic waste containing sites comprises in situ conversion of the site to a self contained process reactor which is then selectively operated by feeding a variety of treatment reagents thereto through a network of feed conduits and removing contaminants through removal conduits which collectively bring the contaminated materials to a collection area in the reactor where they can then be further treated or removed. A mobile trenching machine converts the site to a reactor by simultaneously placing contaminant impermeable walls while processing excavated materials such as by adding reactor reagents thereto and then immediately returning the processed materials to the location from which they were excavated in the site. Hydrocarbons or other useful by-products such as precious metals may be recovered from the soil.

Claims

1. A process for the conversion of a hazardous waste disposal site to an in situ process reactor and operating same to remediate the site comprising the steps of:

a) establishing an essentially impervious contaminant containment wall around the site;

b) placing a liner forming material inside of said wall on the bottom of said site to form an essentially impervious bottom contaminant containment liner in said site which extends to said containment wall while simultaneously excavating and processing contaminated soil excavated from said site at a location above the surface of said site and returning the processed soil into said site above said bottom liner;

c) placing a network of perforated feed conduits and a network of perforated contaminant removal conduits in said reactor, said contaminant removal conduits leading to a contaminant removal location in said reactor;

d) forming an essentially impervious contaminant containment barrier on top of said site whereby said wall, bottom liner and top barrier completely enclose the contaminated soil in said site thereby converting said site to a self contained reactor;

e) operating said reactor to volatilize volatile contaminants therein;

f) moving a fluid stream containing volatiolized contaminants to said collection location in said reactor; and

g) removing said fluid stream of volatized contaminants from said collection location.

2. The process of claim 1, wherein said contaminant containment wall is formed by simultaneously excavating soil from a trench and processing said soil by mixing cementitious wall forming material thereto above said site and returning the mixed soil and liner forming material to said trench.

3. The process of claim 1, wherein said top barrier is formed by simultaneously excavating soil from a trench, mixing hardenable barrier forming material to excavated soil above said site and returning the mixed soil and barrier forming material to form said barrier on top of said trench.

4. The process of claim 1, wherein said above site processing of excavated soil comprises adding treatment reagents thereto.

5. The process of claim 1, wherein said above site processing of excavated soil comprises separation of rocks above a predetermined size therefrom.

6. The process of claim 1, wherein said above site processing of excavated soil comprises adjusting the permeability thereof.

7. The process of claim 1, wherein said network of perforated feed conduits is placed in said site while processing said excavated soil and including the step of operating said reactor by feeding contaminant treatment reagents into said reactor through said conduits.

8. The process of claim 1, further comprising the steps of placing a network of heating means in said reactor and operating said reactor by heating said heating means.

9. The process of claim 8, wherein said heating is electrical resistance heating.

10. The process of claim 1, wherein said network of perforated contaminant removal conduits is placed in said reactor during processing of said excavated soil.

11. The process of claim 1, further comprising the steps of scrubbing said fluid stream to remove contaminants therefrom.

12. The process of claim 1, comprising the steps of operating said reactor by adding surfactant thereto via said feed conduits, removing contaminant laden surfactant from said reactor, separating said contaminants from said surfactant and recycling said surfactant for further use in the process.

13. The process of claim 1, comprising the steps of operating said reactor by adding biological treatment agents thereto via said feed conduits.

14. The process of claim 13, further comprising the step of operating said reactor by maintaining a substantially constant moisture content and temperature in said reactor to enhance biological activity therein.

15. The process of claim 1, further comprising the steps of placing a series of electrodes in said site and operating said reactor by supplying electrokinetic contaminant flushing fluid into said reactor via said feed conduits and establishing a voltage gradient between said electrodes to assist flushing of contaminants from said reactor through said contaminant removal conduits.

16. The process of claim 1, further comprising the step of applying a negative pressure at said removal location to cause said fluid stream to flow thereto.