WO2008009137A1 - Processes for deactivating microorganisms in solid materials - Google Patents

Processes for deactivating microorganisms in solid materials Download PDF

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Publication number
WO2008009137A1
WO2008009137A1 PCT/CA2007/001302 CA2007001302W WO2008009137A1 WO 2008009137 A1 WO2008009137 A1 WO 2008009137A1 CA 2007001302 W CA2007001302 W CA 2007001302W WO 2008009137 A1 WO2008009137 A1 WO 2008009137A1
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WO
WIPO (PCT)
Prior art keywords
solid material
reduce
content
permits
microorganisms comprise
Prior art date
Application number
PCT/CA2007/001302
Other languages
French (fr)
Inventor
Abderrahmane Dermoune
Soraya Mahiout
Roger Paradis
Original Assignee
Les Technologies Elcotech Inc.
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Publication date
Application filed by Les Technologies Elcotech Inc. filed Critical Les Technologies Elcotech Inc.
Publication of WO2008009137A1 publication Critical patent/WO2008009137A1/en
Priority to US12/356,762 priority Critical patent/US20100086437A1/en

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Classifications

    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/03—Electric current
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
    • C02F11/131—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating using electromagnetic or ultrasonic waves
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/32—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
    • F26B3/34—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B7/00—Drying solid materials or objects by processes using a combination of processes not covered by a single one of groups F26B3/00 and F26B5/00
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/46—Apparatus for electrochemical processes
    • C02F2201/461—Electrolysis apparatus
    • C02F2201/46105—Details relating to the electrolytic devices
    • C02F2201/4612—Controlling or monitoring
    • C02F2201/4615—Time
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
    • F26B2200/18—Sludges, e.g. sewage, waste, industrial processes, cooling towers

Definitions

  • the present invention relates to improvements in the field of solid materials decontamination treatment.
  • the invention relates to processes for microorganisms deactivation and/or destruction in solid materials.
  • Such processes can be useful for treating various types of solid materials, such as sludges. They also permit deactivation and/or destruction of various types of pathogenic microorganisms.
  • the management and reclamation of municipal sludge generated by wastewater treatment require a beforehand dewatering and pathogens reduction.
  • the principal microorganisms representative and indicators of treatment efficiency for pathogens reduction are: fecal coliforms or Salmonella sp., enteric viruses and viable helminth ova (US EPA, 2003. Control of Pathogens and Vector Attraction in Sewage Sludge. Environmental Regulations and technology. United States Environmental Protection Agency. EPA/625/R-92/013. Revised July 2003). All those microorganisms are likely to be present at various degrees in municipal sludge.
  • the aim of class A processes is to reduce pathogen densities below the following detection limits: less than 3 most probable number (MPN) per 4 grams of total solid (dry weight basis) for Salmonella sp.; less than 1 plaque-forming unit (PFU) per 4 grams of total solids (dry weight basis) for enteric viruses and less than 1 viable helminth ova per 4 grams of total solid (dry weight basis).
  • MPN most probable number
  • PFU plaque-forming unit
  • the aim is to reduce them to less than 1000 most probable number (MPN) per 1 gram of total solid (dry weight basis).
  • Coliphages are viruses that infect bacteria. Thanks to their characteristics, coliphages are considered by researchers as indicators of fecal pollution and are proposed as a model to follow the fate of enteric viruses in various hydrous environment and wastewater treatment plant.
  • a process for at least partially deactivating microorganisms in a solid material comprises submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm 2 with respect to the surface of electrodes used for generating the current.
  • the process represents an economic and simple manner to decontaminate or to permit hygienization of solid materials.
  • the process can permit to deactivate and/or destroy a plurality of microorganisms such as fecal coliforms, Salmonella spp., enteric viruses, viable helminth ova, enterococus, aerobic and facultative anaerobic heterotrophic bacteria, total coliforms, Escherichia coli, Clostridium perfringens, somatic coliphages and F-specific coliphages.
  • the efficiency of the process is quite impressive since it can permit to considerably decrease the amount of microorganisms present in the solid material. The costs and problems related to the disposal of a solid material contaminated with microorganisms can thus be avoided by using such a process.
  • a process for at least partially deactivating microorganisms in a solid material, and dewatering the solid material comprises submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm 2 with respect to the surface of electrodes used for generating the current density and compacting the solid material.
  • the process represents an economic and simple manner to dewater and decontaminate or to permit hygienization of solid materials.
  • the process can permit to reduce or eliminate a plurality of microorganisms such as fecal coliforms, Salmonella spp., enteric viruses, viable helminth ova, enterococus, aerobic and facultative anaerobic heterotrophic bacteria, total coliforms, Escherichia coli, Clostridium perfringens, somatic coliphages and F-specific coliphages.
  • the process can permit to at least partially eliminate or decrease the amount of microorganisms present in the solid material.
  • a process is very useful since it can convert a contaminated solid material having a considerable volume of water or solution i.e. low dryness into a dewatered solid material with higher dryness, reduced volume and in which the amount of microorganisms has been considerably reduced or in which the microorganisms have been eliminated. Therefore, the costs and difficulties to dispose and handle a solid material are considerably lowered when the solid material is treated with such a process.
  • deactivating microorganisms refers to preventing the microorganisms from being active and causing undesired effects.
  • deactivating microorganisms can refer to preventing the microorganisms from metabolizing and/or multiply. Deactivation of microorganisms can also include reduction, elimination or destruction of the microorganisms.
  • the voltage gradient can be at least 4 V/cm, at least 5 V/cm, at least 6 V/cm, at least 7 V/cm, at least 8 V/cm, at least 9 V/cm, at least 10 V/cm, at least 12 V/cm, at least 14 V/cm, at least 16 V/cm, at least 18 V/cm at least 20 V/cm, at least 22 V/cm, at least 24 V/cm, at least 26 V/cm, at least 28 V/cm, or at least 30 V/cm.
  • the voltage gradient can be about 3 V/cm to about 50 V/cm, 3 V/cm to about 60 V/cm, 3 V/cm to about 80 V/cm or about 15 V/cm to about 30 V/cm.
  • the current can have an average current density of at least 3 mA/cm 2 , at least 4 mA/cm 2 , at least 5 mA/cm 2 at least 6 mA/cm 2 , at least 7 mA/cm 2 , at least 8 mA/cm 2 , at least 9 mA/cm 2 , at least 10 mA/cm 2 , at least 12 mA/cm 2 , at least 14 mA/cm 2 , at least 16 mA/cm 2 , at least 18 mA/cm 2 , at least 20 mA/cm 2 , at least 25 mA/cm 2 or at least 30 mA/cm 2 .
  • the average current density can
  • the current can be applied to the solid material for a period of at least 5 minutes, at least 12 minutes, at least 20 minutes, or at least 25 minutes.
  • the solid material can be submitted to the electrical current and compacted simultaneously.
  • the solid material can be compacted by a pressure applied to it, the pressure varying according to the consistency of the solid material, the pressure increasing when the solid material consistency is increasing.
  • the pressure applied to the solid material can be substantially non-existent at the beginning of the process, and then, the pressure is progressively increased.
  • a pressure of at least about 0.1 bar can be applied to the solid material in order to compact it while submitting it to the electric current.
  • the pressure can also be about 0.15 bar to about 5 bars.
  • the pressure applied to the solid material can be constant.
  • the solid material can be compressed by maintaining a contact substantially constant between at least one electrode and the solid material when the solid material is submitted to the electric current.
  • the solid material, before the treatment can have a dryness of at least 25 %.
  • the dryness can also be about 2 % to about 25 %.
  • the solid material, after the treatment can have a dryness increased of at least 10 % as compared to the dryness of the solid material before the treatment.
  • the processes of the present invention can further comprise imparting a rotation movement to the solid material while the material is being compacted and submitted to the electrical current.
  • the solid material can be moved in a predetermined direction, and the solid material can be compacted by applying a pressure to the solid material in a direction which is substantially perpendicular to the predetermined direction.
  • the processes can permit to reduce of at least 70 %, at least 99%, at least 99.9%, at least 99.99%, at least 99.999%, or at least 99.9996% the content of Escherichia coli in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 %, or at least 99.9999 the content of Salmonella spp. in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, or at least 99.99 % the content of enterococus in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 97 %, at least 99 %, or at least 99.99 % the content of aerobic and facultative anaerobic heterotrophic bacteria in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 %, or at least 99.9999 % the content of total coliforms in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 %, or at least 99.9999 % the content of fecal coliforms in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, or at least 99.999 % the content of Clostrodium perfringens in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, or at least 99.9 % the content of somatic coliphages in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, or at least 99.99 % the content of F-specific coliphages in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 94 %, at least 99.9 %, at least 99.99 %, or at least 99.9999 % the content of enteric viruses in the solid material.
  • the processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 % or at least 99.9999 % the content of helminths ova in the solid material.
  • the processes can also permit to eliminate helminths ova in the solid material.
  • the processes can permit to substantially prevent the microorganisms from metabolizing and/or multiply and/or to substantially reduce or eliminate the presence of microorganisms in the solid material. Moreover, the processes can permit to substantially destroy microorganisms in the solid material.
  • One way to meet the Class A pathogen reduction requirements is to treat sewage sludge in a process equivalent to the processes to further reduce pathogens (US EPA, 2003. Control of Pathogens and Vector Attraction in Sewage Sludge. Environmental Regulations and technology. United States Environmental Protection Agency. EPA/625/R-92/013. Revised July 2003).
  • One of the processes to further reduce pathogens (PFRP) is pasteurization that involves heating sewage sludge to above a predetermined temperature for a minimum time period. During pasteurization, sludge temperature is maintained at 70 0 C or higher for 30 minutes or longer.
  • the processes of the present invention can permit to submit the solid material to a temperature higher than 70 0 C.
  • the processes can be considered as equivalent to a process to further reduce pathogens (PFRP) if they comprise certain parameters.
  • PFRP pathogens
  • the processes can comprise submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm 2 with respect to the surface of electrodes used for generating the current density, and compacting the solid material and submitting the solid material to a temperature of at least 70 0 C for at least 30 minutes.
  • the processes can comprise submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm 2 with respect to the surface of electrodes used for generating the current density, and compacting the solid material and submitting the solid material to a temperature of at least 70 0 C for a time period t ⁇ , wherein ti ⁇ 30 minutes.
  • a system, for maintaining the temperature of the solid material at 70 0 C or more, can then be added at the end of the treatment.
  • ti ⁇ 30 minutes; and X 2 ⁇ 30 minutes.
  • a process for at least partially deactivating microorganisms in a solid material comprising submitting the solid material to an electric current having a voltage gradient of at least 0.5 volt per centimeter of solid material to be treated, and a current density of at least 2 mA per cm 2 with respect to the surface of electrodes used for generating the current.
  • a process for at least partially deactivating microorganisms in a solid material and dewatering the solid material comprising submitting the solid material to an electric current having a voltage gradient of at least 0.5 volt per centimeter of solid material to be treated, and a current density of at least 2 mA per cm 2 with respect to the surface of electrodes used for generating the current density.
  • Examples 1 to 4 treatments were made on a pilot scale in an activated sludge wastewater treatment plant.
  • the apparatus that was used in Examples 1 to 4 was an apparatus similar to the apparatus illustrated in Figs. 13 to 18 of US 2005/0199499 and described in pages 5 to 7 of the latter document. US 2005/0199499 is hereby incorporated by reference in its entirety.
  • Somatic coliphages PFU/4 g dry weight 3576 ⁇ 2
  • E. coli and Salmonella spp. levels where reduced below detection limits.
  • a decrease of at least 4.13 log units was obtained, which corresponds to at least 99.99% reduction.
  • a reduction below detection limits was obtained for: enterococus (decrease of at least 4.14 log units corresponding to at least 99.99% reduction), total coliforms (decrease of at least 4.12 log units corresponding to at least 99.99% reduction), somatic coliphages (decrease of at least 3.25 log units corresponding to at least 99.94% reduction) and F-specific coliphages (decrease of at least 4.17 log units corresponding to at least 99.99% reduction).
  • enterococus decrease of at least 4.14 log units corresponding to at least 99.99% reduction
  • total coliforms decrease of at least 4.12 log units corresponding to at least 99.99% reduction
  • somatic coliphages decrease of at least 3.25 log units corresponding to at least 99.94% reduction
  • F-specific coliphages decrease of at least
  • the sludge was treated in a similar manner as described in Example 1 , but with the specific parameters described in Table 4. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 4, were applied in the process. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 5.
  • Viable helminth ova Ova/4g dry weight Absence Absence During this treatment, E. coli level was reduced below detection limit. A decrease of at least 5.43 log units corresponding to at least 99.9996% was obtained. Moreover, a decrease of at least 6.65 log units was obtained for total coliforms corresponding to at least 99.9999%. For Clostridium perfringens, the results indicated a decrease of 5.09 log units, corresponding to 99.999% reduction. Enteric viruses were reduced to below the detectable limit. For aerobic and facultative anaerobic heterotrophic bacteria a decrease of 2.95 log units corresponding to 99.89% reduction was obtained by the treatment.
  • the sludge was treated in a similar manner as described in Example 1 , but with the specific parameters described in Table 7. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 7, were applied in the process. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 8.
  • Somatic coliphages PFU/4 g dry weight 67x 10 3 ⁇ 3
  • enteric viruses are detected and reduced to below detection limits.
  • For aerobic and facultative anaerobic heterotrophic bacteria a decrease of 4.07 log units, corresponding to 99.99 % reduction was obtained.
  • the sludge was treated in a similar manner as described in Example 1 , but with the specific parameters described in Table 10. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 10, were applied in the process. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 11. As shown in Table 12, the treatment permitted to considerably reduce the fecal coliforms present in the sludge.
  • a reduction of fecal coliforms of at least 3.47 log units corresponding to at least 99.97% reduction was obtained by the treatment.
  • the analyzed samples were free of helminths ova.
  • tests were made on an activated sludge from wastewater treatment plant, which was voluntarily contaminated with helminths ova (Ascaris suis) isolated from pig faeces Wisconsin method (double centrifugation in water and after in saturated sugar solution) was used to isolate Ascaris ova (Foreyt, 2001. Veterinary Parasitology Reference Manual. 5th edition. Iowa State University Press)
  • the solution used for sludge contamination contained approximately 1000 eggs/ml.
  • Example 5 The apparatus used for Example 5 is an apparatus similar to the one illustrated in Fig. 2, of US 2005/0016870 and described in pages 3 and 4 of the latter document. US 2005/0016870 is hereby incorporated by reference in its entirety.
  • the analysis shows less than 10 Colony Forming Unit per 100 ml_.
  • the so-obtained effluent may be used for example as a fertilizer.
  • Table 16 is presented in the example 7 in order to show the variation of the current densities during the treatment. Data were collected from a cell of an apparatus similar to the apparatus illustrated in Figs. 13 to 18 of US 2005/0199499 and described in pages 5 to 7 of the latter document. Table 16. Current density variation during a treatment
  • Tables 17 and 18 show monitoring results and various parameters obtained during the treatment of the sludge sampled at the first sampling, and for each of the five anode-units.
  • Table 19 to 21 show microorganisms reduction for the samples taken during the first, second and third sampling.
  • Examples 1 to 5, 6 and 8 thus clearly demonstrate that the processes of the present invention permit the at least partial deactivation, reduction and/or destruction of microorganisms such as E. CoIi, Salmonella spp., fecal coliforms, enteric viruses and helminths ova.
  • microorganisms such as E. CoIi, Salmonella spp., fecal coliforms, enteric viruses and helminths ova.
  • the processes of the present invention can thus be useful for micoorganisms reduction or elimination in solid materials. They can also be useful for dewatering these solid materials.
  • the solid materials can be, for example, municipal sludge, agro-alimentary sludge, industrial sludge, etc.
  • the processes of the present invention can also be useful for treating and/or dewatering various types of solid materials such as sediment, soil, biosolids, organic and/or inorganic sludge such as colloidal sludge, sludge from pulp and paper industries, agroalimentary sludge, sludge issued from a chemical or biological treatment, sludge from a dairy, sludge from a slaughterhouse, sludge from liquid or semi-liquid manure such as pork manure, and sludge from wastewater treatment plant.
  • solid materials such as sediment, soil, biosolids, organic and/or inorganic sludge such as colloidal sludge, sludge from pulp and paper industries, agroalimentary sludge, sludge issued from a chemical or biological treatment, sludge from a dairy, sludge from a slaughterhouse, sludge from liquid or semi-liquid manure such as pork manure, and sludge from wastewater treatment plant.

Abstract

There is provided a process for at least partially deactivating microorganisms in a solid material. The process comprising submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating the current.

Description

PROCESSES FOR DEACTIVATING MICROORGANISMS IN SOLID MATERIALS
TECHNICAL FIELD
The present invention relates to improvements in the field of solid materials decontamination treatment. In particular, the invention relates to processes for microorganisms deactivation and/or destruction in solid materials. Such processes can be useful for treating various types of solid materials, such as sludges. They also permit deactivation and/or destruction of various types of pathogenic microorganisms.
BACKGROUND OF THE INVENTION
The management and reclamation of municipal sludge generated by wastewater treatment require a beforehand dewatering and pathogens reduction.
The principal microorganisms representative and indicators of treatment efficiency for pathogens reduction are: fecal coliforms or Salmonella sp., enteric viruses and viable helminth ova (US EPA, 2003. Control of Pathogens and Vector Attraction in Sewage Sludge. Environmental Regulations and technology. United States Environmental Protection Agency. EPA/625/R-92/013. Revised July 2003). All those microorganisms are likely to be present at various degrees in municipal sludge.
According to US EPA (1993), the aim of class A processes is to reduce pathogen densities below the following detection limits: less than 3 most probable number (MPN) per 4 grams of total solid (dry weight basis) for Salmonella sp.; less than 1 plaque-forming unit (PFU) per 4 grams of total solids (dry weight basis) for enteric viruses and less than 1 viable helminth ova per 4 grams of total solid (dry weight basis). For fecal coliforms, used as indicator organism, the aim is to reduce them to less than 1000 most probable number (MPN) per 1 gram of total solid (dry weight basis). Other microorganisms like Clostridium perfringens, aerobic and facultative anaerobic heterotrophic bacteria, total conforms, enterococus and coliphages can be used as indicator organisms. Coliphages (bacteriophages) are viruses that infect bacteria. Thanks to their characteristics, coliphages are considered by researchers as indicators of fecal pollution and are proposed as a model to follow the fate of enteric viruses in various hydrous environment and wastewater treatment plant.
Actual technologies for sludge sanitization rely essentially on thermal treatment, heat drying and heat treatment, high pH combined to high temperature process (alkaline treatment), thermophilic digestion, beta and gamma ray irradiation, pasteurization and composting.
It is thus highly desirable to be provided with an alternative to the solutions proposed so far.
SUMMARY OF THE INVENTION
According to one aspect of the invention, there is provided a process for at least partially deactivating microorganisms in a solid material. The process comprises submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating the current.
It was found that such a process is very useful to treat solid materials in order to at least partially deactivate the microorganisms contained therein or even destroy the microorganisms contained therein. The process represents an economic and simple manner to decontaminate or to permit hygienization of solid materials. The process can permit to deactivate and/or destroy a plurality of microorganisms such as fecal coliforms, Salmonella spp., enteric viruses, viable helminth ova, enterococus, aerobic and facultative anaerobic heterotrophic bacteria, total coliforms, Escherichia coli, Clostridium perfringens, somatic coliphages and F-specific coliphages. The efficiency of the process is quite impressive since it can permit to considerably decrease the amount of microorganisms present in the solid material. The costs and problems related to the disposal of a solid material contaminated with microorganisms can thus be avoided by using such a process.
According to another aspect of the invention, there is provided a process for at least partially deactivating microorganisms in a solid material, and dewatering the solid material. The process comprises submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating the current density and compacting the solid material.
It was found that such a process is very useful to treat solid materials in order to dewater it and to at least partially reduce the amount of microorganisms contained therein or even destroy the microorganisms contained therein. The process represents an economic and simple manner to dewater and decontaminate or to permit hygienization of solid materials. The process can permit to reduce or eliminate a plurality of microorganisms such as fecal coliforms, Salmonella spp., enteric viruses, viable helminth ova, enterococus, aerobic and facultative anaerobic heterotrophic bacteria, total coliforms, Escherichia coli, Clostridium perfringens, somatic coliphages and F-specific coliphages. The process can permit to at least partially eliminate or decrease the amount of microorganisms present in the solid material. Thus, such a process is very useful since it can convert a contaminated solid material having a considerable volume of water or solution i.e. low dryness into a dewatered solid material with higher dryness, reduced volume and in which the amount of microorganisms has been considerably reduced or in which the microorganisms have been eliminated. Therefore, the costs and difficulties to dispose and handle a solid material are considerably lowered when the solid material is treated with such a process.
The expression "deactivating microorganisms" as used herein refers to preventing the microorganisms from being active and causing undesired effects. For example, "deactivating microorganisms" can refer to preventing the microorganisms from metabolizing and/or multiply. Deactivation of microorganisms can also include reduction, elimination or destruction of the microorganisms.
The voltage gradient can be at least 4 V/cm, at least 5 V/cm, at least 6 V/cm, at least 7 V/cm, at least 8 V/cm, at least 9 V/cm, at least 10 V/cm, at least 12 V/cm, at least 14 V/cm, at least 16 V/cm, at least 18 V/cm at least 20 V/cm, at least 22 V/cm, at least 24 V/cm, at least 26 V/cm, at least 28 V/cm, or at least 30 V/cm. Alternatively, the voltage gradient can be about 3 V/cm to about 50 V/cm, 3 V/cm to about 60 V/cm, 3 V/cm to about 80 V/cm or about 15 V/cm to about 30 V/cm. The current can have an average current density of at least 3 mA/cm2, at least 4 mA/cm2, at least 5 mA/cm2 at least 6 mA/cm2, at least 7 mA/cm2, at least 8 mA/cm2, at least 9 mA/cm2, at least 10 mA/cm2, at least 12 mA/cm2, at least 14 mA/cm2, at least 16 mA/cm2, at least 18 mA/cm2, at least 20 mA/cm2, at least 25 mA/cm2 or at least 30 mA/cm2. Alternatively, the average current density can be of about 6 mA/cm2 to about 70 mA/cm2 or of about 10 mA/cm2 to about 45 mA/cm2.
The current can be applied to the solid material for a period of at least 5 minutes, at least 12 minutes, at least 20 minutes, or at least 25 minutes. The solid material can be submitted to the electrical current and compacted simultaneously. The solid material can be compacted by a pressure applied to it, the pressure varying according to the consistency of the solid material, the pressure increasing when the solid material consistency is increasing. The pressure applied to the solid material can be substantially non-existent at the beginning of the process, and then, the pressure is progressively increased. A pressure of at least about 0.1 bar can be applied to the solid material in order to compact it while submitting it to the electric current. The pressure can also be about 0.15 bar to about 5 bars. Alternatively, the pressure applied to the solid material can be constant.
The solid material can be compressed by maintaining a contact substantially constant between at least one electrode and the solid material when the solid material is submitted to the electric current. The solid material, before the treatment, can have a dryness of at least 25 %. The dryness can also be about 2 % to about 25 %. For example, the solid material, after the treatment, can have a dryness increased of at least 10 % as compared to the dryness of the solid material before the treatment.
The processes of the present invention can further comprise imparting a rotation movement to the solid material while the material is being compacted and submitted to the electrical current.
Alternatively, the solid material can be moved in a predetermined direction, and the solid material can be compacted by applying a pressure to the solid material in a direction which is substantially perpendicular to the predetermined direction.
The processes can permit to reduce of at least 70 %, at least 99%, at least 99.9%, at least 99.99%, at least 99.999%, or at least 99.9996% the content of Escherichia coli in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 %, or at least 99.9999 the content of Salmonella spp. in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, or at least 99.99 % the content of enterococus in the solid material. The processes can permit to reduce of at least 70 %, at least 97 %, at least 99 %, or at least 99.99 % the content of aerobic and facultative anaerobic heterotrophic bacteria in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 %, or at least 99.9999 % the content of total coliforms in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 %, or at least 99.9999 % the content of fecal coliforms in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, or at least 99.999 % the content of Clostrodium perfringens in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, or at least 99.9 % the content of somatic coliphages in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, or at least 99.99 % the content of F-specific coliphages in the solid material. The processes can permit to reduce of at least 70 %, at least 94 %, at least 99.9 %, at least 99.99 %, or at least 99.9999 % the content of enteric viruses in the solid material. The processes can permit to reduce of at least 70 %, at least 99 %, at least 99.9 %, at least 99.99 %, at least 99.999 % or at least 99.9999 % the content of helminths ova in the solid material. The processes can also permit to eliminate helminths ova in the solid material.
The processes can permit to substantially prevent the microorganisms from metabolizing and/or multiply and/or to substantially reduce or eliminate the presence of microorganisms in the solid material. Moreover, the processes can permit to substantially destroy microorganisms in the solid material.
One way to meet the Class A pathogen reduction requirements is to treat sewage sludge in a process equivalent to the processes to further reduce pathogens (US EPA, 2003. Control of Pathogens and Vector Attraction in Sewage Sludge. Environmental Regulations and technology. United States Environmental Protection Agency. EPA/625/R-92/013. Revised July 2003). One of the processes to further reduce pathogens (PFRP) is pasteurization that involves heating sewage sludge to above a predetermined temperature for a minimum time period. During pasteurization, sludge temperature is maintained at 70 0C or higher for 30 minutes or longer.
During the treatment, the processes of the present invention can permit to submit the solid material to a temperature higher than 70 0C. For example, the processes can be considered as equivalent to a process to further reduce pathogens (PFRP) if they comprise certain parameters. The two following examples represent such processes.
Firstly, the processes can comprise submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating the current density, and compacting the solid material and submitting the solid material to a temperature of at least 70 0C for at least 30 minutes. Secondly, the processes can comprise submitting the solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating the current density, and compacting the solid material and submitting the solid material to a temperature of at least 70 0C for a time period tι, wherein ti < 30 minutes. A system, for maintaining the temperature of the solid material at 70 0C or more, can then be added at the end of the treatment. The solid material is thus subjected to a temperature of 70 0C or more during a time period X2 (X2 ≤ 30 minutes) in such a way that the time period t3 (t3 = t-ι+ t2) is at least 30 minutes. Alternatively, ti < 30 minutes; and X2 < 30 minutes.
According to another aspect of the invention, there is provided a process for at least partially deactivating microorganisms in a solid material, the process comprising submitting the solid material to an electric current having a voltage gradient of at least 0.5 volt per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating the current.
According to another aspect of the invention, there is provided a process for at least partially deactivating microorganisms in a solid material and dewatering the solid material, the process comprising submitting the solid material to an electric current having a voltage gradient of at least 0.5 volt per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating the current density.
DETAILLED DESCRIPTION OF THE INVENTION
Further features and advantages of the invention will become more readily apparent from the following non-limiting examples.
Examples
For Examples 1 to 4 treatments were made on a pilot scale in an activated sludge wastewater treatment plant. The apparatus that was used in Examples 1 to 4 was an apparatus similar to the apparatus illustrated in Figs. 13 to 18 of US 2005/0199499 and described in pages 5 to 7 of the latter document. US 2005/0199499 is hereby incorporated by reference in its entirety.
Example 1
The process was carried out on the sludge with the previously mentioned apparatus, but with the specific parameters described in Table 1. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 1 were applied in the process and superior results in term of microorganisms deactivation were unexpectedly obtained as compared to those mentioned in US 2005/0199499. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 2. The electric current induced a temperature elevation. Temperatures measured in the treated sludge, at the outlet of the apparatus, varied from 70.0 to 76.3 0C. Moreover, as shown in Table 3, the treatment permitted to considerably reduce the amount of microorganisms present in the sludge and event eliminate certain types of microorganisms.
Table 1. Treatment parameters
Figure imgf000009_0001
Table 2. Sludge characteristics
Figure imgf000009_0002
Table 3. Microorganisms reduction
Before After
Microorganisms Units treatment treatment
Escherichia coli MPN/g dry weight 94x 10-3 <7
Salmonella spp. MPN/4g dry weight 71 <3
Enterococus CFU/g dry weight 447 x 103 <32
Aerobic and facultative anaerobic heterotrophic CFU/g dry weight 101x 106 27x 105 bacteria
Total coliforms MPN/g dry weight 94x 103 <7
Clostridium perfringens CFU/g dry weight Absence Absence
Somatic coliphages PFU/4 g dry weight 3576 <2
F-specific coliphages PFU/4 g dry weight 29412 <2
Enteric viruses PFU/4 g dry weight <0.47 <0.24
Enteric viruses
MPNIP1/4 g dry weight <0.94 <0.24 (immunoperoxydase method)
Viable helminth ova Ova/4g dry weight Absence Absence
1MPNlP : Most probable number by immunoperoxidase
As it can be seen from Table 3, E. coli and Salmonella spp. levels where reduced below detection limits. For E. coli, a decrease of at least 4.13 log units was obtained, which corresponds to at least 99.99% reduction. A reduction below detection limits was obtained for: enterococus (decrease of at least 4.14 log units corresponding to at least 99.99% reduction), total coliforms (decrease of at least 4.12 log units corresponding to at least 99.99% reduction), somatic coliphages (decrease of at least 3.25 log units corresponding to at least 99.94% reduction) and F-specific coliphages (decrease of at least 4.17 log units corresponding to at least 99.99% reduction). For aerobic and facultative anaerobic heterotrophic bacteria, a decrease of 1.57 log units, corresponding to a 97.33% reduction, was obtained.
Example 2
The sludge was treated in a similar manner as described in Example 1 , but with the specific parameters described in Table 4. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 4, were applied in the process. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 5. The temperatures measured in the treated sludge, at the outlet of the apparatus, varied from 77.5 to 96.2 0C. Table 6 shows that the treatment permitted to considerably reduce the amount of microorganisms present in the sludge and event eliminate certain types of microorganisms.
Table 4. Treatment parameters
Figure imgf000011_0001
Table 5. Sludge characteristics
Figure imgf000011_0002
Table 6 . Microorganisms reduction
Before After
Microorganisms Units treatment treatment
Escherichia coli MPN/g dry weight 19x 10* <7
Salmonella spp. MPN/4g dry weight <5 <3
Enterococus CFU/g dry weight 38x 104 <32
Aerobic and facultative anaerobic heterotrophic CFU/g dry weight 4250x 103 4750 bacteria
Total conforms MPN/g dry weight 31x 106 <7
Clostridium perfringens CFU/g dry weight 775x 104 63
Somatic coliphages PFU/4 g dry weight 1750 <2.5
F-specific coliphages PFU/4 g dry weight 6400 <2.5
Enteric viruses PFU/4 g dry weight <0.5 <0.25
Enteric viruses (immunoperoxydase method) MPNIP2/4 g dry weight 1.75 <0.25
Viable helminth ova Ova/4g dry weight Absence Absence During this treatment, E. coli level was reduced below detection limit. A decrease of at least 5.43 log units corresponding to at least 99.9996% was obtained. Moreover, a decrease of at least 6.65 log units was obtained for total coliforms corresponding to at least 99.9999%. For Clostridium perfringens, the results indicated a decrease of 5.09 log units, corresponding to 99.999% reduction. Enteric viruses were reduced to below the detectable limit. For aerobic and facultative anaerobic heterotrophic bacteria a decrease of 2.95 log units corresponding to 99.89% reduction was obtained by the treatment.
Example 3
The sludge was treated in a similar manner as described in Example 1 , but with the specific parameters described in Table 7. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 7, were applied in the process. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 8. The temperatures measured in the treated sludge, at the outlet of the apparatus, varied from 96.5 to 98.7 0C. As shown in Table 9, the treatment permitted to considerably reduce the amount of microorganisms present in the sludge and event eliminate certain types of microorganisms.
Table 7. Treatment parameters
Figure imgf000012_0001
Table 8. Sludge characteristics
Table 9. Microorganisms reduction
Before After
Microorganisms Units treatment treatment
Escherichia coli MPN/g dry weight 33 x 10J <8
Salmonella spp. MPN/4g dry weight 5 <3
Enterococus CFU/g dry weight 15 x 105 <38
Aerobic and facultative anaerobic heterotrophic CFU/g dry weight 547 x 105 46x 102 bacteria
Total conforms MPN/g dry weight >107x 103 <8
Clostridium perfringens CFU/g dry weight 550 x 104 327x 102
Somatic coliphages PFU/4 g dry weight 67x 103 <3
F-specific coliphages PFU/4 g dry weight 26x 103 <3
Enteric viruses PFU/4 g dry weight 0.53 <0.3
Enteric viruses
MPNIP2/4 g dry weight 5.33 <0.3 (immunoperoxydase method)
Viable helminth ova Ova/4g dry weight Absence Absence
In this example, enteric viruses are detected and reduced to below detection limits. For aerobic and facultative anaerobic heterotrophic bacteria, a decrease of 4.07 log units, corresponding to 99.99 % reduction was obtained.
Example 4
The sludge was treated in a similar manner as described in Example 1 , but with the specific parameters described in Table 10. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 10, were applied in the process. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 11. As shown in Table 12, the treatment permitted to considerably reduce the fecal coliforms present in the sludge.
Table 10. Treatment parameters
Figure imgf000013_0001
Table11. Sludge characteristics
Figure imgf000014_0001
Table 12. Microorganisms reduction
Figure imgf000014_0002
A reduction of fecal coliforms of at least 3.47 log units corresponding to at least 99.97% reduction was obtained by the treatment.
Example 5
In examples 1 to 3, the analyzed samples were free of helminths ova. To show the effect of the process on helminths ova, tests were made on an activated sludge from wastewater treatment plant, which was voluntarily contaminated with helminths ova (Ascaris suis) isolated from pig faeces Wisconsin method (double centrifugation in water and after in saturated sugar solution) was used to isolate Ascaris ova (Foreyt, 2001. Veterinary Parasitology Reference Manual. 5th edition. Iowa State University Press) The solution used for sludge contamination contained approximately 1000 eggs/ml.
The apparatus used for Example 5 is an apparatus similar to the one illustrated in Fig. 2, of US 2005/0016870 and described in pages 3 and 4 of the latter document. US 2005/0016870 is hereby incorporated by reference in its entirety.
The process was carried out on the sludge with the previously mentioned apparatus but with the specific parameters described in Table 13. In fact, the specific values of voltage gradient, current density, and time of treatment described in Table 13, were applied in the process and superior results in term of microorganisms reduction were unexpectedly obtained as compared to those reported in US 2005/0016870. At the end of the treatment or process, a considerable increase of the sludge dryness was observed as indicated in Table 13. Table 13, also demonstrates that the treatment permitted to considerably reduce the amount of helminthes ova present in the sludge and even eliminate them.
Table 13. Results
Figure imgf000015_0001
Wisconsin method was used for detecting Ascaris ova in treated and untreated samples. Microscopic examination of the untreated sample shows 60 eggs of helminthes ova {Ascaris suis) by 10 grams of sludge. For treated samples (treatment 1 to 6), microscopic examination shows no eggs. These results demonstrate that such a process can permit the complete destruction or elimination of helminths ova. To check the viability of helminths ova, a culture at ambient temperature was made with eggs taken from the untreated sample. The culture showed that larval development was induced for 64% of the eggs.
Example 6
The effluent issued from a sludge, treated with an apparatus similar to the one illustrated in Fig. 2, of US 2005/0016870 and described in pages 3 and 4 of the latter document, has been analyzed for fecal coliforms. The analysis shows less than 10 Colony Forming Unit per 100 ml_. The so-obtained effluent may be used for example as a fertilizer.
Table 14. Treatment parameters
Figure imgf000016_0001
Table15. Sludge characteristics
Figure imgf000016_0002
Example 7
Table 16 is presented in the example 7 in order to show the variation of the current densities during the treatment. Data were collected from a cell of an apparatus similar to the apparatus illustrated in Figs. 13 to 18 of US 2005/0199499 and described in pages 5 to 7 of the latter document. Table 16. Current density variation during a treatment
Figure imgf000017_0001
Example 8
In this example, municipal secondary sludge was treated. The apparatus that was used in Examples 8 was an apparatus similar to the apparatus illustrated in Figs. 1 to 7 of PCT/CA2007/001052 filed on June 13, 2007 and described in pages 14 to 23 of the latter document. PCT/CA2007/001052 is hereby incorporated by reference in its entirety. The total treatment process took about 15 minutes. The applied voltage gradient was about 28.6 V/cm.
During the sludge treatment, three sampling were performed. For each sampling, untreated sludge, treated sludge and generated effluent were sampled for salmonella and fecal coliforms analyses.
Tables 17 and 18 show monitoring results and various parameters obtained during the treatment of the sludge sampled at the first sampling, and for each of the five anode-units. Table 19 to 21 show microorganisms reduction for the samples taken during the first, second and third sampling. First sampling
Table 17. Parameters used for the first, second and third anode-unit
Figure imgf000018_0001
Table 18. Parameters used for the forth, and fifth anode-unit
Figure imgf000019_0001
Table 19. Microorganisms reduction
Figure imgf000019_0002
Second sampling
Table 20. Microorganisms reduction
Figure imgf000020_0001
Third sampling
Table 21. Microorganisms reduction
Figure imgf000020_0002
Examples 1 to 5, 6 and 8 thus clearly demonstrate that the processes of the present invention permit the at least partial deactivation, reduction and/or destruction of microorganisms such as E. CoIi, Salmonella spp., fecal coliforms, enteric viruses and helminths ova.
The processes of the present invention can thus be useful for micoorganisms reduction or elimination in solid materials. They can also be useful for dewatering these solid materials. The solid materials can be, for example, municipal sludge, agro-alimentary sludge, industrial sludge, etc.
The processes of the present invention can also be useful for treating and/or dewatering various types of solid materials such as sediment, soil, biosolids, organic and/or inorganic sludge such as colloidal sludge, sludge from pulp and paper industries, agroalimentary sludge, sludge issued from a chemical or biological treatment, sludge from a dairy, sludge from a slaughterhouse, sludge from liquid or semi-liquid manure such as pork manure, and sludge from wastewater treatment plant. These processes can be used in industrial applications as well as for protecting environment.
While the invention has been described with particular reference to the illustrated embodiment, it will be understood that numerous modifications thereto will appear to those skilled in the art, without however departing from the scope of the claims. Accordingly, the above description and examples should be taken as illustrative of the invention and not in a limiting sense.

Claims

WHAT IS CLAIMED IS:
1. A process for at least partially deactivating microorganisms in a solid material, said process comprising submitting said solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating said current.
2. A process for at least partially deactivating microorganisms in a solid material and dewatering said solid material, said process comprising submitting said solid material to an electric current having a voltage gradient of at least 3 volts per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating said current density and compacting said solid material.
3. The process of claim 2, wherein said solid material is submitted to said electrical current and compacted simultaneously.
4. The process of claim 2 or 3, wherein, said solid material is compacted by a pressure applied to it, said pressure varying according to the consistency of said solid material, the pressure increasing when the solid material consistency is increasing.
5. The process of claim 4, wherein, the pressure applied to said solid material is substantially non-existent at the beginning of the process, and then, the pressure is progressively increased.
6. The process of claim 2 or 3, wherein, said solid material is compacted by a pressure applied to it, and wherein said applied pressure is constant.
7. The process of any one of claims 2 to 6, wherein a pressure of at least about 0.1 bar is applied to said solid material in order to compact it.
8. The process of any one of claims 2 to 6, wherein a pressure of about 0.15 bar to about 5 bars is applied to said solid material in order to compact it.
9. The process of any one of claims 2 to 8, wherein said process further comprises imparting a rotation movement to the solid material while said material is being compacted and submitted to the electrical current.
10. The process of any one of claims 2 to 8, wherein the solid material is moved in a predetermined direction, and wherein the solid material is compacted by applying a pressure to the solid material in a direction which is substantially perpendicular to said predetermined direction.
11. The process of any one of claims 2 to 10, wherein the solid material, before said treatment, has a dryness of about 2 % to about 25 %.
12. The process of any one of claims 2 to 11 , wherein the solid material, after said process, has a dryness of at least 25 %.
13. The process of any one of claims 2 to 10, wherein the solid material, after said treatment, has a dryness increased of at least 10 % as compared to the dryness of the solid material before said treatment.
14. The process of any one of claims 1 to 13, wherein said voltage gradient is at least 8 V/cm.
15. The process of any one of claims 1 to 13, wherein said voltage gradient is at least 10 V/cm.
16. The process of any one of claims 1 to 13, wherein said voltage gradient is at least 12 V/cm.
17. The process of any one of claims 1 to 13, wherein said voltage gradient is at least 14 V/cm.
18. The process of any one of claims 1 to 13, wherein said voltage gradient is at least 16 V/cm.
19. The process of any one of claims 1 to 13, wherein said voltage gradient is at least 18 V/cm.
20. The process of any one of claims 1 to 13, wherein said voltage gradient is at least 20 V/cm.
21. The process of any one of claims 1 to 13, wherein said voltage gradient is about 3 V/cm to about 80 V/cm.
22. The process of any one of claims 1 to 13, wherein said voltage gradient is about 3 V/cm to about 60 V/cm.
23. The process of any one of claims 1 to 13, wherein said voltage gradient is about 3 V/cm to about 50 V/cm.
24. The process of any one of claims 1 to 13, wherein said voltage gradient is about 15 V/cm to about 30 V/cm.
25. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 6 mA/cm2.
26. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 8 mA/cm2.
27. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 10 mA/cm2.
28. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 12 mA/cm2.
29. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 14 mA/cm2.
30. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 20 mA/cm2.
31. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 25 mA/cm2.
32. The process of any one of claims 1 to 24, wherein said current has an average current density of at least 30 mA/cm2.
33. The process of any one of claims 1 to 24, wherein said current has an average current density of about 6 mA/cm2 to about 70 mA/cm2.
34. The process of any one of claims 1 to 24, wherein said current has an average current density of about 10 mA/cm2 to about 45 mA/cm2.
35. The process of any one of claims 1 to 34, wherein said current is applied to said solid material for a period of at least 5 minutes.
36. The process of any one of claims 1 to 34, wherein said current is applied to said solid material for a period of at least 12 minutes.
37. The process of any one of claims 1 to 36, wherein said microorganisms comprise Escherichia coli, and wherein said process permits to reduce of at least 70 % the content of Escherichia coli in said solid material.
38. The process of any one of claims 1 to 36, wherein said microorganisms comprise Escherichia coli, and wherein said process permits to reduce of at least 99 % the content of Escherichia coli in said solid material.
39. The process of any one of claims 1 to 36, wherein said microorganisms comprise Escherichia coli, and wherein said process permits to reduce of at least 99.9 % the content of Escherichia coli in said solid material.
40. The process of any one of claims 1 to 36, wherein said microorganisms comprise Escherichia coli, and wherein said process permits to reduce of at least 99.99 % the content of Escherichia coli in said solid material.
41. The process of any one of claims 1 to 36, wherein said microorganisms comprise Escherichia coli, and wherein said process permits to reduce of at least 99.999 % the content of Escherichia coli in said solid material.
42. The process of any one of claims 1 to 36, wherein said microorganisms comprise Escherichia coli, and wherein said process permits to reduce of at least 99.9996 % the content of Escherichia coli in said solid material.
43. The process of any one of claims 1 to 42, wherein said microorganisms comprise salmonella, and wherein said process permits to reduce of at least 70 % the content of salmonella in said solid material.
44. The process of any one of claims 1 to 42, wherein said microorganisms comprise salmonella, and wherein said process permits to reduce of at least 99 % the content of salmonella in said solid material.
45. The process of any one of claims 1 to 42, wherein said microorganisms comprise salmonella, and wherein said process permits to reduce of at least 99.9 % the content of salmonella in said solid material.
46. The process of any one of claims 1 to 42, wherein said microorganisms comprise salmonella, and wherein said process permits to reduce of at least 99.99 % the content of salmonella in said solid material.
47. The process of any one of claims 1 to 46, wherein said microorganisms comprise enterococus, and wherein said process permits to reduce of at least 70 % the content of enterococus in said solid material.
48. The process of any one of claims 1 to 46, wherein said microorganisms comprise enterococus, and wherein said process permits to reduce of at least 99 % the content of enterococus in said solid material.
49. The process of any one of claims 1 to 46, wherein said microorganisms comprise enterococus, and wherein said process permits to reduce of at least 99.9 % the content of enterococus in said solid material.
50. The process of any one of claims 1 to 46, wherein said microorganisms comprise enterococus, and wherein said process permits to reduce of at least 99.99 % the content of enterococus in said solid material.
51. The process of any one of claims 1 to 50, wherein said microorganisms comprise aerobic and facultative anaerobic heterotrophic bacteria, and wherein said process permits to reduce of at least 70 % the content of aerobic and facultative anaerobic heterotrophic bacteria in said solid material.
52. The process of any one of claims 1 to 50, wherein said microorganisms comprise aerobic and facultative anaerobic heterotrophic bacteria, and wherein said process permits to reduce of at least 97 % the content of aerobic and facultative anaerobic heterotrophic bacteria in said solid material.
53. The process of any one of claims 1 to 50, wherein said microorganisms comprise aerobic and facultative anaerobic heterotrophic bacteria, and wherein said process permits to reduce of at least 99 % the content of aerobic and facultative anaerobic heterotrophic bacteria in said solid material.
54. The process of any one of claims 1 to 50, wherein said microorganisms comprise aerobic and facultative anaerobic heterotrophic bacteria, and wherein said process permits to reduce of at least 99.99 % the content of aerobic and facultative anaerobic heterotrophic bacteria in said solid material.
55. The process of any one of claims 1 to 54, wherein said microorganisms comprise total coliforms, and wherein said process permits to reduce of at least 70 % the content of total coliforms in said solid material.
56. The process of any one of claims 1 to 54, wherein said microorganisms comprise total coliforms, and wherein said process permits to reduce of at least 99 % the content of total coliforms in said solid material.
57. The process of any one of claims 1 to 54, wherein said microorganisms comprise total coliforms, and wherein said process permits to reduce of at least 99.9 % the content of total coliforms in said solid material.
58. The process of any one of claims 1 to 54, wherein said microorganisms comprise total coliforms, and wherein said process permits to reduce of at least 99.99 % the content of total coliforms in said solid material.
59. The process of any one of claims 1 to 54, wherein said microorganisms comprise total coliforms, and wherein said process permits to reduce of at least 99.999 % the content of total coliforms in said solid material.
60. The process of any one of claims 1 to 54, wherein said microorganisms comprise total coliforms, and wherein said process permits to reduce of at least 99.9999 % the content of total coliforms in said solid material.
61. The process of any one of claims 1 to 54, wherein said microorganisms comprise fecal coliforms, and wherein said process permits to reduce of at least 70 % the content of fecal coliforms in said solid material.
62. The process of any one of claims 1 to 54, wherein said microorganisms comprise fecal coliforms, and wherein said process permits to reduce of at least 99 % the content of fecal coliforms in said solid material.
63. The process of any one of claims 1 to 54, wherein said microorganisms comprise fecal conforms, and wherein said process permits to reduce of at least 99.9 % the content of fecal coliforms in said solid material.
64. The process of any one of claims 1 to 54, wherein said microorganisms comprise fecal coliforms, and wherein said process permits to reduce of at least 99.99 % the content of fecal coliforms in said solid material.
65. The process of any one of claims 1 to 54, wherein said microorganisms comprise fecal coliforms, and wherein said process permits to reduce of at least 99.999 % the content of fecal coliforms in said solid material.
66. The process of any one of claims 1 to 54, wherein said microorganisms comprise fecal coliforms, and wherein said process permits to reduce of at least 99.9999 % the content of fecal coliforms in said solid material.
67. The process of any one of claims 1 to 66, wherein said microorganisms comprise Clostrodium perfringens, and wherein said process permits to reduce of at least 70 % the content of Clostrodium perfringens in said solid material.
68. The process of any one of claims 1 to 66, wherein said microorganisms comprise Clostrodium perfringens, and wherein said process permits to reduce of at least 99 % the content of Clostrodium perfringens in said solid material.
69. The process of any one of claims 1 to 66, wherein said microorganisms comprise Clostrodium perfringens, and wherein said process permits to reduce of at least 99.9 % the content of Clostrodium perfringens in said solid material.
70. The process of any one of claims 1 to 66, wherein said microorganisms comprise Clostrodium perfringens, and wherein said process permits to reduce of at least 99.99 % the content of Clostrodium perfringens in said solid material.
71. The process of any one of claims 1 to 66, wherein said microorganisms comprise Clostrodium perfringens, and wherein said process permits to reduce of at least 99.999 % the content of Clostrodium perfringens in said solid material.
72. The process of any one of claims 1 to 71 , wherein said microorganisms comprise somatic coliphages, and wherein said process permits to reduce of at least 70 % the content of somatic coliphages in said solid material.
73. The process of any one of claims 1 to 71 , wherein said microorganisms comprise somatic coliphages, and wherein said process permits to reduce of at least 99 % the content of somatic coliphages in said solid material.
74. The process of any one of claims 1 to 71 , wherein said microorganisms comprise somatic coliphages, and wherein said process permits to reduce of at least 99.9 % the content of somatic coliphages in said solid material.
75. The process of any one of claims 1 to 74, wherein said microorganisms comprise F-specific coliphages, and wherein said process permits to reduce of at least 70 % the content of F-specific coliphages in said solid material.
76. The process of any one of claims 1 to 74, wherein said microorganisms comprise F-specific coliphages, and wherein said process permits to reduce of at least 99 % the content of F-specific coliphages in said solid material.
77. The process of any one of claims 1 to 74, wherein said microorganisms comprise F-specific coliphages, and wherein said process permits to reduce of at least 99.9 % the content of F-specific coliphages in said solid material.
78. The process of any one of claims 1 to 74, wherein said microorganisms comprise F-specific coliphages, and wherein said process permits to reduce of at least 99.99 % the content of F-specific coliphages in said solid material.
79. The process of any one of claims 1 to 78, wherein said microorganisms comprise enteric viruses, and wherein said process permits to reduce of at least 70 % the content of enteric viruses in said solid material.
80. The process of any one of claims 1 to 78, wherein said microorganisms comprise enteric viruses, and wherein said process permits to reduce of at least 94 % the content of enteric viruses in said solid material.
81. The process of any one of claims 1 to 78, wherein said microorganisms comprise enteric viruses, and wherein said process permits to reduce of at least 99.9 % the content of enteric viruses in said solid material.
82. The process of any one of claims 1 to 78, wherein said microorganisms comprise enteric viruses, and wherein said process permits to reduce of at least 99.99 % the content of enteric viruses in said solid material.
83. The process of any one of claims 1 to 78, wherein said microorganisms comprise enteric viruses, and wherein said process permits to reduce of at least 99.9999 % the content of enteric viruses in said solid material.
84. The process of any one of claims 1 to 83, wherein said microorganisms comprise helminths ova, and wherein said process permits to reduce of at least 70 % the content of helminths ova in said solid material.
85. The process of any one of claims 1 to 83, wherein said microorganisms comprise helminths ova, and wherein said process permits to reduce of at least 99 % the content of helminths ova in said solid material.
86. The process of any one of claims 1 to 83, wherein said microorganisms comprise helminths ova, and wherein said process permits to reduce of at least 99.9 % the content of helminths ova in said solid material.
87. The process of any one of claims 1 to 83, wherein said microorganisms comprise helminths ova, and wherein said process permits to reduce of at least 99.99 % the content of helminths ova in said solid material.
88. The process of any one of claims 1 to 83, wherein said microorganisms comprise helminths ova, and wherein said process permits to reduce of at least 99.999 % the content of helminths ova in said solid material.
89. The process of any one of claims 1 to 83, wherein said microorganisms comprise helminths ova, and wherein said process permits to reduce of at least 99.9999 % the content of helminths ova in said solid material.
90. The process of any one of claims 1 to 89, wherein said microorganisms comprise helminths ova, and wherein said process permits to eliminate helminths ova in said solid material.
91. The process of any one of claims 1 to 89, wherein said process permits to substantially reduce or eliminate the presence of microorganisms in said solid material.
92. The process of any one of claims 1 to 89, wherein said process permits to substantially destroy microorganisms in said solid material.
93. The process of anyone of claims 1 to 92, wherein an effluent is so produced and wherein said so-produced effluent substantially contains no microorganisms.
94. The process of any one of claims 1 to 92, wherein during said process the solid material is pasteurized.
95. The process of any one of claims 1 to 92, wherein during said process the solid material is heated at a temperature of at least 70 0C for a period of at least 30 minutes.
96. The process of claim 95, wherein said solid material is heated via the electric current.
97. The process of any one of claims 1 to 92, wherein during said process the solid material is heated, by means of said electric current, at a temperature of at least 70 0C for a period of time ti, and then, said solid material is maintained at a temperature of at least 70 0C during a period of time t.2, and wherein ti < 30 minutes; t2 ≤ 30 minutes; and ti + t2 > 30 minutes.
98. The process of claim 97, wherein ti < 30 minutes; t2 < 30 minutes; and U + 12 ≥ 30 minutes.
99. The process of any one of claims 1 to 98, wherein said solid material is sludge.
100. A process for at least partially deactivating microorganisms in a solid material, said process comprising submitting said solid material to an electric current having a voltage gradient of at least 0.5 volt per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating said current.
101. A process for at least partially deactivating microorganisms in a solid material and dewatering said solid material, said process comprising submitting said solid material to an electric current having a voltage gradient of at least 0.5 volt per centimeter of solid material to be treated, and a current density of at least 2 mA per cm2 with respect to the surface of electrodes used for generating said current density.
PCT/CA2007/001302 2004-08-02 2007-07-20 Processes for deactivating microorganisms in solid materials WO2008009137A1 (en)

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US5846425A (en) * 1994-07-22 1998-12-08 Whiteman; George R. Methods for treatment of waste streams
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US4758318A (en) * 1986-05-02 1988-07-19 Sankyo Yuki Kabushiki Kaisha Method for improvement of soil
US5326530A (en) * 1991-01-22 1994-07-05 Iit Research Institute Energy-efficient electromagnetic elimination of noxious biological organisms
US5846425A (en) * 1994-07-22 1998-12-08 Whiteman; George R. Methods for treatment of waste streams
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