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  • About us Chronology

    Chronology of main stages of development of electrochemical activation technology and electrochemical systems

    Description of technologies of application of electrochemical activation and technical electrochemical systems are accessible only for the registered companies.

    List of selected publications till 2000.

    Date/place Stages of development of electrochemical activation techniques and technology
    1972
    Tashkent
    The beginning of studies of electrochemical methods of water and drilling mud properties regulation.
    1975
    Tashkent
    Discovery of effect of water metastability under unipolar electrochemical influence. («Method of physical-chemical properties regulation»)
    1977
    Tashkent
    Introduction of term "Electrochemical activation" (ECA).
    1978
    Tashkent
    Development of first industrial-scale devices for electrochemical regulation of water and drilling mud properties. Electrochemical reactors with plate steel electrodes parted with chlorine diaphragm.
    1978
    Tashkent
    Discovery of phenomenon of anomalous change of oxidation-reduction potential (ORP) as a result of unipolar electrochemical water treatment and investigation of mechanism of ORP relaxation after stopping of electrochemical influence.
    1979
    Tashkent
    Organization of serial production of devices UOBR-1 for electrochemical treatment of drilling mud and devices UEV-4 for electrochemical activation of water.
    1979
    Tashkent
    Investigation of biological influence of electrochemically activated water and solutions.
    1979
    Tashkent
    Development of the second generation of industrial devices for electrochemical activation of liquids. Electrochemical reactors with cylindrical coaxial electrodes separated by a chlorine diaphragm on the frame.
    1979
    Ташкент
    Organization of serial production of devices UOBR-1M for electrochemical treatment of drilling mud and devices UEV-6 of electrochemical activation of water.
    1980
    Kazan
    Studies of the use of ECA in the petrochemical industry (basic organic synthesis technology).
    1981
    Zagorsk (Sergiev Posad)
    Investigation of ECA application in industrial poultry farming.
    1981
    Sukhumi
    Investigations of ECA application in subtropical economy.
    1981
    Kazan
    Investigations of ECA application in technology of circuit board manufacture and metallization of dielectrics.
    1982
    Moscow
    Investigation of ECA application in food industry.
    1982
    Kazan
    Investigation of ECA application in water treatment industry.
    1982
    Tashkent
    Development of the third generation of devices for electrochemical activation of liquids. Electrochemical reactors with coaxial cylindrical electrodes parted by a ceramic diaphragm.
    1983
    Leningrad (Saint Petersburg)
    Investigation of ECA application in special (defense industry) fields of technique and technology.
    1983
    Moscow
    Investigation of ECA application in cattle breeding, veterinary medicine, beekeeping, fish-breeding, seafoods production.
    1983
    Tashkent
    Investigation of ECA application in plant growing, fodder production, farming.
    1985
    Kazan
    Defense by V.M. Bakhir of the candidate's thesis on the subject 'Regulation of physical and chemical properties of technological aqueous solutions by unipolar electrochemical exposure, and experience of its practical application'
    1985
    Kazan
    Official acknowledgment of the technology of electrochemical activation as the new scientific and technical direction by the Higher certifying commission of the USSR (stated in the Minutes of the Meeting of specialized council at the Defense of V.M. Bakhir of the candidate’s thesis for competition of the degree of Candidate of Technical Science).

     

    1985
    Tashkent
    Development of the forth generation of devices for electrochemical activation of liquids. Electrochemical reactors with several ceramic diaphragms and anodes.
    1986
    Tashkent
    Organization of serial production of universal multi-purpose devices ELCHA-003 for electrochemical activation of water.
    1987
    Moscow
    Development of technology of noncontact electrochemical activation.
    1988
    Moscow
    Introduction of name “STEL” for devices of anolyte production.
    1988
    Moscow
    Development of the fifth generation of devices REDOX, STEL and EMERLD for electrochemical activation of liquids. Development of new generation of electrochemical reactors RPE based on flow-through electrochemical modular elements FEM-1.
    1990
    Moscow
    Organization of serial production of STEL devices for synthesis of detergent, disinfecting and sterilizing solutions, devices EMERALD with electrochemical reactors RPE of FEM-1 elements for drinking water purification.
    1991
    Moscow
    Development of flow-through electrochemical modular elements of the second generation (FEM-2).
    1992
    Moscow
    Organization of serial production of STEL devices for synthesis of detergent, disinfecting and sterilizing solutions, devices EMERALD with electrochemical reactors RPE of FEM-2 elements for drinking water purification.
    1993
    Moscow
    Investigation of ECA application in technology of pharmaceutical plates and dishes cleaning.
    1993
    Moscow
    Development of basic principal of design of devices for electrochemical activation of liquids.
    1994
    Moscow
    Investigation of ECA application in technology of destruction of organic substances in closed space (space ship, submarine), for hands disinfection for surgeons.
    1994
    Moscow
    Development of flow-through electrochemical modular elements of the third generation (FEM-3).
    1995
    Moscow
    Organization of serial production of FEM-3 elements and devices based on it, including new generation of STEL devices for synthesis of detergent, disinfecting and sterilizing solutions – anolytes, devices EMERALD for drinking water treatment.
    1995
    Moscow
    Investigation of ECA application in technology of water disinfection for swimming pools, water treatment stations, cooling towers, for treatment of various diseases (dermathology, general surgery, nephrology, urology, proctology, gastroenterology, etc.)
    1996
    Moscow
    Defense of thesis for a Doctor’s degree on the subject “Medical-technical systems and technologies for synthesis of electrochemically activated sterilizing, disinfecting and detergent solutions”.
    1996
    Moscow
    Development of technology of electrochemical synthesis of gaseous oxidants (chlorine, dioxide chlorine, ozone) realized in AQUACHLOR devices with technology of ion-selective electrolysis with diaphragm.
    1996
    Moscow
    Development of technology of endoscope cleaning and disinfection using ECA solutions.
    1996
    Moscow
    Development of technology of disinfecting solution production from sweet water without salt addition (AQUADEZ devices).
    1996
    Moscow
    Development of technology of high concentrated (till 10 %) hypochlorous solutions production with current efficiency to 97 % in HYPOCHLOR devices.
    1996
    Moscow
    Development and organization of serial production of STEL devices of high productivity (to 2500 l/h).
    1996
    Moscow
    Organization of serial production of AQUACHLOR devices of productivity from 100 to 1000 g/h of gaseous chlorine.
    1996
    Moscow
    Development of ENDOSTERIL devices for cleaning and sterilizing of endoscopes, organization of serial production.
    1996
    Moscow
    Development of technology of cleaning and disinfecting solution of AND type.
    1997
    Moscow
    Development of electrochemical modular elements FEM-4 of the fourth generation.
    1997
    Moscow
    Development of electrochemical reactors RPE-F.
    1997
    Moscow
    Development of electrochemical reactors RPE-S.
    1998
    Moscow
    Development of technology of aerosol disinfection – anolyte use in the form of fog.
    2001
    Moscow
    Development of FEM-7 reactors for ion-selective electrolysis with diaphragm, organization of serial production of FEM-7 reactors and AQUACHLOR devices.
    2004
    Moscow
    Development of technology of water treatment and disinfection in swimming pools realized in ALLIGATOR devices.
    2004
    Moscow
    Development of technology of Anolyte ANK production with low mineralization (less than 1,5 g/l) and high oxidants concentration (till 700 mg/l).
    2004
    Moscow
    Development of technology of increase in 1000 – 10000 times of antimicrobial activity of Anolyte ANK with high oxidants concentration.
    2004
    Moscow
    Development of FEM-9 reactors for ion-selective electrolysis with diaphragm.
    2005
    Moscow
    Development of technology of synthesis of peroxocarbonate cleaning, disinfecting and sterilizing solution Anolyte PEROX.
    2006
    Moscow
    Receipt of pharmaceutical article for Anolyte ANK as a remedy for local and external use for treatment of injured and uninjured mucous and skin.
    2007
    Moscow
    Development of STEL-ANK-PRO devices for production of Anolyte ANK of second generation with mineralization no more than 1,5 g/l/ and oxidants concentration no less than 500 mg/l; devices can work in continuous regime for a long time till several weeks.
    2009
    Moscow
    Development of flow-through electrochemical modular universal elements – Bakhir Modules MB-11.
    2009
    Moscow
    Development of flow-through electrochemical modular universal elements – Bakhir Modules MB-26.
    2010
    Moscow
    Development of technology of synthesis of anolyte of the third generation – with mineralization less than 1 g/l and oxidants concentration more than 500 mg/l in STEL-ANK-SUPER devices with salt level conversion 99,9 %.
    2011
    Moscow
    Development of automated device AQUACHLOR-500M with use of new type MB reactors with function of reduced 1,5 time salt consumption and self-cleaning function, which allows to refuse acid cleaning of reactor.
    2012
    Moscow
    Development of generation of flow-through self-cleaning case (in dielectric case) electrochemical module elements – Bakhir Modules MB-10, MB-20, MB-30, MB-40, MB-50, MB-100, MB-500, MB-1000 – for electrochemical treatment both aqueous and nonaqueous electrolyte solutions of any possible concentration including some models for work at increased pressure (up to 20 krc/cm2sup>) and temperature (till 120 ?С). The model number characterizes the average operating value of current strength in ampere.
    2012
    Moscow
    Development of ECOCHLOR devices for chlorine production in industrial scale.
    2014
    Moscow
    Development of production technology of environmentally friendly electrochemically synthesized cleaning solutions based on percitric acid and solutions of alkyltrimethylammonium hydroxide.
    2015
    Moscow
    Development of next generation of flow-through electrochemical modular MB elements with high volumetric current density with different performance.
    2016
    Moscow
    Organization of serial production of flow-through electrochemical modular MB elements with high volumetric current density at the enterprises of innovative industrial cluster ROSELECTROKHIMINDUSTRIYA.
    2017
    Moscow
    Organization of serial production of devices with the collective name AQUATRON for electrochemical conversion of water and aqueous solutions at the enterprises of innovative industrial cluster ROSELECTROKHIMINDUSTRIYA.