STEL devices: history and new horizons
Name of STEL devices for synthesis of electrochemically activated antimicrobial and detergent solutions first appeared in 1989. This name is a combination of two words: STerility and Electrochemistry. This name united all types of electrochemical devices producing detergent disinfectant and sterilizing electrochemically activated solutions (ECA solutions) and containing electrochemical reactor consisting of flow-through electrochemical modular elements FEM-3. Due to particular qualities of design FEM-3 element has no alternative in the technology of ECA solutionsÒ production. It is in this reactor only that it is possible to create conditions for simultaneous synthesis of chlorine-oxygen and hydroperoxide oxidants of the higher oxidation rates. In this reactor only it is possible to provide conditions for forming in double electric layer at the surface of anode of solid electrically structured ion-hydrated membranes, surrounding freshly formed oxidants and preventing them from the following rapid reciprocal (mutual) neutralization. In this reactor only it is possible to force hydrogen dissolved in catholyte to participate in the anodic reactions of synthesis of the oxidants. The simplest technology of water treatment in flow through diaphragm reactors consists in simultaneous synthesis of approximately equal volumes of catholyte and anolyte Ö that is, of water or solution exposed to cathodic or anodic treatment, respectively. Perfection of the reactor in this technology manifests itself in the opportunity to obtain maximum possible values of anolyteÒs oxidation-reduction potential (ORP) with its pH value being minimal, at that power inputs is minimal, output capacity maximum possible and initial solution or water mineralization minimal possible; as well as to obtain minimum possible ORP-values for catholyte with its pH value being maximal. That were these very conditions that were formerly considered to be the key conditions for ÓlivingÔ and ÓdeadÔ water generation, but in many cases they were achieved at the expense of increased water mineralization level and prolonged time of electrochemical water treatment. As a matter of fact, for obtaining electrochemically activated water Ö that may be called ÓlivingÔ and ÓdeadÔ Ö it is necessary to ensure that each micro-volume of water being treated gets in touch with the surface of the respective not dissolved in water electrode, provided that water temperature changes are minimal (1 Ö 2 degrees), water mineralization is minimal possible usually not exceeding the level of salts content in usual drinking water, and within minimal period of time usually countable in whole seconds or split seconds. It is obvious that the major part of apparatuses for ÓlivingÔ and ÓdeadÔ water generation manufactured in the early eighties, as well as of apparatuses of the similar destination being manufactured at present time, didnÒt correspond and still do not correspond to these principals, as far as this area of electro-chemistry hasnÒt ever been described in respective text-books and represents an independently developing scientific archipelago. Generation of disinfectant solution Ö that is, of acidic anolyte in STEL devices doesnÒt represent any difficulties as regards to technical aspects; however, it is not expedient for the reason of its high corrosiveness level and strong smell of chlorine. It is possible to avoid the strong chlorine smell only in case if usual drinking water with no salt additives is used as an initial solution; however, anolyte obtained of sweet water does not possess sufficiently effective antimicrobial properties so as to be used in PCDPI (LPU) (patient care and disease-prevention institution) as a disinfectant. At the present time, STEL-AK devices for production of electrochemically activated anolyte and catholyte from sweet or distilled water having output capacity equal to 5 to 1000 litres\hour are manufactured in ÓNPO ÓEkranÔ (Scientific-and-production association ÓEkranÔ, JSC). Such electro-chemically activated solutions are applied in various technological processes implemented in agriculture, industry , including food processing, as well as in medicine for the purpose of oxidation-reduction potential regulation in the human beingsÒ organisms. ANOLYTE ÖANneutral anolyte Employees of health care institutions performing practical tasks had a need for solution which would have a neutral pH value. For the first time such an anolyte was obtained in STEL-MT-1 device, the serial production of which was started in NPO ÓEkranÔ in the year of 1990. This anolyte was given the name of a neutral anolyte, shortly ÓAnolyte ANÔ, in contrast to formerly known acidic anolyte with the pH value being lower than 5, and at the same time the latter anolyte was given the name of ÓAnolyte AÔ. Anolyte AN is produced by way of anodic treatment only of the initial sodium chloride solution carried out in RPE-reactor represented by a single or by several FEM-elements. The pH value correction within the anodic treatment is performed by adjustment of the current share transferred by hydroxyl ions from cathodic chamber to anodic chamber, with sodium hydroxide concentration in cathodic chamber being maintained at increased level. Anolyte AN proved to be a more strong antimicrobial solution than acidic anolyte. Moreover, in contrast to Anolyte A and due to particular qualities of the technology, it possesses detergent properties, as well. However, Anolyte A is characterized by high corrosiveness which is nearly the same as that of Anolyte A, but, in contrast to Anolyte A, it has less pungent smell of chlorine. ANOLYTE ANK Ö neutral anolyteobtained using catholyte The further improvement of Anolyte AN properties has resulted in significant changes in the technology of electrochemical synthesis and permitted to create a neutral anolyte of the new type in the year of 1995; this anolyte was given the ÓAnolyte ANKÔ reference name, which means Óneutral anolyte obtained using catholyteÔ. Heavy metals ions removal from the initial sodium chloride solution, dissolved hydrogen properties utilization in oxidants mixture, as well as the technology of correction of the pH value of acidic anolyte solution are considered to be the most important aspects of the Anolyte ANK production technology. As multiple experimental researches and wide experience of many years' practical application have shown, Anolyte ANK proved to be the solution which was the best to correspond with the needs of medicine: it possesses wide and universal spectrum of action, it is not toxic, it doesnÒt create toxic background after desiccation, it doesnÒt permit microorganisms to acquire resistance, and it has lower corroding ability than Anolyte AN. Different hydraulic schemes can be applied for Anolyte ANK production. The most simple among them was used in all of the STEL devices that were manufactured before the year of 2006. In accordance with this scheme, the main point of Anolyte ANK synthesis consists in the whole initial solution volume supply to cathodic chamber of RPE-reactor consisting of FEM-3 elements, where catholyte, during the flowing process, is enriched with metals cations (mainly with sodium cations) coming from anodic chamber, and where heavy metals ions transform into insoluble hydroxides as a result of the medium pH value increase, as well. After that, hydrogen bubbles with the particles of insoluble hydroxides stuck to them and a certain quantity of catholyte are eliminated from the aggregate solution volume available in flotation reactor. Catholyte purified in such a manner is supplied to anodic chamber of the same reactor. As a rule, the pH value of Anolyte ANK to be selected shall lie within the limits of 6,5 to 7,5 and is adjusted with the help of catholyte volume discharged into drainage from flotation reactor. However, this scheme, as well as Anolyte ANK generated with its help, is not free from disadvantages. When anolyte is produced in accordance with this scheme, salt conversion factor doesnÒt exceed 13%, on the average, the latter fact results in necessity to retain the sodium chloride concentration in the initial solution at the level of not less than 5 grams/litre, in case the concentration of oxidants synthesized in Anolyte ANK lies within the limits of 500 Ö 600 milligrams/litre. When smooth shining surfaces are processed such an anolyte leaves the salt traces after its desiccation, with the latter fact calling forth the necessity of rinsing. Sporicidal activity retention cycle of Anolyte ANK doesnÒt exceed 5 days, the latter feature being conditioned on incomplete heavy metals ions elimination from the initial solution. This scheme doesnÒt permit to create technical electrochemical systems destined for long-term commercial operation (with the exception of medicine), as far as it is not able to provide favourable conditions for long-term service of FEM-elements anodic coating, in principle. Within the period covering the years of 2000-2001 both the advantages and the accumulated problems of the technology and technique of Anolyte ANK production and practical application were revealed and studied. The main advantages of Anolyte ANK are as follows:
There should be the following facts revealed within the period covering the years of 2000 Ö 2001 referred to disadvantages and problems of the technology and technique of electrochemically activated Anolyte ANK production and practical application in PCDPI. Anolyte ANK possesses corrosiveness and is not recommended for cleansing of instruments manufactured of alloys which do not possess corrosion-resistance properties. The effectiveness of objects disinfection with Anolyte ANK considerably decreases in the albuminous contaminating agents presence. After its desiccation Anolyte ANK leaves the salt traces on smooth shining surfaces of objects. The companies which which illegally manufacture and distribute STEL devices and are also involved in counterfeit FEM-elements manufacturing have caused ideological harm to original electrochemical activation technology and actual damage to customers. Within the years of 2001 Ö 2005 the main Anolyte ANK disadvantages were successfully surmounted through the efforts of the group of specialists representing Electrochemical Medical Equipment Department of ÓNPO ÓEkranÔ, JSC, ÓVitold Bakhir Electrochemical Systems and Technologies InstituteÔ, American company ÓElectrochemical Technologies, Ltd.Ô: c.t.s (candidate of technical science) S.A. Panicheva, c.m.n (candidate of medical science) V.I. Prilutsky, c.t.s. (candidate of technical science) N.Yu. Shomovskaya.
The table given below represents the characteristics of new electrochemically activated solutions compared with that of existing chemical reagents solutions and of Anolyte ANK produced in STEL-10N-120-01 device. Comparative characteristics of chemically stable and electrochemically activated disinfectant solutions.
Examination of infringing products (STEL devices, counterfeited electrochemical reactors manufactured by such Anglo-American company as ÓSTERILOXÔ that presently changed itÒs name for ÓPuricoreÔ, or Russian company ÓEmeraldÔ (NPP ÓIzumrudÔ) located in Saint-Petersburg, for instance) which appear in the Russian market and abroad has shown that neither of the counterfeited electrochemical reactors permit to ensure that chlorine-oxygen and hydroperoxide compounds are generated in the Anolyte ANK synthesis scheme in proportions necessary for imparting of the required antimicrobial activity parameters to Anolyte ANK and does not permit to provide the conditions ensuring long-term simultaneous presence of chlorine-oxygen and hydroperoxide compounds in Anolyte ANK, as well. As a rule, the counterfeit STEL devices are equipped with either unoriginal reactors or with reactors consisting of standard FEM-3 elements manufactured by their only legal manufacturer all over the world Ö the Russian company ÓLaboratory of ElectrotechnologyÔ (ÓLETÔ, LLC), Ö with their quantity still being much less than the quantity required for achieving of the device output capacity stated in the respective documentation. There are multiple violations of Anolyte ANK production equipment, of its generation technology and of its practical application methods committed by different companies which are not the authorised representatives of the authors. In order to give the STEL devices consumers Ö that is, the responsible employees of PCDPI, Ö an opportunity not to expose to risk the health of those people who have entrusted themselves to them as their patients there has been developed a system of the AUTHORÒS INFORMATION provision to interested persons and organisations (www.vbinstitute.org), the abovementioned authorÒs information covers all problems of electrochemical technique and technology. This system has been created on the basis of information database provided by the group of enterprises considered to be the leaders in the sphere of electrochemical systems and technologies of electrochemically activated solutions production and application and includes databases of the group of enterprises authorised by the authors - owners of the main patents issued in the described area; the latter fact permits to provide the customers with reliable information and high-quality products on their demands. For more information please see: |
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> Devices STEL electrochemical devices STEL devices: history and new horizons |
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