UA96400C2 - Process for preparation of bio-masut - Google Patents

Abstract

The invention relates to the technology of preparation of ecologically clean composite fuels and can be used for preparation of water-masut emulsions. A process includes preparation of organic raw material: biosludge, technical phenol waters formed in the process of coke production, and oil product, dozing the components in a hopper of dozing mixer according to fuel preparation rules and preliminary dozed mixing biosludge and liquids, and further supply of the mixture into an emulsifier, where said substances are grinded and structurized into a fluid emulsion due to cavitation effect.

Claims (1)

( (б13) МПК Си СОЇ. 1/32 (2006.01) ХО ДЕРЖАВНА СЛУЖБА ІНТЕЛЕКТУАЛЬНОЇ ВЛАСНОСТІ (Ф) Пи С УКРАЇНИ ДО ПАТЕНТУ НА ВИНАХІД нЛляМШЛМНЛООВООНВЦ ТТ ЮІЕИКККІІИІІІІІОООТІТЬЬОООЬЬИЕІШШШШШШОЛІО.О ООЛІООИООВВОВООЛОВЛЛІЕИТОКОЛИЛОЬИХОХВОИСТЛООХХЬТТЬТЬИТНЬТЬТЬОСХХІХОТЛТИТТООХЗООТОВОООООВВЛОЛОВТИИОТОТИОТОИТНЯ» (54) СПОСІБ ОДЕРЖАННЯ БІОМАЗУТУ 1 2 (21) аго1015760 дальшою обробкою and production of bio fuel oil, which (22) 12.27.2010 differs in that organic raw materials are used as raw materials: biomul, technical phenolic (46) 10.25.2011, Byul.Mo 20, 2011 water, formed in the process of obtaining coke, and naphtha (72) TRETYAKOV VALERIY VALERIYOVYCH, TRO-product, and biomulch is poured into the hopper of the TsKO IHOR BORYSOVYCH mixer-dispenser, after which pre- (73) TRETYAKOV VALERIY VALERIYOVYCH, TROD , technical center IHOR BORISOVYCH of phenolic water and petroleum product, and then the mixture (56) OA 36738, I, 10.11.2008 is fed into an emulsifier, where it is crushed and stru- PA 76911, Sg, 09/15/2006 tour into a liquid emulsion using the phenomenon of ER 0545683, AT, 06/09/1993 cavitation. 05 5211723, A, 18.05.1993 2. The method according to claim 1, which differs in that the input and V.V. Klochai, S.N. Ivanchuk, I.D. Eliseev etc. The output of the emulsifier is regulated by a lock apparatus, and neutralization by phenol-formal - controlled valves, with the possibility of regu- dehydrogen and ammonia water./Coke and chemistry. Me10, drawing of watering of raw materials and its aggregate 2000. P.34-35 state, and control and management of the process is carried out by E.Yu. Andriyenko, A.V. Basteev, O.V. Kravchenko. use a biolubricant preparation management system etc. The method of fiery dephenolization of sewage water using a cavitation nozzle, after pre-coke chemical plants/coal chemical gurgling, the obtained bio-fuel oil is fed to the waste nal. Mo5-6, 2009. P.69-74 capacity. Ha (57) 1. The method of obtaining bio-fuel oil, which includes the preparation of raw materials, dosing of components from po- o, o The invention belongs to the technologies of obtaining environmentally friendly composite fuels with a pulsation device at the frequency of rotation of ro- (av) and can be tora Z 103-41 -10 min." (ав) used for the production of water-fuel oil emulsions (VME) and water-coal-fuel oil suspensions. However, this method has a number of disadvantages due to the limitation of the field of application. (Se) (VVMS), water- peat, water-biomud sums - The closest to the claimed invention, according to (is) shey the technical essence, purpose and result, which t- Many thermal power plants and thermoelectric- is achieved, is a method of obtaining liquid biofuel, may power plants in Ukraine are oriented to the use (KO Mo2385900, publ. 10.04.2010), which includes liquid fuels. Therefore, an urgent problem today is the preparation of raw materials, dosing of components from the energy industry, and the search for new alternative ones, with further processing and production of fuel. Heated energy sources that could partially weaken the prepared raw materials lead to an energy deficit at the temperature. 55-60 "C with subsequent separation of moisture and domi- - This problem is partially solved by the known method of shock, and the processing of the prepared raw materials would be carried out by obtaining a fuel composition (SHA Mo 36738, M, in a reaction boiler by means of a simultaneous reaction with publ. 11.10.2008, Bull. Me21, 2008), which includes esterification and transesterification during mixing and cavitation treatment of a mixture of crushed raw materials with alcohol in the ratio (5:1)-(7:1), of fuel, water-containing liquid and heavy carbon respectively, and the addition of heterogeneous acidic days. In this method, the catalyst is pre-mixed in the amount of 5-10 95 wt., while crushed solid fuel with water-containing liquid, the process is carried out at a temperature of 120-150 "C, and the obtained suspension together with heavy hydrocarbons - hum 60-120 min. with turbulent mixing, they are subjected to dispersion in a rotor at 1200-1500 revolutions per minute and atmospheric pressure. The disadvantage of this known method is the composi- In fig. 1. the graph of the dependence of the speed and energy consumption of the method due to the necessity of the flow of the gas mixture in the mixing chamber and the presence of a complex energy-consuming cavitation nozzle on the air pressure at the inlet is shown; for heating the prepared raw materials and fig. 2 - the dependence of the average diameter of the drops in the subsequent separation of moisture and impurities, as well as the sprayed jet, on the average speed for processing the prepared raw materials in the reactive gas-water mixture in the mixing chamber of the boiler nozzle. In addition, to implement the method, cavitation is necessary; in fig. C - the dependence of the average diameter - the performance of additional operations of moisture extraction, the collection of droplets of the atomized jet of the nozzle, cavitation, settling and separation of components, distillation. alcohol, etc. The method is implemented as follows. Another disadvantage of the method is the limitation. First, organic raw materials are poured into the bin due to the use of expensive mixer-dispenser heads, after which components such as alcohol, glycerin, catalyst, pre-dosed mixing of biomulch and liquid are carried out - as well as vegetable raw materials of oily cultures technical phenol waters formed in the process. The invention is based on the task of producing coke and petroleum products. Further, the implementation of mixing and reduction of energy intensity will fall into the emulsifier for grinding and structuring, as well as the task of expanding the field of application of the substance into a liquid emulsion using the method. cavitation phenomena. The task is solved by the fact that the input and output of the emulsifier are regulated by a lock system. Biofuel production includes preparation of raw material (controlled valves) with the possibility of reflow, dosing of components with further processing of raw material watering and its aggregate, and obtaining fuel. According to the invention, the state, and the control and management are carried out by sys- as raw materials use organic raw materials: the topic of managing the preparation of fuel from biomul, technical phenolic waters, formed in the process using a cavitation nozzle. Prepared production of coke and petroleum products. the fuel suspension is fed into the consumption container. In one of the options for the implementation of the method, organic raw materials are poured into the hopper of the fuel mixer based on a water-biosludge emulsion. On the compositor, after which a preliminary dose-positive product is analyzed for the quality of mixing bioslurry and liquid - oil product according to organic compounds similar to the components of the regulations for fuel preparation, and then a mixture of oil products. are fed into the emulsifier, where they are crushed and structur- Based on the results of numerical and physical ruminating the substance into a liquid emulsion with the help of modeling, a technique for calculating the phenomenon of cavitation has been developed. of the flow part of the cavitation nozzle depending on In another variant of the invention, the input and output properties of the liquid and thermodynamic parameters of the emulsifier are regulated by the locking device at the input to the spraying device. In fig. 1-3 controlled valves, with the ability to adjust the dependence of the spraying parameters on the hydration of the raw material and its aggregate state, as well as on the pressure and flow rates. control and management is carried out by the system. The prepared fuel composition can serve as management of the preparation of fuel for use in boilers, replacing fuel oil, and cavitation nozzles, after which the fuel suspension can also be a raw material ("artificial oil") for friction. into the consumable capacity. motor fuels. The invention solves the task of simplifying the effect of the application of VME in that water (to the method and reducing its energy intensity thanks to 30 95) in such fuel compositions is not a ballast - the use of organic raw materials - biomud, which volume, but a kind of catalyst that improves and fills in hopper mixer-dispenser, after which accelerates the process of combustion of the hydrocarbon base. which pre-dosed mixing is carried out. The presence of bound water in such fuels contributes to biomud and liquid, according to the preparation regulations, to more complete combustion of hydrocarbons with less fuel. Next, the mixture is fed into the emulsifier, where air is supplied. The amount of soot (less smoke), nitrogen oxides, and I am sowing Thus, it is possible to obtain various compotes and sulfur, benzopyrene, etc. The ecological situation of long-lived liquid environments is improving significantly. have new properties. When preparing suspensions, the use of VME allows to increase eco- or emulsions in the device, powerful nomic power plants arise, first of all, due to wave fields (shock waves, cavitation, etc.), which, in order to reduce chemical and mechanical misfires, affect sorption processes, coagulation, chemistry, as well as reduction of pollution, working reactions and mechanical interaction of substances. heating surfaces in boiler units. The task of expanding the field of application of fine-dispersed droplets in fuel emulsions is achieved in the method thanks to the use of local water (up to 5 microns) evenly distributed in hydrocarbon raw materials of organic origin (waste in the new phase (inverse emulsion - "B-m-" water in mass as a liquid phase (carrier) in the liquid phase). During the combustion of reverse emulsions, water in the drops of composite fuels are used technical microexplosives. fuel preparation (various liquid coal fuels. At the same time, the torch increases in volume and water oil refining). fills the combustion chamber more densely. A significant increase in the area of contact of fuel with air causes