UA57255U - Process for preparation of bio fuel oil - Google Patents

Abstract

A process for preparation of bio fuel oil, where organic raw material (bio mud) and technical (phenolic) water, formed during production of coke, are used as raw material.

Claims (2)

And | (b1) IPC (2011.01) How many! 8/00 ХО МІНІСТЕРСТВО ОСВІТИ й І НАУКИ УКРАЇНИ Ф. П И (Фе відповідал сть ЕРЖАВНИЙ ДЕПАРТАМЕНТ власний й ІНТЕЛЕКТУАЛЬНОЇ до ПАТЕНТУ патенту ВЛАСНОСТІ НА КОРИСНУ МОДЕЛЬ нЛляМШЛМНЛООВООНВЦ ТТ ЮІЕИКККІІИІІІІІОООТІТЬЬОООЬЬИЕІШШШШШШОЛІО.О ООЛІООИООВВОВООЛОВЛЛІЕИТОКОЛИЛОЬИХОХВОИСТЛООХХЬТТЬТЬИТНЬТЬТЬОСХХІХОТЛТИТТООХЗООТОВОООООВВЛОЛОВТИИОТОТИОТОИТНЯ» (54) СПОСІБ ОТРИМАННЯ БІОМАЗУТУ 1 2 (21) иго1015762 дозатора , after which a preliminary dose- (22) 12.27.2010 mixing of bioslurry and liquid (petroleum product according to (24) 10.02.2011 fuel preparation regulations) is carried out, and then the mixture (46) 10.02.2011, Byul.Mo 3, 2011 fed into an emulsifier, where the structuring and (72) TRETYAKOV VALERIY VALERIYOVYCH, TRO- substance into a liquid emulsion with the help of TsKO IHOR BORYSOVYCH cavitation phenomenon. differs in that TsKO IHOR BORISOVYCH the input and output of the emulsifier are regulated by a locking device ovated valves) with the possibility of regulating the preparation of raw materials, dosing of components from the watering of raw materials and its aggregate further processing and obtaining fuel, which is also controlled and managed by the system differs in that how raw materials are used, management of fuel preparation organic raw materials (biomulch) and technical (phenolic) cavitation nozzles are used, after which the fuel suspension is water formed in the process of obtaining coke. feed is fed into the consumable container. 2. The method according to claim 2, which differs in that organic raw materials are poured into the hopper of the mixer. The useful model refers to technologies, the result achieved is a method of obtaining "32 environmentally friendly composite fuels and liquid biofuels (Patent RF Me2385900, publ. . o can be used for the production of water- 10.04.2010), which includes the preparation of raw materials, - fuel oil emulsions (VME) and water-coal-fuel oil dosing of components with further processing and suspensions (VUMO), water-peat, water- obtaining fuel. The heating of the prepared raw bio-sludge mixtures is carried out at a temperature of 55-607C with subsequent IR F. Many thermal power plants and thermoelectric power plants separate moisture and impurities, and the processing of the prepared IR power plants in Ukraine is focused on the use of cast raw materials is carried out in a reaction cauldron of liquid fuel. Therefore, the search for new alternative re-esterification in the mixture of conversion of raw materials with alcohol into IR sources of energy, which could partially weaken the ratios of 5:1-7:1, respectively, and by adding t energy deficit. of a heterogeneous acid catalyst in the amount of Mai Dan, the problem is partially solved by the well-known method 5-1095 to the mass, while the process is carried out under the conditions of obtaining a fuel composition (Ukraine Patent at temperature 120-1507C for 60-120 min. with turbulence, a useful model Me36738 , published on November 10, 2008, with belt mixing at 1200-1500 revolutions in Bul. Me21, 2008), which includes cavitation volume and atmospheric pressure. making a mixture of crushed solid fuel, water, and heavy hydrocarbons. In this case, the efficiency and energy-intensiveness of the method is due to the fact that the ground solid fuel is pre-mixed with a water-containing liquid in the presence of complex energy-intensive equipment, and the resulting suspension is used for heating the prepared raw materials and the mixture with heavy hydrocarbons is subjected to dispersion for further separation moisture and impurities, as well as bathing in the rotor-pulsation apparatus during the treatment of the prepared raw materials in the reaction time of the rotation of the rotor 3-102-1-107 waves." (due to the performance of additional operations to separate it - the limitation of the field of application). logs, sedimentation and separation of components, distillation. Another shortcoming of the method is the limited use of pre-dosed mixing of bioslurry and liquid due to the use of expensive (petroleum product according to the regulations for the preparation of fuel components, such as alcohol, glycerin, catalyst, lye). Next, the mixture is fed into an emulsifier for sub- and vegetable raw materials of oil crops. grinding and structuring of a substance into a liquid emul- The basis of a useful model is the task of using the phenomenon of cavitation. simplification of implementation and reduction of energy consumption. The input and output of the emulsifier are regulated by the lock of the method, as well as the task of expanding the area behind the equipment (controlled valves) with the possibility of adjusting the method. watering of the raw material and its aggregating. The task is solved by the fact that the control and management of the biodiesel production system includes the preparation of the raw material, the control of fuel preparation from the wine, dosing of components with further processing, and the use of a cavitation nozzle. Prepared koya and obtaining fuel. According to the useful fuel suspension is fed into the expendable container. models that use organic The work carried out on the production of composite raw materials (biosludge) and technical (phenolic) water, as a raw material for fuel based on a water-biosludge emulsion. On rhenium in the process of obtaining coke. composite product obtained analysis of qualitative In one of the variants of implementation of the method of organic composition of organic compounds, similar component raw materials are poured into the bunker by mixers of petroleum products. dispenser, after which a preliminary dosing is carried out. In the basis of the processes of activation of hydrodynamic non-mixing of biomud and liquid (petroleum product under the flow of liquid in the claimed method, the regulations for fuel preparation), and then the mixture does not cause cavitation. are fed into the emulsifier, where they are crushed and structured. Based on the results of numerical and physical ruminating the substance into a liquid emulsion with the help of modeling, a method of calculating the cavitation phenomenon has been developed. of the flow part of the cavitation nozzle depending on In another variant of the useful model, the input and properties of the liquid and the thermodynamic parame- output of the emulsifier are regulated by the lock apparatus at the entrance to the spraying device. Fig. 1-3 shows the dependence of the parameters of spraying and dewatering of the raw material and its state of aggregation, as well as on the pressure and flow velocities. control and management is carried out by the system. The prepared fuel composition can serve as management of the preparation of fuel from use for burning in boilers, replacing fuel oil and cavitation nozzles, after which the fuel suspension can also be a raw material ("artificial oil") for atrising. into the consumable capacity. consumption of motor fuels. A useful model solves the problem of simplifying the effect of the application of VME in the fact that water (providing the method and reducing its energy intensity) in such fuel compositions is not ballast, thanks to the use of organic raw materials (biomass) but a kind of catalyst that improves and - la), which is poured into the hopper of the mixer-dispenser, controls the combustion process of the hydrocarbon base. After that, pre-dosed miscibility of the bound water in such fuels contributes to the increase of biomud and liquid (petroleum product under the regulation of hydrocarbon combustion with a lower consumption of fuel preparation). Then the mixture is fed into the air. In the products of combustion, the emulsifier is significantly reduced, where the amount of soot (less smoke), nitrogen and sulfur oxides, wine is crushed and structured into a liquid emulsion. Thus, it is possible to benzopyrene, etc. The ecological situation is significantly improving to obtain different compositions of liquid media. that are long-lived and have new properties. With the use of VME, it is possible to increase the eco-preparation of suspensions or emulsions in the device nomic power plants, first of all, powerful wave fields arise (shock waves, reduction of chemical and mechanical under-paluvitation, etc.), which affect the sorption pro - contamination, as well as reduction of contamination of working processes, coagulation, chemical reactions and mechanical interaction of heating surfaces in boiler units. fashion of substances. In fuel emulsions, finely dispersed droplets of water (up to 5 micron) are evenly distributed in the hydrocarbon emulsion, which is achieved in the method by using a local phase (inverse emulsion - "In-m--water in mass raw materials of organic origin ( waste li"). During the burning of reverse emulsions, water in the drops of biomud of sewage treatment plants). As a liquid phase (carrier) in a subject to a microexplosion. As a result of this, water is used in decomposite fuels, ultra-fine atomization of hydrocarbons (drifts) and various liquid hydrocarbons, oil refining fuels. At the same time, the torch increases in volume and Ky. more densely fills the combustion chamber. A significant increase is shown in Fig. 1 as a graph of the dependence of the acceleration of the area of contact of fuel with air as a result of the flow of the gas mixture in the mixing chamber before the increase of the radiation surface and the cavitation nozzle on the air pressure at the inlet; on the increase in intensity of radiation of the torch Fig. 2 - the dependence of the average droplet diameter on 11-1295, while the share of heat absorbed by the atomized jet from the average speed of the furnace increases by 7-1095, and the efficiency of the cauldron of the gas-water mixture in the nozzle mixing chamber increases by 3-495. cavitation; in Fig. 3 - the dependence of the average diameter. The degree of hydrocarbon burnout can reach drops of the atomized jet of the cavitation nozzle. 99,595. At the same time, saving hydrocarbon fuel The method is implemented as follows. due to the introduction of water and improvement of the processes. First, organic raw materials are poured into the fuel burn-up can be from 5 to 2595.