


Vol 53, No 2 (2019)
- Year: 2019
- Articles: 17
- URL: https://bakhtiniada.ru/0040-5795/issue/view/10541
Article
Distribution of Heavy Hydrogen and Oxygen Isotopes in Water Distillation
Abstract
The possibility of high-precision determination of mass transfer characteristics of stainless steel packings in the separation of hydrogen and oxygen isotopes by vacuum distillation of water in columns with a diameter of 60–250 mm was shown. An algorithm for calculating the parameters of separation and the concentration profile of deuterium and oxygen-18 during their simultaneous separation in a closed type unit with product selection by vacuum distillation of water was presented.



Liquid–Liquid Equilibrium in an Extraction System Based on Polyvinylpyrrolidone-3500 and Sodium Nitrate
Abstract
Liquid–liquid phase equilibrium for a new extraction system based on polyvinylpyrrolidone-3500 and sodium nitrate at 298.15, 313.15, and 333.15 K has been studied. Binodal data and phase diagrams with liquid–liquid tie lines have been presented. Mathematical modeling of phase equilibrium in the given system has been performed. New parameters for the UNIQUAC equation have been selected. The UNIQUAC model can be successfully used to describe phase equilibrium in the system. The results of this study can be used in the development of new extraction processes for the recovery of organic compounds.



Application of Thermodynamic-Topological Analysis in the Design of Biorefineries: Development of a Design Strategy
Abstract
Biorefineries have been widely studied during the last years and proposed as the best option to transform biomass systems into value-added products. Different methodologies have been proposed for the design of biorefineries: knowledge-based approach, early-stage approach, and superstructures, among others, which have been coupled to process improvement schemes as pinch analysis and process intensification. Regarding process design, it is necessary to ensure that the most advanced concepts are applied on the design to ensure efficient processes that direct to more sustainable processes. The processes that are currently being designed as biorefineries in many cases cannot be considered as completely efficient, because they are generally biased to designs based only in typical methods of process engineering. It is still necessary to implement further design strategies focused on increasing the efficiency and decreasing energy consumption. Multiple methods have been used for the design and improvement of chemical/biotechnological processes. Among these, shortcut methods, especially thermodynamic-topological analysis, are highlighted as a useful tool in the process engineering stage of a given process and might be useful to decrease energy consumption and to increase the efficiency since the design stage. This work proposes a design strategy for biorefineries using a shortcut method as the thermodynamic-topological analysis. For this, a biorefinery based on cocoyam, which is a rural raw material with a high potential for the obtainment of added-value products, was used as a case study. The chosen products were ethanol, lactic acid, starch, and feed additive. The biorefinery was simulated in Aspen Plus. Thermodynamic-topological analysis was implemented in the proposed biorefinery and both biorefineries (with and without the application of thermodynamic-topological analysis) were assessed in economic, environmental, efficiency, and energy-consumption terms. It was determined that the application of thermodynamic-topological analysis generated a more efficient process. After the validation of the results, it was possible to establish a design strategy for biorefineries complementing the knowledge-based approach and based on thermodynamic-topological analysis.



Phase Equilibrium of Reaction Mixtures for the Production of Epichlorohydrin in the Presence of Solvents
Abstract
An alternative solvent for the production of epichlorohydrin via the epoxidation of allyl chloride with an aqueous hydrogen peroxide solution over a heterogeneous catalyst based on a granulated titanium-containing zeolite has been selected. The problem of replacing toxic methanol with other solvents, which provide, in particular, a simplification of the separation flowsheet, has been solved. Five water–allyl chloride–epichlorohydrin–solvent–heavily boiling fraction five-component systems have been studied (methanol, ethanol, propanol-1, propanol-2, and butanol-1). A thermodynamic topological analysis of phase equilibrium diagrams and an assessment of the possibility and feasibility of separating the mixtures via a method based on a combination of distillation and splitting have been conducted. The most promising solvent for the allyl chloride epoxidation reaction is propanol-2.



Separation of Nickel Isotopes during the Filling of a Cascade of Gas Centrifuges with Different Numbers of Stages
Abstract
The results of our study of the filling of a cascade of gas centrifuges with different numbers of stages for separation of nickel isotopes used in nuclear physical research and production of radioactive isotopes are presented. During the filling of the cascade, the natural mixture of nickel isotopes is separated, and the isotopes are concentrated in different cascade stages. The concentrations of nickel isotopes in the stages and flows of light and heavy fractions after the filling of the cascade were shown to depend on the number of stages in the cascade.



Characteristics of the Air–Steam Gasification of Carbonaceous Fuels by Filtration Combustion at an Elevated Pressure
Abstract
Calculation results on the stationary mode of the filtration combustion of carbon mixtures with a solid incombustible material in a counterflow of an oxidant gas (air–steam mixture) under the assumption of a thermodynamically equilibrium composition of gaseous products and a self-consistent combustion temperature are presented. The influence of pressure in the reactor on the temperature of combustion and composition of gaseous products is considered. An increase in the pressure leads to a higher combustion temperature, a lower hydrogen yield, and a decreasing sensitivity of the combustion temperature to the concentration of water vapor in the oxidant gas.



Analysis of Reverse Currents Parameters and Gas Content in Liquid behind the Roughness Ridge
Abstract
Based on experimental studies, the effect of gas content in the liquid behind the ridges of artificial helical roughness on film thickness and the value of the heat transfer coefficient is shown. The numerical results for the reverse currents velocity distribution and pressure difference along the ridge height and the cavity length, as well as experimental values of gas content in the liquid separation zone, arising from the flow over a regular roughness, are presented. The scale of reverse currents, their location behind the roughness ridge, and gas content depend on the height and shape of the ridge, the irrigation density, and the physical properties of the liquid. It was concluded that the gas bubbles in the liquid form in reverse current zones in the cavities of the artificial roughness due to reduced pressure compared to gas pressure at the interface and, therefore, gas suction from the interface zone. The dependence for calculating gas content via the thickness of the liquid layer in the roughness cavity is proposed.



Ultrafiltration Modeling Allowing for Axial Dispersion in a Solution under Purification
Abstract
Formulas for ultrafiltration operating and geometric parameters that take into account the longitudinal diffusion of solute molecules in a solution under treatment have been derived based on differential equations of material balance. The effect of longitudinal diffusion on the concentration of solute molecules in the permeate and the retentate in comparison with plug flow and perfect mixing conditions has been evaluated.



Continuous Mixing of Granular Materials under Pulse Action on a Segregated Flow of an Intermittently Dosed Component
Abstract
A controlled segregated process flows principle was used to design a process of continuous mixing of granular materials with intermittent dosing of a microcomponent. Technology opportunities of mixing under reverse-pulse action on a segregated flow of a component in a drum mixer were analyzed. It was determined by experimental and analytical investigation of the mixing dynamics that the selective action of a sequence of reverse pulses on the segregated flow of the microcomponent ensures the production of a mixture the variation of the composition of which is many times smaller than a mixture in a mixer of a flow pattern that corresponds to perfect mixing.



Elastic Turbulence Origination and Evolution in Polymeric Flows
Abstract



Simulation of Swirling Turbulent Flow Aerodynamics in a Centrifugal Machine
Abstract
This work presents a numerical simulation of the aerodynamics of a swirling turbulent flow in a vortex chamber of a combined pneumatic centrifugal machine with a rotor located in its upper part and consisting of a system of rotating blades. Numerical analysis of the swirling turbulent flow made it possible to determine the main patterns in the behavior of the carrier agent in the machine. As a result, a modification of the rotor blade shape is proposed, which allows the distribution change of the radial velocity field as necessary. Numerical studies have shown the promise of this approach for controlling the radial velocity component in the rotor, which is a necessary condition for the separator to operate efficiently. The conducted numerical calculations are validated using test studies and a comparison with experimental data.



Electroflotation in Wastewater Treatment from Oil Products, Dyes, Surfactants, Ligands, and Biological Pollutants: A Review
Abstract
Various aspects of electroflotation technology for wastewater treatment and extraction of organic and inorganic compounds from process solutions were reviewed. The achievements in the extraction of organic pollutants from sewage (oil products, dyes, surfactants, biological components) and ligands were described in detail. The results of studies on the effect of various surfactants on the electroflotation process were presented.



Removal of Starch Glue from Wastewater by Coupling Coagulation and Electroflotation Processes
Abstract
The aim of the current study is to optimize the treatment of wastewater rich in starch glue issued from the card board industry by coupling coagulation and electroflotation processes. The treatment consists of maximizing the removal rate of suspended solids contained in wastewater. This study includes both batch and continuous modes. In batch mode, a model water solution was used in order to evaluate the influence of pH, current density, and coagulant concentration, which were selected as operating parameters to be optimized. The methodology of experimental research, with an orthogonal central composite plan, was approved. In order to approach the process to the industrial scale and to improve the suspended solids removal rate, a continuous mode was also studied. The purification efficiency consisting in the elimination of suspended solids exceeded 95%. Physicochemical characterization of the effluent was performed before and after the treatment in batch and continuous modes to improve the efficiency of this process. This characterization included pH, conductivity, salinity, chemical oxygen demand, biochemical oxygen demand, and suspended solids.



Galvanic Corrosion of Steel in Agitated Vessels Used in Fertilizer Industry
Abstract
Rates of mass transfer controlled Fe/Cu galvanic corrosion at the wall lining of a cylindrical agitated vessel in different fertilizer electrolytic media were studied. Variables investigated are impeller rotation speed, impeller geometry, electrolyte type, electrolyte concentration, area ratio (anode/cathode), electrolyte temperature, and effect of polyethylene oxide (drag reducing polymer) as a corrosion inhibitor. The corrosion rate was determined by following the change of the concentration of anode metal ions (Fe++) in the electrolyte with time. Scanning electron microscopy (SEM) was carried out for steel sheets subjected to different electrolytes. The results showed that the galvanic corrosion rate increased with increasing the impeller rotation speed, the electrolyte concentration, and temperature. The presence of polyethylene oxide decreased the rate of corrosion by 11–35.21% depending on polymer concentration and operating conditions. Axial flow impeller produces corrosion rates higher than that with the radial flow type under the same operating parameters. Application of the results in the design of agitated vessels handling fertilizer media was discussed.



Stochastic Model of Parallel or Sequential Processes of Deaeration and Mixing of Granular Media Using the Operation of a Centrifugal Device as an Example
Abstract
Based on the theory of Markov processes, a deaeration model of bulk materials in parallel and sequential operations that include mixing with a degree of mixture heterogeneity and with a compaction method is proposed. Based on one-dimensional or multidimensional Poisson laws, distribution functions over the microscopic states of a system of particles are constructed for the random relative change of a selected deaerated volume. The model is illustrated by combining these processes in the working chamber of a centrifugal device. The random porosity of the mixture is constructed using a one-dimensional Poisson equation, which is discrete in system states and continuous over time parameters, and the relevant moments were estimated using moment generating functions.



Modeling Gas Hydrate Formation from Ice Powders Based on Diffusion Theory
Abstract
Based on the diffusion theory, a gas–solid reaction model for gas hydrate formation from monosize ice powders was constructed and an effective diffusion coefficient through the gas hydrate shell was obtained by solving the diffusion equation. This model can be applied for a gas–solid reaction process with gas pressure drop during hydrate formation. Two cases termed as M1 and M2 were discussed and compared with each other. In the M1 case, the spherical particle geometry was assumed to be squeezed by adjacent particles. In the M2 case, the effect of adjacent particles on the object particle geometry was neglected. The results showed that the gas effective diffusion coefficient was a critical parameter for accurately simulating the reaction process, and it was found to vary during hydrate formation. In this model, the time-dependent gas effective diffusion coefficient was calculated by means of the measured gas pressure during hydrate formation, and the degrees of hydrate formation were obtained. In addition, the geometrical changes of the hydrate shell and ice powders were obtained during hydrate formation.



A General Hybrid GMDH–PNN Model to Predict Thermal Conductivity for Different Groups of Nanofluids
Abstract
In this study, a general model for estimating the nanofluids (NFs) thermal conductivity by using a hybrid group method of data handling polynomial neural network (GMDH–PNN) has been investigated. NFs thermal conductivity was modeled as a function of nanoparticle size and volume fraction, nanoparticle and base fluid thermal conductivity, and base fluid temperature. For this purpose, a network that contains 6 hidden layers with 2 inputs in each layer and with training algorithm of least squares regression has been applied. The results showed a good accuracy for estimating the thermal conductivity of NFs with a root mean squared error (RMSE) of 0.03027 for 118 systems containing 1929 training data sets. Furthermore, the RMSE for 27 systems containing 244 data as the validation sets was 0.02843 and also mean absolute percentage errors (MAPE) for training and validation data sets were 4.47 and 4.59%, respectively. Moreover, the proposed hybrid GMDH–PNN model was compared with different models from literature for different groups of NFs. The results indicated an improvement in prediction of thermal conductivity with lower errors compared to the previous models.


