Adsorption mechanism of Chromium(III) from water solution on bone char: effect of operating conditions

Adsorption ◽  
2016 ◽  
Vol 22 (3) ◽  
pp. 297-308 ◽  
Author(s):  
Jose Valente Flores-Cano ◽  
Roberto Leyva-Ramos ◽  
Francisco Carrasco-Marin ◽  
Antonio Aragón-Piña ◽  
Jacob Josafat Salazar-Rabago ◽  
...  
2014 ◽  
Vol 20 (6) ◽  
pp. 4014-4021 ◽  
Author(s):  
N.A. Medellin-Castillo ◽  
R. Leyva-Ramos ◽  
E. Padilla-Ortega ◽  
R. Ocampo Perez ◽  
J.V. Flores-Cano ◽  
...  

2014 ◽  
Vol 747 ◽  
pp. 119-140 ◽  
Author(s):  
E. Vandre ◽  
M. S. Carvalho ◽  
S. Kumar

AbstractCharacteristic substrate speeds and meniscus shapes associated with the onset of air entrainment are studied during dynamic wetting failure along a planar substrate. Using high-speed video, the behaviour of the dynamic contact line (DCL) is recorded as a tape substrate is drawn through a bath of a glycerol/water solution. Air entrainment is identified by triangular air films that elongate from the DCL above some critical substrate speed. Meniscus confinement within a narrow gap between the substrate and a stationary plate is shown to delay air entrainment to higher speeds for a wide range of liquid viscosities, expanding upon the findings of Vandre, Carvalho & Kumar (J. Fluid Mech., vol. 707, 2012, pp. 496–520). A pressurized liquid reservoir controls the meniscus position within the confinement gap. It is found that liquid pressurization further postpones air entrainment when the meniscus is located near a sharp corner along the stationary plate. Meniscus shapes recorded near the DCL demonstrate that operating conditions influence the size of entrained air films, with smaller films appearing in the more viscous solutions. Regardless of size, air films become unstable to thickness perturbations and ultimately rupture, leading to the entrainment of air bubbles. Recorded critical speeds and air-film sizes compare well to predictions from a hydrodynamic model for dynamic wetting failure, suggesting that strong air stresses near the DCL trigger the onset of air entrainment.


2020 ◽  
Vol 231 (5) ◽  
Author(s):  
Diana Elizabeth Villela-Martínez ◽  
Roberto Leyva-Ramos ◽  
Antonio Aragón-Piña ◽  
Roberto Navarro-Tovar

2011 ◽  
Vol 695 ◽  
pp. 13-16
Author(s):  
Xuan Liang ◽  
Xue Gang Luo ◽  
Xiao Yan Lin

Expansion-treated rice husk (ERH) had been used as adsorbent for removing copper(II) ions, and showed strong adsorption ability and removal efficiency for copper(II) ions. In this paper, the surface and bulk structures of ERH adsorbent were investigated by X-ray photoelectron spectroscopy (XPS) and scanning electronic microscopy (SEM), ERH was treated by water solution with different pH value, and the adsorption performance of ERH for copper(II) ions was investigated through adsorption static experiments in order to study the adsorption mechanism. The result showed that ERH treated by alkaline solution had high removal efficiency for copper(II) ions, the reason ascribed to the large surface area of ERH. ERH had competitive adsorption for H+ and Cu2+, and a monolayer adsorption process played an important role in the whole process.


2014 ◽  
Vol 1051 ◽  
pp. 813-818
Author(s):  
Adam Rylski ◽  
Krzysztof Siczek

The micropumps driven by AC, DC brush, DC brushless or stepper motors can be used in pharmaceutical industry. The particular property of such pumps is magnet coupling between motor and pump. The aim of the analysis has been to investigate the operating conditions for bearing in such pump during flow of water, oil and glycerin – water solution and to investigate the dependency of the glycerin – water solution flow upon the outlet – inlet pressure difference and upon the speed of motor driving pump. It has been also investigated the possibility of application for NdFeB – NdFeB magnet assembly in the magnet coupling. The loading of pump are connected of flow resistance determined by outlet and inlet pressure difference, speed and temperature of pumped liquid, geometry and material properties of pump elements. The driving motor is loaded by mechanical resistance of pump element motion either. The moment – pressure difference relationship and flow – pressure difference – speed relationship have been made for water and oil and then approximated equation for them have been elaborated. With help of such equation scheme of moment – pressure difference relationship and flow – pressure difference – speed relationship for glycerin – water solution have been made for various values of glycerin strength. The model of pump bearing has been elaborated using Finite Element Method. Auxiliary mathematical equations have been utilized for calculating sliding velocity in bearing and loading force. The obtained contact pressure in bearing has been presented in the article. The model of magnet coupling has been elaborated with use of Finite Element Method and presented in the paper. Dimensions of model are closed to the one used in original pump. It has been observed that for up to 50% glycerin - water solution the moment – pressure difference relationship and flow – pressure difference – rotational speed relationship are very similar to these in the water case. With increasing of solution strength above 50% they start to be more different. Values of contact pressure nonlinearly increase with driving moment value increasing. Calculated values of torque excited values given out by manufacturer with about 20%. Calculated value of decoupling torque for NdFeB – NdFeB magnet assemblies is greater more than 50 % comparing SmCo – NdFeB case.


Author(s):  
Maung Naing Naing Tun ◽  
Nilufer Egrican

This paper presents computer software developed for rating and optimum selection of finned circular tubes compact heat exchangers with various coil geometries. The software is developed to use as a computing tool for commercial and R&D purposes in FRITERM A.S, an original equipment manufacturer (OEM) of finned tube heat exchangers. Finned-tube heat exchangers are highly utilized in refrigeration and process industries and heat transfer and pressure drop calculations are very important to manufactures and design engineers. For this purpose, a simulation and design software to predict the performance of finned-tube heat exchangers is presented. In finned-tube coils fin side fluid is air and tube side fluid can be water, oil, glycol water solution mixture and refrigerants. The analysis and rating of coils at dry and wet operating conditions are presented. Design and the most suitable selections of coils at the given parameters and design constraints from many different coil geometries are also performed in the software. User-friendly object-oriented programming C# is applied in developing the software. The software is developed in modular basic. Six modules are developed: Heating Coils, Cooling Coils, Condenser Coils, Steam Coils, Heat Recovery Coils and Evaporator (DX) Coils. REFPROP is also integrated in the software and all fluids’ thermal and transport properties are obtained from REFPROP. Heat transfer and pressure drop correlations available from literature are evaluated with recommendations. Simulated results are verified against experimental results.


2010 ◽  
Vol 7 (4) ◽  
pp. 1258-1265 ◽  
Author(s):  
Xiu-Yan Pang

Expanded graphite (EG) shows higher adsorption capacity for oils such as salad oil and SD300 oil than polyethylene glycol (PEG) with different MW (4000, 10000, 20000). To illustrate their different adsorption mechanism, adsorption capacities of EG for these pollutants are firstly detected. And then stepwise adsorption for oils is carried out with EG which has been saturated first by PEG with different MW. Then difference between stepwise adsorbance of oil is checked with deviation analysis. Scanning electronic microscopy (SEM) analysis is used to show structure difference of EG adsorbed different adsorbates. It is testified adsorption isotherms of PEG are all type I, PEG molecules lay flat on EG surface and equilibrium adsorbance decrease with the increase of PEG MW. Adsorbance for SD 300 oil and salad oil can reach 131.3 g/g and 127.8 g/g respectively. Deviation analysis for stepwise adsorbance of oil shows no statistical significance. EG saturated firstly by PEG, still has an average adsorption capacity of 98 g/g for SD300 oil and 85 g/g for salad oil and it does not change with the initial PEG concentration. SEM photos illustrate the adsorption of oil on EG is mainly filling. In the adsorption of PEG water solution, there is severe breakage of the V-type pore and shrinkage of the particle.


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