scholarly journals Understanding the Effect of Stepwise Irrigation on Liquid Holdup and Hysteresis Behavior of Unsaturated Ore Heap

Minerals ◽  
2021 ◽  
Vol 11 (11) ◽  
pp. 1180
Author(s):  
Leiming Wang ◽  
Shenghua Yin ◽  
Bona Deng

Liquid is a crucial medium to contain soluble oxygen, valuable metal ions, and bacteria in unsaturated heap leaching. Liquid retention behavior is the first critical issue to be considered to efficiently extract low-grade minerals or wastes. In this study, the residual liquid holdup of an unsaturated packed bed was quantitatively discussed by liquid holdup (θ), residual liquid holdup (θresidual), relative liquid holdup (θ’), and relative porosity (n*) using the designed measuring device. The detailed liquid holdup and the hysteresis behavior under stepwise irrigation are indicated and discussed herein. The results show that relative porosity of the packed bed was negatively related to particle size, and intra-particle porosity was more developed in the −4.0 + 2.0 mm packed bed. The higher liquid retention of the unsaturated packed bed could be obtained by using stepwise irrigation (incrementally improved from 0.001 to 0.1 mm/s) instead of uniform irrigation (0.1 mm/s). It could be explained in that some of the immobile liquid could not flow out of the unsaturated packed bed, and this historical irrigation could have accelerated formation of flow paths. The θ was sensitive to superficial flow rate (or irrigation rate) in that it obviously increased if a higher superficial flow rate (u) was introduced, however, the θresidual was commonly affected by n* and θ’. Moreover, the liquid hysteresis easily performed under stepwise irrigation condition, where θ and θresidual were larger at u of the decreasing flow rate stage (DFRS) instead of u of the increasing flow rate stage (IFRS). These findings effectively quantify the liquid retention and the hysteresis behavior of ore heap, and the stepwise irrigation provides potential possibility to adjust liquid retention conditions.

2021 ◽  
Vol 1 (3) ◽  
pp. 13-27
Author(s):  
Vladimir I Golik ◽  
Iurii I. Razorenov ◽  
Vladimir S. Vagin ◽  
Vasilii I. Liashenko

Relevance. Phosphogypsum, the product of apatites chemical processing, is one of the most common mining wastes. Phosphogypsum utilization is not widespread yet, therefore its cost is low. Integrated research has been carried out to determine the technological capacity and economic feasibility of phosphogypsum, sludge, and dolomite utilization as binders in the conversion of ore production techniques. Research aim is to develop a hardening mixture composition based on unconventional industrial waste, determine the technological capacity and economic feasibility of utilizing phosphogypsum, sludge, dolomite, and other accessible low activity wastes as a substitute for expensive and relatively scarce binder material. Research methodology. Initial data are studied of the wastes possessing binding properties. The efficiency of admixing them is determined from the robustness of hardening backfill mixtures control samples that have been produced in laboratory conditions. Based on the research, a database is created to apply the results in practice for mining development. Results. The hardening materials compositions were obtained based on unconventional industrial waste including hydrometallurgical and dressing tailings, furnace clinker, low-grade sand, thermal power plants (TPP) and chemical industry ashes. The optimal composition of the mixture per cubic meter: tailings – 600–750 kg; TPP ash – 180–220 kg; cement dust – 250–315 kg; cement – 35–40 kg; tempering water – 450–515 l under the mixture’s fluidity of about 14 cm according to the readings of the mortar consistency measuring device (StroyTsNIL cone). To ensure radiation safety of the hardening mixture that is based on unconventional industrial waste, it is advisable to take into account not only their chemical and physical-mechanical indicators but the value of naturally radioactive nuclides’ effective activity as well. Conclusions. It has been stated that the robustness of mixtures containing gypsum is 1.5–2.0 times higher, and under the hardening time of 3, 6 and 12 months makes up 3.1; 5.7 and 7.6 MPa correspondingly. It has been shown that the compositions with the binder’s flow rate of 450 kg per cubic meter under the cement : sludge ratio of 1 : 2 show the robustness from 2.8 to 4.9 MPa in 28 days. The content of low-grade sand levigate particles reaches 20% and more. Classes with a specific area of 28.4 m2/kg refer to fine sand, and with a specific area of 27.7 m2/kg refer to medium sand. The robustness of the 28 days old composition reaches 0.5 MPa, 90 days – 0.9 MPa depending on the cement flow rate. It has been substantiated that binders based on fluorine gypsum, phosphogypsum, and belite sludge by mixed grinding of the granulated 26 "Izvestiya vysshikh uchebnykh zavedenii. Gornyi zhurnal". No. 3. 2021 ISSN 0536-1028 blast-furnace slug with the ferrochrome sludge and phosphogypsum up to 70%, 0.08 mm size, show the robustness of the binder up to 3.0 MPa with the flow rate of 450 kg per a cubic meter of the mixture. Keywords: industrial waste; hardening mixture; binder; PPT ash; ash and slag; cement; fluorine gypsum; phosphogypsum; non-reactive aggregate; belite sludge; naturally radioactive nuclides. Acknowledgements. Specialists from Platov South-Russian State Polytechnic University (Novocherkassk, Russia), Ukrainian Research and Design Institute of Industrial Technology (Zhovti Vody, Ukraine), Vostochnyy (Eastern) Mining and Enrichment Combine (Zhovti Vody, Ukraine), Dnipro University of Technology (Dnipro, Ukraine) and others took part in creating, improving, and introducing R&D.


2020 ◽  
Vol 17 (4) ◽  
pp. 47-52
Author(s):  
Vibha Goswami ◽  
Renu Upadhyaya ◽  
Sumanta Kumar Meher

In this study, synthesised Azadirachta indica adsorbent was used for the removal of methylene blue dye using a packed bed column. The effect of feed flow rate, feed methylene blue dye concentration, and bed height of column on percentage removal of dye was studied. It was observed that the column bed exhausted rapidly at a higher flow rate and therefore, a breakthrough occurred faster. However, it was observed that bed exhaustion time increases on increasing the bed height from 2 to 10 inch at 10 mg/L feed dye concentration and feed flow rate of 40 ml/min. It was also found that the breakthrough curve is more dispersed and the percentage removal of dye increases on decreasing the feed methylene dye concentration from 150 to 10 mg/L. The percentage removal was found to be 96.89% at 20 ml/min of feed flow rate under 10 inch of bed height and 10 mg/L of feed dye concentration. The atomic absorption spectrophotometer and scanning electron microscope were used for estimating the effluent dye concentration from the column and morphological study, respectively.


2012 ◽  
Vol 1380 ◽  
Author(s):  
S. Bello-Teodoro ◽  
R. Pérez-Garibay

ABSTRACTA method, based in leaching with SO2, to process low grade pyrolusite minerals has shown good results at laboratory scale. After the separation of the solid impurities, the dissolved manganese is subsequently precipitated using the SO2/O2 gas mixture as oxidising agent. In this research it was obtained a mathematical model to estimate the oxidative precipitation process, as a function of temperature, pH and SO2 gas flow rate. It was found that pH and temperature have the main influence in the reaction rate. An optimal SO2 concentration in the mixture must be used to avoid generation of reductive conditions. It was observed a most efficient reaction with a low gas flow rate injection. The predicted reaction rates presents a good concordance with the experimental results (R2=0.97), showing a worthy potential for practical uses.


2013 ◽  
Vol 781-784 ◽  
pp. 1637-1645 ◽  
Author(s):  
Ting Jun Ma ◽  
Yi Qing Xu

The degradation effectiveness and reaction kinetics of representative organophosphorus (OP) pesticide in a packed-bed plasma reactor have been studied. Important parameters, including peak voltage, pulse frequency, gas-flow rate, initial concentration, diameter of catalyst particles, and thickness of catalyst bed which influences the removal efficiency, were investigated. Experimental results indicated that rogor removal efficiency as high as 80% can be achieved at 35 kV with the gas flow rate of 800 mL/min and initial concentration of 11.2 mg/m3.The removal efficiency increased with the increase of pulsed high voltage, and pulse frequency, the decrease of the diameter of catalyst particles and the thickness of catalyst bed. Finally, a model was established to predict the degradation of the rogor, which generally can simulate the experimental measurements to some degree.


2011 ◽  
Vol 2011 ◽  
pp. 1-6 ◽  
Author(s):  
Hsiao-Ching Chen ◽  
Hen-Yi Ju ◽  
Tsung-Ta Wu ◽  
Yung-Chuan Liu ◽  
Chih-Chen Lee ◽  
...  

An optimal continuous production of biodiesel by methanolysis of soybean oil in a packed-bed reactor was developed using immobilized lipase (Novozym 435) as a catalyst in atert-butanol solvent system. Response surface methodology (RSM) and Box-Behnken design were employed to evaluate the effects of reaction temperature, flow rate, and substrate molar ratio on the molar conversion of biodiesel. The results showed that flow rate and temperature have significant effects on the percentage of molar conversion. On the basis of ridge max analysis, the optimum conditions were as follows: flow rate 0.1 mL/min, temperature52.1∘C, and substrate molar ratio 1 : 4. The predicted and experimental values of molar conversion were83.31±2.07% and82.81±.98%, respectively. Furthermore, the continuous process over 30 days showed no appreciable decrease in the molar conversion. The paper demonstrates the applicability of using immobilized lipase and a packed-bed reactor for continuous biodiesel synthesis.


Author(s):  
V Sureshkannan ◽  
TV Arjunan ◽  
D Seenivasan ◽  
SP Anbuudayasankar ◽  
M Arulraj

Compressed air free from traces of water vapour is vital in many applications in an industrial sector. This study focuses on parametric optimization of a pressure-based packed bed adsorption system for air dehumidification through the Taguchi method and Genetic Algorithm. The effect of operational parameters, namely absolute feed air pressure, feed air linear velocity, and purge air flow rate percent on adsorption uptake rate of molecular sieve 13X-water pair, are studied based on L25 orthogonal array. From the analysis of variance, it has been found that absolute feed air pressure and purge air flow rate percent were the parameters making significant improvement in the adsorption uptake rate. A correlation representing the process was developed using regression analysis. The optimum adsorption conditions were obtained through the Taguchi method and genetic algorithm and verified through the confirmation experiments. This system can be recommended for the industrial and domestic applications that require product air with the dew point temperature below 0°C.


2012 ◽  
Vol 2012 ◽  
pp. 1-6 ◽  
Author(s):  
R. Chandra ◽  
V. K. Vijay ◽  
P. M. V. Subbarao

This paper presents the results of an automated water scrubbing system used for enrichment of methane content in the biogas, to produce vehicular grade biomethane fuel. Incorporation of automatic control systems for precisely regulating the water level and maintaining constant operating pressure in the packed bed absorption column of water scrubbing system resulted in steady-state operation of the scrubbing system and a consistent supply of methane-enriched biogas from the gas outlet. The improved automated water scrubbing system was found to enrich 97% methane at an operating column pressure of 1.0 MPa with 2.5 m3/h biogas in-flow rate and 2.0 m3/h water in-flow rate into the scrubbing column unit.


2014 ◽  
Vol 908 ◽  
pp. 277-281
Author(s):  
Fei Wu ◽  
Jie Wu ◽  
Mei Jin ◽  
Fang Wang ◽  
Ping Lu

Based on acetone-H2O system, the influence of the gas-liquid distribution inducer on the mass transfer coefficient in the rotating packed bed with the stainless steel packing was investigated. Furthermore, the absorption performance was also obtained under the experimental condition of the rotational speed of 630 rpm, the gas flow rate of 2 m3/h and the liquid flow rate of 100 L/h in the rotating packed bed with different types and different installation ways of the distribution inducer. The experimental results showed that the volumetric mass transfer coefficient Kyα per unit contact length of gas-liquid was increased by 8.6% for the forward-curved fixed blade, by 19.8% for the backward-curved rotor blade and by 33.2% with the combination of the straight radial rotor blade and the backward-curved fixed blade, respectively. Furthermore, when the gas flow rate was 2.5 m3/h, Kyα per unit contact length of gas-liquid was increased by 2.9% for the forward-curved fixed blade, by 25.3% for the backward-curved rotor blade, by 42.7% for the combination of the straight radial rotor blade and the backward-curved fixed blade, respectively. The results indicated that the distribution inducer play an important role on the improvement of the mass transfer coefficient in acetone-H2O system.


2000 ◽  
Vol 78 (3) ◽  
pp. 397-403 ◽  
Author(s):  
Chia-Chang Lin ◽  
Yu-Shao Chen ◽  
Hwai-Shen Liu

Sign in / Sign up

Export Citation Format

Share Document