The dissolution equilibrium of calcium vapor in liquid iron was carried out at 1873 K in a two-temperature zone furnace by using vapor pressure method.A sealed Mo reaction chamber and a self-made CaO crucible were use...The dissolution equilibrium of calcium vapor in liquid iron was carried out at 1873 K in a two-temperature zone furnace by using vapor pressure method.A sealed Mo reaction chamber and a self-made CaO crucible were used in this experiment.The thermodynamic parameters obtained are as follows for reaction Ca(g) =[Ca]\nK = 4.27-15040/T△G^0 = 125000-35.5T J/mol The relation between dissolved amount of calcium in liquid iron(1873K) and calcium vapor pressure is expressed as[%Ca]= 0.028 pc.展开更多
Commercial grade weakly basic resin D301 was impregnated with iron through a simple method using ferric chloride. Experiments for single, bisolute and trinary competitive adsorption were carried out to investigate the...Commercial grade weakly basic resin D301 was impregnated with iron through a simple method using ferric chloride. Experiments for single, bisolute and trinary competitive adsorption were carried out to investigate the adsorption behavior of 2-naphthalenesulfonic acid(NSA), sulfuric acid and sulfurous acid from their solution at 298 K onto the novel hybrid iron impregnated D301(Fe-D301). Adsorption affinity of NSA on Fe-D301 was found to be much higher than that of sulfuric acid, while adsorption affinity of sulfuric acid was slightly higher than that of sulfurous acid. The data of single-solute adsorption were fitted to the Langmuir model and the Freundlich adsorption model. The non-ideal competitive adsorbed model coupled with the single-solute adsorption models were used to predict the bisolute and trinary-solute competitive adsorption equilibria. The NICM coupled with the Langmuir model yields the favorable representation of the bisolute and trinary-solute competitive adsorption behavior.展开更多
The equilibria of Al-N and Nb-N in molten iron at 1600℃ to 1700℃ by using of samplingmethod have been conducted. The thermodynamic parameters obtained areFor the reaction of 1/2N_2=[N] , lgK=-1106/T-0. 771lgK_(AiN) ...The equilibria of Al-N and Nb-N in molten iron at 1600℃ to 1700℃ by using of samplingmethod have been conducted. The thermodynamic parameters obtained areFor the reaction of 1/2N_2=[N] , lgK=-1106/T-0. 771lgK_(AiN) =- 9909/T + 3. 81=- 1 89800- 73.0/T J/mol, =- 0. 530+ 936/TlgK_(NbN)= - 34700/T+ 1 8. 37= - 664650- 352T J/mol, =- 0. 090- 258. 8/T展开更多
Experiments were carried out at 1873 K in a double-temperature zone furnace using vapor pressure method. The equilibriumtests of bedum vapor with liquid iron were conducted in CaO crucibles sealed in a Mo chamber. As ...Experiments were carried out at 1873 K in a double-temperature zone furnace using vapor pressure method. The equilibriumtests of bedum vapor with liquid iron were conducted in CaO crucibles sealed in a Mo chamber. As a result, the experiments obtainedthe relation between the dissolved content of Ba in liquid iron and the vapor pressure of Ba and the standard Gibbs energies for the re-actions Ba(g)=[Ba] and Ba(l)=[Ba].展开更多
The adsorption of aluminium(III) and iron(III) ions from their single and binary systems, by RHAC was investigated in a batch system. The activated carbon prepared from rice hulls was characterized by scanning electro...The adsorption of aluminium(III) and iron(III) ions from their single and binary systems, by RHAC was investigated in a batch system. The activated carbon prepared from rice hulls was characterized by scanning electron microscopy and Fourier transformation infrared techniques. Batch adsorption experiments were performed under different operating conditions including pH (2 - 5), adsorbent dosage (0.5 - 2.0 g/l), initial ion concentration (5 - 100 mg/l), and contact time (30 - 240 min). The equilibrium time for maximum ions removal was found to be 180 min in single and binary ions systems. The kinetics of adsorption was evaluated using the pseudo-first order, pseudo-second order and Elovich kinetic models. The Langmuir, Freundlich and Temkin equilibrium models were applied to the adsorption experimental data. Real wastewater samples were collected from different locations to investigate the efficiency of rice hull activated carbon in treating real samples. The real wastewater samples were treated with the activated carbon prepared from rice hulls and a commercial activated carbon. The results showed that the activated carbon prepared in the present work was more efficient in the removal of aluminium and iron from real wastewater as compared to the commercial activated carbon which is more advantageous considering both economics and environmental parameters.展开更多
以硅藻土及硝酸铁为原料,制备了改性硅藻土,并进行了改性硅藻土吸附模拟含磷废水的试验研究。结果表明,改性硅藻土对磷的吸附率远高于硅藻土原土;60 min为吸附平衡时间;对于100 m L 5 mg/L的模拟含磷废水,投加改性硅藻土0.6 g,磷去除率...以硅藻土及硝酸铁为原料,制备了改性硅藻土,并进行了改性硅藻土吸附模拟含磷废水的试验研究。结果表明,改性硅藻土对磷的吸附率远高于硅藻土原土;60 min为吸附平衡时间;对于100 m L 5 mg/L的模拟含磷废水,投加改性硅藻土0.6 g,磷去除率超过90%;酸性环境有利于磷的吸附;温度对改性硅藻土吸附磷影响不大;改性硅藻土对磷的吸附行为较符合Langmuir吸附等温式。展开更多
文摘The dissolution equilibrium of calcium vapor in liquid iron was carried out at 1873 K in a two-temperature zone furnace by using vapor pressure method.A sealed Mo reaction chamber and a self-made CaO crucible were used in this experiment.The thermodynamic parameters obtained are as follows for reaction Ca(g) =[Ca]\nK = 4.27-15040/T△G^0 = 125000-35.5T J/mol The relation between dissolved amount of calcium in liquid iron(1873K) and calcium vapor pressure is expressed as[%Ca]= 0.028 pc.
基金Supported by the National Natural Science Foundation of China(No.21276027)the Higher Educational Science and Technology Program of Shandong Province,China(No.J14LC05)
文摘Commercial grade weakly basic resin D301 was impregnated with iron through a simple method using ferric chloride. Experiments for single, bisolute and trinary competitive adsorption were carried out to investigate the adsorption behavior of 2-naphthalenesulfonic acid(NSA), sulfuric acid and sulfurous acid from their solution at 298 K onto the novel hybrid iron impregnated D301(Fe-D301). Adsorption affinity of NSA on Fe-D301 was found to be much higher than that of sulfuric acid, while adsorption affinity of sulfuric acid was slightly higher than that of sulfurous acid. The data of single-solute adsorption were fitted to the Langmuir model and the Freundlich adsorption model. The non-ideal competitive adsorbed model coupled with the single-solute adsorption models were used to predict the bisolute and trinary-solute competitive adsorption equilibria. The NICM coupled with the Langmuir model yields the favorable representation of the bisolute and trinary-solute competitive adsorption behavior.
文摘The equilibria of Al-N and Nb-N in molten iron at 1600℃ to 1700℃ by using of samplingmethod have been conducted. The thermodynamic parameters obtained areFor the reaction of 1/2N_2=[N] , lgK=-1106/T-0. 771lgK_(AiN) =- 9909/T + 3. 81=- 1 89800- 73.0/T J/mol, =- 0. 530+ 936/TlgK_(NbN)= - 34700/T+ 1 8. 37= - 664650- 352T J/mol, =- 0. 090- 258. 8/T
文摘Experiments were carried out at 1873 K in a double-temperature zone furnace using vapor pressure method. The equilibriumtests of bedum vapor with liquid iron were conducted in CaO crucibles sealed in a Mo chamber. As a result, the experiments obtainedthe relation between the dissolved content of Ba in liquid iron and the vapor pressure of Ba and the standard Gibbs energies for the re-actions Ba(g)=[Ba] and Ba(l)=[Ba].
文摘The adsorption of aluminium(III) and iron(III) ions from their single and binary systems, by RHAC was investigated in a batch system. The activated carbon prepared from rice hulls was characterized by scanning electron microscopy and Fourier transformation infrared techniques. Batch adsorption experiments were performed under different operating conditions including pH (2 - 5), adsorbent dosage (0.5 - 2.0 g/l), initial ion concentration (5 - 100 mg/l), and contact time (30 - 240 min). The equilibrium time for maximum ions removal was found to be 180 min in single and binary ions systems. The kinetics of adsorption was evaluated using the pseudo-first order, pseudo-second order and Elovich kinetic models. The Langmuir, Freundlich and Temkin equilibrium models were applied to the adsorption experimental data. Real wastewater samples were collected from different locations to investigate the efficiency of rice hull activated carbon in treating real samples. The real wastewater samples were treated with the activated carbon prepared from rice hulls and a commercial activated carbon. The results showed that the activated carbon prepared in the present work was more efficient in the removal of aluminium and iron from real wastewater as compared to the commercial activated carbon which is more advantageous considering both economics and environmental parameters.
基金financial support from industrial sponsors Aurubis AG(Germany)the Australian Research Council Linkage Program+5 种基金Boliden(Sweden)Metso Outotec Oyj(Finland)Nyrstar(Australia)Kazzinc LtdGlencore(Kazakhstan)Umicore NV(Belgium)are gratefully acknowledged。
文摘以硅藻土及硝酸铁为原料,制备了改性硅藻土,并进行了改性硅藻土吸附模拟含磷废水的试验研究。结果表明,改性硅藻土对磷的吸附率远高于硅藻土原土;60 min为吸附平衡时间;对于100 m L 5 mg/L的模拟含磷废水,投加改性硅藻土0.6 g,磷去除率超过90%;酸性环境有利于磷的吸附;温度对改性硅藻土吸附磷影响不大;改性硅藻土对磷的吸附行为较符合Langmuir吸附等温式。
