Ming-Sheng Miao
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Research Subjects
Ming-Sheng Miao has a total of 19 co-authors. Here are the top co-authors by number of shared publications:
- Qiang Kong
College of Geography and Environment, Shandong Normal University, Jinan, Shandong 250014, PR China; Shandong Province Key Laboratory of Emerging Contaminants Risk Prevention and Control, Jinan, Shandong 250014, PR China; Dongying Institute, Shandong Normal University, Dongying, Shandong 257092, PR China
6 shared publications - Li Shu
LJS Environment, Australia
3 shared publications - Yan-Na Wang
College of Life Science, Shandong Normal University, 88 Wenhua Donglu, Jinan 250014, Shandong, P.R. China, Tel. +86 531 86182550; Fax: +86 531 86180107
3 shared publications - Qingfeng Chen
Guangxi University
2 shared publications - Qun Liu
College of Life Science, Shandong Normal University, 88 Wenhua Donglu, Jinan 250014, Shandong, P.R. China, Tel. +86 531 86182550; Fax: +86 531 86180107
2 shared publications - Yu-Zhen Liu
College of Geography and Environment, Shandong Normal University, 88 Wenhua Donglu, Jinan 250014, Shandong, P.R. China
2 shared publications
Latest Publications
- Open Access
- 1 December 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (60) , 29467-29478
Removal of Cr(VI) from aqueous solution using Fe-modified activated carbon prepared from luffa sponge: kinetic, thermodynamic, and isotherm studies
In this study, the removal of Cr(VI) from aqueous solution using Fe-modified activated carbon (AC-Fe) was investigated. AC-Fe before and after Cr(VI) adsorption was characterized by scanning electron microscopy, Fourier transform infrared spectroscopy (FTIR), and Brunauer–Emmett–Teller surface area. The effects of various parameters were investigated by batch experiments, such as contact time, temperature, pH, adsorbent dose, and initial Cr(VI). The results showed that the modification method greatly improves the adsorption property. The surface area of the activated carbon was relatively high (834.006 m2), and the Fe-AC structure was found to be a well-developed array of microvoids and mesopores. FTIR revealed that the abundance of O–H, N–H, C–O, metal-oxygen, and metal-hydroxyl functional groups on the surface of the Fe-AC may play an important role for the adsorption of Cr(VI). The optimum pH was 1 with maximum removal efficiency of 98.71%. The batch equilibrium data fitted well to the Langmuir isotherm (R2 = 0.9960) at 308 K, which indicated monolayer adsorption. Kinetic data were best fitted with the pseudo-second-order kinetic model, which was considered as the rate-limiting factor. The negative ΔG values confirmed the spontaneity of the adsorption process. Positive ΔH and ΔS values indicated endothermic and irreversible adsorption.
- 1 December 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (60) , 29467-29478
Open AccessRemoval of Cr(VI) from aqueous solution using Fe-modified activated carbon prepared from luffa sponge: kinetic, thermodynamic, and isotherm studies
In this study, the removal of Cr(VI) from aqueous solution using Fe-modified activated carbon (AC-Fe) was investigated. AC-Fe before and after Cr(VI) adsorption was characterized by scanning electron microscopy, Fourier transform infrared spectroscopy (FTIR), and Brunauer–Emmett–Teller surface area. The effects of various parameters were investigated by batch experiments, such as contact time, temperature, pH, adsorbent dose, and initial Cr(VI). The results showed that the modification method greatly improves the adsorption property. The surface area of the activated carbon was relatively high (834.006 m2), and the Fe-AC structure was found to be a well-developed array of microvoids and mesopores. FTIR revealed that the abundance of O–H, N–H, C–O, metal-oxygen, and metal-hydroxyl functional groups on the surface of the Fe-AC may play an important role for the adsorption of Cr(VI). The optimum pH was 1 with maximum removal efficiency of 98.71%. The batch equilibrium data fitted well to the Langmuir isotherm (R2 = 0.9960) at 308 K, which indicated monolayer adsorption. Kinetic data were best fitted with the pseudo-second-order kinetic model, which was considered as the rate-limiting factor. The negative ΔG values confirmed the spontaneity of the adsorption process. Positive ΔH and ΔS values indicated endothermic and irreversible adsorption.
- Open Access
- 1 December 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (60) , 29363-29370
Effects of urban wastewater dilution on growth and biochemical properties of Scenedesmus sp.
Microalgal cultivation coupled with urban wastewater treatment can promote the large-scale production of algal biodiesel. However, most studies conducted to date have focused on effects of the nitrogen lipid production and nutrient removal, while ignoring the effects of dilution levels on the growth and biochemical properties. In this study, synthetic urban wastewater (SUW) was adopted to cultivate Scenedesmus sp. to explore the effects of dilution levels on the growth and biochemical properties, especially the lipid and protein properties. Microalgae reached maximum cell density (4.12 × 106 cell/mL) at 100% dilution, maximum specific growth rate (0.5815 d−1) at 100% dilution, maximum total lipid content (25.4%) at 25% dilution, and maximum protein content (49.97%) at 75% dilution after 5 d of cultivation. The maximum removal rate was COD 69.5 mg/L/d (100% dilution), NH3-N 7.33 mg/L/d (100% dilution) and TP 0.325 mg/L/d (75% dilution). Overall, SUW is a feasible medium for Scenedesmus sp. and 100% dilution is suggested.
- 1 December 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (60) , 29363-29370
Open AccessEffects of urban wastewater dilution on growth and biochemical properties of Scenedesmus sp.
Microalgal cultivation coupled with urban wastewater treatment can promote the large-scale production of algal biodiesel. However, most studies conducted to date have focused on effects of the nitrogen lipid production and nutrient removal, while ignoring the effects of dilution levels on the growth and biochemical properties. In this study, synthetic urban wastewater (SUW) was adopted to cultivate Scenedesmus sp. to explore the effects of dilution levels on the growth and biochemical properties, especially the lipid and protein properties. Microalgae reached maximum cell density (4.12 × 106 cell/mL) at 100% dilution, maximum specific growth rate (0.5815 d−1) at 100% dilution, maximum total lipid content (25.4%) at 25% dilution, and maximum protein content (49.97%) at 75% dilution after 5 d of cultivation. The maximum removal rate was COD 69.5 mg/L/d (100% dilution), NH3-N 7.33 mg/L/d (100% dilution) and TP 0.325 mg/L/d (75% dilution). Overall, SUW is a feasible medium for Scenedesmus sp. and 100% dilution is suggested.
- Open Access
- 22 July 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (60) , 29421-29433
Rhodamine B removal from aqueous solutions using loofah sponge and activated carbon prepared from loofah sponge
Loofah sponge and activated carbon (AC) made from it were used to adsorb rhodamine B (RhB) onto aqueous solutions. Scanning electron microscopy of the two materials revealed they possessed rough surfaces; loofah sponge featured a high surface area of 132.6 m2/g, which increased to 842.3 m2/g for AC. Fourier transform infrared spectroscopy indicated that the surface of both materials was abundant in O–H, C–H, and C=O groups, which may increase their adsorption capacities. The kinetics, isotherms, and optimum conditions for RhB removal were studied. RhB adsorption by the adsorbents was consistent with pseudo-second-order equations. The adsorption isotherms revealed that the adsorption process of loofah sponge involved multilayer adsorption, while that of AC was monolayer adsorption. The optimal performance of AC (removal ratio of 99.20% and equilibrium adsorption of 191.43 mg/g) was achieved using a temperature of 313 K, AC content of 0.6 mg/L, and initial RhB concentration of 120 mg/L. AC displayed an increased adsorption capacity for RhB compared with that of loofah sponge; the maximum equilibrium adsorption of AC reached 333.33 mg/L, which is 14 times that of loofah sponge. AC derived from loofah sponge is a promising adsorbent for RhB removal from aqueous wastewater.
- 22 July 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (60) , 29421-29433
Open AccessRhodamine B removal from aqueous solutions using loofah sponge and activated carbon prepared from loofah sponge
Loofah sponge and activated carbon (AC) made from it were used to adsorb rhodamine B (RhB) onto aqueous solutions. Scanning electron microscopy of the two materials revealed they possessed rough surfaces; loofah sponge featured a high surface area of 132.6 m2/g, which increased to 842.3 m2/g for AC. Fourier transform infrared spectroscopy indicated that the surface of both materials was abundant in O–H, C–H, and C=O groups, which may increase their adsorption capacities. The kinetics, isotherms, and optimum conditions for RhB removal were studied. RhB adsorption by the adsorbents was consistent with pseudo-second-order equations. The adsorption isotherms revealed that the adsorption process of loofah sponge involved multilayer adsorption, while that of AC was monolayer adsorption. The optimal performance of AC (removal ratio of 99.20% and equilibrium adsorption of 191.43 mg/g) was achieved using a temperature of 313 K, AC content of 0.6 mg/L, and initial RhB concentration of 120 mg/L. AC displayed an increased adsorption capacity for RhB compared with that of loofah sponge; the maximum equilibrium adsorption of AC reached 333.33 mg/L, which is 14 times that of loofah sponge. AC derived from loofah sponge is a promising adsorbent for RhB removal from aqueous wastewater.
- Open Access
- 1 April 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (17) , 7933-7942
Isotherm, kinetic, and thermodynamic equations for cefalexin removal from liquids using activated carbon synthesized from loofah sponge
Activated carbon (AC) developed from loofah sponge with phosphoric acid activation was applied to absorb cefalexin (CEX) in aqueous solution. AC was characterized by N2 adsorption–desorption isotherms and Fourier transform infrared spectroscopy (FTIR). Factors influencing the adsorption process were investigated. The equilibrium adsorption isotherms and kinetics of CEX were also studied. The results showed that AC prepared from loofah sponge had rough surface and abundant pores. The determination results of specific surface area (810.12 m2/g) and average pore size (5.28 nm) suggested the high adsorption capability. At low concentration, the AC could adsorb about 95% of CEX. The adsorption effect was independent of the temperature and pH. The maximum adsorption amount of CEX was about 55.11 mg/g at 308 K. The equilibrium data agreed well with Freundlich isotherm equation (R2 = 0.9957) at 308 K, which indicated multilayer adsorption. FTIR analysis suggested the existence of phosphorus-containing functional groups, C–O bond, and C=C bond on the surface of AC of which the peak intensity of AC after adsorption was slightly lower after adsorption, indicating that the AC surface groups interacted with or were covered by the CEX species.
- 1 April 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (17) , 7933-7942
Open AccessIsotherm, kinetic, and thermodynamic equations for cefalexin removal from liquids using activated carbon synthesized from loofah sponge
Activated carbon (AC) developed from loofah sponge with phosphoric acid activation was applied to absorb cefalexin (CEX) in aqueous solution. AC was characterized by N2 adsorption–desorption isotherms and Fourier transform infrared spectroscopy (FTIR). Factors influencing the adsorption process were investigated. The equilibrium adsorption isotherms and kinetics of CEX were also studied. The results showed that AC prepared from loofah sponge had rough surface and abundant pores. The determination results of specific surface area (810.12 m2/g) and average pore size (5.28 nm) suggested the high adsorption capability. At low concentration, the AC could adsorb about 95% of CEX. The adsorption effect was independent of the temperature and pH. The maximum adsorption amount of CEX was about 55.11 mg/g at 308 K. The equilibrium data agreed well with Freundlich isotherm equation (R2 = 0.9957) at 308 K, which indicated multilayer adsorption. FTIR analysis suggested the existence of phosphorus-containing functional groups, C–O bond, and C=C bond on the surface of AC of which the peak intensity of AC after adsorption was slightly lower after adsorption, indicating that the AC surface groups interacted with or were covered by the CEX species.
- Open Access
- 1 April 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (17) , 7763-7772
Adsorption kinetics and optimum conditions for Cr(VI) removal by activated carbon prepared from luffa sponge
Activated carbon (AC) prepared from luffa sponge was firstly used as an adsorbent to remove Cr(VI) from aqueous solution. The Cr(VI) adsorption behaviors of AC under different conditions, including initial Cr(VI) concentration, quantity of AC, solution pH, and temperature were investigated. The optimal conditions for adsorption of Cr(VI) by AC were pH = 1, initial Cr(VI) concentration = 80 mg/L, T = 303 K, and AC content = 1.6 g/L. The adsorption kinetics could be described by the pseudo-second-order model. Fourier transform infrared spectroscopy was used to investigate the sorption mechanism. Some functional groups such as C–O and O–H were formed on the carbon surface, which could then react with Cr(VI). The surface structure of AC before and after adsorption was analyzed by scanning electronic microscopy. Adsorbed ions choked some of the pores in AC after adsorption. The Brunauer–Emmett–Teller surface area and average pore size of the AC were 834.13 m2/g and 5.17 nm, respectively. The maximum adsorption of Cr(VI) by AC was 149.06 mg/g, which makes AC prepared from luffa sponge promising for removing Cr(VI) from wastewater.
- 1 April 2016
- Published by Elsevier in Desalination and Water Treatment
- Vol. 57 (17) , 7763-7772
Open AccessAdsorption kinetics and optimum conditions for Cr(VI) removal by activated carbon prepared from luffa sponge
Activated carbon (AC) prepared from luffa sponge was firstly used as an adsorbent to remove Cr(VI) from aqueous solution. The Cr(VI) adsorption behaviors of AC under different conditions, including initial Cr(VI) concentration, quantity of AC, solution pH, and temperature were investigated. The optimal conditions for adsorption of Cr(VI) by AC were pH = 1, initial Cr(VI) concentration = 80 mg/L, T = 303 K, and AC content = 1.6 g/L. The adsorption kinetics could be described by the pseudo-second-order model. Fourier transform infrared spectroscopy was used to investigate the sorption mechanism. Some functional groups such as C–O and O–H were formed on the carbon surface, which could then react with Cr(VI). The surface structure of AC before and after adsorption was analyzed by scanning electronic microscopy. Adsorbed ions choked some of the pores in AC after adsorption. The Brunauer–Emmett–Teller surface area and average pore size of the AC were 834.13 m2/g and 5.17 nm, respectively. The maximum adsorption of Cr(VI) by AC was 149.06 mg/g, which makes AC prepared from luffa sponge promising for removing Cr(VI) from wastewater.
- 1 August 2014
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 279, 511-517
Enhancement of aerobic granulation by zero-valent iron in sequencing batch airlift reactor
- 1 August 2014
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 279, 511-517
Enhancement of aerobic granulation by zero-valent iron in sequencing batch airlift reactor