Effectiveness of Cupressus sempervirens cones as biosorbent for the removal of basic dyes from aqueous solutions in batch and dynamic modes
The feasibility of using cypress cone chips from Cupressus sempervirens as a low-cost biosorbent for the removal of two representative basic dyes, methylene blue (MB) and rhodamine B (RhB), from aqueous solutions was investigated in batch and continuous modes. Dyes biosorption was strongly dependent...
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2010
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| LEADER | 15383caa a22019337a 4500 | ||
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| 001 | PAPER-7471 | ||
| 003 | AR-BaUEN | ||
| 005 | 20230518203713.0 | ||
| 008 | 190411s2010 xx ||||fo|||| 00| 0 eng|d | ||
| 024 | 7 | |2 scopus |a 2-s2.0-77956154288 | |
| 024 | 7 | |2 cas |a methylene blue, 61-73-4; rhodamine B, 81-88-9; Coloring Agents; Methylene Blue, 61-73-4; Rhodamines; Solutions; rhodamine B, 14899-08-2 | |
| 040 | |a Scopus |b spa |c AR-BaUEN |d AR-BaUEN | ||
| 030 | |a BIRTE | ||
| 100 | 1 | |a Fernandez, M.E. | |
| 245 | 1 | 0 | |a Effectiveness of Cupressus sempervirens cones as biosorbent for the removal of basic dyes from aqueous solutions in batch and dynamic modes |
| 260 | |c 2010 | ||
| 270 | 1 | 0 | |m Cukierman, A.L.; Departamento de Tecnología Farmacéutica, Facultad de Farmacia y Bioquímica, Universidad de Buenos Aires, Junín 956, (C113AAD) Buenos Aires, Argentina; email: analea@di.fcen.uba.ar |
| 506 | |2 openaire |e Política editorial | ||
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| 520 | 3 | |a The feasibility of using cypress cone chips from Cupressus sempervirens as a low-cost biosorbent for the removal of two representative basic dyes, methylene blue (MB) and rhodamine B (RhB), from aqueous solutions was investigated in batch and continuous modes. Dyes biosorption was strongly dependent on the solution's pH. Sorption kinetics was determined and properly described by the pseudo-second-order rate model. Experimental equilibrium isotherms fitted the Langmuir model, showing maximum biosorption capacities of 0.62. mmol/g for MB and 0.24. mmol/g for RhB. Competitive experiments from a binary solution of the dyes demonstrated the preference of the cone chips for biosorbing MB. Very low desorption efficiencies were obtained for both dyes. Dynamic experiments showed that the breakthrough time was three times higher for MB biosorption than for RhB for the same conditions. Breakthrough curves were properly represented by a mathematical model. © 2010 Elsevier Ltd. |l eng | |
| 536 | |a Detalles de la financiación: Agencia Nacional de Promoción Científica y Tecnológica | ||
| 536 | |a Detalles de la financiación: Universidad de Buenos Aires | ||
| 536 | |a Detalles de la financiación: Consejo Nacional de Investigaciones Científicas y Técnicas | ||
| 536 | |a Detalles de la financiación: The authors gratefully acknowledge Consejo Nacional de Investigaciones Científicas y Técnicas (CONICET) , Universidad de Buenos Aires (UBA) , and Agencia Nacional de Promoción Científica y Tecnológica (ANPCyT-FONCyT) from Argentina, for financial support. | ||
| 593 | |a Programa de Investigación y Desarrollo de Fuentes Alternativas de Materias Primas y Energia, PINMATE, Departamento de Industrias, Facultad de Ciencias Exactas y Naturales, Universidad de Buenos Aires, Intendente Güiraldes 2620, Ciudad Universitaria, C1428BGA Buenos Aires, Argentina | ||
| 593 | |a Cátedra de Farmacotecnia II, Departamento de Tecnología Farmacéutica, Facultad de Farmacia y Bioquímica, Universidad de Buenos Aires, Junín 956, C113AAD Buenos Aires, Argentina | ||
| 690 | 1 | 0 | |a BASIC DYES |
| 690 | 1 | 0 | |a BIOSORPTION |
| 690 | 1 | 0 | |a CYPRESS CONE CHIPS |
| 690 | 1 | 0 | |a TEXTILE WASTEWATER TREATMENT |
| 690 | 1 | 0 | |a UP-FLOW COLUMN |
| 690 | 1 | 0 | |a AQUEOUS SOLUTIONS |
| 690 | 1 | 0 | |a BASIC DYES |
| 690 | 1 | 0 | |a BINARY SOLUTIONS |
| 690 | 1 | 0 | |a BIOSORBENTS |
| 690 | 1 | 0 | |a BIOSORPTION CAPACITY |
| 690 | 1 | 0 | |a BREAK THROUGH CURVE |
| 690 | 1 | 0 | |a BREAKTHROUGH TIME |
| 690 | 1 | 0 | |a COMPETITIVE EXPERIMENTS |
| 690 | 1 | 0 | |a CONTINUOUS MODE |
| 690 | 1 | 0 | |a CYPRESS CONE CHIPS |
| 690 | 1 | 0 | |a DESORPTION EFFICIENCY |
| 690 | 1 | 0 | |a DYNAMIC EXPERIMENT |
| 690 | 1 | 0 | |a DYNAMIC MODES |
| 690 | 1 | 0 | |a EQUILIBRIUM ISOTHERMS |
| 690 | 1 | 0 | |a LANGMUIR MODELS |
| 690 | 1 | 0 | |a METHYLENE BLUE |
| 690 | 1 | 0 | |a PSEUDO SECOND ORDER RATE MODEL |
| 690 | 1 | 0 | |a RHODAMINE B |
| 690 | 1 | 0 | |a SORPTION KINETICS |
| 690 | 1 | 0 | |a TEXTILE WASTEWATER TREATMENT |
| 690 | 1 | 0 | |a UP-FLOW COLUMN |
| 690 | 1 | 0 | |a ADSORPTION |
| 690 | 1 | 0 | |a BIOSORPTION |
| 690 | 1 | 0 | |a DESORPTION |
| 690 | 1 | 0 | |a DYES |
| 690 | 1 | 0 | |a MATHEMATICAL MODELS |
| 690 | 1 | 0 | |a SOLUTIONS |
| 690 | 1 | 0 | |a TEXTILES |
| 690 | 1 | 0 | |a WASTEWATER |
| 690 | 1 | 0 | |a WASTEWATER TREATMENT |
| 690 | 1 | 0 | |a WATER TREATMENT PLANTS |
| 690 | 1 | 0 | |a STRIPPING (DYES) |
| 690 | 1 | 0 | |a ABSORBENT |
| 690 | 1 | 0 | |a CYPRESS CONE CHIP |
| 690 | 1 | 0 | |a METHYLENE BLUE |
| 690 | 1 | 0 | |a RHODAMINE B |
| 690 | 1 | 0 | |a UNCLASSIFIED DRUG |
| 690 | 1 | 0 | |a ADSORPTION |
| 690 | 1 | 0 | |a AQUEOUS SOLUTION |
| 690 | 1 | 0 | |a BREAKTHROUGH CURVE |
| 690 | 1 | 0 | |a CONIFEROUS TREE |
| 690 | 1 | 0 | |a DESORPTION |
| 690 | 1 | 0 | |a DYE |
| 690 | 1 | 0 | |a EXPERIMENTAL STUDY |
| 690 | 1 | 0 | |a FEASIBILITY STUDY |
| 690 | 1 | 0 | |a ISOTHERM |
| 690 | 1 | 0 | |a NUMERICAL MODEL |
| 690 | 1 | 0 | |a POLLUTANT REMOVAL |
| 690 | 1 | 0 | |a REACTION KINETICS |
| 690 | 1 | 0 | |a TEXTILE INDUSTRY |
| 690 | 1 | 0 | |a WASTEWATER |
| 690 | 1 | 0 | |a AQUEOUS SOLUTION |
| 690 | 1 | 0 | |a ARTICLE |
| 690 | 1 | 0 | |a BIOSORPTION |
| 690 | 1 | 0 | |a CUPRESSUS |
| 690 | 1 | 0 | |a CUPRESSUS SEMPERVIREN |
| 690 | 1 | 0 | |a DESORPTION |
| 690 | 1 | 0 | |a ISOTHERM |
| 690 | 1 | 0 | |a MATHEMATICAL MODEL |
| 690 | 1 | 0 | |a PRIORITY JOURNAL |
| 690 | 1 | 0 | |a UPFLOW REACTOR |
| 690 | 1 | 0 | |a ADSORPTION |
| 690 | 1 | 0 | |a BIODEGRADATION, ENVIRONMENTAL |
| 690 | 1 | 0 | |a COLORING AGENTS |
| 690 | 1 | 0 | |a CUPRESSUS |
| 690 | 1 | 0 | |a HYDROGEN-ION CONCENTRATION |
| 690 | 1 | 0 | |a KINETICS |
| 690 | 1 | 0 | |a METHYLENE BLUE |
| 690 | 1 | 0 | |a MODELS, CHEMICAL |
| 690 | 1 | 0 | |a RHODAMINES |
| 690 | 1 | 0 | |a SOLUTIONS |
| 690 | 1 | 0 | |a TEMPERATURE |
| 690 | 1 | 0 | |a WATER PURIFICATION |
| 690 | 1 | 0 | |a CUPRESSUS |
| 690 | 1 | 0 | |a CUPRESSUS SEMPERVIRENS |
| 650 | 1 | 7 | |2 spines |a PH |
| 650 | 1 | 7 | |2 spines |a PH |
| 700 | 1 | |a Nunell, G.V. | |
| 700 | 1 | |a Bonelli, P.R. | |
| 700 | 1 | |a Cukierman, A.L. | |
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