Removal of copper(II) ions from aqueous solution by biosorption onto agricultural waste sugar beet pulp

2005 ◽  
Vol 40 (9) ◽  
pp. 3031-3044 ◽  
Author(s):  
Zümriye Aksu ◽  
İ. Alper İşoğlu
Keyword(s):  
Aqueous Solution ◽  
Sugar Beet ◽  
Agricultural Waste ◽  
Sugar Beet Pulp ◽  
Beet Pulp

scholarly journals Feasibility Assessment of a Bioethanol Plant in the Northern Netherlands

2019 ◽  
Vol 9 (21) ◽  
pp. 4586 ◽  
Author(s):  
Spyridon Achinas ◽  
Nienke Leenders ◽  
Janneke Krooneman ◽  
Gerrit Jan Willem Euverink
Keyword(s):  
Sugar Beet ◽  
Lignocellulosic Biomass ◽  
Fossil Fuels ◽  
Net Present Value ◽  
Agricultural Waste ◽  
Simulation Software ◽  
Sugar Beet Pulp ◽  
Bioenergy Crops ◽  
Renewable Energy Resources ◽  
Beet Pulp

Due to the exhaustion and increased pressure regarding the environmental and political aspects of fossil fuels, the industrial focus has switched towards renewable energy resources. Lignocellulosic biowaste can come from several sources, such as industrial waste, agricultural waste, forestry waste, and bioenergy crops and processed into bioethanol via a biochemical pathway. Although much research has been done on the ethanol production from lignocellulosic biomass, the economic viability of a bioethanol plant in the Northern Netherlands is yet unknown, and therefore, examined. In this thesis, the feasibility study of a bioethanol plant treating sugar beet pulp, cow manure, and grass straw is conducted using the simulation software SuperPro Designer. Results show that it is not economically viable to treat the tested lignocellulosic biomass for the production of bioethanol, since all three original cases result in a negative net present value (NPV). An alternative would be to exclude the pretreatment step from the process. Although this results in a lower production of bioethanol per year, the plant treating sugar beet pulp (SBP) and grass straw (GS) becomes economically viable since the costs have significantly decreased.

scholarly journals Study of Cadmium Adsorption from Aqueous Solution on Activated Carbon from Sugar Beet Pulp

1998 ◽  
Vol 19 (11) ◽  
pp. 1119-1125 ◽  
Author(s):  
A. Özer ◽  
M. S. Tanyildizi ◽  
F. Tümen
Keyword(s):  
Aqueous Solution ◽  
Activated Carbon ◽  
Sugar Beet ◽  
Sugar Beet Pulp ◽  
Beet Pulp ◽  
Cadmium Adsorption

Biosorption of Ca(II), Cu(II), Pb(II) from aqueous solution by a novel adsorbent of ferric hydroxide-loaded sugar beet pulp

2020 ◽  
Vol 174 ◽  
pp. 336-343
Author(s):  
Qiang Liu ◽  
Ziyuan Gao ◽  
Na Li ◽  
Siming Zhu
Keyword(s):  
Aqueous Solution ◽  
Sugar Beet ◽  
Ferric Hydroxide ◽  
Sugar Beet Pulp ◽  
Beet Pulp

Removal of thallium(I) from aqueous solution using modified sugar beet pulp

2011 ◽  
Vol 93 (2) ◽  
pp. 207-214 ◽  
Author(s):  
J. Zolgharnein ◽  
N. Asanjarani ◽  
T. Shariatmanesh
Keyword(s):  
Aqueous Solution ◽  
Sugar Beet ◽  
Sugar Beet Pulp ◽  
Beet Pulp

Obtaining of sorbing material based on sugar beet pulp

2019 ◽  
pp. 10-16
Author(s):  
S.V. Meshcheryakov ◽  
◽  
I.S. Eremin ◽  
D.O. Sidorenko ◽  
M.S. Kotelev ◽  
...  
Keyword(s):  
Sugar Beet ◽  
Sugar Beet Pulp ◽  
Beet Pulp

Kinetic and thermodynamic study of the adsorption of calcium onto sugar beet pulp

2016 ◽  
pp. 565-570
Author(s):  
Huang Qin ◽  
Zhu Si-ming ◽  
Zeng Di ◽  
Yu Shu-juan
Keyword(s):  
Sugar Beet ◽  
Adsorption Equilibrium ◽  
Ph Value ◽  
Hard Water ◽  
Sugar Beet Pulp ◽  
Order Kinetic ◽  
Factors Affecting ◽  
Isotherm Equation ◽  
Equilibrium Data ◽  
Beet Pulp

Sugar beet pulp (SBP) was used as low value adsorbent for the removal of calcium from hard water. Batch experiments were conducted to determine the factors affecting adsorption of the process such as pH value and Ca concentration. The adsorption equilibrium of Ca2+ by the SBP is reached after 100min and a pseudo second-order kinetic model can describe the adsorption process. The initial concentrations of Ca varied from 927 to 1127mgCa2+/L. A dose of 30g/L sugar beet pulp was sufficient for the optimum removal of calcium. The overall uptake of Ca ions by sugar beet pulp has its maximum at pH=8. The adsorption equilibrium data fitted well with the Langmuir adsorption isotherm equation.

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