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Adsorption properties of BEA zeolites and their aluminum phosphate extrudates for purification of isomaltose

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Abstract

The disaccharide isomaltose is produced via an enzymatic reaction and is adsorbed to BEA zeolite. This reaction integrated adsorption can be achieved as fluidized bed as well as fixed bed. We investigated isotherms, adsorption enthalpies and sorption kinetics of BEA zeolite and extrudates with a novel aluminum phosphate sintermatrix. These extrudates contain 50% (w/w) of BEA 150 zeolites (Si/Al = 75) as primary crystals. BET-surface for extrudates is 245 m2⋅g−1 and 487 m2⋅g−1 for zeolite. Extrudates show a monomodal macropore structure with a maximum at 90 nm. All isotherms show a type I shape. For lower equilibrium concentrations, which occur during the enzymatic reaction, Henry’s law is applied and compared to a Langmuir model. Adsorption equilibrium constant K i,L calculated from Langmuir for extrudates at 4 °C is 64.7 mL⋅g−1 and more than twice as high as obtained from Henry’s law with K i is 26.8 mL⋅g−1. Adsorption on extrudates at 4 °C is much stronger than on zeolite crystals where the Henry coefficient K i is 17.1 mL⋅g−1. Adsorption enthalpy Δh Ad calculated from van’t Hoff plot with the Henry equation is −44.3 kJ⋅mol−1 for extrudates and −29.6 kJ⋅mol−1 for zeolite crystals. Finally, the kinetics for ad- and desorption were calculated from the initial slope. The diffusion rate for ad- and desorption on extrudates were in the same range while adsorption on zeolites is three orders of magnitudes faster than desorption.

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Abbreviations

A :

External area of adsorbent, m2

b i :

Langmuir parameter for component i, L⋅g−1

c e :

Equilibrium concentration, g⋅L−1

c i :

Initial concentration, g⋅L−1

d crit :

Critical diameter of a molecule, nm

d cry,ex :

Diameter of primary crystals in extrudates, nm

d cry :

Diameter of zeolite crystals, μm

dp :

Diameter of pores, nm

D :

Diffusion coefficient, m2⋅s−1

Δh Ad :

Adsorption enthalpy, kJ⋅mol−1

K i :

Henry coefficient for component i, mL⋅g−1

K i,L :

Adsorption equilibrium constant calculated from Langmuir parameters, mL⋅g−1

l ex :

Length of extrudates, mm

m Ad :

Mass of adsorbent, g

m 0 :

Mass of solvent, g

q 0 :

Loading at t=0 s, mg⋅g−1

q i :

Loading of component i, mg⋅g−1

q s :

Saturation loading of water, mg⋅g−1

q i,max  :

Saturation loading of component i, mg⋅g−1

\(q_{i}^{\mathrm{Ex}}\) :

Excess loading of component i, mg⋅g−1

q t :

Loading at t, mg⋅g−1

q :

Loading at equilibrium, mg⋅g−1

r cry,ex :

Radius of primary crystals in extrudates, nm

r cry :

Radius of zeolite crystals, μm

r ex :

Radius of extrudates, mm

R :

Ideal gas constant 8.3144, J⋅K−1⋅mol−1

t :

Time, s

T :

Absolute temperature, K

V :

Volume of adsorbent, m3

V L :

Volume of liquid solvent during adsorption, mL

ϑ :

Temperature, °C

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Correspondence to Stephan Scholl.

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Presented at FoA 10—10th International Conference on Fundamentals of Adsorption.

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Holtkamp, M., Scholl, S. Adsorption properties of BEA zeolites and their aluminum phosphate extrudates for purification of isomaltose. Adsorption 17, 801–811 (2011). https://doi.org/10.1007/s10450-011-9339-1

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  • DOI: https://doi.org/10.1007/s10450-011-9339-1

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