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Journal articles on the topic 'Affinity adsorption'

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Author: Grafiati

Published: 4 June 2021

Last updated: 1 February 2022

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1

Prasanna, Rajasekar R., and Mookambeswaran A. Vijayalakshmi. "Immobilized metal-ion affinity systems for recovery and structure–function studies of proteins at molecular, supramolecular, and cellular levels." Pure and Applied Chemistry 82, no. 1 (January 3, 2010): 39–55. http://dx.doi.org/10.1351/pac-con-09-01-18.

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Immobilized metal-ion affinity (IMA) adsorption is a collective term that is used to include all kinds of adsorptions where the metal ion serves as the characteristic and most essential part of adsorption center. Of all the IMA techniques, immobilized metal-affinity chromatography (IMAC) has been gaining popularity as the choice of purification technique for proteins. IMAC represents a separation technique that is primarily useful for proteins with natural surface exposed-histidine residues and for recombinant proteins with engineered histidine tag. This review also gives insight into other nonchromatographic applications of IMA adsorption such as immobilized metal-ion affinity gel electrophoresis (IMAGE), immobilized metal-ion affinity capillary electrophoresis (IMACE), and immobilized metal-ion affinity partitioning (IMAP).

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2

Hubble, J. "Stochastic Modeling of Affinity Adsorption." Biotechnology Progress 17, no. 3 (June 1, 2001): 565–67. http://dx.doi.org/10.1021/bp010014o.

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3

Ghose, S., G. M. Forde, and N. K. H. Slater. "Affinity Adsorption of Plasmid DNA." Biotechnology Progress 20, no. 3 (June 4, 2004): 841–50. http://dx.doi.org/10.1021/bp034257n.

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4

Shi, Wei, Yuanyuan Ma, Cunfeng Song, Hairong Jiang, Xiaoning Ru, Jing Tu, Shuhui Jiang, Jun Wang, and Dongtao Ge. "Affinity electromembrane: Electrically facilitated adsorption." Journal of Membrane Science 354, no. 1-2 (May 2010): 86–92. http://dx.doi.org/10.1016/j.memsci.2010.02.072.

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5

Undabeytia, T., E. Morillo, and C. Maqueda. "Adsorption of Cd and Zn on montmorillonite in the presence of a cationic pesticide." Clay Minerals 31, no. 4 (December 1996): 485–90. http://dx.doi.org/10.1180/claymin.1996.031.4.05.

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AbstractThe adsorption of Cd and Zn on a standard montmorillonite (SAZ-1) in the presence of the cationic pesticide chlordimeform, both in solution (simultaneous adsorption) and when the pesticide is previously adsorbed on the clay (successive adsorption) has been studied. The adsorption of Zn decreases when the chlordimeform concentration increases in both simultaneous and successive adsorptions, following the sequence: chlordimeform-free solutions > successive > simultaneous. In the adsorption of Cd the sequence is different: successive > chlordimeform-free solutions > simultaneous, indicating that a small amount of pesticide adsorbed favours Cd adsorption. In all cases, the apparent affinity of the metal for adsorption on montmorillonite, on the basis of distribution coefficients, KD, is higher for lower metal surface coverage, and decreases largely with the amount of the metal adsorbed. This indicates the existence of high affinity sites on the clay, probably those of variable charge edge regions. The contribution of edge and interlamellar positions to adsorption of Zn and Cd on SAZ-1 has been studied.

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6

BOI, C., F. CATTOLI, R. FACCHINI, M. SORCI, and G. SARTI. "Adsorption of lectins on affinity membranes." Journal of Membrane Science 273, no. 1-2 (March 31, 2006): 12–19. http://dx.doi.org/10.1016/j.memsci.2005.12.011.

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7

Bayraktaroğlu, Melis, Hande Orhan, Sinem Evli, Sinan Akgöl, Deniz Aktaş Uygun, and Murat Uygun. "Lectin attached affinity cryogels for amyloglucosidase adsorption." Journal of Carbohydrate Chemistry 37, no. 5 (June 13, 2018): 302–17. http://dx.doi.org/10.1080/07328303.2018.1487972.

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8

Yavuz, Handan, Mehmet Odabaşi, Sinan Akgöl, and Adil Denizli. "Immobilized metal affinity beads for ferritin adsorption." Journal of Biomaterials Science, Polymer Edition 16, no. 5 (January 2005): 673–84. http://dx.doi.org/10.1163/1568562053783713.

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9

Pechenyuk, S. I., Yu P. Semushina, and L. F. Kuz’mich. "Adsorption affinity of anions on metal oxyhydroxides." Russian Journal of Physical Chemistry A 87, no. 3 (February 3, 2013): 490–96. http://dx.doi.org/10.1134/s0036024413030205.

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10

Tolner, Berend, Lisa Smith, Richard H. J. Begent, and Kerry A. Chester. "Expanded-bed adsorption immobilized-metal affinity chromatography." Nature Protocols 1, no. 3 (August 2006): 1213–22. http://dx.doi.org/10.1038/nprot.2006.127.

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11

de Pinho, Samantha Cristina, Ricardo L. Zollner, Marcel De Cuyper, and Maria Helena A. Santana. "Adsorption of antiphospholipid antibodies on affinity magnetoliposomes." Colloids and Surfaces B: Biointerfaces 63, no. 2 (June 2008): 249–53. http://dx.doi.org/10.1016/j.colsurfb.2007.12.008.

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12

Boi, Cristiana, Simone Dimartino, and Giulio C. Sarti. "Modelling and simulation of affinity membrane adsorption." Journal of Chromatography A 1162, no. 1 (August 2007): 24–33. http://dx.doi.org/10.1016/j.chroma.2007.02.008.

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13

Altıntaş, Evrim B., and Adil Denizli. "Affinity adsorption of recombinant human interferon-α on monosize dye-affinity beads." Journal of Applied Polymer Science 103, no. 2 (2006): 975–81. http://dx.doi.org/10.1002/app.25273.

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14

GALVANO, FABIO, AMEDEO PIETRI, BIAGIO FALLICO, TERENZIO BERTUZZI, SALVATORE SCIRÈ, MARCO GALVANO, and ROSARIO MAGGIORE. "Activated Carbons: In Vitro Affinity for Aflatoxin B1 and Relation of Adsorption Ability to Physicochemical Parameters." Journal of Food Protection 59, no. 5 (May 1, 1996): 545–50. http://dx.doi.org/10.4315/0362-028x-59.5.545.

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Affinity in vitro tests were conducted of the efficacy of 17 activated carbons (ACs) in binding aflatoxin B1 from solution. Relationships between adsorption ability and physicochemical parameters of the ACs (surface area, iodine number, methylene blue index, and surface acidity) were tested. Using 5 ml of a 4 μg/ml aqueous solution of aflatoxin B1 and 2 mg of an AC, adsorption abilities ranged from 44.47% to 99.82%. Four ACs showed very high adsorption abilities, binding more than 99% of the available aflatoxin B1. In comparative testing five ACs showed a greater ability to bind aflatoxin B1 than hydrated sodium calcium aluminosilicate (HSCAS). Three ACs also showed high adsorption abilities (ca. 99%) at increasing aflatoxin B1 concentrations (50 and 250 μg/ml) whereas HSCAS adsorption ability greatly declined. With the exception of three ACs, aflatoxin B1 adsorption was significantly correlated with all the physicochemical parameters, confirming a close relationship between molecule trapping and the surface physicochemical adsorption process. The methylene blue index was more reliable than iodine number and surface area in predicting AC adsorptive ability. The results suggested that ACs with a high methylene blue index and low surface acidity have a very high in vitro affinity for aflatoxin B1; however, their efficacy in protecting against aflatoxicosis should be verified further by in vivo tests.

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15

Tang, Xu, Zhaofeng Wang, Nino Ripepi, Bo Kang, and Gaowei Yue. "Adsorption Affinity of Different Types of Coal: Mean Isosteric Heat of Adsorption." Energy & Fuels 29, no. 6 (June 4, 2015): 3609–15. http://dx.doi.org/10.1021/acs.energyfuels.5b00432.

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16

Riemsdijk, W. H. van, L. K. Koopal, and J. C. M. de Wit. "Heterogeneity and electrolyte adsorption: intrinsic and electrostatic effects." Netherlands Journal of Agricultural Science 35, no. 3 (August 1, 1987): 241–57. http://dx.doi.org/10.18174/njas.v35i3.16722.

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Adsorption of electrolytes in natural systems is an important phenomenon. Natural systems contain sorbents with a predominantly constant surface charge, such as clay minerals, as well as a complex mixture of mainly variable charge sorbents like organic matter, both in the dissolved and in the soil solid phase, and metal oxides. The effect of a combination of an intrinsic-affinity distribution (both discrete and continuous) and a variable surface potential on adsorption behaviour of protons is discussed both for random and patchwise heterogeneity. It is shown that the variable charge (potential) or intrinsically homogeneous metal oxides and organic model colloids leads to an apparent heterogeneity of binding sites. This effect is quantified with simulated data and condensation approximation. For heterogeneous charged sorbents, where the apparent affinity represents both chemical heterogeneity and electrostatic interactions, very wide apparent-affinity distributions will be found. The apparent-affinity distribution is in general only a poor representation of the intrinsic-affinity distribution. (Abstract retrieved from CAB Abstracts by CABI’s permission)

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17

Karakoç, Veyis, Handan Yavuz, and Adil Denizli. "Affinity adsorption of recombinant human interferon-α on a porous dye-affinity adsorbent." Colloids and Surfaces A: Physicochemical and Engineering Aspects 240, no. 1-3 (June 2004): 93–99. http://dx.doi.org/10.1016/j.colsurfa.2004.03.005.

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18

Jakšić, Olga, Marko Spasenović, Zoran Jakšić, and Dana Vasiljević-Radović. "Monolayer Gas Adsorption on Graphene-Based Materials: Surface Density of Adsorption Sites and Adsorption Capacity." Surfaces 3, no. 3 (August 24, 2020): 423–32. http://dx.doi.org/10.3390/surfaces3030031.

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Surface density of adsorption sites on an adsorbent (including affinity-based sensors) is one of the basic input parameters in modeling of process kinetics in adsorption based devices. Yet, there is no simple expression suitable for fast calculations in current multiscale models. The published experimental data are often application-specific and related to the equilibrium surface density of adsorbate molecules. Based on the known density of adsorbed gas molecules and the surface coverage, both of these in equilibrium, we obtained an equation for the surface density of adsorption sites. We applied our analysis to the case of pristine graphene and thus estimated molecular dynamics of adsorption on it. The monolayer coverage was determined for various pressures and temperatures. The results are verified by comparison with literature data. The results may be applicable to modeling of the surface density of adsorption sites for gas adsorption on other homogeneous crystallographic surfaces. In addition to it, the obtained analytical expressions are suitable for training artificial neural networks determining the surface density of adsorption sites on a graphene surface based on the known binding energy, temperature, mass of adsorbate molecules and their affinity towards graphene. The latter is of interest for multiscale modelling.

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19

Shi, Jie, Zhiwei Zhao, Zhijie Liang, and Tianyi Sun. "Adsorption characteristics of Pb(II) from aqueous solutions onto a natural biosorbent, fallen arborvitae leaves." Water Science and Technology 73, no. 10 (February 24, 2016): 2422–29. http://dx.doi.org/10.2166/wst.2016.104.

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In this study, the potential of the oriental arborvitae leaves for the adsorption of Pb(II) from aqueous solutions was evaluated. Brunauer–Emmett–Teller analysis showed that the surface area of arborvitae leaves was 29.52 m2/g with pore diameter ranging from 2 to 50 nm. X-ray photoelectron spectroscopy and Fourier transform infrared spectroscopy showed C—;C or C—;H, C—;O, and O—;C=O were the main groups on the arborvitae leaves, which were the main sites for surface complexation. Finally, effects of adsorbent dose, initial pH, contact time, and coexisting natural organic matters (humic acid (HA)) on the adsorption of Pb(II) were investigated. The results indicated that the pHZPC (adsorbents with zero point charge at this pH) was 5.3 and the adsorption reached equilibrium in 120 min. Isotherm simulations revealed that the natural arborvitae leaves exhibit effective adsorption for Pb(II) in aqueous solution, giving adsorptive affinity and capacity in an order of ‘no HA’ > 5 mg/L HA > 10 mg/L HA, and according to the Langmuir models, the maximum adsorptions of Pb(II) were 43.67 mg/g, 38.61 mg/g and 35.97 mg/g, respectively. The results demonstrated that the oriental arborvitae leaves showed high potentials for the adsorption of Pb(II) from aqueous solutions.

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20

Eggert, Martin, Thomas Baltes, Frédéric Garret-Flaudy, and Ruth Freitag. "Affinity precipitation – an alternative to fluidized bed adsorption?" Journal of Chromatography A 827, no. 2 (December 1998): 269–80. http://dx.doi.org/10.1016/s0021-9673(98)00656-6.

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21

Iwata, Hideki, Kyoichi Saito, Shintaro Furusaki, Takanobu Sugo, and Jiro Okamoto. "Adsorption characteristics of an immobilized metal affinity membrane." Biotechnology Progress 7, no. 5 (September 1991): 412–18. http://dx.doi.org/10.1021/bp00011a005.

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22

Tong, X. D., and Y. Sun. "Agar-Based Magnetic Affinity Support for Protein Adsorption." Biotechnology Progress 17, no. 4 (August 3, 2001): 738–43. http://dx.doi.org/10.1021/bp010054s.

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23

de Lucena, S. L., R. G. Carbonell, and C. C. Santana. "Peptide affinity chromatography process for adsorption of fibrinogen." Powder Technology 101, no. 2 (February 1999): 173–77. http://dx.doi.org/10.1016/s0032-5910(98)00169-7.

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24

Hao, Weiqiang, Zhaoan Chen, Junde Wang, and Xueliang Liu. "Modeling of Protein Adsorption in Membrane Affinity Chromatography." Analytical Letters 37, no. 7 (December 28, 2004): 1319–38. http://dx.doi.org/10.1081/al-120035901.

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25

Zollner, Terezinha Célia A., Ricardo de L. Zollner, Marcel De Cuyper, and Maria Helena A. Santana. "Adsorption of Isotype “E” Antibodies on Affinity Magnetoliposomes." Journal of Dispersion Science and Technology 24, no. 3-4 (January 7, 2003): 615–22. http://dx.doi.org/10.1081/dis-120021818.

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26

Yoshimatsu, Keiichi, Lei Ye, Johanna Lindberg, and Ioannis S. Chronakis. "Selective molecular adsorption using electrospun nanofiber affinity membranes." Biosensors and Bioelectronics 23, no. 7 (February 2008): 1208–15. http://dx.doi.org/10.1016/j.bios.2007.12.002.

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27

Rawls, H. Ralph, Israel Cabasso, Barbara F. Zimmerman, and Keith B. Lescale. "Fluoride ion binding and adsorption affinity of polyelectrolytes." Colloids and Surfaces 26 (January 1987): 89–100. http://dx.doi.org/10.1016/0166-6622(87)80108-7.

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28

Lee, Wing-Hin, Ching-Yee Loo, Kim Linh Van, Alexander V. Zavgorodniy, and Ramin Rohanizadeh. "Modulating protein adsorption onto hydroxyapatite particles using different amino acid treatments." Journal of The Royal Society Interface 9, no. 70 (September 28, 2011): 918–27. http://dx.doi.org/10.1098/rsif.2011.0586.

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Hydroxyapatite (HA) is a material of choice for bone grafts owing to its chemical and structural similarities to the mineral phase of hard tissues. The combination of osteogenic proteins with HA materials that carry and deliver the proteins to the bone-defective areas will accelerate bone regeneration. The study investigated the treatment of HA particles with different amino acids such as serine (Ser), asparagine (Asn), aspartic acid (Asp) and arginine (Arg) to enhance the adsorption ability of HA carrier for delivering therapeutic proteins to the body. The crystallinity of HA reduced when amino acids were added during HA preparation. Depending on the types of amino acid, the specific surface area of the amino acid-functionalized HA particles varied from 105 to 149 m 2 g –1 . Bovine serum albumin (BSA) and lysozyme were used as model proteins for adsorption study. The protein adsorption onto the surface of amino acid-functionalized HA depended on the polarities of HA particles, whereby, compared with lysozyme, BSA demonstrated higher affinity towards positively charged Arg-HA. Alternatively, the binding affinity of lysozyme onto the negatively charged Asp-HA was higher when compared with BSA. The BSA and lysozyme adsorptions onto the amino acid-functionalized HA fitted better into the Freundlich than Langmuir model. The amino acid-functionalized HA particles that had higher protein adsorption demonstrated a lower protein-release rate.

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29

Oshima, Tatsuya, Toshihiko Sakamoto, Hodzumi Tachiyama, Kenzo Kanemaru, Kaoru Ohe, and Yoshinari Baba. "Dominant factors for adsorptive recovery of carnosine based on immobilized metal affinity adsorption." Journal of Bioscience and Bioengineering 108 (November 2009): S64. http://dx.doi.org/10.1016/j.jbiosc.2009.08.190.

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30

Rengga, Wara Dyah Pita, Sri Wahyuni, and Agung Feinnudin. "Thermodynamics of Formaldehyde Removal by Adsorption onto Nanosilver Loaded Bamboo-Based Activated Carbon." Materials Science Forum 890 (March 2017): 93–97. http://dx.doi.org/10.4028/www.scientific.net/msf.890.93.

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The performance of nanosilver loaded bamboo-based activated carbon as an adsorbent used for the adsorptive removal of formaldehyde in the air. The size porous of the active carbon is predominantly on the size of mesoporous and microporous. Adsorption tests have been evaluated in laboratory scale fixed-bed column, at different temperatures and initial formaldehyde concentration. In order to investigate is both equilibrium and thermodynamic aspects. The experimental data was fitted with Langmuir model and fit well with the adsorption capacity of 91-110 mg/g. The increase in temperature reduces the adsorption capacity. The thermodynamic parameters show that the values of ∆Go obtained to confirm the feasibility of activated carbon effective sorbents of formaldehyde. The formaldehyde adsorption process is exothermic and adsorbent has a good affinity to formaldehyde.

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31

Rachmania Juliastuti, Sri, Pratiwi Putri Pranowo, and Rizka Yuliana Purbandi. "Separation of Heavy Metals Copper (Cu) and Nickel (Ni) from Industrial Wastewater by Adsorption Using Chitosan Shrimp Shell." Modern Applied Science 9, no. 7 (July 1, 2015): 86. http://dx.doi.org/10.5539/mas.v9n7p86.

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Shrimp shell contains chittin that can be processed become chitosan. Chitosan can be used as bioadsorbent totreat heavy metals content in wastewater. The purposes of this research are to find deacethylation degree ofchitosan from shrimp shell, the constant value of adsorption affinity (k) and adsorption efficiency for variousvariation mass and size of chitosan, heavy metal concentration (solute) in wastewater and to compare adsorptionefficiency between syntetic solution and industrial wastewater. The size variation of the chitosan are 20 meshand 40 mesh. The type of adsorption used is batch until 4 hours with 5 rpm as agitation rate. Deasethylizationdegree for chitosan 20 mesh and 40 mesh are resulted as 75,61% and 77,71 %. More amount of chitosan usedand the smaller size of chitosan make the adsorption efficiency higher as 92,52%. A synthetic solution and PTSIER industrial wastewater are types of wastewater used. PT SIER wastewater contains other metals that canhamper the adsorption of desired metals. Ni is easier to adsorp with 92,52% efficiency than Cu which hasefficiency of 88,52%, because atomic radius of Ni is smaller than Cu. Adsorption affinity constant is influencedby size of the chitosan. The smaller size of chitosan make adsorption affinity constant higher than the bigger size(which is 0,13).

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32

Siwek, Hanna, and Krzysztof Pawelec. "Competitive Interaction of Phosphate with Selected Toxic Metals Ions in the Adsorption from Effluent of Sewage Sludge by Iron/Alginate Beads." Molecules 25, no. 17 (August 31, 2020): 3962. http://dx.doi.org/10.3390/molecules25173962.

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Wastewater is characterized by a high content of phosphate and toxic metals. Many studies have confirmed the sorption affinity of alginate adsorbents for these ions. In this study, the adsorption of phosphate from effluent of sewage sludge on biodegradable alginate matrices cross-linked with Fe3+ ions (Fe_Alg) was investigated. Kinetics and adsorption isotherms were tested in laboratory conditions in deionized water (DW_P) and in the effluent (SW_P), and in the same solutions enriched in toxic metals ions—Cu2+, Cd2+, Pb2+, and Zn2+ (DW_PM and SW_PM). Batch experiments were performed by changing the concentration of phosphate at constant metal concentration. Kinetics experiments indicated that the pseudo-second-order model displayed the best correlation with adsorption kinetics data for both metals and phosphate. The Freundlich equation provided the best fit with the experimental results of phosphate adsorption from DW_P and DW_PM, while the adsorption from SD_P and SD_PM was better described by the Langmuir equation. For tested systems, the affinity of the Fe_Alg for metal ions was in the following decreasing order: Pb2+ > Cu2+ > Cd2+ > Zn2+ in DW_PM, and Pb2+ > Cu2+ > Cd2+ > Zn2+ in SW_PM. The metals’ enrichment of the DW_P solution increased the affinity of Fe_Alg beads relating to phosphate, while the addition of the metals of the SW_P solution decreased this affinity.

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33

Liu, Jun Jian, Hong Yun Chen, Jing Tao Liu, Yu Xi Zhang, Guang Xing Huang, and Ji Chao Sun. "Characteristic of Phthalates Adsorption on the Organic Medium." Advanced Materials Research 599 (November 2012): 331–34. http://dx.doi.org/10.4028/www.scientific.net/amr.599.331.

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Phthalates were of heath concern in groundwater and drink water. In order to understand how Phthalates were transported at organic medium of the aquatic environment, adsorption experiments were conducted using sludge as organic adsorbents for adsorbing Di-n-butyl phthalate and Bis(2-Ethylhexyl) phthalate. As a result, The adsorption of Phthalates by the sludge displayed Freundlich adsorption characteristics, and the much larger Freundlich affinity coefficient for Bis(2-Ethylhexyl) phthalate than that for Di-n-butyl phthalate is an indication of higher affinity of the sludge particles for Bis(2-Ethylhexyl) phthalate. By Scanning electron microscope analysis of the sludge, in principle very porous structure of the sludge would not be the limit condition and multilayer adsorption would become possible.

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34

Gladytz, A., T. John, T. Gladytz, R. Hassert, M. Pagel, H. J. Risselada, S. Naumov, A. G. Beck-Sickinger, and B. Abel. "Peptides@mica: from affinity to adhesion mechanism." Physical Chemistry Chemical Physics 18, no. 34 (2016): 23516–27. http://dx.doi.org/10.1039/c6cp03325c.

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Molecular dynamics (MD) simulations of an interacting and adsorbing RTHRK peptide on a mica surface. (A) start; (B) 1 ns; (C) energy during interaction/adsorption process of the RTHRK peptide on mica; (D) 2 ns; (E) 20 ns; (F) 41 ns.

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35

Southichak, B., K. Nakano, M. Nomura, N. Chiba, and O. Nishimura. "Differences in adsorption mechanisms of heavy metal by two different plant biomasses: reed and brown seaweed." Water Science and Technology 59, no. 2 (January 1, 2009): 339–46. http://dx.doi.org/10.2166/wst.2009.867.

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The adsorption of Pb(II) by two different biomaterials, reed (Phragmites australis) and brown seaweed (Sargassum horneri) biomass pretreated with CaCl2, were compared in an attempt to explain the differences in adsorption performance between the two biosorbents. A very interesting characteristic was found in their individual adsorption performances; the Pb(II) adsorption capacity of brown seaweed (Qmax=0.45 mmol/g) was much higher than that of reed (Qmax=0.05 mmol/g), but its adsorption affinity (b=112 L/mmol) was much lower compared with that of reed (b=471 L/mmol). To elucidate the mechanism, the elemental components, ion exchange phenomenon and roles of functional groups of these two biosorbents were compared. The higher Pb(II) adsorption by brown seaweed could be due to its richness in total functional groups and calcium contents on its surface. In contrast, the functional complexity, higher zeta potential and pKa value (deprotonation state) of reed are believed to lead to its high adsorption affinity.

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36

Liu, Jiawei, Yingying Liu, Yixun Liang, Fen Ma, and Quan Bai. "Poly-l-lysine-functionalized magnetic graphene for the immobilized metal affinity purification of histidine-rich proteins." New Journal of Chemistry 45, no. 15 (2021): 6817–25. http://dx.doi.org/10.1039/d1nj00059d.

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Metal affinity-poly-l-lysine functionalization on a magnetic graphene substrate for simultaneously improving the adsorption selectivity toward histidine-rich proteins and inhibiting the non-specific adsorption.

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37

QIAO Jian-liang, 乔建良, 徐源 XU Yuan, 高有堂 GAO You-tang, 牛军 NIU Jun, and 常本康 CHANG Ben-kang. "Cs Adsorption Mechanism for Negative Electron Affinity GaN Photocathode." ACTA PHOTONICA SINICA 45, no. 4 (2016): 425001. http://dx.doi.org/10.3788/gzxb20164504.0425001.

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38

Wood, G. O. "Affinity coefficients of the Polanyi/Dubinin adsorption isotherm equations." Carbon 39, no. 3 (March 2001): 343–56. http://dx.doi.org/10.1016/s0008-6223(00)00128-7.

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39

Tang, Shouwan, Liang Kong, Junjie Ou, and Hanfa Zou. "Adsorption of Endotoxin on Polymyxin B Immobilized Affinity Matrices." Chinese Journal of Analytical Chemistry 34, no. 4 (April 2006): 455–59. http://dx.doi.org/10.1016/s1872-2040(06)60024-8.

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40

Wang, Jun, Guisen Wu, Wei Shi, Xin Liu, Changqing Ruan, Maoqiang Xue, and Dongtao Ge. "Affinity electromembrane with covalently coupled heparin for thrombin adsorption." Journal of Membrane Science 428 (February 2013): 70–77. http://dx.doi.org/10.1016/j.memsci.2012.11.015.

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41

Kamimura, Eliana Setsuko, Oscar Medieta, Maria Isabel Rodrigues, and Francisco Maugeri. "Studies on lipase-affinity adsorption using response-surface analysis." Biotechnology and Applied Biochemistry 33, no. 3 (June 1, 2001): 153. http://dx.doi.org/10.1042/ba20000081.

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42

Martins, Fernanda, Samantha C. Pinho, Terezinha C. A. Zollner, Ricardo L. Zollner, Marcel de Cuyper, and Maria Helena A. Santana. "Surface-modified magnetic colloids for affinity adsorption of immunoglobulins." Journal of Magnetism and Magnetic Materials 320, no. 13 (July 2008): 1867–70. http://dx.doi.org/10.1016/j.jmmm.2008.02.121.

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43

Forde, Gareth M., Siddhartha Ghose, Nigel K. H. Slater, Anna V. Hine, Richard A. J. Darby, and Anthony G. Hitchcock. "LacO-LacI interaction in affinity adsorption of plasmid DNA." Biotechnology and Bioengineering 95, no. 1 (2006): 67–75. http://dx.doi.org/10.1002/bit.20955.

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44

Akgöl, Sinan, Nilay Bereli, and Adil Denizli. "Magnetic Dye Affinity Beads for the Adsorption ofβ-Casein." Macromolecular Bioscience 5, no. 8 (August 12, 2005): 786–94. http://dx.doi.org/10.1002/mabi.200400230.

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Chase, Howard Allaker. "The use of affinity adsorbents in expanded bed adsorption." Journal of Molecular Recognition 11, no. 1-6 (December 1998): 217–21. http://dx.doi.org/10.1002/(sici)1099-1352(199812)11:1/6<217::aid-jmr426>3.0.co;2-d.

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Basar, Nilgün, Lokman Uzun, Ali Güner, and Adil Denizli. "Spectral characterization of lysozyme adsorption on dye-affinity beads." Journal of Applied Polymer Science 108, no. 6 (2008): 3454–61. http://dx.doi.org/10.1002/app.27972.

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Erickson, Anna C., and Gail V. W. Johnson. "Metal (Fe3+) affinity chromatography: differential adsorption of tau phosphoproteins." Journal of Neuroscience Methods 46, no. 3 (March 1993): 245–49. http://dx.doi.org/10.1016/0165-0270(93)90073-z.

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Shi, Wei, Fengbao Zhang, Guoliang Zhang, Liqin Jiang, Yongjiang Zhao, and Shulan Wang. "Polylysine-immobilized Affinity Nylon Membrane used for Bilirubin Adsorption." Molecular Simulation 29, no. 12 (December 2003): 787–90. http://dx.doi.org/10.1080/0892702031000121851.

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Labrou, Nikos E. "Optimization of Adsorption Conditions for Dye-Ligand Affinity Chromatography." Cold Spring Harbor Protocols 2006, no. 1 (January 1, 2006): pdb.prot4210. http://dx.doi.org/10.1101/pdb.prot4210.

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Sarı, Müfrettin Murat, Canan Armutcu, Nilay Bereli, Lokman Uzun, and Adil Denizli. "Monosize microbeads for pseudo-affinity adsorption of human insulin." Colloids and Surfaces B: Biointerfaces 84, no. 1 (May 2011): 140–47. http://dx.doi.org/10.1016/j.colsurfb.2010.12.025.

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