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[Adsorption of anthraquinone dyes by biosorbent GX2].

The GX2 growing mycelium shows excellent adsorptive capacity on the four kinds of anthraquinone dyes, however, due to the difference of molecular structure of dyes, the adsorption rates are different. Although the dyes show inhibiting effect on the growth of GX2, when the concentration of reactive brilliant blue KN-R is 250 and 400 mg/L, the adsorption rate of dye by the GX2 growing mycelium reaches 100% and 91.4%, respectively. With the increase of salinity (NaCl), the dry weight of GX2 mycelium increases; the diameter of granular mycelium decreases and its adsorption surface area increases accordingly, the salinity shows evident enhancement on the adsorption of reactive brilliant blue KN-R by GX2 growing mycelium in the range of 0%-2% salinity. The adsorption process is influenced by the concentration of carbon source as well, reactive brilliant blue KN-R with the concentration of 120 mg/L can be completely adsorbed only when the concentration of glucose is more than 2.5 g/L. The GX2 growing mycelium has better adsorptive capacity than resting living mycelium and dead mycelium.

Adsorption↗

[EXAFS studies on adsorption-desorption mechanism of Zn at delta-MnO2-water interface].

Microscopic structures of Zn(II) surface complexes adsorbed at a delta-MnO2-water interface were studied using extended X-ray absorption fine structure (EXAFS) spectroscopy. In a 0.1 mol/L NaNO3 solution of pH 5.50, Zn(II) was adsorbed onto the solid surface in the form of octahedral hydrous Zn(II) ions. The octahedral Zn(II) was linked to the structural unit of octahedral MnO6 of the delta-MnO2 surface by sharing the O atoms. The average bond length of RZn-O was (2.071 +/- 0.007)A (n = 3) and the Zn-Mn atomic distance was (3.528 +/- 0.006) A (n = 3), which corresponded to a corner-sharing linkage adsorption mode (weaker adsorption). Macroscopic adsorption-desorption isotherm experiments showed that, in contrast to that of Zn-manganite, adsorption of Zn(II) on delta-MnO2 was highly reversible and no apparent adsorption hysteresis was observed. EXAFS results indicated that the microscopic mechanism for the high adsorption reversibility was corresponded to the weak adsorption sites of corner sharing linkage between the adsorbate and adsorbent polyhedra.

Adsorption↗

Intensification of adsorption process by using the pyrolytic char from waste tires to remove chromium (VI) from wastewater.

Pyrolysis has the potential of transforming waste into valuable recyclable products. Pyrolytic char (PC) is one of the most important products from the pyrolysis of used tires. One of the most significant applications for pyrolytic char recovered is used for the removal of Cr(VI) in the wastewater effluent to control waste by waste. The surface chemistry properties of surface element distribution/concentration and chemical structure were examined for the pyrolytic char and the commercial activated carbon (CAC) respectively. The results showed that surfaces of PC possesses a large amount of ester and hydrocarbon graft, whereas there are mainly carbon functional components of C-OH, C=O and COOH on the surface of CAC. Therefore the surface electronegativity of PC is lower than that of CAC in the water. The repulsive interactions between the surfaces of PC and the negatively charged Cr(VI) ion are weaker than that of CAC, which results in an intensification of the adsorption process by the utilization of PC. The adsorption isotherms of Cr(VI) ion on the two kinds of carbons were determined experimentally. The larger adsorption amount on the PC in the case of Cr(VI) may be attributed mainly to its special surface micro-chemical environment. The mechanism of the removal Cr(VI) from aqueous solution was assumed to be the integration of adsorption and redox reaction. The adsorption was the rate-controlled step for Cr(VI) removal. The adsorption of Cr(VI) was identified as pseudo-second-order kinetics. The rate constants of adsorption were evaluated.

Adsorption↗

Adsorption of Pb, Cd to Fe, Mn oxides in natural freshwater surface coatings developed in different seasons.

Metal oxides( Fe, Mn oxides) in natural surface coatings(biofilms and associated minerals) are believed to play a significant role in the fate and transport of trace metal in aquatic environments. Seasonal variation of Fe, Mn oxides and organic materials in surface coatings, which were developed periodically on glass slides in Nanhu Lake, Jilin Province, China over the time frame of three seasons, was investigated in order to understand the influence of metal oxides on Pb and Cd adsorption to heterogeneous surface coating materials (biofilm). Pb and Cd adsorption was measured under controlled laboratory conditions(mineral salts solution with defined speciation, ionic strength 0.05 mol/L, 25 degrees C and pH 6.0). The classical Langmuir adsorption isotherm was applied to estimate equilibrium coefficients of Pb and Cd adsorption to the surface coatings. In general, components in the surface coatings varied greatly with seasons altering and obtained higher concentrations in summer while the content of iron oxides always exceeded that of manganese oxides. Correlation analyses between the maximum adsorption of Pb and Cd and components in the surface coatings developed periodically indicated that Pb phase association with Mn oxides and Cd phase association with Fe oxides as well as Mn oxides were statistically significant. Effect of Mn oxides on Cd adsorption was confirmed in view of its higher content in the surface coatings. The importance of ferromanganese oxides for Pb and Cd adsorption to the natural surface coatings developed in different seasons was evidenced.

Adsorption↗

[Phosphate adsorption characteristics onto the sediments from shallow lakes in the middle and lower reaches of the Yangtze River].

Adsorption isotherms and kinetics of phosphate onto the 11 sediments taken from shallow lakes in the middle and lower reaches of the Yangtze River were determined in laboratory, and the effect of physical and chemical properties of the sediments on its phosphate adsorption characteristics was also analyzed. The results indicate that: (1) The process of phosphate adsorption onto sediments mainly occurred within 0-10 h, the maximum adsorption rates occurred within 0-0.5 h, and then attends to a dynamic equilibrium; (2) Between the NAP and its organic matter, CEC, total phosphorus, inorganic phosphorus, organic phosphorus, Fe/Al-phosphorus and total nitrogen have remarkable positive correlation; between the maximum adsorption of phosphate and its CEC, inorganic phosphorus, organic matter and total phosphorus have remarkable negative correlation; between the total maximum adsorption of phosphate and its organic matter, CEC, total phosphorus, inorganic phosphorus, organic phosphorus, Fe/Al-phosphorus and total nitrogen have remarkable positive correlation; (3) As regards water quality of the shallow lakes in the middle and lower reaches of the Yangtze River at present, its sediment exists desorption. Between the adsorption-desorption equilibrium concentrations of phosphate onto the sediments and its organic matter, CEC, total nitrogen, the total phosphorus and the content of every form phosphorous have a remarkable positive correlation. Even the sediment from heavily polluted lake also has the tendency to release phosphate into the overlying water in this study.

Adsorption↗

[Adsorption performance of haloacetic acids onto 5 GACs from water].

Adsorption performance of 5 GACs were compared on two abundant haloacetic acids (HAAs) as disinfection by-products (dichloroacetic acid and trichloroacetic acid). The adsorption behaviours of the two HAAs were well correlated with Langmuir equation. When the two HAAs co-existed, trichloroacetic acid tended to be adsorbed more easily. The adsorption capacity of a foreign GAC-A for dichloroacetic acid was 4.4-5.7 times that of domestic GACs, and 3.8 times that of another foreign GAC-B, while the adsorption capacity of a foreign GAC-A for trichloroacetic acid was 4.0-5.4 times that of domestic GACs, and 2.6 times that of another foreign GAC-B. The equilibrium study of competitive adsorption between dichloroacetic acid and trichloroacetic acid on GAC-A demonstrates that the relative adsorption capacity of HAAs has a linear increase with their relative equilibrium concentration. The adsorption capacity for trichloroacetic acid is sensitive to changes at its equilibrium concentration greater than that for dichloroacetic acid.

Adsorption↗

Adsorption of catechol from aqueous solution by aminated hypercrosslinked polymers.

Adsorption of catechol from aqueous solution with the hypercrosslinked polymeric adsorbent NDA-100 and its derivatives AH-1, AH-2 and AH-3 aminated by dimethylamine, the commercial resin Amberlite XAD-4 and weakly basic anion exchanger resin D301 was compared. It was found that the aminated hypercrosslinked resins had the highest adsorption capacities among the tested polymers. The empirical Freundlich equation was successfully employed to describe the adsorption process. Specific surface area and micropore structure of the adsorbent, in company with tertiary amino groups on matrix affected the adsorption performance towards catechol. In addition, thermodynamic study was carried out to interpret the adsorption mechanism. Kinetic study testified that the tertiary amino groups on the polymer matrix could decrease the adsorption rate and increase the adsorption apparent activation energy.

Adsorption↗

Effects of phosphate on the adsorption of glyphosate on three different types of Chinese soils.

Glyphosate (GPS) is a non-selective, post-mergence herbicide that is widely used throughout the world. Due to the similar molecular structures of glyphosate and phosphate, adsorption of glyphosate on soil is easily affected by coexisting phosphate, especially when phosphate is applied at a significant rate in farmland. This paper studied the effects of phosphate on the adsorption of glyphosate on three different types of Chinese soils including two variable charge soils and one permanent charge soil. The results indicated that Freundlich equations used to simulate glyphosate adsorption isotherms gave high correlation coefficients (0.990-0.998) with K values of 2751, 2451 and 166 for the zhuanhong soil(ZH soil, Laterite), red soil(RS, Udic Ferrisol) and Wushan paddy soil (WS soil, Anthrosol), respectively. The more the soil iron and aluminum oxides and clay contained, the more glyphosate adsorbed. The presence of phosphate significantly decreased the adsorption of glyphosate to the soils by competing with glyphosate for adsorption sites of soils. Meanwhile, the effects of phosphate on adsorption of glyphosate on the two variable charge soils were more significant than that on the permanent charge soil. When phosphate and glyphosate were added in the soils in different orders, the adsorption quantities of glyphosate on the soils were different, which followed GPS-soil > GPS-P-soil = GPS-soil-P > P-soil-GPS, meaning a complex interaction occurred among glyphosate, phosphate and the soils.

Adsorption↗

[Effect of acid-base two steps surface modification on the adsorption of Cr(VI) onto activated carbon].

Effect of HNO3-NaOH two steps surface modification on the adsorption of Cr(VI) from aqueous solution onto activated carbon was evaluated. Activated carbon was oxidized in HNO3 aqueous solution at first (AC1), then treated in the mixture of NaOH and NaCl solution (AC2). Batch equilibrium and continuous adsorption experiments were conducted to determine the adsorption characteristics. Boehm titration method, element analysis were used to characterize the surface properties. N2/77 K adsorption isotherm method was used to characterize the pore structure. The results reveal that adsorption capacity and adsorption rate increase significantly, which in the following order: AC2>AC1>AC0. Surface modification caused BET surface area decreased and the total number of surface oxygen acid groups increased. First oxidation modification in HNO3 solution produced positive acid groups on the surface of activated carbon. Subsequent 2nd modification replaced H+ of carbon surface groups by Na+, the acidity of AC2 was decreased. The main cause of higher Cr(VI) adsorption capacity and rate for AC2 was the more oxygen surface acid groups, and suitable solution pH provide by surface groups.

Adsorption↗

[Capability of Cu2+ adsorption on cell surface of Pseudomonas putida 5-x].

Analysis of Cu2+ adsorption on cell surface of a Gram-negative bacterium P. putida 5-x was carried out. Isolated cell envelopes possess fivefold more Cu2+ adsorption capacity than that of the fresh intact cells. Experimental results also indicate that the content of the peptidoglycan layer, the outer membrane and inner membrane in the cell envelope is in order of inner membrane > outer membrane > PEG layer, while their Cu2+ adsorption capacity is in order of PEG layer > outer membrane > inner membrane. The total contribution of the separated PEG layer material to Cu2+ adsorption is no more than 15% part, and the cell outer membrane and inner membrane contribute about 30%-35% and 25%-30% part, respectively, to Cu2+ adsorption by the cell envelope. The relatively high phospholipid content in the outer wall might result in its higher adsorption capacity to Cu2+, and leads to a higher adsorption capacity of the cell envelope of P. putida 5-x.

Adsorption↗

[Kinetics of enhanced adsorption by polarization for organic pollutants on activated carbon fiber].

The adsorption kinetics for model pollutants on the activated carbon fiber (ACF) by polarization was investigated. Kinetics data obtained for the adsorption of these model pollutants at open-circuit and 400mV, -400mV polarization was applied to the Lagergren equation, and adsorption rate constants (Ka) were determined. With the anodic polarization of 400mV, the capacity of sodium phenoxide increases from 0.0083mmol x g(-1) at open-circuit to 0.18mmol x g(-1), and a seventeen-fold enhancement is achievable; however, the capacity of p-nitrophenol decreases from 2.93 mmol x g(-1) at open-circuit to 2.65 mmol x g(-1). With the cathodal polarization of -400mV, the capacity of aniline improves from 3.60 mmol x g(-1) at open-circuit to 3.88 mmol x g(-1); however, the capacity of sodium dodecylbenzene sulfonate reduces from 2.20 mmol x g(-1) at open-circuit to 1.59 mmol x g(-1). The enhancement for electrosorption changes with different groups substituting. Anodic polarization enhances the adsorption of benzene with electron-donating group. But whether anodic or not cathodal polarization has less effect on the adsorption of electron-accepting aromatic compounds, and decreases the adsorption of benzene bearing donor-conjugate bridge-acceptor but increases the adsorption rate. Electrostatic interaction plays a very important role in electrosorption of ion-pollutants.

Adsorption↗

[Adsorption of toluene and naphthalene on Beijing soils and its influence factor].

Static adsorption experiments were carried out to investigate the adsorption of toluene and naphthalene on Beijing soils, and to determine the influence of temperature and surfactants on adsorption. Although the affinity of petroleum hydrocarbons for seven soils is different, the adsorption isotherms of toluene and naphthalene on seven soils are well described by the Freundlich type. The adsorbed amount of naphthalene is higher than that of toluene on the same soil. High temperature doesn't benefit adsorption. Cetylrimethyl ammonium bromide (CTAB) and sodium dodecyl benzene sulfonate (SDBS) both have a positive effect on desorption of toluene and naphtalaene from soil. The desorption rate of toluene and naphthalene in the presence of CTAB and SDBS is 27.5%, 12.1% and 64.3%, 48.8%, respectively, which show that SDBS plays a much more important role in desorption than CTAB. The adsorbed quantities of toluene and naphthalene decrease with increasing SDBS concentration. When CTAB concentration is lower than the critical micelle concentration (CMC), adsorption increases with increasing CTAB concentration; When CTAB concentration is equal to or higher than CMC, adsorption decreases with increasing CTAB concentration.

Adsorption↗

The adsorption of quinine and quinidine to activated charcoal with and without magnesium sulfate.

The effect of magnesium sulfate on the in vitro adsorption of quinine and quinidine to activated charcoal (AC) was studied. Solutions of quinine and quinidine were prepared at concentrations of 5 and 10 micrograms/ml and at simulated toxic concentrations of 62.5, 125 and 250 micrograms/ml in distilled water. Drug-charcoal slurries were vortex mixed, centrifuged and analysed for free drug in the supernatant. Quinine had adsorption capacities of 78.2 to 100% with 12.5 or 50 mg AC; 12.5 or 50 mg AC adsorbed 29.5-87.2% of the quinidine. Quinine (250 micrograms/ml) had adsorption capacities of 0.0, 21.1, 52.4, 78.3 or 93.8% to 12.5, 50, 125, 250 or 500 mg AC, respectively. There was a corresponding increase quinine and quinidine adsorption at increasing concentrations of AC. The adsorption of quinine and quinidine seemed dose dependent. Magnesium sulfate (7.5 mg/ml) enhanced the adsorption of quinine to AC, but increased the amount of AC required for quinidine-charcoal adsorption.

Adsorption↗

[Adsorption of dyes as an indicator of the biological activity of mineral dust].

A study is made on the adsorption capacity of several types silicates and quartz dusts, prepared from pure mineral standards with respect to methylene blue and fuchsin. There are differences in the adsorption capacity of the minerals referring to unit surface. The quantity of the adsorption for samples of the same mineral, broken to pieces of different dispersity, also differs. However, between the adsorption capacity of test samples, divided into 3 groups--quartz, zeolite and mixed from the work environment, with respect to methylene blue, and their biological aggressiveness, tested "in vivo" after intratracheal test and the subcutaneous pocket method and the zeolite dusts on diploid culture, an inverse dependence is established. The adsorption capacity of the test dusts from the work environment is many times higher than the examined quartz and zeolite dusts, because of the presence of mineral components in them, especially argillaceous, which have high affinity toward the dye. The inverse dependence established between the adsorption capacity with respect to methylene blue and the biological effect of the tested dusts give grounds to propose the adsorption capacity as one of the induces for studying and hygienic evaluation of different types dusts, which have no components manifesting specific affinity to the dye.

Adsorption↗

[Differences in the allele state of genes controlling the specificity of adsorption in transposable phages of Pseudomonas aeruginosa].

To reveal possible differences in adsorptional specificities of transposable phages of Pseudomonas aeruginosa and to study the genetical control of this character, we isolated a group of phage-resistant P. aeruginosa mutants using some temperate and virulent phages. The study of resistance of the mutants to all the phages permitted us to find some types of mutants and to build a formal scheme of distribution of adsorptional receptors on the surface of P. aeurginosa cell. According to the results obtained, there are two main "receptor chains", where the receptors for all phages under study are grouped. For the majority of phages, just a single adsorptional receptor is obligatory, and at least two essential receptors are needed for adsorption of virulent phage E79. Two receptors were found also for another virulent phage, phi 11, one of them only being essential. Transposable phages can be grouped into three types, according to their adsorptional specificities. No correlations of adsorptional specificity types and all other characteristics of transposable phages studied (including the sub-groups of transposable phages belonging to different DNA homology types) were found. Genes of natural transposable phages controlling the differences in adsorptional specificities revealed can recombine in phage crosses.

Adsorption↗

Adsorption thermodynamics of acidic proline-rich human salivary proteins onto calcium apatites.

The thermodynamics of adsorption of four acidic proline-rich salivary proteins from their aqueous solutions onto hydroxyapatite (HA) and fluorapatite (FA) have been analyzed. Enthalpies and entropies of adsorption were derived from isotherms at 37 degrees C and 4 degrees C and led to the unexpected conclusion that adsorption of the macromolecules studied is an endothermic process. Consequently, adsorption is driven by an increase in entropy. Most of this increase originates in the adsorbate molecules, probably through disruption of internal ion pairs, hydrogen bonds, and displacement of water molecules. Integral free energies of adsorption (delta G) and the partial contributions of adsorbent and adsorbate were both calculated as a function of the adsorption coverages. For equal coverages (of each adsorbate), delta G is lower with FA than with HA. Most of the contribution to delta G originates from the adsorbate, although the adsorbent contribution becomes significant as adsorption saturation is approached. The differences in the various thermodynamic quantities are qualitatively related to the known structural features of the four proteins. The results are important in understanding the role played by the proline-rich proteins in the oral environment.

Adsorption↗

The effect of radiolabeling of human fibrinogen on its adsorption behaviour on a polystyrene surface.

Human fibrinogen (HFB) was labeled with different radioactive labels (Technetium -99m and iodine -125) in various ways. Characterization by chromatographic and electrophoretic methods did not show differences between the labeled and the nonlabeled proteins. The effect of the label and the labeling method on the adsorption behaviour of 99mTc and 125I labeled HFB at a polystyrene surface was investigated. In all cases labeled HFB showed preferential adsorption as compared to nonlabeled HFB. The preferential adsorption was expressed in terms of a factor ø (van der Scheer et al. 1978a), which will be 1, when no preferential adsorption occurs. 99mTc - and 125I - HFB showed ø values from 1.48 - 1.88. It is concluded that only meaningful adsorption experiments with labeled proteins can be performed when the possible occurrence of preferential adsorption has been investigated by appropriate methods. The results of prior work on protein adsorption at biomaterials using radiolabeled proteins have to be reconsidered.

Adsorption↗

Effect of pretreatment of wells in polystyrene plates on adsorption of some human serum proteins.

Coating of Immulon polystyrene plates with 0.2% casein in phosphate buffered saline (PBS) completely abolishes adsorption of human serum proteins to these plates. However, pretreatment of such plates with PBS or 0.15 M NaCl in deionized water (10 microS) before coating makes possible adsorption of human immunoglobulins G (HIgG) and M but not serum albumin (HSA) and transferrin (HTrf). Effect of pretreatment with PBS on adsorption of HIgG is long-term and rather stable. Results of experiments with radioiodinated HIgG, mouse IgG, HSA and human chorionic gonadotropin confirm the peculiar effect of pretreatment with PBS on casein coating. Pretreatment with deionized water, instead of PBS, markedly diminish adsorption but tap or commercial spring waters (> 1000 microS), even without 0.15 M NaCl, affect adsorption similarly to PBS in deionized water. Super pure water (0.05 microS) even with NaCl used for pretreatment does not influence adsorption of HIgG to plates coated with casein. Distinct differences in adsorption of HIgG and HTrf was demonstrated using solutions for ELISA prepared from super pure, deionized and tap waters.

Adsorption↗