Informacja

Drogi użytkowniku, aplikacja do prawidłowego działania wymaga obsługi JavaScript. Proszę włącz obsługę JavaScript w Twojej przeglądarce.

English (EN)·Polski (PL)·Yкраїнський (UK)
Przejdź do strony domowej biblioteki Centralna Biblioteka Wojskowa Link otwiera się w nowym oknie Logo biblioteki Prolib Integro - strona głównaCentralna Biblioteka Wojskowa

Wyszukujesz frazę "phenol adsorption" wg kryterium: Temat

  Lista filtrów
Wyrównaj
Wyświetlanie 1-15 z 19
Tytuł:
Effect of textural and chemical characteristics of activated carbons on phenol adsorption in aqueous solutions
Autorzy:
Vargas, D. P.
Giraldo, L.
Moreno-Piraján, J. C.
Powiązania:
https://bibliotekanauki.pl/articles/779420.pdf
Data publikacji:
2017
Wydawca:
Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:
activated carbon monoliths
phenol adsorption
textural and chemical characteristics
immersion calorimetry
Opis:
The effect of textural and chemical properties such as: surface area, pore volume and chemical groups content of the granular activated carbon and monoliths on phenol adsorption in aqueous solutions was studied. Granular activated carbon and monolith samples were produced by chemical activation. They were characterized by using N2  adsorption at 77 K, CO2  adsorption at 273 K, Boehm Titrations and immersion calorimetry in phenol solutions. Microporous materials with different pore size distribution, surface area between 516 and 1685 m2  g−1  and pore volumes between 0.24 and 0.58 cm3  g−1  were obtained. Phenol adsorption capacity of the activated carbon materials increased with increasing BET surface area and pore volume, and is favored by their surface functional groups that act as electron donors. Phenol adsorption capacities are in ranged between 73.5 and 389.4 mg · g−1 .
Źródło:
Polish Journal of Chemical Technology; 2017, 19, 4; 87-93
1509-8117
1899-4741
Pojawia się w:
Polish Journal of Chemical Technology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Adsorpcja fenolu w ciekłej fazie fluidalnej na adsorbencie polimerowym Amberlite XAD-4
Adsorption of phenol in liquid fluidised phase on Amberlite XAD-4 polymeric adsorbent
Autorzy:
Nastaj, J.
Kamińska, A.
Witkiewicz, K.
Powiązania:
https://bibliotekanauki.pl/articles/2071133.pdf
Data publikacji:
2010
Wydawca:
Stowarzyszenie Inżynierów i Techników Mechaników Polskich
Tematy:
adsorpcja fenolu
faza fluidalna ciekła
adsorbent polimerowy XAD-4
modelowanie matematyczne
phenol adsorption
liquid fluidized phase
Amberlite XAD-4 polymeric adsorbent
mathematical modelling
Opis:
Przeprowadzono badania równowagi i kinetyki procesu adsorpcji w ciekłej fazie fluidalnej w układzie: fenol - woda - adsorbent polimerowy Amberlite XAD-4. Model matematyczny procesu adsorpcji ciecz - ciało stałe w złożu fluidalnym bazuje na wartościach współczynników dyspersji osiowej fenolu w fazie ciekłej i fazie stałej, współczynnika przenikania masy oraz warunkach izotermicznych. Przeprowadzona weryfikacja eksperymentalna rezultatów symulacji komputerowej modelu wykazała dobrą zgodność.
The adsorption equilibrium and kinetic investigations of liquid - solid fluidized bed adsorption process in phenol — water — polymeric adsorbents Amberlite XAD-4 system are presented. A mathematical model of liquid -- solid fluidized bed adsorption was developed based on liquid and solid phase axial dispersion coefficients, overall mass transfer coefficients and isothermal conditions. Comparisons of modelling results (computer simulation) with observed experimental data were performed giving fairly good agreement.
Źródło:
Inżynieria i Aparatura Chemiczna; 2010, 3; 85-86
0368-0827
Pojawia się w:
Inżynieria i Aparatura Chemiczna
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Adsorption of Phenol from Water on Natural Minerals
Autorzy:
Puszkarewicz, A.
Kaleta, J.
Papciak, D.
Powiązania:
https://bibliotekanauki.pl/articles/123900.pdf
Data publikacji:
2018
Wydawca:
Polskie Towarzystwo Inżynierii Ekologicznej
Tematy:
phenol
adsorption
attapulgite
alganite
Opis:
Phenol and its derivatives (chlorophenol, nitrophenol, methylphenol, cresol etc.) belong to highly toxic contaminants, and their occurrence in industrial and municipal sewage as well as in groundwater carries a high threat to the environment and human health. Elimination of such contaminants is one of the major challenges in solving the global environmental problems. Implementation of pro-ecological methods of water treatment is associated with the use of natural, cheap and unprocessed materials, with the possibility of their repeated use. The article presents the results of the studies on the use of powdery adsorbents for the removal of phenol from aqueous solutions. The following natural minerals were used: attapulgite – Abso'net Superior Special (ASS) and alganite – Abso'net Multisorb (AM). Tests were performed under non-flowing conditions, in series, depending on the type and dose of adsorbents. Tests were conducted on a model solution of phenol with the initial concentration of C0 = 20 mg /dm3, at the temp. of 20° C. Alganite mineral (AM) proved to be effective in adsorption of phenol. Maximum adsorption capacity P = 0.21 g/g, was obtained for a dose 10 mg/dm3. Almost complete removal of phenol (99.9%) was obtained for a dose of 500 mg/dm3. For natural attapulgite – Abso'net Superior Special (ASS) the maximum adsorption capacity (at a dose 5 mg/dm3) amounted to P = 0.15 g/g. The efficiency of phenol removal at the level 99% was obtained at a dose of 1000 mg/dm3).
Źródło:
Journal of Ecological Engineering; 2018, 19, 6; 132-138
2299-8993
Pojawia się w:
Journal of Ecological Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Pretreatment of coking wastewater by an adsorption process using fine coking coal
Autorzy:
Gao, L.
Li, S.
Wang, Y.
Gui, X.
Xu, H.
Powiązania:
https://bibliotekanauki.pl/articles/110417.pdf
Data publikacji:
2016
Wydawca:
Politechnika Wrocławska. Oficyna Wydawnicza Politechniki Wrocławskiej
Tematy:
coking coal
coking wastewater
adsorption
COD
phenol
Opis:
A new technique for pretreatment of coking wastewater is introduced based on the concept of circular economy. Coal is fed into a coking system after adsorption. This study validates the feasibility of using coking coal to adsorb organic pollutants in coking wastewater. The sorption kinetics and equilibrium sorption isotherms of coking coal for removal of chemical oxygen demand (COD) and phenol from coking wastewater was also discussed in this paper. Gas chromatograph/mass spectroscopy (GC/MS) was used to detect changes in the quality of coking wastewater. The results showed that when coking coal dosage was 120 g/dm3, 65% of COD and 34% of phenol in waste water can be removed after 40 min of agitation. The surface functional groups of coking coal before and after adsorption were observed with a Fourier transform infrared spectrometer. The kinetics of COD and phenol adsorption from coking wastewater by coking coal fitted the pseudo second-order model. The adsorption process of coking coal can be classified into two categories, namely, rapid and slow. The Freundlich isotherm provided a better fit with all adsorption isotherms than the Langmuir isotherm. Coking coal could be a suitable low-cost adsorbent for recalcitrant organic pollutants.
Źródło:
Physicochemical Problems of Mineral Processing; 2016, 52, 1; 422-436
1643-1049
2084-4735
Pojawia się w:
Physicochemical Problems of Mineral Processing
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Removal of Octyl Phenol Ethoxylate (OPE) Using Processed and Unprocessed Industrial Biological Waste Sludge
Autorzy:
Dinçer, Ali Rıza
Aral, İbrahim Feda
Powiązania:
https://bibliotekanauki.pl/articles/1845422.pdf
Data publikacji:
2021
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
waste sludge
adsorption
octyl phenol ethoxylate
pyrolyzed sludge
Opis:
This study investigated the Octyl Phenol Ethoxylate (OPE) removal potentials of raw and treated industrial treatment sludges (ITS) at different pH. Experiments were conducted in a set of 500 ml Erlenmeyer flasks, into which OPE solutions of 300 ml with different initial concentrations (50-300 μg/l) were added into. Adsorption of Octyl Phenol Ethoxylate from an aqueous solution into ITS105 (T=105°C), ITS300 (T=300°C), ITS600 (T=600°C) and ITS450 (pyrolyzed, T=450°C) was carried out at a room temperature. The OPE adsorption rate increase in the treatment sludge processed at 600°C. As opposed to the sludge treated at 105°C, the adsorption rate decreased as the concentration increased. The reason for this was that the porous structure was degraded at 600°C, and the surface charge balance was disrupted. ITS300 had a lower adsorption capacity for Octyl Phenol Ethoxylate removal than ITS105, ITS600 and ITS450 (pyrolyzed). The treatment sludge pyrolyzed at 450°C conformed with the Freundlich isotherm at pH 4 (R2=0.94) and pH 7 (R2=0.89). The treatment sludge heat-treated at 600°C conformed with the Freundlich isotherm at pH 4 (R2=0.97), pH 7 (R2=0.98) and pH 10 (R2=0.99). Additionally, for ITS600, the Brunauer, Emmett and Teller (BET) isotherm was valid at neutral pH. The OPE adsorption coefficient for ITS600 at pH 4 and pH 7 was calculated as 1.05 L/μg and 1.083 L/μg, respectively. According to the BET isotherm (for ITS600) the qm values at pH 4 and pH 7 were respectively 8.21 μg/g and 2.92 μg/g. The temperature of the adsorption value obtained with the Temkin isotherm showed that the interaction between the OPE and the adsorbent substances was not a chemical or ionic interaction but probably a physical interaction.
Źródło:
Archives of Environmental Protection; 2021, 47, 1; 53-60
2083-4772
2083-4810
Pojawia się w:
Archives of Environmental Protection
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Uptake of phenol from aqueous solution by burned water hyacinth
Autorzy:
Uddin, M.T.
Islam, M.S.
Islam, M.A.
Abedin, M.Z.
Powiązania:
https://bibliotekanauki.pl/articles/779654.pdf
Data publikacji:
2008
Wydawca:
Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:
fenol
adsorpcja
równowaga
kinetyka adsorpcji
phenol
adsorption
burned water hyacinth
equilibrium
adsorption kinetics
Opis:
The potential of burned water hyacinth (BWH) for phenol adsorption from aqueous solution was studied. Batch kinetic and isotherm studies were carried out under varying experimental conditions of contact time, phenol concentration, adsorbent dosage and pH. The pH at the point of zero charge (pH(PZC)) of the adsorbent was determined by the titration method and the value of 8.8 š 0.2 was obtained. The FTIR of the adsorbent was carried out in order to find the potential adsorption sites for the interaction with phenol molecules. The Freundlich and Langmuir adsorption models were used for the mathematical description of adsorption equilibrium and it was found that the experimental data fitted very well to the Langmuir model. Maximum adsorption capacity of the adsorbent was found to be 30.49 mg/g. Batch adsorption models, based on the assumption of the pseudo-first-order and pseudo-second-order models, were applied to examine the kinetics of the adsorption. The results showed that kinetic data closely followed the pseudo-second-order model.
Źródło:
Polish Journal of Chemical Technology; 2008, 10, 2; 43-49
1509-8117
1899-4741
Pojawia się w:
Polish Journal of Chemical Technology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Simultaneous removal of phenol and Cu(II) from wastewater by tallow dihydroxyethyl betaine modified bentonite
Autorzy:
Hu, Xiangyang
Wang, Bao
Yan, Gengsheng
Ge, Bizhou
Powiązania:
https://bibliotekanauki.pl/articles/2203123.pdf
Data publikacji:
2022
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
simultaneous adsorption
tallow dihydroxyethyl betaine
bentonite
Cu(II)
phenol
Opis:
An organobentonite modified with an amphoteric surfactant, tallow dihydroxyethyl betaine (TDHEB), was used as an adsorbent to simultaneously remove Cu(II) and phenol from wastewater. The characteristic of the organobentonite (named TDHEB-bentonite) was analyzed by X-ray diffraction, Fourier-transform infrared spectra and nitrogen adsorption-desorption isotherm. Batch tests were conducted to evaluate the adsorption capacities of TDHEB-bentonite for the two contaminants. Experiment results demonstrated that the adsorption of both contaminants is highly pH-dependent under acidic conditions. TDHEB-bentonite had about 2.0 and 5.0 times higher adsorption capacity toward Cu(II) and phenol, respectively, relative to the corresponding raw Na-bentonite. Adsorption isotherm data showed that the adsorption processes of both contaminants were well described by Freundlich model. Kinetic experiment demonstrated that both contaminants adsorption processes correlated well with pseudo-second-order model. Cu(II) had a negative impact on phenol adsorption, but not vice versa. Cu(II) was removed mainly through chelating with the organic groups (-CH2CH2OH and -COO-) of TDHEB. Otherwise, partition into the organic phase derived from the adsorbed surfactant was the primarily mechanism for phenol removal. Overall, TDHEB-bentonite was a promising adsorbent for removing Cu(II) and phenol simultaneously from wastewater.
Źródło:
Archives of Environmental Protection; 2022, 48, 3; 37--47
2083-4772
2083-4810
Pojawia się w:
Archives of Environmental Protection
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Minimization of phenol by natural occurrence adsorbent
Autorzy:
Joshi, J.
Sahu, O.
Powiązania:
https://bibliotekanauki.pl/articles/10823.pdf
Data publikacji:
2014
Wydawca:
Przedsiębiorstwo Wydawnictw Naukowych Darwin / Scientific Publishing House DARWIN
Tematy:
alga
clay
phenol
natural adsorbent
effluent adsorbent
adsorption
environment pollution
Opis:
Phenol and chlorophenols are long-lived pollutants frequently found in industrial effluents. Phenols are widely used for the commercial production of a wide variety of resins including phenolic resins, epoxy resins and adhesives, and polyamide for various applications. Adsorption process has been proven one of the best water treatment technologies around the world and the removal of diverse types of pollutants from water. However, widespread use of commercial adsorbent is sometimes restricted due to its higher costs. Attempts have been made to develop inexpensive adsorbents utilizing for the reduction of phenol from water. Four types of adsorbent clay, algae, moringa oleifera and rice husk has been used. Among all rice husk shown 97 % of phenol adsorption at 1mm particle size, pH 4, 3 g/l dosing and 150min contact time.
Źródło:
International Letters of Natural Sciences; 2014, 11, 1
2300-9675
Pojawia się w:
International Letters of Natural Sciences
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Phenol Biosorption from Polluted Aqueous Solutions by Ulva lactuca Alga Using Batch Mode Unit
Autorzy:
Abbas, Mohammed Nsaif
Al-Hermizy, Suadat Mustafa Mohammed
Abudi, Zaidun Naji
Ibrahim, Thekra Atta
Powiązania:
https://bibliotekanauki.pl/articles/124215.pdf
Data publikacji:
2019
Wydawca:
Polskie Towarzystwo Inżynierii Ekologicznej
Tematy:
sea lettuce
Ulva lactuca
adsorption
phenol
aqueous solutions
isotherm
thermodynamic
Opis:
This paper is related to study the using sea lettuce (Ulva lactuca) as a low-cost adsorbent for removing the phenol compounds from aqueous solutions by adsorption under different operating conditions in a batch unit. The SEM and FTIR tests were performed to determine the morphological characteristics and the functional groups existing on the adsorbent material, respectively, while the surface area was identified by means of two techniques which were blue color method and BET method. The results of the adsorption experiments showed that the efficiency of the removal process is inversely proportional with initial concentration of phenol, pH and temperature; while the efficiency was directly proportional to adsorbent amount, agitation speed and treatment time. The results showed that the percentage of removal of phenol from processed water solutions ranged from 25.446% to 90.125%. The Langmuir and Freundlich isotherm models were chosen to estimate the amounts of phenol adsorption by the sea lettuce powder. The kinetic study shows that the adsorption was obeyed pseudo second order also the thermodynamic parameters were calculated.
Źródło:
Journal of Ecological Engineering; 2019, 20, 6; 225-235
2299-8993
Pojawia się w:
Journal of Ecological Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Usuwanie fenolu na węglach aktywnych otrzymanych z paku antracenowego
Phenol Removal on Anthracene Pitch-based Activated Carbon
Autorzy:
Lorenc-Grabowska, E.
Torchała, K
Machnikowski, J.
Powiązania:
https://bibliotekanauki.pl/articles/297248.pdf
Data publikacji:
2013
Wydawca:
Politechnika Częstochowska. Wydawnictwo Politechniki Częstochowskiej
Tematy:
węgle aktywne z paku
adsorpcja
fenol
pitch-based activated carbons
adsorption
phenol
Opis:
W pracy zbadano zdolność węgla aktywnego otrzymanego z paku antracenowego do adsorpcyjnego usuwania fenolu. W celach porównawczych zastosowano również komercyjny węgiel aktywny otrzymany z łupin orzecha kokosowego. Węgle scharakteryzowano w oparciu o analizę techniczną, elementarną oraz sorpcję azotu w 77 K. Badane węgle są węglami typowo mikroporowatymi. Adsorpcję fenolu przeprowadzono w warunkach statycznych w temperaturze pokojowej. Wyznaczono czasy osiągania stanu równowagi oraz nadmiarowe izotermy adsorpcji, które scharakteryzowano w oparciu o równania Langmuira i Freundlicha. Stwierdzono, że węgle aktywne otrzymane z paku adsorbują fenol lepiej niż komercyjny węgiel aktywny. Zaobserwowano, że sorpcja w monowarstwie wyznaczona z równania Langmuira zależy od objętości porów o szerokości mniejszej niż 1,4 nm.
The adsorptive properties of anthracene pitch-based powder activated carbons (AACs) towards the phenol removal have been studied. The AACs were prepared by steam or CO2 activation of the preoxidized precursor. Different methods of pitch preoxidation were used, i.e. air oxidation and wet oxidation with mixture of sulfuric/nitric acid, and sulfuric acid/peroxide. For comparison the commercial activated carbon from coconut shell has been used (OK). The studied ACs have been characterized in terms of proximate, elemental analysis and porous texture. The studied activated carbons are predominantly microporous. The AACs are almost ash free with slightly acidic surface characteristics. The OK has low ash content and slightly basic surface characteristics. The heteroatoms content N+O is comparable for AACs whereas the OK has the lowest heteroatom content. The phenol adsorption processes were carried out in static condition at ambient temperature. The equilibrium time and equilibrium sorption isotherms were determined. The equilibrium time varied from 8 to 48 hours. The Langmuir and Freundlich models were applied to interpret the data. The sorption capacity of AACs was twofold higher than the sorption capacity of the commercial OK. The correlation between the Langmuir sorption capacity and volume of pores smaller than 1.4 nm were observed.
Źródło:
Inżynieria i Ochrona Środowiska; 2013, 16, 3; 303-312
1505-3695
2391-7253
Pojawia się w:
Inżynieria i Ochrona Środowiska
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Effect of Zeolite and Activated Carbon Thickness Variation as Adsorbent Media in Reducing Phenol and Manganese Levels in Wastewater of Non-Destructive Testing Unit
Autorzy:
Fikri, Elanda
Farid, Reta Athaya Mutiara
Septiati, Yosephina Ardiani
Djuhriah, Nanny
Hanurawaty, Neneng Yetty
Khair, Amar Sharaf Eldin
Powiązania:
https://bibliotekanauki.pl/articles/2173279.pdf
Data publikacji:
2022
Wydawca:
Polskie Towarzystwo Inżynierii Ekologicznej
Tematy:
NDT wastewater
non-destructive testing wastewater
adsorption
zeolite
activated carbon
phenol
manganese
Opis:
The production wastewater contains phenol from the Non-Destructive Testing (NDT) unit because it uses solvents; meanwhile, the manganese originates from the metal material washing process. On the basis of laboratory test results, the wastewater originating from the NDT unit of Y Industry, resulted in a phenol level of 2.33 mg/L, exceeding the quality standard of 0.5 mg/L and manganese level of 14.13 mg/L that exceeded the quality standard of 2 mg/L, based on the Regulation of the Minister of the Environment Number 5 of 2014 concerning Wastewater Quality Standards. This research used the pretest-posttest experimental research design without control. The sample in this study was wastewater from the NDT unit of the Y Industry. The average phenol level after passing through the adsorbent media at a thickness of 40 cm, 60 cm, and 80 cm resulted in 0.99 mg/L with 63% reduction, 0.60 mg/L with 77% reduction, and 0,28 mg/L with 89% reduction, respectively. The average manganese level after passing through the adsorbent media at a thickness of 40 cm, 60 cm, and 80 cm resulted in 0.10 mg/L with 61% reduction, 0.06 mg/L with 76% reduction, and 0,05 mg/L with 80% reduction, respectively. The most effective thickness variation in reducing the phenol and manganese levels of NDT wastewater is 80 cm thickness.
Źródło:
Journal of Ecological Engineering; 2022, 23, 8; 40--48
2299-8993
Pojawia się w:
Journal of Ecological Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Covalent immobilization of laccase on Fe3O4-graphene oxide nanocomposite for biodegradation of phenolic compounds
Autorzy:
Rouhani, Shamila
Azizi, Shohreh
Maaza, Malik
Mamba, Bhekie
Msagati, Titus A. M.
Powiązania:
https://bibliotekanauki.pl/articles/2032944.pdf
Data publikacji:
2021
Wydawca:
Politechnika Wrocławska. Oficyna Wydawnicza Politechniki Wrocławskiej
Tematy:
phenol
adsorption
biodegradation
Fe3O4
Trametes versicolor
laccase
fenol
adsorbcja
biodegradacja
lakaza
Opis:
Laccase from Trametes Versicolor (E.C. 1.10.3.2) was immobilized on the Fe3O4–graphene hybrid nanocomposite through the covalent attachment method (Lac/Fe3O4/GO). The effect of immobilization conditions on the activity and recovered activities such as contact time, the concentration of glutaraldehyde and enzyme was evaluated. The recovered activity of the immobilized laccase on the Fe3O4–graphene oxide nanocomposite was ca. 86%. Immobilized laccase unlike free laccase retained the activity and exhibited higher resistance to temperature and pH changes and also improved storage and thermal stability. Approximately 70% of relative activity for immobilized laccase was remained after being incubated for 2 h at 55 °C, but free laccase only remained 48%. Immobilized laccase retained 88% of initial activity after storage for 20 days, however, the free laccase only 32%. Finally, Lac/Fe3O4/GO capability was evaluated by the oxidation of phenol, p-chlorophenol, and 2,4-dichlorophenol. Lac/Fe3O4/GO was characterized by SEM, EDX, FT-IR, and AGFM.
Źródło:
Environment Protection Engineering; 2021, 47, 1; 85-99
0324-8828
Pojawia się w:
Environment Protection Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Adsorpcja fenoli z roztworów wodnych na pylistych węglach aktywnych
Adsorption of phenols from aqueous solutions on powdered activated carbons
Autorzy:
Dąbek, L.
Kuśmierek, K.
Świątkowski, A.
Powiązania:
https://bibliotekanauki.pl/articles/297684.pdf
Data publikacji:
2016
Wydawca:
Politechnika Częstochowska. Wydawnictwo Politechniki Częstochowskiej
Tematy:
phenol
4-cresol
adsorption
powdered activated carbon
fenol
4-krezol
adsorpcja
pylisty węgiel aktywny
Opis:
The adsorption process by solid adsorbents is one of the most efficient methods for the removal of organic pollutants from water. Adsorption is attractive for its relative flexibility and simplicity of design, low cost, ease of operation and regeneration. Activated carbons are now the most commonly used adsorbents of proven adsorption efficiency for organic compounds due to their physicochemical properties including specific surface area, pore volume, pore size distribution and surface chemistry. For water treatment on a commercial scale granular activated carbon is most commonly used. In this paper the adsorption of phenol (Ph) and 4-cresol (4K) from aqueous solutions on powdered activated carbons (PAC) was studied. As adsorbents, two activated carbons L2S and SX2 with similar physicochemical properties were used. The adsorption was studied in a batch adsorption system, including both kinetics and equilibrium. The kinetics was fitted with the pseudo-first order and pseudo- second order models. The adsorption kinetics was found to follow the pseudo-second order model with the coefficient of determination values greater than 0.99. The adsorption isotherms were determined and modeled with the Freundlich and Langmuir equations. The equilibrium data obtained for both adsorbates were better described by the Langmuir model than by the Freundlich isotherm model. It was found that the 4K was adsorbed better than Ph on both adsorbents. The adsorption capacities of the L2S and SX2 activated carbons towards phenols were comparable. The values of the Langmuir adsorption capacity qm for phenol were 1.634 and 1.591 mmol/dm3 for the L2S and SX2 activated carbons, respectively. The qm values for 4-cresol were 1.885 and 1.844 mmol/dm3 for the L2S and SX2, respectively. The influence of solution pH on the adsorption was also investigated. The adsorption of the Ph and 4K was almost constant from the pH 2 to 8, and decreased significantly with further increase in the pH (above the pKa of the adsorbates and pHPZC of the adsorbents).
W pracy porównano właściwości adsorpcyjne dwóch pylistych węgli aktywnych (L2S i SX2) o zbliżonych właściwościach fizykochemicznych jako adsorbentów do usuwania fenolu i 4-krezolu z roztworów wodnych. Zbadano kinetykę adsorpcji, adsorpcję w warunkach równowagowych oraz wpływ pH roztworu. Adsorpcja obydwu adsorbatów przebiegała zgodnie z modelem kinetycznym pseudo 2. rzędu, a w warunkach równowagowych była dobrze opisana równaniem izotermy Langmuira. W każdym przypadku 4-krezol adsorbował się szybciej i z większą wydajnością niż fenol. Różnice w pojemnościach adsorpcyjnych poszczególnych pylistych węgli aktywnych były niewielkie. Adsorpcja utrzymywała się na stałym poziomie w środowisku o pH od 2 do 8, jej znaczny spadek był obserwowany w wysokich wartościach pH (> 8), powyżej wartości pKa adsorbatów i pHPZC adsorbentów.
Źródło:
Inżynieria i Ochrona Środowiska; 2016, 19, 2; 217-226
1505-3695
2391-7253
Pojawia się w:
Inżynieria i Ochrona Środowiska
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Analiza adsorpcji fenolu na surowych i modyfikowanych diatomitach karpackich
Analysis of phenol adsorption on raw and rnodified carpathian diatomite
Autorzy:
Puszkarewicz, A.
Powiązania:
https://bibliotekanauki.pl/articles/106662.pdf
Data publikacji:
2010
Wydawca:
Towarzystwo Chemii i Inżynierii Ekologicznej
Tematy:
fenol
adsorpcja
filtracja
surowy diatomit
modyfikowany diatomit
phenol
adsorption
filtration
raw diatomite
surface-modified diatomite
Opis:
Dwa naturalne adsorbenty diatomitowe (surowy i modyfikowane powierzchniowo) zostały użyte do usuwania związków fenolu z roztworów wodnych. Właściwości adsorpcyjne diatomitów zostały określone metodą statyczną i dynamiczną. Badania przeprowadzono na modelowym roztworze fenolu o stężeniu początkowym C0 = 20 mg/dm3 dla temp. 20°C. Przeprowadzona modyfikacja surowego diatomitu związkami manganu zwiększyła jego powierzchnię właściwą o 80% i zmieniła strukturę powierzchni. Dla obu testowanych diatomitów proces adsorpcji dobrze opisywały izotermy adsorpcji Freundlicha. Zdecydowanie lepszym adsorbentem (większą pojemnością adsorpcyjną) wykazał się diatomit modyfikowany D-Mn. W badaniach stwierdzono, że adsorpcja fenolu nieco lepiej zachodziła przy odczynie kwaśnym. Usuwanie fenolu w warunkach dynamicznych, w procesie filtracji na złożu D-Mn, z czasem kontaktu tk = 9 min, okazało się bardzo skuteczne. Pojemność adsorpcyjną w punkcie przebicia złoża wyniosła Pp = 12,6 mg/g. Diatomit D-Mn może być przydatny do oczyszczania wody lub ścieków zawierających fenol.
Two natural diatomite adsorbents (raw and surface-modified diatomite) were used for removing phenol compounds from water solutions. The adsorptive properties of diatomite have been determined using static and dynamie methods. The tests were performed with a model solution of phenol at initial concentration of C0 = 20 mg/dm3, at the temperature of 20°C. A modification of raw diatomite with manganese increased its specific surface area by 80% and changed its surface srructure. For both tested diatomite grades the adsorption processes were described adequately by Freundlich adsorption isotherms. Modified diatomite, D-Mn, exhibited markedly better adsorbent properties (including higher adsorptive capacity). The tests showed that phenol adsorption proceeded slightly better in acid environment. Phenol removal in dynamie conditions, in a process of flltration on D-Mn bed, with contact time of tk = 9 min, appeared very effective. The adsorptive capacity at bed breakthrough point was PMn = 12.6 mg/g. The test conducted within the project showed that the D-Mn diatomite could be useful for conditioning of water or wastewater containing phenol.
Źródło:
Chemistry-Didactics-Ecology-Metrology; 2010, 15, 2; 189-193
2084-4506
Pojawia się w:
Chemistry-Didactics-Ecology-Metrology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Sorpcja fenolu z roztworów wodnych na konwencjonalnych i niekonwencjonalnych sorbentach
Phenol sorption from water solution onto conventional and unconventional sorbents
Autorzy:
Dudziak, M.
Werle, S.
Powiązania:
https://bibliotekanauki.pl/articles/297793.pdf
Data publikacji:
2015
Wydawca:
Politechnika Częstochowska. Wydawnictwo Politechniki Częstochowskiej
Tematy:
fenol
wysuszony osad ściekowy
popiół
sorpcja
izotermy adsorpcji
phenol
dried sewage sludge
ash
sorption
adsorption isotherms
Opis:
Badania własne przedstawione w niniejszej pracy dotyczą procesu sorpcji fenolu z wody na wysuszonych osadach ściekowych i na stałych produktach ubocznych powstających podczas procesu ich zgazowania (popiół). Zgazowanie jest obiecującą metodą termicznego zagospodarowania palnych substancji organicznych, niemniej jednak wciąż nierozwiązanym problemem jest sposób zagospodarowania powstających stałych produktów odpadowych. W ramach badań statyki procesu określono zarówno zdolność sorpcyjną, jak i czas osiągnięcia stanu równowagi fenolu na badanych materiałach sorpcyjnych. Badano także wpływ początkowego stężenia fenolu na jego pojemność sorpcyjną. Do matematycznego opisu sorpcji wykorzystano równania Langmuira oraz Freundlicha. Zakres pracy obejmował również ocenę zjawiska uwalniania z materiałów adsorpcyjnych pierwotnych substancji nieorganicznych i organicznych wraz z wyznaczeniem efektu toksycznego roztworu, stosując metody pośrednie. W podsumowaniu pracy, bazując na rezultatach wyników badań eksperymentalnych oraz różnych źródłach literaturowych, porównano pojemność sorpcyjną fenolu na konwencjonalnych i niekonwencjonalnych sorbentach.
The use of adsorption methods in wastewater treatment allows achieving high quality levels of the streams discharged into the environment. This is particularly taking into account the presence of different toxic and hazardous organic and inorganic substances in the wastewater. This problem applies to both municipal wastewater after mechanical-biological treatment as well as to industrial wastewater. Active carbon is the most commonly used for this purpose. However, novel opportunities are sought, including, for example, the use of waste (with appropriate physicochemical characteristics) as sorbents. The studies presented in this paper are related to the process of sorption of phenol from water on the dried sewage sludge and solid by-products generated during the gasification process (ash). Gasification is a promising method of thermal management of combustible organic substances. Nevertheless, there is still an unresolved problem connected with management of solid waste by-products generated during the process. In the frame of the study of the process statics susceptibility to sorption and the time to reach steady state of the phenol on sorption materials studied were determined. The effect of the initial concentration of the phenol on his sorption was also examined. For the mathematical description of adsorption Langmuir and Freundlich equations were used. The scope of the work also included an assessment of the phenomenon of release from adsorbent materials the primary inorganic and organic substances. Simultaneously, a solution toxic effect based on the indirect methods was determined. Additionally, based on the literature results, efficiency of the phenol sorption using conventional and non-conventional sorbents was determined. Phenol sorption proceeded to a greater extent on the ash produced during the gasification process than on the dried sludge subjected to heat treatment. The adsorption equilibration depended also on the absorbent material. Moreover, the increase of initial phenol concentration corresponded to the increase of phenol sorption. The goodness of fit of the theoretical adsorption isotherm (according to the Langmuir or Freundlich equations) to experimental data in the tested range of phenol concentrations (from 60 to 90 mg/dm3) depended on the tested sorbent material. In the case of phenol sorption on the ash the determination coefficients for both isotherms were similar, and in the case of the dried sludge better determination coefficient was obtained for the Freundlich isotherm. The analysis of the isotherm coefficients confirmed high sorption of phenol on the ashes as in the previous studies. Phenol sorption capacity on the sorbents tested in this study was greater than for the other unconventional adsorbents (bagasse fly ash, neutralized red mud, olive pomace) only in the case of ash. The tested sorbent materials released primary organic and inorganic substances on the contact with deionized water. The intensity of this phenomenon was greater for the dried sludge than for the ash. The increase of the toxic effect of the solution of this material was also observed. These studies, however, require continuation for better understanding of this phenomenon.
Źródło:
Inżynieria i Ochrona Środowiska; 2015, 18, 1; 67-81
1505-3695
2391-7253
Pojawia się w:
Inżynieria i Ochrona Środowiska
Dostawca treści:
Biblioteka Nauki
Artykuł
Wyświetlanie 1-15 z 19

Ta witryna wykorzystuje pliki cookies do przechowywania informacji na Twoim komputerze. Pliki cookies stosujemy w celu świadczenia usług na najwyższym poziomie, w tym w sposób dostosowany do indywidualnych potrzeb. Korzystanie z witryny bez zmiany ustawień dotyczących cookies oznacza, że będą one zamieszczane w Twoim komputerze. W każdym momencie możesz dokonać zmiany ustawień dotyczących cookies