Dust Characterization and Source Apportionment at an Active Surface Mine in West Virginia by Dr. Nick Basta, Shane Whitacre, Dr. Vlad Kecojevic, Ali Lashgari, and Dr. Braden Lusk
Dust Characterization and Source Apportionment at an Active Surface Mine in West Virginia by Dr. Nick Basta, Shane Whitacre, Dr. Vlad Kecojevic, Ali Lashgari, and Dr. Braden Lusk
Proposing a new empirical adsorption isotherm known as Adejo-Ekwenchi isothermIOSR Journals
The derivation of an adsorption isotherm is, largely, by empirical deductions on which basis isotherms like the Langmuir, Freundlich, Temkin, Frumkin, Flory-Huggins, El-Awady, Dubinin-Radushkevich, etc. were developed. We hereby propose yet another two-parameter empirical adsorption isotherm known as Adejo-Ekwenchi isotherm, derived from the data obtained from our corrosion inhibition of mild steel in 2 M H2SO4 using three plant extracts using weight loss method studied at the temperature between 303 and 315 K. The isotherm is centred on the fact that, for any adsorption process, the amount of adsorbate uptake from bulk concentration is, always, inversely proportional to the difference between the total available surface on the adsorbent and the fraction that is covered by the adsorbate at a given temperature, prior to the attainment of maximum value of surface coverage. Therefore, at any time during the adsorption process, (1 - θ) is the available surface and this decreases with increase in concentration, and thus;
(1)
“Equation 1” in a linear form is,
log1/(1–θ) = logKAE + blogC (2)
“Equation 2” is known as Adejo-Ekwenchi isotherm. Results obtained therefrom the isotherm correlate very well with those obtained through other well-known isotherms.
Applications for Water Activity and Sorption Isotherms in PharmaceuticalsLabFerrer LabFerrer
The pharmaceutical industry has been measuring moisture for decades.
Why? Because most people think water is the enemy of API stability. Turns out they're only partly right.
Water activity is the moisture content of the food which is available for microbial growth.By controlling water activity the food can be preserved for longer duration
Effect of Carbon and MgAl Oxide Supports and Potassium Promoter on Higher Alc...Jinwai Goh
Higher alcohol synthesis from syngas was studied over MoS2 during the induction period by varying the support, carbon (C) and MgAl mixed oxide (MMO), and the presence of the K promoter. MoS2 on C and MMO supports produced longer chain hydrocarbons compared to unsupported MoS2. Potassium is known to shift product distribution from hydrocarbons to higher alcohols. Before potassium addition, the C support was selective towards methanol and hydrocarbons while the MMO support was predominantly selective towards hydrocarbons. After K addition, the MMO support produced primarily higher alcohols, whereas the C support remained selective towards hydrocarbons with enhanced alcohol selectivity.
Proposing a new empirical adsorption isotherm known as Adejo-Ekwenchi isothermIOSR Journals
The derivation of an adsorption isotherm is, largely, by empirical deductions on which basis isotherms like the Langmuir, Freundlich, Temkin, Frumkin, Flory-Huggins, El-Awady, Dubinin-Radushkevich, etc. were developed. We hereby propose yet another two-parameter empirical adsorption isotherm known as Adejo-Ekwenchi isotherm, derived from the data obtained from our corrosion inhibition of mild steel in 2 M H2SO4 using three plant extracts using weight loss method studied at the temperature between 303 and 315 K. The isotherm is centred on the fact that, for any adsorption process, the amount of adsorbate uptake from bulk concentration is, always, inversely proportional to the difference between the total available surface on the adsorbent and the fraction that is covered by the adsorbate at a given temperature, prior to the attainment of maximum value of surface coverage. Therefore, at any time during the adsorption process, (1 - θ) is the available surface and this decreases with increase in concentration, and thus;
(1)
“Equation 1” in a linear form is,
log1/(1–θ) = logKAE + blogC (2)
“Equation 2” is known as Adejo-Ekwenchi isotherm. Results obtained therefrom the isotherm correlate very well with those obtained through other well-known isotherms.
Applications for Water Activity and Sorption Isotherms in PharmaceuticalsLabFerrer LabFerrer
The pharmaceutical industry has been measuring moisture for decades.
Why? Because most people think water is the enemy of API stability. Turns out they're only partly right.
Water activity is the moisture content of the food which is available for microbial growth.By controlling water activity the food can be preserved for longer duration
Effect of Carbon and MgAl Oxide Supports and Potassium Promoter on Higher Alc...Jinwai Goh
Higher alcohol synthesis from syngas was studied over MoS2 during the induction period by varying the support, carbon (C) and MgAl mixed oxide (MMO), and the presence of the K promoter. MoS2 on C and MMO supports produced longer chain hydrocarbons compared to unsupported MoS2. Potassium is known to shift product distribution from hydrocarbons to higher alcohols. Before potassium addition, the C support was selective towards methanol and hydrocarbons while the MMO support was predominantly selective towards hydrocarbons. After K addition, the MMO support produced primarily higher alcohols, whereas the C support remained selective towards hydrocarbons with enhanced alcohol selectivity.
metal organic framework-carbon capture and sequestrationVasiUddin Siddiqui
MOF is a porous crystal like a spunge having an enormous surface area and provide much more rooms for storage the gases preferentially hydrogen and carbon dioxide and work as storage for next generation fuel.
This PPT deals with the effect of confinement/ encapsulation of different molecules inside fullerenes such as C16, C20, C60, C70 etc. Targeted drug delivery has also been extensively discussed. This is a group PPT done by Jyoti Devi, Vikas Katoch, Zeeshan Nazir and Aryaveer Singh. Some primary data has Also been collected by the publishers to find out the threshold fullerene for encapsulation of different di-atomic molecules inside fullerenes of different size.
Computationally Driven Characterization of Magnetism, Adsorption, and Reactiv...Joshua Borycz
Metal organic frameworks (MOFs) are a class of nanoporous materials that are com- posed of metal-containing nodes connected by organic linkers. The study of MOFs has grown in importance due to the wide range of possible node and linker combinations, which allow tailoring towards specific applications. This work demonstrates that the- ory can complement experiment in a way that advances the chemical understanding of MOFs. This thesis contains the results of several investigations on three different areas of MOF research: 1) magnetism, 2) CO2 adsorption, and 3) catalysis.
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Automobile Management System Project Report.pdfKamal Acharya
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Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
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Adsorption Isotherm Parameters of CH4 and CO2 on MIL-100 and MIL-101
1. Jin Wai Goh, Yoona Choung, Aloysius Davin Oetomo
School of Chemical & Biomolecular Engineering, Georgia Institute of Technology
Linearization of Adsorption Models
Methods & Theories
Introduction
• CO2 and CH4 are most common greenhouse gases emitted.
• Adsorbing using zeolites and activated carbons, but cost of
regeneration process is expensive.
• Turn towards metal-organic frameworks (MOFs), particularly
MIL-100(Cr) and MIL-101(Cr)
• Extremely high surface areas
• Crystalline open structure
• Tunable pore size
• Catalysis, gas storage, liquid-phase separation
References
1. Llewellyn, P.L.; Bourrelly, S.; Serre, C.; Vimont, A.; Daturi, M.; Hamon, L.; De Weireld, G.; Chang, J.S.;
Hong, D.Y.; Kyu Hwang, Y.; Hwa Jhung, S. High Uptakes of CO2 and CH4 in Mesoporous Metal–
Organic Frameworks MIL-100 and MIL-101. Langmuir, 2008, 24(14), pp.7245-7250.
2. Dada, A.O.; Olalekan, A.P.; Olatunya, A.M.; Dada, O. Langmuir, Freundlich, Temkin and Dubinin–
Radushkevich isotherms studies of equilibrium sorption of Zn2+ unto phosphoric acid modified rice husk.
Journal of Applied Chemistry, 2012, 3(1), 38-45.
3. Temkin, M.I.; Pyzhev, V. Kinetics of ammonia synthesis on promoted iron catalysts. Acta physiochim.
URSS, 1940, 12(3), 327-356.
4. Aharoni, C.; Ungarish, M. Kinetics of activated chemisorption. Part 2.—Theoretical models. Journal of
the Chemical Society, Faraday Transactions 1: Physical Chemistry in Condensed Phases, 1977, 73, 456-
464.
5. Munusamy, K.; Sethia, G.; Patil, D.V.; Rallapalli, P.B.S.; Somani, R.S.; Bajaj, H.C. Sorption of carbon
dioxide, methane, nitrogen and carbon monoxide on MIL-101 (Cr): volumetric measurements and
dynamic adsorption studies. Chemical engineering journal, 2012, 195, 359-368.
6. Ruthven, D.M. Principles of adsorption and adsorption processes. John Wiley & Sons, 1984.
7. Zhang, Y.; Su, W.; Sun, Y.; Liu, J.; Liu, X.; Wang, X. Adsorption Equilibrium of N2, CH4, and CO2 on
MIL-101. Journal of Chemical & Engineering Data, 2015, 60(10), 2951-2957.
Results
Conclusions
Adsorption Isotherm Parameters
of CH4 and CO2 on MIL-100 and MIL-101
n=1 n=3
∆H(kJ/mol) 21.77 20.386
• Langmuir, Freundlich, and Temkin models described the adsorption of CO2 and CH4
on MIL-100(Cr) and MIL-101(Cr) relatively well (R2 > 0.97).
• The Langmuir model had the smallest distribution of deviation of the linearized
experimental loading to the fitted loading over the adsorption pressure.
• The uniform isosteric heat of adsorption supported the Langmuir model, which
assumed constant amount of energy of adsorption.
• The adsorption of CH4 and CO2 on MIL-100 and MIL-101 are monolayer
adsorption.
• In the Langmuir model, the synthesis method of MIL-101 has a greater effect on the
max loading parameter than the adsorption constant.
Langmuir Isotherm Parameters
CH4 CO2
MIL-
100
MIL-
101
MIL-
100
MIL-
101
nm
(mmol/g)
13.32 23.92 21.65 51.55
K (MPa-1) 0.3103 0.2072 0.7086 0.2891
R2 0.9944 0.9990 0.9907 0.9964
Freundlich Isotherm Parameters
CH4 CO2
MIL-
100
MIL-
101
MIL-
100
MIL-
101
K 2.844 3.976 7.737 11.09
m 1.460 1.434 1.870 1.566
R2 0.9872 0.9888 0.9795 0.9718
Temkin Isotherm Parameters
CH4 CO2
MIL-
100
MIL-
101
MIL-
100
MIL-
101
bT 837.1 514.6 490.6 236.7
AT 3.327 2.496 6.149 3.379
R2 0.9539 0.9678 0.9886 0.9833
Literature Langmuir Isotherm Parameters7
CH4 CO2
MIL-101 MIL-101
nm (mmol/g) 8.708 22.91
K (MPa-1) 0.257 0.349