Other — Synthesis, identification and application of metal organic framework for removal of industrial cationic dyes

Measurement evidence

Other

Synthesis, identification and application of metal organic framework for removal of industrial cationic dyes · Kiwaan H.A., Sh. Mohamed F., El-Bindary A.A. et al. · Journal of Molecular Liquids · 2021 · 117435

7 measurement groups · 20 results

Reported values remain attached to the sample, method, conditions, extraction quality and source location that produced them.

Batch adsorption isotherm for brilliant green

Vacuum-dried ZIF-7 · Powder

20 mg ZIF-7 with 25 mL BG solution, C0 2.65e-4 to 5.27e-3 mol L-1, pH 8, 90 min; UV-vis at 626 nm.

Temperature
298
Atmosphere
aqueous
Context
pristine ZIF-7 adsorbent
Measurement source
2 · 2.4. Adsorption studies of MB and BG dyes · Table 3; Figs. 10, 12
PropertyReported valueNormalised valueUncertaintyOrigin and qualitySource
BG Langmuir calculated qmqm = 0.1851 mmol g-10.1851 mmol/gTable
Exact Reported
7 · 3.2.6. Adsorption isotherms · Table 3
BG Langmuir experimental maximum capacityMarked as a best value within this paperqm exp = 0.181 mmol g-10.181 mmol/gTable
Exact Reported
7 · 3.2.6. Adsorption isotherms · Table 3
BG Langmuir R2Marked as a best value within this paperR2 = 0.999750.99975Table
Exact Reported
7 · 3.2.6. Adsorption isotherms · Table 3

Batch adsorption isotherm for methylene blue

Vacuum-dried ZIF-7 · Powder

20 mg ZIF-7 with 25 mL MB solution, C0 2.76e-4 to 2.94e-3 mol L-1, pH 9, 90 min; UV-vis at 662 nm.

Temperature
298
Atmosphere
aqueous
Context
pristine ZIF-7 adsorbent
Measurement source
2 · 2.4. Adsorption studies of MB and BG dyes · Table 2; Figs. 9, 11
PropertyReported valueNormalised valueUncertaintyOrigin and qualitySource
MB Langmuir calculated qmqm = 2.47 mmol g-12.47 mmol/gTable
Exact Reported
6 · 3.2.6. Adsorption isotherms · Table 2
MB Langmuir experimental maximum capacityMarked as a best value within this paperqm exp = 2.42 mmol g-12.42 mmol/gTable
Exact Reported
6 · 3.2.6. Adsorption isotherms · Table 2
MB Langmuir R2Marked as a best value within this paperR2 = 0.999520.99952Table
Exact Reported
6 · 3.2.6. Adsorption isotherms · Table 2

Batch uptake kinetics for brilliant green

Vacuum-dried ZIF-7 · Powder

120 mg ZIF-7 with 150 mL BG solution, C0 3.6e-3 mol L-1, pH 8, 25 C, 200 rpm; UV-vis after sampled intervals.

Temperature
298
Atmosphere
aqueous
Context
pristine ZIF-7 adsorbent
Measurement source
3 · 2.4. Adsorption studies of MB and BG dyes · Table 5; Figs. 14, 16
PropertyReported valueNormalised valueUncertaintyOrigin and qualitySource
BG pseudo-second-order kinetic R2Marked as a best value within this paperR2 = 0.9890.989Table
Exact Reported
10 · 3.2.7. Kinetics of adsorption and mechanism studies · Table 5
BG experimental kinetic qeMarked as a best value within this paperqe (exp) = 0.1442 mmol g-10.1442 mmol/gTable
Exact Reported
10 · 3.2.7. Kinetics of adsorption and mechanism studies · Table 5

Batch uptake kinetics for methylene blue

Vacuum-dried ZIF-7 · Powder

120 mg ZIF-7 with 150 mL MB solution, C0 1.9e-4 mol L-1, pH 9, 25 C, 200 rpm; UV-vis after sampled intervals.

Temperature
298
Atmosphere
aqueous
Context
pristine ZIF-7 adsorbent
Measurement source
3 · 2.4. Adsorption studies of MB and BG dyes · Table 4; Figs. 13, 15
PropertyReported valueNormalised valueUncertaintyOrigin and qualitySource
Adsorption equilibrium timehighest adsorption at 100 min100 minText
Rounded Reported
7 · 3.2.7. Kinetics of adsorption and mechanism studies · Figs. 13-16
MB pseudo-second-order kinetic R2Marked as a best value within this paperR2 = 0.99950.9995Table
Exact Reported
10 · 3.2.7. Kinetics of adsorption and mechanism studies · Table 4
MB experimental kinetic qeMarked as a best value within this paperqe (exp) = 2.32 mmol g-12.32 mmol/gTable
Exact Reported
10 · 3.2.7. Kinetics of adsorption and mechanism studies · Table 4

Temperature-dependent adsorption thermodynamics

Vacuum-dried ZIF-7 · Powder

Adsorption at 293, 298, 303, 308, 313 and 318 K for MB/BG; van't Hoff analysis from ln Kc vs 1/T.

Temperature
293-318
Atmosphere
aqueous
Context
pristine ZIF-7 adsorbent
Measurement source
11-12 · 3.2.8. Parameters of thermodynamics · Table 6; Figs. 17, 18
PropertyReported valueNormalised valueUncertaintyOrigin and qualitySource
BG standard enthalpy changeDelta H = 52.126 kJ mol-152.126 kJ/molTable
Exact Reported
12 · 3.2.8. Parameters of thermodynamics · Table 6
BG standard entropy changeDelta S = 151.96 J mol-1 K-1151.96 J/mol/KTable
Exact Reported
12 · 3.2.8. Parameters of thermodynamics · Table 6
BG zero standard free-energy temperatureT0 = 285 K285 KTable
Exact Reported
12 · 3.2.8. Parameters of thermodynamics · Table 6
MB standard enthalpy changeDelta H = 89.644 kJ mol-189.644 kJ/molTable
Exact Reported
12 · 3.2.8. Parameters of thermodynamics · Table 6
MB standard entropy changeDelta S = 33.729 J mol-1 K-133.729 J/mol/KTable
Exact Reported
12 · 3.2.8. Parameters of thermodynamics · Table 6
MB zero standard free-energy temperatureT0 = 265.7 K265.7 KTable
Exact Reported
12 · 3.2.8. Parameters of thermodynamics · Table 6

Point of zero charge determination

White ZIF-7 crystals · Powder

Solid addition method; initial/final pH relationship used to determine pHPZC.

Atmosphere
aqueous
Context
pristine ZIF-7
Measurement source
4 · 3.2.1. Point of zero charge determination · Fig. 5
PropertyReported valueNormalised valueUncertaintyOrigin and qualitySource
Point of zero chargeMarked as a best value within this paperpHPZC = 7.57.5 pHText
Exact Reported
4 · 3.2.1. Point of zero charge determination · Fig. 5

Adsorption-desorption regeneration cycling

Vacuum-dried ZIF-7 · Powder

Three consecutive adsorption-desorption cycles; regenerated with 0.01 M HCl to pH 7, water, ethanol, and 60 C oven drying for 4 h.

Atmosphere
aqueous
Context
ZIF-7 adsorbent after MB/BG loading and regeneration
Measurement source
12-13 · 3.2.11. Reusability test of adsorbent
PropertyReported valueNormalised valueUncertaintyOrigin and qualitySource
BG regeneration efficiencies over three cycles98.8%, 96.3%, 94.6%Text
Exact Reported
12 · 3.2.11. Reusability test of adsorbent
MB regeneration efficiencies over three cycles97.8%, 95.5%, 93.6%Text
Exact Reported
12 · 3.2.11. Reusability test of adsorbent