Measurement evidence
Plasma-catalytic removal of toluene over bimetallic M/Mn-BTC catalysts in dielectric barrier discharge reactor · Zang X., Sun H., Wang W. et al. · Separation and Purification Technology · 2024 · 125667
Reported values remain attached to the sample, method, conditions, extraction quality and source location that produced them.
Ce/Mn-BTC · Powder
O3 measured with ozone analyser; NOx monitored with flue gas analyser across SED values
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 565.39 J/L | 109.6 mg/m3 | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 7 |
| O3 concentration at SED 343.59 J/L | 485.29 mg/m3 | — | — | Text Exact Reported | p007 · 3.2 · Fig. 7 |
Co/Mn-BTC / Co/Mn-BTC-1 · Powder
O3 measured with ozone analyser; NOx monitored with flue gas analyser across SED values
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 565.39 J/L | 103.0 mg/m3 | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 7 |
| O3 concentration at SED 343.59 J/LMarked as a best value within this paper | 183.99 mg/m3 | — | — | Text Exact Reported | p007 · 3.2 · Fig. 7 |
Cu/Mn-BTC · Powder
O3 measured with ozone analyser; NOx monitored with flue gas analyser across SED values
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 565.39 J/LMarked as a best value within this paper | 79.2 mg/m3 | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 7 |
| O3 concentration at SED 343.59 J/L | 406.29 mg/m3 | — | — | Text Exact Reported | p007 · 3.2 · Fig. 7 |
DBD-alone · Model
O3 measured with ozone analyser; NOx monitored with flue gas analyser across SED values
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 565.39 J/L | 138.4 mg/m3 | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 7 |
| O3 concentration at SED 343.59 J/L | 538.64 mg/m3 | — | — | Text Exact Reported | p007 · 3.2 · Fig. 7 |
Fe/Mn-BTC · Powder
O3 measured with ozone analyser; NOx monitored with flue gas analyser across SED values
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 565.39 J/L | 111.4 mg/m3 | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 7 |
| O3 concentration at SED 343.59 J/L | 468.57 mg/m3 | — | — | Text Exact Reported | p007 · 3.2 · Fig. 7 |
Co/Mn-BTC / Co/Mn-BTC-1 · Powder
Exhaust gas absorbed in n-hexane for 20 min; fixed SED 689.01 J/L with Co/Mn-BTC catalyst
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| DBD + Co/Mn-BTC organic byproducts detected | Toluene; 3-Hexanone; Cyclopentanol, 1-methyl-; 3-Hexanol; Heptane, 2,4-dimethyl-; Benzene, 1,4-dimethyl-; Benzaldehyde; Nonanal; Phenol, 2-nitro-; Benzoic acid; Benzaldehyde, 2,5-dimethyl-; Nonadecane, 2-methyl-; n-Hexadecanoic acid | — | — | Table Qualitative | p012 · 3.4.3 · Table 6 |
| DBD-alone organic byproducts detected | 3-Pentanol, 3-methyl-; Toluene; 3-Hexanone; Cyclopentanol, 1-methyl-; 3-Hexanol; Heptane, 2,4-dimethyl-; Benzene, 1,4-dimethyl-; Benzaldehyde; Benzyl alcohol; Phenol, 2-nitro-; Benzoic acid; Benzaldehyde, 2,5-dimethyl-; Dodecane, 2,6,11-trimethyl-; Heptacosance; n-Hexadecanoic acid; Octadecanoic acid | — | — | Table Qualitative | p012 · 3.4.3 · Table 6 |
Co/Mn-BTC-0.33 · Powder
500 ppm toluene, 4 vol% O2, SED 267.24-808.99 J/L; Co/Mn ratio varied
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 689.01 J/L | 115.2 mg/m3 | — | — | Text Exact Reported | p009-p010 · 3.3 · Fig. 10 |
| O3 concentration at SED 689.01 J/LMarked as a best value within this paper | 7.71 mg/m3 | — | — | Text Exact Reported | p010 · 3.3 · Fig. 10 |
Co/Mn-BTC-0.5 · Powder
500 ppm toluene, 4 vol% O2, SED 267.24-808.99 J/L; Co/Mn ratio varied
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 689.01 J/L | 132.9 mg/m3 | — | — | Text Exact Reported | p009-p010 · 3.3 · Fig. 10 |
| O3 concentration at SED 689.01 J/L | 10.35 mg/m3 | — | — | Text Exact Reported | p010 · 3.3 · Fig. 10 |
Co/Mn-BTC / Co/Mn-BTC-1 · Powder
500 ppm toluene, 4 vol% O2, SED 267.24-808.99 J/L; Co/Mn ratio varied
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| Co/Mn-BTC-1 degradation efficiency at SED 808.99 J/LMarked as a best value within this paper | 96.2% | — | — | Text Rounded Reported | p009 · 3.3 · Fig. 9 |
| Co/Mn-BTC-1 maximum energy efficiencyMarked as a best value within this paper | 18.85 g/kWh at SED 267.24 J/L | — | — | Text Exact Reported | p009 · 3.3 · Fig. 9 |
| Co/Mn-BTC-1 mineralization degree at SED 808.99 J/LMarked as a best value within this paper | 93.9% | — | — | Text Rounded Reported | p009 · 3.3 · Fig. 9 |
| NOx concentration at SED 689.01 J/L | 140.5 mg/m3 | — | — | Text Exact Reported | p009-p010 · 3.3 · Fig. 10 |
| O3 concentration at SED 689.01 J/L | 15.41 mg/m3 | — | — | Text Exact Reported | p010 · 3.3 · Fig. 10 |
| Co/Mn ratio performance orderMarked as a best value within this paper | Co/Mn-BTC-1 > Co/Mn-BTC-0.5 > Co/Mn-BTC-2 > Co/Mn-BTC-0.33 | — | — | Text Qualitative | p008-p009 · 3.3 · Fig. 9 |
Co/Mn-BTC-2 · Powder
500 ppm toluene, 4 vol% O2, SED 267.24-808.99 J/L; Co/Mn ratio varied
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| NOx concentration at SED 689.01 J/LMarked as a best value within this paper | 110.0 mg/m3 | — | — | Text Exact Reported | p009-p010 · 3.3 · Fig. 10 |
| O3 concentration at SED 689.01 J/L | 13.16 mg/m3 | — | — | Text Exact Reported | p010 · 3.3 · Fig. 10 |
Ce/Mn-BTC · Powder
500 ppm toluene, 1 L/min gas flow, 4 vol% O2, SED 267.24-808.99 J/L; 0.3 g catalyst plus 1.5 g quartz sand for catalyst tests
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| Energy efficiency at SED 267.24 J/L | 14.2 g/kWh | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 267.24 J/L | 54.4% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 808.99 J/L | 95.2% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
Co/Mn-BTC / Co/Mn-BTC-1 · Powder
500 ppm toluene, 1 L/min gas flow, 4 vol% O2, SED 267.24-808.99 J/L; 0.3 g catalyst plus 1.5 g quartz sand for catalyst tests
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| CO2 concentration at SED 343.59 J/L with Co/Mn-BTC | 1825.17 mg/m3 | — | — | Text Exact Reported | p006 · 3.2 · Fig. 6 |
| CO concentration at SED 343.59 J/L with Co/Mn-BTC | 1226.28 mg/m3 | — | — | Text Exact Reported | p006 · 3.2 · Fig. 6 |
| CO2 selectivity at SED 689.01 J/L with Co/Mn-BTCMarked as a best value within this paper | 52.6% | — | — | Text Rounded Reported | p006 · 3.2 · Fig. 6 |
| Energy efficiency at SED 267.24 J/LMarked as a best value within this paper | 18.8 g/kWh | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Mineralization degree at SED 343.59 J/L with Co/Mn-BTC | 66.4% | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 6 |
| Mineralization degree at SED 808.99 J/L with Co/Mn-BTCMarked as a best value within this paper | 94.1% | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 6 |
| Co/Mn-BTC energy efficiency rangeMarked as a best value within this paper | 8.32-18.85 | — | — | Table Range | p007 · 3.2 · Table 4 |
| Toluene degradation efficiency at SED 267.24 J/L | 72.0% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 808.99 J/LMarked as a best value within this paper | 96.2% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
Cu/Mn-BTC · Powder
500 ppm toluene, 1 L/min gas flow, 4 vol% O2, SED 267.24-808.99 J/L; 0.3 g catalyst plus 1.5 g quartz sand for catalyst tests
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| Energy efficiency at SED 267.24 J/L | 17.74 g/kWh | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 267.24 J/L | 67.9% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 808.99 J/L | 95.5% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
DBD-alone · Model
500 ppm toluene, 1 L/min gas flow, 4 vol% O2, SED 267.24-808.99 J/L; 0.3 g catalyst plus 1.5 g quartz sand for catalyst tests
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| CO2 concentration at SED 343.59 J/L for DBD alone | 885.03 mg/m3 | — | — | Text Exact Reported | p006 · 3.2 · Fig. 6 |
| CO concentration at SED 343.59 J/L for DBD alone | 707.31 mg/m3 | — | — | Text Exact Reported | p006 · 3.2 · Fig. 6 |
| CO2 selectivity at SED 689.01 J/L for DBD alone | 46.1% | — | — | Text Rounded Reported | p006 · 3.2 · Fig. 6 |
| Energy efficiency at SED 267.24 J/L | 11.77 g/kWh | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Mineralization degree at SED 343.59 J/L for DBD alone | 50.6% | — | — | Text Rounded Reported | p007 · 3.2 · Fig. 6 |
| Toluene degradation efficiency at SED 267.24 J/L | 45.0% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 808.99 J/L | 88.9% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
Fe/Mn-BTC · Powder
500 ppm toluene, 1 L/min gas flow, 4 vol% O2, SED 267.24-808.99 J/L; 0.3 g catalyst plus 1.5 g quartz sand for catalyst tests
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| Energy efficiency at SED 267.24 J/L | 13.06 g/kWh | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 267.24 J/L | 50.0% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |
| Toluene degradation efficiency at SED 808.99 J/L | 93.5% | — | — | Text Rounded Reported | p005 · 3.2 · Fig. 5 |