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EC number: 280-445-7 | CAS number: 83411-71-6
- Life Cycle description
- Uses advised against
- Endpoint summary
- Appearance / physical state / colour
- Melting point / freezing point
- Boiling point
- Density
- Particle size distribution (Granulometry)
- Vapour pressure
- Partition coefficient
- Water solubility
- Solubility in organic solvents / fat solubility
- Surface tension
- Flash point
- Auto flammability
- Flammability
- Explosiveness
- Oxidising properties
- Oxidation reduction potential
- Stability in organic solvents and identity of relevant degradation products
- Storage stability and reactivity towards container material
- Stability: thermal, sunlight, metals
- pH
- Dissociation constant
- Viscosity
- Additional physico-chemical information
- Additional physico-chemical properties of nanomaterials
- Nanomaterial agglomeration / aggregation
- Nanomaterial crystalline phase
- Nanomaterial crystallite and grain size
- Nanomaterial aspect ratio / shape
- Nanomaterial specific surface area
- Nanomaterial Zeta potential
- Nanomaterial surface chemistry
- Nanomaterial dustiness
- Nanomaterial porosity
- Nanomaterial pour density
- Nanomaterial photocatalytic activity
- Nanomaterial radical formation potential
- Nanomaterial catalytic activity
- Endpoint summary
- Stability
- Biodegradation
- Bioaccumulation
- Transport and distribution
- Environmental data
- Additional information on environmental fate and behaviour
- Ecotoxicological Summary
- Aquatic toxicity
- Endpoint summary
- Short-term toxicity to fish
- Long-term toxicity to fish
- Short-term toxicity to aquatic invertebrates
- Long-term toxicity to aquatic invertebrates
- Toxicity to aquatic algae and cyanobacteria
- Toxicity to aquatic plants other than algae
- Toxicity to microorganisms
- Endocrine disrupter testing in aquatic vertebrates – in vivo
- Toxicity to other aquatic organisms
- Sediment toxicity
- Terrestrial toxicity
- Biological effects monitoring
- Biotransformation and kinetics
- Additional ecotoxological information
- Toxicological Summary
- Toxicokinetics, metabolism and distribution
- Acute Toxicity
- Irritation / corrosion
- Sensitisation
- Repeated dose toxicity
- Genetic toxicity
- Carcinogenicity
- Toxicity to reproduction
- Specific investigations
- Exposure related observations in humans
- Toxic effects on livestock and pets
- Additional toxicological data
Acute Toxicity: inhalation
Administrative data
- Endpoint:
- acute toxicity: inhalation
- Data waiving:
- study scientifically not necessary / other information available
- Justification for data waiving:
- the study does not need to be conducted because exposure of humans via inhalation is not likely taking into account the vapour pressure of the substance and/or the possibility of exposure to aerosols, particles or droplets of an inhalable size
Cross-reference
- Reason / purpose for cross-reference:
- data waiving: supporting information
Reference
- Endpoint:
- vapour pressure
- Type of information:
- experimental study
- Adequacy of study:
- key study
- Study period:
- From 16 Feburary 2012 to 26 June 2012
- Reliability:
- 1 (reliable without restriction)
- Rationale for reliability incl. deficiencies:
- guideline study
- Qualifier:
- according to guideline
- Guideline:
- OECD Guideline 104 (Vapour Pressure Curve)
- Deviations:
- no
- Qualifier:
- according to guideline
- Guideline:
- EU Method A.4 (Vapour Pressure)
- Deviations:
- no
- GLP compliance:
- yes (incl. QA statement)
- Remarks:
- 2011-08-31
- Type of method:
- effusion method: vapour pressure balance
- Temp.:
- 25 °C
- Vapour pressure:
- 0.002 Pa
- Transition / decomposition:
- no
- Conclusions:
- The vapour pressure of the test item has been determined to be 0.0024 Pa at 25°C
- Executive summary:
The determination was carried out with the vapour pressure balance according to Method A4 Vapour Pressure of Commission Regulation (EC) No 440/2008 of 30 May 2008, Method 104 of the OECD Guidelines for Testing of Chemicals, 23 March 2006 and GLP. No deviation from the guidelines was observed during the test.
The vapour pressure was determined using a vapour pressure balance with measurements being made at several temperatures and linear regression analysis used to calculate the vapour pressure at 25°C. After evacuating the system, opening the shutter above the sample oven causes the escaping vapour jet to be directed at the scale pan. The difference in mass readings with the orifice covered and uncovered is proportional to the vapour pressure at the given oven temperature.
A preliminary run was undertaken over the temperature range 20 to 247 °C to provide information for a suitable temperature range for the determination. A final sequence of ten runs was started after a sample of test item had been under vacuum for approximately 46 hours. Temperature and pressure readings were taken between 80 and 90 °C with a one hour dwell at 80 °C between runs.
The test item didn't change in appearance under the conditions used in the determination.The vapour pressure of the test item has been determined to be 0.0024 Pa at 25 °C.
Results run 1:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
38,74 |
3,874E-08 |
0,053781045 |
-1,269370762 |
81 |
354,15 |
0,002823662 |
39,44 |
3,944E-08 |
0,054752824 |
-1,261593472 |
82 |
355,15 |
0,002815712 |
39,54 |
3,954E-08 |
0,05489165 |
-1,260493714 |
83 |
356,15 |
0,002807806 |
39,74 |
3,974E-08 |
0,055169301 |
-1,258302516 |
84 |
357,15 |
0,002799944 |
44,83 |
4,483E-08 |
0,062235525 |
-1,205961640 |
85 |
358,15 |
0,002792126 |
48,42 |
4,842E-08 |
0,067219365 |
-1,172505594 |
86 |
359,15 |
0,002784352 |
50,52 |
5,052E-08 |
0,070134703 |
-1,154067037 |
87 |
360,15 |
0,002776621 |
52,42 |
5,242E-08 |
0,07277239 |
-1,138033362 |
88 |
361,15 |
0,002768933 |
53,62 |
5,362E-08 |
0,074438297 |
-1,128203569 |
89 |
362,15 |
0,002761287 |
56,61 |
5,661E-08 |
0,078589183 |
-1,104637224 |
90 |
363,15 |
0,002753683 |
57,71 |
5,771E-08 |
0,080116265 |
-1,096279304 |
A plot of log Vp versus reciprocal temperature fur Run 1 gives the following statistical data using an unweighted least squares treatment:
Slope |
-2,54*103 |
Intercept |
5,92 |
Standard deviation |
185 |
Standard deviation |
0,515 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-2.54*103/ temp(K)]+5.92
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.62
Results run 2:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
37,34 |
3,734E-08 |
0,051837486 |
-1,285356065 |
81 |
354,15 |
0,002823662 |
37,24 |
3,724E-08 |
0,051698661 |
-1,286520706 |
82 |
355,15 |
0,002815712 |
37,74 |
3,774E-08 |
0,052392789 |
-1,280728483 |
83 |
356,15 |
0,002807806 |
39,84 |
3,984E-08 |
0,055308127 |
-1,257211049 |
84 |
357,15 |
0,002799944 |
41,04 |
4,104E-08 |
0,056974034 |
-1,244323027 |
85 |
358,15 |
0,002792126 |
45,33 |
4,533E-08 |
0,062929653 |
-1,201144660 |
86 |
359,15 |
0,002784352 |
47,03 |
4,703E-08 |
0,065289689 |
-1,185155400 |
87 |
360,15 |
0,002776621 |
50,02 |
5,002E-08 |
0,069440575 |
-1,158386691 |
88 |
361,15 |
0,002768933 |
56,61 |
5,661E-08 |
0,078589183 |
-1,104637224 |
89 |
362,15 |
0,002761287 |
53,82 |
5,382E-08 |
0,074715949 |
-1,126586685 |
90 |
363,15 |
0,002753683 |
60,21 |
6,021E-08 |
0,083586906 |
-1,077861752 |
A plot of log Vp versus reciprocal temperature fur Run 2 gives the following statistical data using an unweighted least squares treatment:
Slope |
-2,87*103 |
Intercept |
6,81 |
Standard deviation |
218 |
Standard deviation |
0,609 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-2.87*103/ temp(K)]+6.81
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.81
Results run 3:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
34,45 |
3,445E-08 |
0,047825426 |
-1,320341152 |
81 |
354,15 |
0,002823662 |
37,74 |
3,774E-08 |
0,052392789 |
-1,280728483 |
82 |
355,15 |
0,002815712 |
38,74 |
3,874E-08 |
0,053781045 |
-1,269370762 |
83 |
356,15 |
0,002807806 |
41,63 |
4,163E-08 |
0,057793106 |
-1,238123968 |
84 |
357,15 |
0,002799944 |
41,83 |
4,183E-08 |
0,058070757 |
-1,236042514 |
85 |
358,15 |
0,002792126 |
44,83 |
4,483E-08 |
0,062235525 |
-1,205961640 |
86 |
359,15 |
0,002784352 |
48,12 |
4,812E-08 |
0,066802888 |
-1,175204760 |
87 |
360,15 |
0,002776621 |
52,22 |
5,222E-08 |
0,072494739 |
-1,139693511 |
88 |
361,15 |
0,002768933 |
55,91 |
5,591E-08 |
0,077617404 |
-1,110040886 |
89 |
362,15 |
0,002761287 |
57,01 |
5,701E-08 |
0,079144486 |
-1,101579338 |
90 |
363,15 |
0,002753683 |
60,01 |
6,001E-08 |
0,083309254 |
-1,079306752 |
A plot of log Vp versus reciprocal temperature fur Run 3 gives the following statistical data using an unweighted least squares treatment:
Slope |
-3,10*103 |
Intercept |
7,45 |
Standard deviation |
118 |
Standard deviation |
0,331 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-3.10*103/ temp(K)]+7.45
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.94
Results run 4:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
37,14 |
3,714E-08 |
0,051559835 |
-1,287688479 |
81 |
354,15 |
0,002823662 |
37,94 |
3,794E-08 |
0,05267044 |
-1,278433052 |
82 |
355,15 |
0,002815712 |
39,54 |
3,954E-08 |
0,05489165 |
-1,260493714 |
83 |
356,15 |
0,002807806 |
37,34 |
3,734E-08 |
0,051837486 |
-1,285356065 |
84 |
357,15 |
0,002799944 |
42,33 |
4,233E-08 |
0,058764885 |
-1,230882110 |
85 |
358,15 |
0,002792126 |
42,23 |
4,223E-08 |
0,058626059 |
-1,231909297 |
86 |
359,15 |
0,002784352 |
44,03 |
4,403E-08 |
0,061124692 |
-1,213781693 |
87 |
360,15 |
0,002776621 |
48,82 |
4,882E-08 |
0,067774668 |
-1,168932604 |
88 |
361,15 |
0,002768933 |
53,42 |
5,342E-08 |
0,074160646 |
-1,129826495 |
89 |
362,15 |
0,002761287 |
59,71 |
5,971E-08 |
0,082892778 |
-1,081483308 |
90 |
363,15 |
0,002753683 |
62,6 |
6,260E-08 |
0,086904838 |
-1,060956046 |
A plot of log Vp versus reciprocal temperature fur Run 4 gives the following statistical data using an unweighted least squares treatment:
Slope |
-2.98*103 |
Intercept |
7,12 |
Standard deviation |
333 |
Standard deviation |
0,930 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-2.98*103/ temp(K)]+7.12
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.88
Results run 5:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
36,54 |
3,654E-08 |
0,050726881 |
-1,294761836 |
81 |
354,15 |
0,002823662 |
37,64 |
3,764E-08 |
0,052253963 |
-1,281880764 |
82 |
355,15 |
0,002815712 |
35,24 |
3,524E-08 |
0,048922148 |
-1,310494479 |
83 |
356,15 |
0,002807806 |
39,74 |
3,974E-08 |
0,055169301 |
-1,258302516 |
84 |
357,15 |
0,002799944 |
42,13 |
4,213E-08 |
0,058487234 |
-1,232938920 |
85 |
358,15 |
0,002792126 |
45,13 |
4,513E-08 |
0,062652002 |
-1,203065045 |
86 |
359,15 |
0,002784352 |
48,02 |
4,802E-08 |
0,066664063 |
-1,176108223 |
87 |
360,15 |
0,002776621 |
51,52 |
5,152E-08 |
0,071522959 |
-1,145554524 |
88 |
361,15 |
0,002768933 |
46,83 |
4,683E-08 |
0,065012038 |
-1,187006221 |
89 |
362,15 |
0,002761287 |
54,51 |
5,451E-08 |
0,075673845 |
-1,121054197 |
90 |
363,15 |
0,002753683 |
59,21 |
5,921E-08 |
0,08219865 |
-1,085135318 |
A plot of log Vp versus reciprocal temperature fur Run 5 gives the following statistical data using an unweighted least squares treatment:
Slope |
-2.73*103 |
Intercept |
6.42 |
Standard deviation |
282 |
Standard deviation |
0.787 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-2.73*103/ temp(K)]+6.42
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.74
Results run 6:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,00283166 |
35,44 |
3,544E-08 |
0,0491998 |
-1,308036666 |
81 |
354,15 |
0,00282366 |
36,44 |
3,644E-08 |
0,05058806 |
-1,295952010 |
82 |
355,15 |
0,00281571 |
36,64 |
3,664E-08 |
0,05086571 |
-1,293574914 |
83 |
356,15 |
0,00280781 |
40,84 |
4,084E-08 |
0,05669638 |
-1,246444645 |
84 |
357,15 |
0,00279994 |
41,93 |
4,193E-08 |
0,05820958 |
-1,235005516 |
85 |
358,15 |
0,00279213 |
45,53 |
4,553E-08 |
0,06320731 |
-1,199232728 |
86 |
359,15 |
0,00278435 |
43,23 |
4,323E-08 |
0,06001432 |
-1,221745143 |
87 |
360,15 |
0,00277662 |
49,02 |
4,902E-08 |
0,06805232 |
-1,167157072 |
88 |
361,15 |
0,00276893 |
52,92 |
5,292E-08 |
0,07346652 |
-1,133910543 |
89 |
362,15 |
0,00276129 |
57,51 |
5,751E-08 |
0,07983861 |
-1,097787011 |
90 |
363,15 |
0,00275368 |
61,4 |
6,140E-08 |
0,08523893 |
-1,069362008 |
A plot of log Vp versus reciprocal temperature fur Run 6 gives the following statistical data using an unweighted least squares treatment:
Slope |
-3.07*103 |
Intercept |
7.37 |
Standard deviation |
222 |
Standard deviation |
0.619 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-3.07*103/ temp(K)]+7.37
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.93
Results run 7:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
35,64 |
3,564E-08 |
0,049477451 |
-1,305592683 |
81 |
354,15 |
0,002823662 |
37,14 |
3,714E-08 |
0,051559835 |
-1,287688479 |
82 |
355,15 |
0,002815712 |
37,84 |
3,784E-08 |
0,052531615 |
-1,279579251 |
83 |
356,15 |
0,002807806 |
38,14 |
3,814E-08 |
0,052948091 |
-1,276149690 |
84 |
357,15 |
0,002799944 |
41,34 |
4,134E-08 |
0,057390511 |
-1,241159906 |
85 |
358,15 |
0,002792126 |
45,93 |
4,593E-08 |
0,063762607 |
-1,195433933 |
86 |
359,15 |
0,002784352 |
46,53 |
4,653E-08 |
0,064595561 |
-1,189797326 |
87 |
360,15 |
0,002776621 |
52,42 |
5,242E-08 |
0,072772390 |
-1,138033362 |
88 |
361,15 |
0,002768933 |
50,52 |
5,052E-08 |
0,070134703 |
-1,154067037 |
89 |
362,15 |
0,002761287 |
54,31 |
5,431E-08 |
0,075396194 |
-1,122650576 |
90 |
363,15 |
0,002753683 |
55,81 |
5,581E-08 |
0,077478578 |
-1,110818356 |
A plot of log Vp versus reciprocal temperature fur Run 7 gives the following statistical data using an unweighted least squares treatment:
Slope |
-2.73*103 |
Intercept |
6.40 |
Standard deviation |
185 |
Standard deviation |
0.516 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-2.73*103/ temp(K)]+6.40
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.74
Results run 8:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
33,95 |
3,395E-08 |
0,047131298 |
-1,326690600 |
81 |
354,15 |
0,002823662 |
31,55 |
3,155E-08 |
0,043799483 |
-1,358531015 |
82 |
355,15 |
0,002815712 |
37,84 |
3,784E-08 |
0,052531615 |
-1,279579251 |
83 |
356,15 |
0,002807806 |
36,14 |
3,614E-08 |
0,050171579 |
-1,299542231 |
84 |
357,15 |
0,002799944 |
42,03 |
4,203E-08 |
0,058348408 |
-1,233970989 |
85 |
358,15 |
0,002792126 |
41,63 |
4,163E-08 |
0,057793106 |
-1,238123968 |
86 |
359,15 |
0,002784352 |
48,02 |
4,802E-08 |
0,066664063 |
-1,176108223 |
87 |
360,15 |
0,002776621 |
48,22 |
4,822E-08 |
0,066941714 |
-1,174303173 |
88 |
361,15 |
0,002768933 |
46,33 |
4,633E-08 |
0,064317910 |
-1,191668079 |
89 |
362,15 |
0,002761287 |
52,92 |
5,292E-08 |
0,073466518 |
-1,133910543 |
90 |
363,15 |
0,002753683 |
53,73 |
5,373E-08 |
0,074577123 |
-1,127394375 |
A plot of log Vp versus reciprocal temperature fur Run 8 gives the following statistical data using an unweighted least squares treatment:
Slope |
-2.88*103 |
Intercept |
6.80 |
Standard deviation |
291 |
Standard deviation |
0.813 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-2.88*103/ temp(K)]+6.80
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -2.85
Results run 9:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
34,65 |
3,465E-08 |
0,048103077 |
-1,317827140 |
81 |
354,15 |
0,002823662 |
35,74 |
3,574E-08 |
0,049616277 |
-1,304375831 |
82 |
355,15 |
0,002815712 |
36,34 |
3,634E-08 |
0,050449230 |
-1,297145456 |
83 |
356,15 |
0,002807806 |
39,14 |
3,914E-08 |
0,054336348 |
-1,264909557 |
84 |
357,15 |
0,002799944 |
41,53 |
4,153E-08 |
0,057654280 |
-1,239168448 |
85 |
358,15 |
0,002792126 |
43,13 |
4,313E-08 |
0,059875490 |
-1,222750921 |
86 |
359,15 |
0,002784352 |
46,93 |
4,693E-08 |
0,065150863 |
-1,186079825 |
87 |
360,15 |
0,002776621 |
51,22 |
5,122E-08 |
0,071106482 |
-1,148090805 |
88 |
361,15 |
0,002768933 |
53,12 |
5,312E-08 |
0,073744169 |
-1,132272312 |
89 |
362,15 |
0,002761287 |
57,91 |
5,791E-08 |
0,080393916 |
-1,094776814 |
90 |
363,15 |
0,002753683 |
79,08 |
7,908E-08 |
0,109783300 |
-0,959463718 |
A plot of log Vp versus reciprocal temperature fur Run 9 gives the following statistical data using an unweighted least squares treatment:
Slope |
-3.97*103 |
Intercept |
9.89 |
Standard deviation |
435 |
Standard deviation |
1.22 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-3.97*103/ temp(K)]+9.89
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -3.43
Results run 10:
Temperature (°C) |
Temperature (K) |
Reciprocal temperature (K-1) |
Mass difference (µg) |
Mass difference (kg) |
Vapour pressure (Pa) |
Log Vp |
80 |
353,15 |
0,002831658 |
34,75 |
3,475E-08 |
0,048241903 |
-1,316575570 |
81 |
354,15 |
0,002823662 |
30,75 |
3,075E-08 |
0,042688878 |
-1,369685259 |
82 |
355,15 |
0,002815712 |
36,74 |
3,674E-08 |
0,051004533 |
-1,292391227 |
83 |
356,15 |
0,002807806 |
34,45 |
3,445E-08 |
0,047825426 |
-1,320341152 |
84 |
357,15 |
0,002799944 |
40,14 |
4,014E-08 |
0,055724604 |
-1,253953011 |
85 |
358,15 |
0,002792126 |
38,44 |
3,844E-08 |
0,053364568 |
-1,272747000 |
86 |
359,15 |
0,002784352 |
46,03 |
4,603E-08 |
0,063901433 |
-1,194489404 |
87 |
360,15 |
0,002776621 |
49,82 |
4,982E-08 |
0,069162924 |
-1,160126656 |
88 |
361,15 |
0,002768933 |
55,11 |
5,511E-08 |
0,076506799 |
-1,116299968 |
89 |
362,15 |
0,002761287 |
57,21 |
5,721E-08 |
0,079422137 |
-1,100058431 |
90 |
363,15 |
0,002753683 |
61,4 |
6,140E-08 |
0,085238931 |
-1,069362008 |
A plot of log Vp versus reciprocal temperature fur Run 10 gives the following statistical data using an unweighted least squares treatment:
Slope |
-3.75*103 |
Intercept |
9.25 |
Standard deviation |
380 |
Standard deviation |
1.06 |
The results obtained indicate the following vapour pressure relationship:
Log Vp= [-3.75*103/ temp(K)]+9.25
The above yields a vapour pressure (Pa) at 298.15K with a common logarithm of -3.33
Summary of results:
The values of vapour pressure at 25 °C extrapolated from each graph are summarized in the following table:
Run | log Vp at 25 °C | Vapour pressure |
1 | -2,62 | 2,42*103 |
2 | -2,81 | 1,54*103 |
3 | -2,94 | 1,16*103 |
4 | -2,88 | 1,33*103 |
5 | -2,74 | 1,81*103 |
6 | -2,93 | 1,17*103 |
7 | -2,74 | 1,82*103 |
8 | -2,85 | 1,42*103 |
9 | -3,53 | 3,74*103 |
10 | -3,33 | 4,66*103 |
Data source
Materials and methods
Results and discussion
Applicant's summary and conclusion
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