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EC number: 284-664-9 | CAS number: 84961-74-0
- 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
Vapour pressure
Administrative data
Link to relevant study record(s)
- Endpoint:
- vapour pressure
- Type of information:
- experimental study
- Adequacy of study:
- key study
- Reliability:
- 2 (reliable with restrictions)
- Rationale for reliability incl. deficiencies:
- other: Recent guideline study not to GLP
- Qualifier:
- according to guideline
- Guideline:
- OECD Guideline 104 (Vapour Pressure Curve)
- GLP compliance:
- no
- Type of method:
- dynamic method
- Key result
- Temp.:
- 339 °C
- Vapour pressure:
- 1 009 mBar
- Temp.:
- 225 °C
- Vapour pressure:
- 3 mBar
- Conclusions:
- The vapour pressure of the substance is estimated to be <0.01Pa at 20 degC.
- Executive summary:
In a non-GLP study conducted in line with OECD guideline 104, the test material was found to have an estimated vapour pressure of <0.01 Pa at 20 degrees centigrade.
Reference
Description of key information
The vapour pressure of the substance is estimated to be <0.01Pa at 20 degC.
Key value for chemical safety assessment
- Vapour pressure:
- 0.009 Pa
- at the temperature of:
- 20 °C
Additional information
A test report is available for the vapour pressure of LAS-IPA. The report suggests a minimum boiling point for LAS-IPA of 340°C at atmospheric pressure (1001 hPa), based on Differential Scanning Calorimetry (DSC). It also presents results of a ThermoGravimetric Analysis (TGA) at 1009 hPa and results of a DSC analysis at reduced pressure (3.0 hPa). It applies the Modified Grain method to calculate vapour pressure at ambient temperature (20°C), referencing OECD Guideline 104, and Boethling and Mackay, Handbook of Property Estimation Methods for Chemicals. The report arrives at a vapour pressure at ambient temperature of ≤ 0.028 Pa.
However, the report does not present evidence to support the (implicit) claim therein that the temperature effect observed in the DSC (and TGA) is in fact associated with boiling. With reference to available information on LAS-salts including LAS-MIPA and LAS-TEA, as well as related substances (LAS free acid, LAS-Na, LAS-ammonium salt), it is deemed very likely that a true boiling point would be found only at much higher temperatures, and that the observed temperature effect is in fact associated with decomposition rather than boiling. For example, note in this respect that LAS-MIPA is reported to start thermal decomposition at 290°C. As such, vapour pressure is expected to be much lower than the reported maximum of 0.028 Pa.
It is also noted that when recalculating vapour pressure with the modified Grain algorithm, with an in-house implementation in MATLAB, a liquid with a boiling point of 340°C at 1001 hPa is predicted to have a vapour pressure of 0.018 Pa (rather than 0.028 Pa; this reflects the report’s omission of theDZbcompressibility factor in the calculation equation).
Finally the report states that ‘a modified version of the modified Grain method’ was used, as described in Boethling and Mackay, to support explicit treatment of solids (note that the modified Grain method calculates VP for a liquid or supercooled liquid - additional energy is required for solidification, which means that solids at room temperature have a lower vapour pressure than the corresponding supercooled liquids at the same temperature). However, it incorrectly claims that the equation defining the 'm' exponent of the modified Grain method “takes into account the aggregate state at the interesting temperature”; this is incorrect (possibly suggested by the fact that in the original definition of the modified Grain method in Lyman (1982), ‘m’ was not a continuous variable, but could only adopt a few discrete values based on the aggregation state of a substance). In fact, as can also be ascertained from the EPISuite documentation, a separate term needs to be introduced to account for the difference in vapour pressure between supercooled liquids and solids - this fact itself is already mentioned in Lyman (1982), although a much simpler term is suggested there. Note also that although the material tested is described as a pasty substance, LAS-IPA itself is solid at ambient temperature. The calculated value presented in the test report is in fact a supercooled liquid value. If we calculate a value for a solid with a boiling point at 340°C at 1001 hPa, a melting point for that solid of 56°C is sufficient to lower the resulting vapour pressure to below 0.01 Pa. It is deemed likely that the melting point of LAS-IPA exceeds 56°C. As such, given a reported minimum boiling point of 340°C at 1001 hPa (which is likely a gross underestimation of the true boiling point as pointed out already), the vapour pressure of LAS-IPA is very likely < 0.01 Pa.
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