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9/19/2014Johan Jacquemin
Database on ionic liquids solubilities
in molecular solvents: progress and
prospects
Johan JACQUEMINQueen’s University Belfast
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IUPAC Project # 2011-065-3-500
Zdeněk Wagner and Magdalena BendovaInstitute of Chemical Process Fundamentals - Prague
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Scope of Presentation
Motivation
Current state of the IUPAC project
Database philosophy, workflow and presentation
Data processing
Example: [C4mim][PF6] + 1-butanol
Conclusions
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Property database
Data analysis Recommended data
LLE – IL based binary mixtures
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Motivation
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Property database
Establishment / validation of predictive models
LLE – IL based binary mixtures
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Motivation
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Property database
Relationships between structure and property
LLE – IL based binary mixtures
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Motivation
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Property database
Web-based interface General public
LLE – IL based binary mixtures
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Motivation
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Motivation
Ionic Liquids:
Application as task-specific solvents
Structure-property relationships
To critically evaluate existing correlation / prediction models e.g.
UNIFAC, NRTL, COSMO-RS, EoS, etc
Thermodynamic model parameters implementation into e.g. Aspen
Plus.
Why the LLE?
• Organic co-solvents to modify their properties (density,
viscosity, etc)
• Separation processes – azeotrope breaking, CO2 capture,
olefin/paraffin separations
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Current state of project
Data literature research and database up to 2013
Complete containing more than:
• 60 different ILs structure
• 100 organic solvents
• 300 articles
• 3000 data points
Data literature research and database 2014-now
Under way
Web-based interface ready for data upload
Accessible only to project members
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Database philosophy and Access
A user-friendly interface
Easy data upload
Multistage control of uploaded datasets
XML-based communication language
Interconnectivity of different databases
Easy data export
Access
Administrators – full access
Maintainers - add and edit data
Ordinary users - read-only access to data in the public part
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Database editing
Multistage control of data upload:
Editing
Incomplete table owned by one of the maintainers
Other maintainers may view but cannot edit
Private
Complete table not yet approved by administrator
Any maintainer may start editing
Public
Publicly accessible table by ordinary users
If need be, any maintainer is allowed to edit it
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Workflow
Multistage control of data upload:
New table started by maintainer
Editing stage
Other maintainers read-only access to check and prevent duplicity
of tables
Maintainer finishes table
Table marked as completed and becomes private
Table approval by administrator
Public table
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Workflow troubleshooting
Multistage control of data upload:
Bug spotted in private or public table
Any maintainer may revert to editing stage and edit
After completion the table becomes private and requires approval
Table in editing stage for a long time (e.g. due to illness of
a maintainer)
Administrator may force it to private stage
Another maintainer can continue
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Database contents
Relational database with following tables:
1. ILs (formula, name, alias/trivial names, CAS number)
2. Molecular Solvents (formula, name, alias/trivial names,
CAS number)
3. Journals (name, abbreviation, CODEN), CODEN search
at http://cassi.cas.org
4. Authors (name, alias names if known, unique ID for the
database purposes)
5. Citation using information from Tables 3 and 4
6. Measurement methods
7. Data
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Required content
Apart from data:
link to the measurement method,
precisions of measurement of all variables,
purity (contents of water, halides, lithium, etc.),
optional unformatted comment:
• e.g. separate information on the contents of chlorides,
bromides, iodides should be entered rather than summing them
up and reporting them as halides.
Literature reference
DOI whenever available: XML formatted record from CrossRef may
be requested by SW.
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Data storage & search procedure
Relational database should be sufficient
Database should contain only controlled vocabulary
Contents must conform to IUPAC standards for data
publication
Search procedure
Ionic liquid
Solvent
Table of systems
• defined by links to table of ILs and table of solvents
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Database presentation
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Data presentation
The user interface should offer:
download in several data formats, especially in ThermoML
graphical display
support for critical evaluation using modern robust tools based on
mathematical gnostics:
see http://www.math-gnostics.com
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Mathematical gnostics
Non-statistical tool used to efficiently treat small samples
of strongly uncertain data
Robust regression of data: bi-dimensional (true and
uncertain) contributions
No a priori assumption of error distribution function
Let the data speak for themselves
Outlier detection
Determination of typical data and tolerance intervals
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Data processing
Critical assessment of data
Mathematical gnostics
Recommended data
Data correlation
Modified Flory-Huggins equation
UNIFAC group-contribution parameters (R, Q, aij)
Implementation of requested parameters into Aspen
• NB. Other fitting parameters must be also implemented into
Aspen (e.g. CpIG, Cp, density, viscosity, etc)
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An example of data processing
Binary system x [C4mim][PF6] + (1-x) 1-butanol
See Bendová M., Wagner Z.: Liquid-Liquid Equilibrium in Binary
System [bmim][PF6] + 1-Butanol. J. Chem. Eng. Data 2006, 51(6),
2126–2131.
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Good agreement between
experimental data with the
modified FH equation, except
for the critical region
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An example of data processing
Binary system x [C4mim][PF6] + (1-x) 1-butanol
See Bendová M., Wagner Z.: Liquid-Liquid Equilibrium in Binary
System [bmim][PF6] + 1-Butanol. J. Chem. Eng. Data 2006, 51(6),
2126–2131.
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The logarithmic scale: clearer
comparison between the exp.
and calculated values at low
concentrations.
It is evident that there may be
discrepancies in the alcohol-
rich phase.
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An example of data processing
Binary system [C4mim][PF6] + 1-butanol
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Each homogeneity test shows error distribution for all the data together.
Residuals were weighed with the corresponding estimated concentration
measurement uncertainty in the given phase.
The main part = the normal distribution of errors.
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An example of data processing
Binary system [C4mim][PF6] + 1-butanol
Data by Maurer et al. IL phase
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Errors in the IL phase are
nonhomogeneous, e.g. the
maximum is shifted towards
negative values.
Correlation of this single
dataset highlights a problem in
the experimental method
(sensibility too low, different IL
batches were used,
measurement were done by
more than one person ?)
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Towards a database of databases?
Our database – a „mould“ for all the IUPAC databases
Interconnection of the individual databases?
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Towards a database of databases?
Our database – a „mould“ for all the IUPAC databases
Interconnection of the individual databases?
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Massive properties databases
Relationships between structure and properties
Pure ILs Mixtures containing ILs
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Conclusions
Progress of the IUPAC Project # 2011-065-3-500
Web-based interface up and running
Complete database of solubility data from 2000 to 2014 by the
end of 2014
Towards a JPCRD publication in 2015
• Critical analysis experimental methods and data sets
• Modified Flory-Huggins equation
• UNIFAC group-contribution parameters (R, Q, aij)
Prospects of the project
Implementation of the database into database of databases?
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Acknowledgements
From QUB – Belfast – UK
Prof. Chris Hardacre
Prof. David Rooney
From ICPF – Prague – Czech Republic
Dr Magdalena Bendova
Dr Zdeněk Wagner
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IUPAC for funding under project
# 2011-065-3-500