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Empirical determination of Henrys Law constants in hydrocarbon liquids

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Changes in temperature cause the saturation vapor pressure value and the KFT ... The picture shown here describes equilibrium at saturation. ... – PowerPoint PPT presentation

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Title: Empirical determination of Henrys Law constants in hydrocarbon liquids


1
Empirical determination of Henrys Law
constants in hydrocarbon liquids Session 1680
Fuels and Petrochemical Analysis Abstract
1680-9 Pittcon 2003 Orlando,Fl March 12,2003,
425 PM, Room 203A   LPTalarico COSA Instrument
Corporation
2
Experimental design
  • Literature investigation yielded no comprehensive
    source of water saturation values (ppmw) for the
    hydrocarbons of interest
  • Due to the importance of ppmw(ug/g) at saturation
    ..testing began here
  • Next a pilot plant was constructed to vary
    temperature, flow and moisture concentration.
    This facilitated measurements in the
    concentration ranges desired by hydrocarbon
    producers and processors
  •  
  • Based on the results of the first two
    investigations it became clear an ESS (Extractive
    Sample System) could link these approaches
    enabling more reliable moisture measurement. The
    system highlighted here incorporates Dew Point
    measurement with KFT(Karl Fischer Titration) and
    Gas Chromatography to ensure accuracy and
    validation with relative ease

3
Henrys Law
  • CakPa
  • Ca(KFT ppmwug/g)
  • k(Henrys constant)
  • Pa (saturation vapor pressure of water at
    TmmHg)
  •  
  • Temperature is the key parameter..different
    T.different k
  • Changes in temperature cause the saturation vapor
    pressure value and the KFT value of the
    hydrocarbon to change
  • Mixtures
  •  
  • Average saturation values are calculated by
    weight fractions of the individual components

4
Special case of Henrys Law
  • Saturated hydrocarbon chains exhibit a unique
    physical property
  • Their k factor does not vary significantly with
    temperature
  •  
  • This special case is where we did our work.
  • With sample temperature falling from the
    equation our experiments investigated important
    sensor calibration and aging issues

5
Physical Chemistry
  • Goff-Gratch equations express the physical
    property defined as saturation vapor pressure in
    the pure phase over plane surfaces of pure water
    and pure ice
  • Their integration of the Clausius-Clapeyron
    equations led to Saturation Vapor Tables adopted
    by the International Meteorological Organization
    in 1947
  • References
  • Keyes, F.G., Journ. Chem. Phys., vol. 15 No.8,
    pp. 602-12, 1947
  • Goff, J.A and Gratch, S., Trans. Amer. Soc. Heat.
    And Vent. Eng., vol. 52, 1946
  • Smithsonian Meteorological Tables, publication
    4014, 1949

6
Dew Formation
The picture shown here describes equilibrium at
saturation. The excess water globules in the
organic demonstrate saturation in the liquid
phase and the dew formation demonstrates water
saturation in the gas phase
7
Analytical Chemistry
  • Karl Fischer Titration
  •  
  • H2OI2SO23BaseCH3OH---2Base.HIBase.HSO4CH3
  •  
  • Coulometric type
  •  
  • 2I- - 2e I2
  •  
  • Stochiometry
  •  
  • 10.72 coulombs---1 mole of H2O
  •  
  • This approach is best suited to low level
    moisture determinations Detection levels of less
    than 10 ug absolute H2O are possible
  •  
  • Reference
  • Mitsubishi Chemical Corporation, Karl Fischer
    Reagents, 2000

8
Results of the investigations
  • The following hydrocarbons were chosen for
    testing
  • They represent the alkane, alkene, aromatic and
    cyclic
  • families
  • The saturation values were calculated by KFT and
    the
  • Vapor Pressures by Goff-Gratch equations yielding
    the
  • following Henrys constants
  • Hexanes2.5
  • Benzene20.6
  • Hexene8.3
  • Transformer Oil2.3
  • 50/50 Mixture Hexanes/Benzene11.5

9
Measuring Saturation PPMW
  • Method..simple form
  • Prepare water saturated hydrocarbon sample
    (excess water observable) mix continuously _at_ 300
    rpm with magnetic stirrer.
  • Place sample and stirrer in environmental chamber
    at set temperature.
  • Prepare coulometric KF titration cell and dry to
    acceptable background. Place titrator and
    titration cell into chamber
  • Connect buret to sample flask. Equilibrate by
    cycling buret to and from sample flask
  • Measure the mass of 1 ml volume at set
    temperature
  • Verify accuracy of KFT by check solution
    injections
  • Measure moisture concentration by KFT. KFT
    samples taken after 18 hours in the
    environmental chamberenough time to reach
    equilibrium
  • Comments
  • Titrator temperature stabilized
  • Sample temperature stabilized

10
Environmental Chamber
11
Environmental Chamber
12
Results for various Organics tested
The raw data and graphs for hexene, transformer
oil, benzene and a mixture of benzene and hexane
are available. If you have interest please
contact me after the presentation The rest of
this presentation focuses on Hexane
13
Raw dataTransformer Oil
14
GraphTransformer oil
15
Raw data Benzene
16
Graph Benzene
17
Raw dataHexene
18
GraphHexene
19
Raw data mixture Benzene/Hexane
20
Graph mixture Benzene/Hexane
21
Raw dataHexane
22
GraphHexane
23
Pilot Plant Measuring System
  • In order to investigate Henrys constants in
    organic liquids in real world concentrations a
    number of parameters had to be controlled
  • A pilot plant system was designed
  • The system incorporates Dew Point measurement
    both gas and liquid with Karl Fischer Titration
    while maintaining stable temperature and flow and
    the ability to vary moisture concentration
  •  

24
Schematic Pilot Plant System
25
Picture Pilot Plant System
26
Measurements in Hexane 0.5 PPMW to 75.0 PPMW
27
Graph of working range data
28
Theoretical and Empirical Data Hexane
29
What does this all mean
  • Xentaurs Al2O3 sensor calibrated to report Dew
    Point
  • seems to be good trend indicator of moisture
  • concentration
  • Calibration to report PVP may be more useful
  • Reliable PPMW (ug/g) values are possible using
  • Henrys constant (special case) if rigorous
    attention is paid to
  • sensor calibration
  • Simple validation will insure accuracy
  • The matrix can be confirmed by GC
  • The moisture can be confirmed by KFT

30
A new approachESS with integral
validation
31
Extractive Sample System Components
  • The ESS has three components
  • Xentaur AL2O3 sensor.the essence
  • The Xentaur HDT.the brain
  • The sample BOMB.the validation

32
Xentaur Al2O3 sensor
33
Comments on sensor stabilization
  • Our research has confirmed with proprietary
    manufacturing procedures a stable sensor is
    produced
  • Our research has confirmed sensors calibrated
    with gas can report PVP in both liquids and gases

34
The HDT
  • A multipoint calibration table with temperature
    compensation over the full range provides
    unsurpassed accuracy
  • Loop power provides ease of use
  • HART interface provides 4-20 mA and digital
    outputs and alarms

35
The BOMB
  • Provides possibilities for integral calibration
    and validation of both important
    parameters.matrix and moisture concentration

36
Summary/Conclusions
  • Al2O3 sensors measure increases and decreases in
    PVP and are good
  •   moisture concentration trend indicators
  • Al2O3 sensors in hydrocarbon liquid streams are
    quite stable and accurate
  •  
  • KFT accounts for sample matrix variations. Thus
    its the measurement
  • to rely on for absolute moisture concentration
  •  
  • GC can verify the matrix providing concrete
    insight into Henrys Law
  • constants for the sample steam of concern
  •  
  • By combining PVP measurement with GC and KFT via
    an Extractive
  • Sample System process control is truly
    possible..NO MORE
  • MYSTERY
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