AI Chat Paper
Note: Please note that the following content is generated by AMiner AI. SciOpen does not take any responsibility related to this content.
{{lang === 'zh_CN' ? '文章概述' : 'Summary'}}
{{lang === 'en_US' ? '中' : 'Eng'}}
Chat more with AI
PDF (9.7 MB)
Collect
Submit Manuscript AI Chat Paper
Show Outline
Outline
Show full outline
Hide outline
Outline
Show full outline
Hide outline
Publishing Language: Chinese

Optimization of thermogravimetric method for measuring very low saturation vapor pressure

Zhongwei LIXiaofei LIZuozhou TangWenting XUQiang SONG( )
Key Laboratory for Thermal Science and Power Engineering of Ministry of Education, Tsinghua University, Beijing 100084, China
Show Author Information

Abstract

Objective

Vapor pressure is a fundamental thermodynamic property, the measurement of which is particularly important. Coal-fired pollution control research needs basic data on the vapor pressure of heavy metals, but it is very low and is difficult to measure. A common method for measuring very low vapor pressure is thermogravimetric analysis, wherein vapor pressure is estimated using the evaporation rate. The key factors affecting the measurement accuracy are the conditions under which the linear relationship between the vapor pressure and the evaporation rate is established and the similarity of the calibration constants k of different substances.

Methods

Taking the TA Q500 thermogravimetric analyzer as an example, this paper establishes a mathematical model for isothermal evaporation in a thermogravimetric analyzer. The thermogravimetric analyzer's flow field and evaporation process are analyzed via computational fluid dynamics (CFD) method. Numerical simulations are conducted for six organic substances and 160 model substances under various temperature and carrier gas flow conditions. The independence of the grids used in the numerical simulations is verified through examination of the x-direction velocities, y-direction velocities, and mass fraction distributions for different numbers of grids. The reliability of the calculated results is verified using the experimental results obtained for the vapor pressure of benzoic acid.

Results

A comparison of the mass distribution diagrams of organic substances revealed that the evaporative mass transfer in the thermogravimetric analyzer was due to the combined effect of molecular diffusion and convective transport. The evaporation process, which was typically analyzed using the Langmuir equation, was based on molecular diffusion, which meant that the Langmuir equation was not be applicable to describe the evaporation process inside the thermogravimetric analyzer. The experimental conditions (carrier gas flow rate and temperature) and substance properties (molar mass, vapor pressure, and diffusion coefficient) would affect the evaporation and mass transfer of the substance and further affected the calibration constant k. A numerical simulation of the isothermal evaporation process of 160 model substances revealed that the difference in the physical properties of these substances could result in significant differences in k. k increased with decreasing molar mass and diffusion coefficient and increasing vapor pressure. The dimensionless analysis of the governing equations showed that the evaporation process was determined by the dimensionless quantities Re(Reynolds number), Pe(Peclet number), and wi(the dimensionless form of the sample vapor mass fraction on the crucible surface). Through the dimensionless analysis of the governing equations, the nonlinear relationship between evaporation rate and vapor pressure was obtained via fitting. When the molar mass and vapor pressure of the substance were small, the relationship between the vapor pressure and the evaporation rate was more linear. The deviations obtained from the different calibration-constant calculation methods were compared. The results confirmed that the calibration constant k was related to the vapor pressure. The results also proved that the key influencing parameters obtained through the dimensionless analysis of the governing equation were reliable. The influence of physical properties on pressure measurement deviation was analyzed, and the results revealed that the closer the molar mass and diffusion coefficient values between the substance to be measured and the calibration substance, the smaller the difference in k between the two substances.

Conclusions

Based on the analysis of the results, it is found that: The relationship between evaporation rate and vapor pressure is approximately linear only when the molar mass and vapor pressure of the substance are small. When choosing a calibration substance, in order to reduce the measurement deviation of vapor pressure, the substance with the diffusion coefficient and molar mass of the substance to be measured should be selected as close as possible.

CLC number: TK312 Document code: A Article ID: 1000-0054(2023)11-1833-11

References

[1]

XU W T, SONG Q, SONG G C, et al. The vapor pressure of Se and SeO2 measurement using thermogravimetric analysis[J]. Thermochimica Acta, 2020, 683: 178480.

[2]

LI S H, YANG F F, ZHANG K, et al. Vapor pressure measurements and correlation for trans-1-chloro-3, 3, 3-trifluoroprop-1-ene[J]. Journal of Chemical & Engineering Data, 2019, 64(7): 2947-2954.

[3]

SITE A D. The vapor pressure of environmentally significant organic chemicals: A review of methods and data at ambient temperature[J]. Journal of Physical and Chemical Reference Data, 1997, 26(1): 157-193.

[4]

LANGMUIR I. The vapor pressure of metallic tungsten[J]. Physical Review, 1913, 2(5): 329-342.

[5]

PRICE D M, HAWKINS M. Calorimetry of two disperse dyes using thermogravimetry[J]. Thermochimica Acta, 1998, 315(1): 19-24.

[6]

PRICE D M. Vapor pressure determination by thermogravimetry[J]. Thermochimica Acta, 2001, 367-368: 253-262.

[7]

CUDDY M F, PODA A R, CHAPPELL M A. Estimations of vapor pressures by thermogravimetric analysis of the insensitive munitions IMX-101, IMX-104, and individual components[J]. Propellants, Explosives, Pyrotechnics, 2014, 39(2): 236-242.

[8]

BARRETO GOMES A P, FREIRE F D, SOARES ARAGÃO C F. Determination of vapor pressure curves of warifteine and methylwarifteine by using thermogravimetry[J]. Journal of Thermal Analysis and Calorimetry, 2012, 108(1): 249-252.

[9]

DE OLIVEIRA C E L, CREMASCO M A. Determination of the vapor pressure of Lippia gracilis Schum essential oil by thermogravimetric analysis[J]. Thermochimica Acta, 2014, 577: 1-4.

[10]

PHANG P, DOLLIMORE D, EVANS S J. A comparative method for developing vapor pressure curves based on evaporation data obtained from a simultaneous TG-DTA unit[J]. Thermochimica Acta, 2002, 392-393: 119-125.

[11]

SUROV O V. Thermogravimetric method used to determine the saturated vapor pressure in a wide range of values[J]. Russian Journal of Applied Chemistry, 2009, 82(1): 42-46.

[12]

RONG Y H, GREGSON C M, PARKER A. Thermogravimetric measurements of liquid vapor pressure[J]. The Journal of Chemical Thermodynamics, 2012, 51: 25-30.

[13]

BARONTINI F, COZZANI V. Thermogravimetry as a screening tool for the estimation of the vapor pressures of pure compounds[J]. Journal of Thermal Analysis and Calorimetry, 2007, 89(1): 309-314.

[14]

FOCKE W W. A revised equation for estimating the vapour pressure of low-volatility substances from isothermal TG data[J]. Journal of Thermal Analysis and Calorimetry, 2003, 74(1): 97-107.

[15]

PIETERSE N, FOCKE W W. Diffusion-controlled evaporation through a stagnant gas: Estimating low vapour pressures from thermogravimetric data[J]. Thermochimica Acta, 2003, 406(1-2): 191-198.

[16]

PARKER A, BABAS R. Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube[J]. Thermochimica Acta, 2014, 595: 67-73.

[17]

ZGHAL I, FARJAS J, CAMPS J, et al. Thermogravimetric measurement of the equilibrium vapour pressure: Application to water and triethanolamine[J]. Thermochimica Acta, 2018, 665: 92-101.

[18]

SZCZOTOK A M, KJØNIKSEN A L, RODRIGUEZ J F, et al. The accurate diffusive model for predicting the vapor pressure of phase change materials by thermogravimetric analysis[J]. Thermochimica Acta, 2019, 676: 64-70.

[19]

VLASOV V A. Diffusion-kinetic model of liquid evaporation from a Stefan tube: A solution to the Stefan diffusion problem[J]. International Journal of Heat and Mass Transfer, 2020, 163: 120379.

[20]

FULLER E N, SCHETTLER P D, GIDDINGS J C. New method for prediction of binary gas-phase diffusion coefficients[J]. Industrial & Engineering Chemistry, 1966, 58(5): 18-27.

[21]

POLING B E, PRAUSNITZ J M, O'CONNELL J P. Properties of gases and liquids[M]. New York: McGraw-HillEducation, 2001.

[22]

TANG M J, SHIRAIWA M, PÖSCHL U, et al. Compilation and evaluation of gas phase diffusion coefficients of reactive trace gases in the atmosphere: Volume 2. Diffusivities of organic compounds, pressure-normalised mean free paths, and average Knudsen numbers for gas uptake calculations[J]. Atmospheric Chemistry and Physics, 2015, 15(10): 5585-5598.

[23]

MONTE M J S, SANTOS L M N B F, FULEM M, et al. New static apparatus and vapor pressure of reference materials: Naphthalene, benzoic acid, benzophenone, and ferrocene[J]. Journal of Chemical & Engineering Data, 2006, 51(2): 757-766.

[24]

LIU G Q, MA L X, XIANG S G. Handbook of physical properties for chemistry and chemicals (Organic Volume)[M]. Beijing: Chemical Industry Press, 2013. (in Chinese)

Journal of Tsinghua University (Science and Technology)
Pages 1833-1843
Cite this article:
LI Z, LI X, Tang Z, et al. Optimization of thermogravimetric method for measuring very low saturation vapor pressure. Journal of Tsinghua University (Science and Technology), 2023, 63(11): 1833-1843. https://doi.org/10.16511/j.cnki.qhdxxb.2023.26.030

110

Views

1

Downloads

0

Crossref

0

Scopus

0

CSCD

Altmetrics

Received: 27 October 2022
Published: 15 November 2023
© Journal of Tsinghua University (Science and Technology). All rights reserved.
Return