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1.广东工业大学 材料与能源学院,广东 广州 510006
2.广东工业大学 广东省生态安全与绿色发展卓越基础研究中心,广东 广州 510006
3.广东工业大学 碳中和与绿色发展协同创新研究院,广东 广州 510006
4.深圳市燃气集团股份有限公司,广东 深圳 518040
吴世浩(2000—),硕士研究生,研究方向为碳捕集技术,E-mail:2497436946@qq.com。
王珺瑶(1990—),博士,副教授,研究方向为碳捕集技术,E-mail:wangjungyao_hkust@126.com。
收稿日期:2024-05-20,
修回日期:2024-06-17,
纸质出版日期:2025-03-25
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吴世浩,杨智,谢汉林等.基于SAFT类状态方程的CO2、C1~C4烷醇及其混合物气液相平衡特性的预测研究[J].低碳化学与化工,2025,50(03):123-134.
WU Shihao,YANG Zhi,XIE Hanlin,et al.Study on prediction of vapor-liquid phase equilibrium of CO2, C1~C4 alkanols and their mixtures based on SAFT-type equations of state[J].Low-carbon Chemistry and Chemical Engineering,2025,50(03):123-134.
吴世浩,杨智,谢汉林等.基于SAFT类状态方程的CO2、C1~C4烷醇及其混合物气液相平衡特性的预测研究[J].低碳化学与化工,2025,50(03):123-134. DOI: 10.12434/j.issn.2097-2547.20240220.
WU Shihao,YANG Zhi,XIE Hanlin,et al.Study on prediction of vapor-liquid phase equilibrium of CO2, C1~C4 alkanols and their mixtures based on SAFT-type equations of state[J].Low-carbon Chemistry and Chemical Engineering,2025,50(03):123-134. DOI: 10.12434/j.issn.2097-2547.20240220.
相变吸收剂捕集CO
2
作为一种新型低能耗碳捕集技术已受到广泛关注。物理溶剂型相变吸收剂具有分相后富相溶液CO
2
负载更低的优点,具有较好的应用潜力。精确预测溶剂组分的相平衡特性对于相变吸收法CO
2
捕集系统的设计与优化至关重要。针对纯质体系(CO
2
、C
1
、C
2
、C
3
或C
4
烷醇)和二元混合体系(CO
2
+ C
1
烷醇、CO
2
+ C
2
烷醇、CO
2
+ C
3
烷醇或CO
2
+ C
4
烷醇),采用3种典型的统计缔合流体理论(SAFT)类状态方程(分别为CPA、PC-SAFT和SAFT-VR-SW状态方程),系统评估了不同缔合方案对纯质体系气液相平衡特性的预测性能。通过引入二元交互作用系数(
k
ij
),探究了不同状态方程对二元混合体系气液相平衡特性的预测性能。结果表明,对于CO
2
,非缔合方案显示出更高的预测精度,其中采用非缔合方案的PC-SAFT状态方程的预测性能最优;对于C
1
~C
4
烷醇,SAFT-VR-SW状态方程具有最大的预测偏差,而使用CPA或PC-SAFT状态方程时,不论是采用2B方案还是3B方案,整体无显著差异。当
k
ij
为0时,3种状态方程对不同二元混合体系相平衡特性的预测存在显著差异,其中PC-SAFT状态方程对二元混合体系具有较好的预测性能。通过引入最优
k
ij
,3种状态方程对二元混合体系相平衡特性的预测精度均显著提升,其中SAFT-VR-SW状态方程的提升最为显著,预测偏差从35.37%降至5.42%。
Phase change absorbents for CO
2
capture have garnered significant attention as a novel low energy carbon capture technology. Physical solvent-based phase change absorbents exhibit the advantage of lower CO
2
loading of rich-phase solution after phase splitting
indicating strong application potential. Accurate prediction of the phase equilibrium properties of solvent components is crucial for the design and optimization of CO
2
capture systems by phase change absorption. Three typical statistical associating fluid theory (SAFT) equations of state (CPA
PC-SAFT and SAFT-VR-SW EoSs
respectively) were used to systematically evaluate the predictive performance of different association schemes on the vapor-liquid phase equilibrium properties for pure component (CO
2
C
1
C
2
C
3
or C
4
alkanol) and binary mixtures (CO
2
+ C
1
alkanol
CO
2
+ C
2
alkanol
CO
2
+ C
3
alkanol or CO
2
+ C
4
alkanol). By introducing binary interaction parameters (
k
ij
)
the predictive performances of different EoSs for the vapor-liquid phase equilibrium properties of binary mixtures were investigated. The results indicate that for CO
2
the non-association scheme demonstrates higher predictive accuracy
with the PC-SAFT EoS providing the best performance. For C
1
alcohol to C
4
alcohol
the SAFT-VR-SW EoS shows the largest predictive deviation
while the CPA and PC-SAFT EoSs exhibit no significant differences
regardless of using the 2B or 3B association schemes. When
k
ij
is 0
there is a significant difference in the phase equilibrium properties prediction of the three EoSs for different binary mixtures
with the PC-SAF
T EoS yields superior predictive capabilities. By introducing the optimal
k
ij
the prediction accuracies of the phase equilibrium properties of the three EoSs for the binary mixtures are significantly improved
with the most notable improvement in the SAFT-VR-SW EoS
where the predicted deviation decreases from 35.37% to 5.42%.
桑伟 , 唐建峰 , 花亦怀 , 等 . 物理溶剂及有机胺的性质对相变吸收性能的影响 [J ] . 化工进展 , 2023 , 42 ( 4 ): 2151 - 2159 .
SANG W , TANG J F , HUA Y H , et al . Effects of physical solvent and amine properties on the performance of biphasic solvent [J ] . Chemical Industry and Engineering Progress , 2023 , 42 ( 4 ): 2151 - 2159 .
BORHANI T N , WANG M . Role of solvents in CO 2 capture processes: The review of selection and design methods [J ] . Renewable and Sustainable Energy Reviews , 2019 , 114 : 109299 .
JIN L J , HOU X Y , ZHAN L X , et al . Analysis of the changes in the absorption and regeneration performance of diethylenetriamine in carbon capture environments with functionalized alcohols and mixed amines [J ] . Fuel , 2024 , 368 : 131375 .
JIN X H , REN E , YANG Y . Effect of solvents on the phase separation behavior and CO 2 capture performance of MEA-based nonaqueous absorbents [J ] . Energy & Fuels , 2022 , 36 ( 13 ): 6965 - 6973 .
ZHANG G Y , LIU J S , QIAN J , et al . Review of research progress and stability studies of amine-based biphasic absorbents for CO 2 capture [J ] . Journal of Industrial and Engineering Chemistry , 2024 , 134 : 28 - 50 .
石玉美 , 汪荣顺 , 顾安忠 , 等 . CH 4 -N 2 -CO 2 三元气液相平衡试验研究 [J ] . 天然气工业 , 2002 , 22 ( 5 ): 84 - 87 .
SHI Y M , WANG R S , GU A Z , et al . Experimental study on CH 4 -N 2 -CO 2 ternary vapor-liquid phase equilibrium [J ] . Natural Gas Industry , 2002 , 22 ( 5 ): 84 - 87 .
ALKHATIB I I , GALINDO A , VEGA L F . Systematic study of the effect of the co-solvent on the performance of amine-based solvents for CO 2 capture [J ] . Separation and Purification Technology , 2022 , 282 : 120093 .
LIU H L , CHAN C , TONTIWACHWUTHIKUL P , et al . Analysis of CO 2 equilibrium solubility of seven tertiary amine solvents using thermodynamic and ANN models [J ] . Fuel , 2019 , 249 : 61 - 72 .
DONG Y , PING T T , SHEN S F . Solubility of CO 2 in nonaqueous system of 2-(butylamino) ethanol with 2-butoxyethanol: Experimental data and model representation [J ] . Chinese Journal of Chemical Engineering , 2022 , 41 : 441 - 448 .
LI Q , GAO H X , LIU S , et al . Novel thermodynamic model for vapor-liquid equilibrium of CO 2 in aqueous solution of 4-(ethyl-methyl-amino)-2-butanol with designed structures [J ] . Chemical Engineering Science , 2020 , 218 : 115557 .
KWAK C , SANDLER S I , BYUN H S . Correlation of vapor-liquid equilibria for binary mixtures with free energy-based equation of state mixing rules: Carbon dioxide with alcohols, hydrocarbons, and several other compounds [J ] . Korean Journal of Chemical Engineering , 2006 , 23 : 1016 - 1022 .
YU C H , LIN Y J , WONG D S , et al . Modeling fluid phase equilibria of carbon dioxide-methanol binary system [J ] . Fluid Phase Equilibria , 2021 , 529 : 112866 .
TAHERI M , DAI C N , LEI Z G . CO 2 capture by methanol, ionic liquid, and their binary mixtures: Experiments, modeling, and process simulation [J ] . Aiche Journal , 2018 , 64 ( 6 ): 2168 - 2180 .
SIMA S , SECUIANU C , FEROIU V , et al . Phase equilibrium experiments and modeling for the carbon dioxide + ethanol system at high pressures [J ] . Bulletin of Romanian Chemical Engineering Society , 2014 , 1 ( 1 ): 130 - 138 .
SUN R , WANG J Y , TIAN H , et al . Critical points calculation of CO 2 -based binary mixture working fluids: Evaluation of PC-SAFT equation of state [J ] . Fluid Phase Equilibria , 2024 , 577 : 113986 .
JIA W L , SONG S S , LI C J , et al . Simulation of multiphase behavior in supercritical CO 2 -heavy oil-water sludge extraction systems using Cubic-Plus-Association equation of state [J ] . The Journal of Supercritical Fluids , 2023 , 200 : 106001 .
ALKHATIB I I , PEREIRA L M , ALHAJAJ A , et al . Performance of non-aqueous amine hybrid solvents mixtures for CO 2 capture: A study using a molecular-based model [J ] . Journal of CO 2 Utilization , 2020 , 35 : 126 - 144 .
SCHICK D , BIERHAUS L , STRANGMANN A , et al . Predicting CO 2 solubility in aqueous and organic electrolyte solutions with ePC-SAFT advanced [J ] . Fluid Phase Equilibria , 2023 , 567 : 113714 .
SCHULZE-HULBE A , SHAAHMADI F , BURGER A J , et al . Toward nonaqueous alkanolamine-based carbon capture systems: Parameterizing amines, secondary alcohols, and carbon dioxide-containing systems in s-SAFT- γ Mie [J ] . Industrial & Engineering Chemistry Research , 2023 , 62 ( 35 ): 14061 - 14083 .
OLIVEIRA M B , QUEIMADA A J , KONTOGEORGIS G M , et al . Evaluation of the CO 2 behavior in binary mixtures with alkanes, alcohols, acids and esters using the Cubic-Plus-Association equation of state [J ] . The Journal of Supercritical Fluids , 2011 , 55 ( 3 ): 876 - 892 .
KONTOGEORGIS G M , MICHELSEN M L , FOLAS G K , et al . Ten years with the CPA (Cubic-Plus-Association) equation of state. Part 1. Pure compounds and self-associating systems [J ] . Industrial & Engineering Chemistry Research , 2006 , 45 ( 14 ): 4855 - 4868 .
GROSS J , SADOWSKI G . Perturbed-chain SAFT: An equation of state based on a perturbation theory for chain molecules [J ] . Industrial & Engineering Chemistry Research , 2001 , 40 ( 4 ): 1244 - 1260 .
GIL-VILLEGAS A , GALINDO A , WHITEHEAD P J , et al . Statistical associating fluid theory for chain molecules with attractive potentials of variable range [J ] . The Journal of Chemical Physics , 1997 , 106 ( 10 ): 4168 - 4186 .
毛元敬 , 杨智 , 莫松平 , 等 . C 6 ~C 10 烷醇的 SAFT-VR Mie 状态方程参数回归及其热物性研究 [J ] . 化工学报 , 2023 , 74 ( 3 ): 1033 - 1041 .
MAO Y J , YANG Z , MO S P , et al . Estimation of SAFT-VR Mie equation of state parameters and thermodynamic properties of C 6 ~C 10 alcohols [J ] . CIESC Journal , 2023 , 74 ( 3 ): 1033 - 1041 .
SOAVE G . Equilibrium constants from a modified Redlich-Kwong equation of state [J ] . Chemical Engineering Science , 1972 , 27 ( 6 ): 1197 - 1203 .
WERTHEIM M S . Fluids with highly directional attractive forces. I. Statistical thermodynamics [J ] . Journal of Statistical Physics , 1984 , 35 ( 1/2 ): 19 - 34 .
HUANG S H , RADOSZ M . Equation of state for small, large, polydisperse, and associating molecules [J ] . Industrial & Engineering Chemistry Research , 1990 , 29 ( 11 ): 2284 - 2294 .
TSIVINTZELIS I , KONTOGEORGIS G M , MICHELSEN M L , et al . Modeling phase equilibria for acid gas mixtures using the CPA equation of state. I. Mixtures with H 2 S [J ] . AIChE Journal , 2010 , 56 ( 11 ): 2965 - 2982 .
GALINDO A , BLAS F J . Theoretical examination of the global fluid phase behavior and critical phenomena in carbon dioxide + n -alkane binary mixtures [J ] . The Journal of Physical Chemistry B , 2002 , 106 ( 17 ): 4503 - 4515 .
TOCHIGI K , NAMAE T , SUGA T , et al . Measurement and prediction of high-pressure vapor-liquid equilibria for binary mixtures of carbon dioxide + n -octane, methanol, ethanol, and perfluorohexane [J ] . The Journal of Supercritical Fluids , 2010 , 55 ( 2 ): 682 - 689 .
WATSON G , LAFITTE T , ZÉBERG-MIKKELSEN C K , et al . Volumetric and derivative properties under pressure for the system 1-propanol + toluene: A discussion of PC-SAFT and SAFT-VR [J ] . Fluid Phase Equilibria , 2006 , 247 ( 1/2 ): 121 - 134 .
CUEVAS J , LLOVELL F , GALINDO A , et al . Solid-liquid equilibrium using the SAFT-VR equation of state: Solubility of naphthalene and acetic acid in binary mixtures and calculation of phase diagrams [J ] . Fluid Phase Equilibria , 2011 , 306 ( 1 ): 137 - 147 .
DOS RAMOS M C . Phase equilibria of complex mixtures involving supercritical carbon dioxide, water, polymers and surfactants using the SAFT equation of state [D ] . Huelva : Universidad de Huelva , 2006 .
DIAMANTONIS N I , ECONOMOU I G . Modeling the phase equilibria of a H 2 O-CO 2 mixture with PC-SAFT and tPC-PSAFT equations of state [J ] . Molecular Physics , 2012 , 110 ( 11/12 ): 1205 - 1212 .
GROSS J , SADOWSKI G . Application of the perturbed-chain SAFT equation of state to associating systems [J ] . Industrial & Engineering Chemistry Research , 2002 , 41 ( 22 ): 5510 - 5515 .
LAFITTE T , PIÑEIRO M M , DARIDON J , et al . A comprehensive description of chemical association effects on second derivative properties of alcohols through a SAFT-VR approach [J ] . The Journal of Physical Chemistry B , 2007 , 111 ( 13 ): 3447 - 3461 .
MARSHALL B D . A PC-SAFT model for hydrocarbons V: Alcohol-hydrocarbon phase behavior with application to petroleum pseudo-components [J ] . Fluid Phase Equilibria , 2020 , 507 : 112420 .
LEMMON E W , BELL I H , HUBER M L , et al . NIST standard reference database 23: Reference fluid thermodynamic and transport properties-REFPROP, Version 10.0, National Institute of Standards and Technology [EB/OL ] . ( 2018 )[ 2024-05-20 ] . https://www.nist.gov/srd/nist23.cfm https://www.nist.gov/srd/nist23.cfm .
GREEN D W , SOUTHARD M Z . Perry’s chemical engineers’ handbook [M ] . 9th ed . New York : McGraw-Hill Education , 2019 .
AMBROSE D , TOWNSEND R . 681. Thermodynamic properties of organic oxygen compounds. Part IX. The critical properties and vapour pressures, above five atmospheres, of six aliphatic alcohols [J ] . Journal of the Chemical Society (Resumed) , 1963 , 3614 - 3625 .
SINGH R , SHEMILT L W . Critical constants of n -butanol [J ] . The Journal of Chemical Physics , 1955 , 23 ( 7 ): 1370 - 1371 .
CHANG C J , CHIU K L , DAY C Y . A new apparatus for the determination of p - x - y diagrams and Henry’s constants in high pressure alcohols with critical carbon dioxide [J ] . The Journal of Supercritical Fluids , 1998 , 12 ( 3 ): 223 - 237 .
VANDANA V , TEJA A S . Vapor-liquid equilibria in the carbon dioxide + 1-propanol system [J ] . Journal of Chemical and Engineering Data , 1995 , 40 ( 2 ): 459 - 461 .
上接第 96 页)
JENNINGS D W , LEE R J , TEJA A S . Vapor-liquid equilibria in the carbon dioxide + ethanol and carbon dioxide + 1-butanol systems [J ] . Journal of Chemical and Engineering Data , 1991 , 36 ( 3 ): 303 - 307 .
光明网 . 沪深北交易所就可持续发展披露指引公开征求意见 [N/OL ] . ( 2024-02-09 )[ 2024-05-15 ] . https://baijiahao.baidu.com/s?id=1790395262592592381&wfr=spider&for=pc https://baijiahao.baidu.com/s?id=1790395262592592381&wfr=spider&for=pc .
Guang Ming Net . Shanghai , Shenzhen and Beijing stock exchanges ask public comments on sustainable development disclosure guidelines [N/OL ] . ( 2024-02-09 )[ 2024-05-15 ] . https://baijiahao.baidu.com/s?id=1790395262592592381&wfr=spider&for=pc https://baijiahao.baidu.com/s?id=1790395262592592381&wfr=spider&for=pc .
国家发展改革委办公厅 . 国家发展改革委办公厅关于印发首批10个行业企业温室气体排放核算方法与报告指南(试行)的通知 [EB/OL ] . ( 2022-03-10 )[ 2024-05-15 ] . https://www.ndrc.gov.cn/xxgk/zcfb/tz/201311/t20131101_963960. html https://www.ndrc.gov.cn/xxgk/zcfb/tz/201311/t20131101_963960.html .
General Office of National Development and Reform Commission . Notice of the General Office of the National Development and Reform Commission on issuing the first batch of greenhouse gas emission accounting methods and reporting guidelines for enterprises in 10 industries (trial) [EB/OL ] . ( 2022-03-10 )[ 2024-05-15 ] . https://www.ndrc.gov.cn/xxgk/zcfb/tz/201311/t20131101_963960. html https://www.ndrc.gov.cn/xxgk/zcfb/tz/201311/t20131101_963960.html .
科技日报 . 年产400万吨“煤制油”项目加紧二代技术研发 [EB/OL ] . ( 2024-03-26 )[ 2024-05-15 ] . https: //xbj.nea.gov.cn/dtyw/hyxx/202403/t20240326_259660.html https://xbj.nea.gov.cn/dtyw/hyxx/202403/t20240326_259660.html .
Science and Technology Daily . The annual output of 4 million tons of “coal to oil” project has stepped up the research and development of second-generation technology [EB/OL ] . ( 2024-03-26 )[ 2024-05-15 ] . https://xbj.nea.gov.cn/dtyw/hyxx/202403/t20240326_259660. html https://xbj.nea.gov.cn/dtyw/hyxx/202403/t20240326_259660.html .
中国国家标准化管理委员会 . 煤直接液化制油单位产品能源消耗限额 : GB/T 30178—2013 [S ] . 北京 : 中国标准出版社 , 2014 .
Standardization Administration of China . Energy consumption quota per unit product of direct coal liquefaction to oil : GB/T 30178—2013 [S ] . Beijing : Standards Press of China , 2014 .
中国标准化研究院资源环境研究分院 . 关于对《煤化工单位产品能源消耗限额》国家标准征求意见的通知 [EB/OL ] . ( 2020-09-22 )[ 2024-05-15 ] . https://www.cnis.ac.cn/ynbm/zhfy/bzyjzq/gbyjzq/202009/t20200922_50318.html https://www.cnis.ac.cn/ynbm/zhfy/bzyjzq/gbyjzq/202009/t20200922_50318.html .
Resources and Environment Research Branch, China Institute of Standardization . Notice on soliciting opinions on the national standard “energy consumption quota per unit product of coal chemical industry” [EB/OL ] . ( 2020-09-22 )[ 2024-05-15 ] . https://www.cnis.ac. cn/ynbm/zhfy/bzyjzq/gbyjzq/202009/t20200922_50318.html https://www.cnis.ac.cn/ynbm/zhfy/bzyjzq/gbyjzq/202009/t20200922_50318.html .
王力伟 , 陈曦 . 某钢铁厂余热梯级回收用于城市清洁供热案例 [J ] . 暖通空调 , 2024 , 54 ( 1 ): 37 - 39 .
WANG L W , CHEN X . A case of one steel plant step recovering waste heat for clean urban heating [J ] . Heating Ventilating & Air Conditioning , 2024 , 54 ( 1 ): 37 - 39 .
王峰 , 侯学文 , 李云 . 氯碱行业二氧化碳排放量核算方法 [J ] . 氯碱工业 , 2022 , 58 ( 6 ): 30 - 37 .
WANG F , HOU X W , LI Y . Accounting method of carbon dioxide emission in chlor-alkali industry [J ] . Chlor-Alkali Industry , 2022 , 58 ( 6 ): 30 - 37 .
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