[1] |
巩金龙. CO2化学转化研究进展概述[J]. 化工学报, 2017, 68(4):1282-1285. GONG J L. A brief overview on recent progress on chemical conversion of CO2[J]. CIESC Journal, 2017, 68(4):1282-1285.
|
[2] |
中华人民共和国国家统计局. 中华人民共和国2015年国民经济和社会发展统计公报[N]. 人民日报, 2016-02-29(10). National Bureau of Statistics, the People's Republic of China. Statistical bulletin of the national economic and social development of the People's Republic of China in 2015[N]. People's Daily, 2016-02-29(10).
|
[3] |
张琦, 吴佳艺, 卢平, 等. 磁场对氨水吸收烟气中CO2的促进作用[J]. 化工学报, 2017, 68(6):2555-2562. ZHANG Q, WU J Y, LU P, et al. CO2 absorption by aqueous ammonia solution with use of external magnetic field[J]. CIESC Journal, 2017, 68(6):2555-2562.
|
[4] |
喻健良, 郑阳光, 闫兴清, 等. 工业规模CO2管道大孔泄漏过程中的射流膨胀及扩散规律[J]. 化工学报, 2017, 68(6):2298-2305. YU J L, ZHENG Y G, YAN X Q, et al. Under-expanded jest and dispersion during big hole leakage of high pressure CO2 pipeline in industrial scale[J]. CIESC Journal, 2017, 68(6):2298-2305.
|
[5] |
Al-HWAITI M, Al-KHASHMAN O. Health risk assessment of heavy metals contamination in tomato and green pepper plants grown in soils amended with phosphogypsum waste materials[J]. Environmental Geochemistry & Health, 2015, 37(2):287-304.
|
[6] |
包炜军, 赵红涛, 李会泉, 等. 磷石膏加压碳酸化转化过程中平衡转化率分析[J]. 化工学报, 2016, 68(3):1155-1162. BAO W J, ZHAO H T, LI H Q, et al. Equilibrium conversion analysis of pressurized carbonation with phosphogypsum[J]. CIESC Journal, 2016, 68(3):1155-1162.
|
[7] |
ZHU J H, XIE H P, XIA S L, et al. One step conversion technology of carbon dioxide and phosphogypsum:201210223218.4[P]. 2012-10-22.
|
[8] |
李季, 周加贝, 朱家骅, 等. 磷石膏强化氨法CO2捕集机理与模型[J]. 化工学报, 2015, 66(8):3218-3224. LI J, ZHOU J B, ZHU J H, et al. Mechanism and model of ammoniabased carbon dioxide trapping enhanced by gypsum particles[J]. CIESC Journal, 2015, 66(8):3218-3224.
|
[9] |
王子宁, 周加贝, 朱家骅, 等. 二水硫酸钙溶解动力学[J]. 化工学报, 2015, 66(3):1001-1006. WANG Z N, ZHOU J B, ZHU J H, et al. Dissolution kinetics of calcium sulfate dihydrate[J]. CIESC Journal, 2015, 66(3):1001-1006.
|
[10] |
RAINES M A, DEWERS T A. Mixed transport/reaction control of gypsum dissolution kinetics in aqueous solutions and initiation of gypsum karst[J]. Chemical Geology, 1997, 140(1/2):29-48.
|
[11] |
DEWERS T, RAINES M. Reply to comment on:mixed transport/reaction control of gypsum dissolution kinetics[J]. Chemical Geology, 2000, 168(3):275-278.
|
[12] |
LASAGA A C. Kinetic Theory in the Earth Sciences[M]. Princeton:Princeton University Press, 1998:2-15.
|
[13] |
HILL A E, YANICK N S. Ternary systems. XX. calcium sulfate, ammonium sulfate and water[J]. Journal of the American Chemical Society, 2002, 56(5):1071-1078.
|
[14] |
SULLIVAN E C. Calcium sulfate in ammonium sulfate solution1[J]. Journal of the American Chemical Society, 1905, 27(5):529-539.
|
[15] |
BELL J M, TABER W C. The solubility of gypsum in solutions of ammonium sulfate[J]. J. Phys. Chem., 1906, 10(2):121-122.
|
[16] |
刘仕忠, 朱家骅, 周加贝, 等. (NH4)2SO4-H2O体系中CaSO4·2H2O 溶解度的突变现象[J]. 磷肥与复肥, 2017, 32(4):5-8. LIU S Z, ZHU J H, ZHOU J B, et al. Saltation phenomenon of lean production of CaSO4·2H2O solubility in (NH4)2SO4-H2O system[J]. Phosphate & Compound Fertilizer, 2017, 32(4):5-8.
|
[17] |
顾雪萍, 田璐璐, 冯连芳, 等. 基于新UNIFAC基团的尼龙66盐溶解度的计算方法[J]. 化工学报, 2016, 67(2):435-441. GU X P, TIAN L L, FENG L F, et al. Thermodynamic modeling with new UNIFAC groups for solubility of Nylon66-salt in water system[J]. CIESC Journal, 2016, 67(2):435-441.
|
[18] |
李以圭, 陆九芳.电解质溶液理论[M]. 清华大学出版社, 2005:62, 105-107. LI Y G, LU J F. Theory for Electrolyte Solutions[M]. Beijing:Tsinghua University Press, 2005:62, 105-107.
|
[19] |
BROMLEY L A. Approximate individual ion values of β(or B) in extended Debye-Hückel theory for univalent aqueous solutions at 298.15 K1[J]. Journal of Chemical Thermodynamics, 1972, 4(5):669-673.
|
[20] |
BROMLEY L A. Thermodynamic properties of strong electrolytes in aqueous solutions[J]. AIChE Journal, 1973, 19(2):313-320.
|
[21] |
WILLIAM L M, RUTH S, ERNEST V J. Aqueous systems at high temperatures, XIV. solubility and thermodynamic relationships for CaSO4 in NaCl-H2O solutions from 40 to 200℃. 0 to 4 mole NaCl[J]. Journal of Chemical and Engineering Data, 1964, 9(2):1467-1468.
|
[22] |
WILLIAM L M, RUTH S. Thermodynamics of calcium sulfate dihydrate in aqueous sodium chloride solutions, 0-110°1, 2[J]. Journal of Physical Chemistry, 1966, 70(12):4015-4027.
|
[23] |
吉晓燕, 张吕正, 陆小华, 等. 混合电解质水溶液固液平衡计算[J]. 化工学报, 1997, 48(5):532-539. JI X Y, ZHANG L Z, LU X H, et al. The solid-liquid equilibrium calculation of mixed electrolyte aqueous solution[J]. Journal of Chemical Industry and Engineering(China), 1997, 48(5):532-539.
|
[24] |
孔令启, 王渊朴, 曹婺, 等. 乙酸乙酯-间苯二酚-酸性盐水液液相平衡测定及关联[J]. 化工学报, 2016, 67(4):1098-1102. KONG L Q, WANG Y P, CAO W, et al. Measurement and correlation of liquid-liquid equilibrium data for acetic ether-resorcinol-acid brine system[J]. CIESC Journal, 2016, 67(4):1098-1102.
|
[25] |
CHRISTENSEN C, SANDER B, FREDENSLUND A, et al. Towards the extension of UNIFAC to mixtures with electrolytes[J]. Fluid Phase Equilibria, 1983, 13:297-309.
|
[26] |
YAN W, TOPPHOFF M, ROSE C, et al. Prediction of vapor-liquid equilibria in mixed-solvent electrolyte systems using the group contribution concept[J]. Fluid Phase Equilibria, 1999, 162(1/2):97-113.
|
[27] |
GARAIA A V, THOMSON K, STENBY E H. Prediction of mineral scale formation in geothermal and oilfield operations using the extended UNIQUAC model(Ⅱ):Carbonate-scaling minerals[J]. Geothermics, 2006, 34(1):61-97.
|
[28] |
THOMSON K. Aqueous electrolytes:model parameters and process simulation[D]. Denmark:Department of Chemical Engineering Technical University of Denmark, 1997.
|
[29] |
HAGHTALAB A, PEYVANDI K. Electrolyte-UNIQUAC-NRF model for the correlation of the mean activity coefficient of electrolyte solutions[J]. Fluid Phase Equilibria, 2009, 281(2):163-171.
|
[30] |
THOMSON K, RASMUSSEN P, GANI R. Correlation and prediction of thermal properties and phase behavior for a class of aqueous electrolyte systems[J]. Chemical Engineering Science, 1996, 51(14):3675-3683.
|
[31] |
MESSNAOUI B, OUIAZZANE S, BOUHAOUSS A, et al. A modified electrolyte-UNIQUAC model for computing the activity coefficient and phase diagrams of electrolytes systems[J]. Calphad-computer Coupling of Phase Diagrams & Thermochemistry, 2008, 32(3):566-576.
|
[32] |
BISGAARD T, KADHIM A S. Aktivitetsko efficient model for saltopløsninger:udvikling af et nyt parameter sæt for ammoniumionen til extended UNIQUAC[D]. Denmark:Technical University of Denmark Kgs Lyngby Denmark, 2010.
|
[33] |
付雪梅. 尿素生产解吸及水解系统热力学研究与设备模拟[D]. 重庆:重庆大学, 2011. FU X M. Thermodynamic model and simulation for desorber and hydrolyzer of urea process[D]. Chongqing:Chongqing University, 2011.
|
[34] |
TIAN P, NING P G, CAO K B, et al. Determination and modeling of solubility for CaSO4·2H2O-NH4+-Cl--SO42--NO3-H2O system[J]. Journal of Chemical & Engineering Data, 2012, 57(12):3664-3671.
|
[35] |
HASHEMI S H, DEHGHANI S, DINMOHANNAD M, et al. Prediction of water activity of electrolyte solutions with extended UNIQUAC model[J]. Journal of Chemical and Pharmaceutical Research, 2017, 9(1):247-252.
|