无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ
化工装备与设计

氯盐体系硝酸/盐酸脉冲萃取分离装置水力学研究

  • 潘柏成 ,
  • 孙泽 ,
  • 马珍 ,
  • 张海军 ,
  • 董昌吉 ,
  • 宋兴福
展开
  • 1.资源(盐湖)过程工程教育部工程研究中心,华东理工大学,上海 200237
    2.青海盐湖工业股份有限公司
    3.青海盐湖硝酸盐业股份有限公司
潘柏成(1996— ),男,硕士研究生,研究方向为萃取设备;E-mail: baicpan@163.com

收稿日期: 2021-03-10

  网络出版日期: 2022-03-14

基金资助

国家重点研发计划(2018YFC1903803)

Study on hydraulics of pulsed extraction separation device for nitric acid/hydrochloric acid in chloride salt system

  • Baicheng PAN ,
  • Ze SUN ,
  • Zhen MA ,
  • Haijun ZHANG ,
  • Changji DONG ,
  • Xingfu SONG
Expand
  • 1. Engineering Research Center of Resources(Salt Lake) Process Engineering,Ministry of Education,East China University of Science and Technology,Shanghai 200237,China
    2. Qinghai Salt Lake Industry Corporation Limited
    3. Qinghai Salt Lake Nitrate Industry Corporation Limited

Received date: 2021-03-10

  Online published: 2022-03-14

摘要

硝酸-氯化钾直接法可低成本制备熔盐级硝酸钾,溶剂萃取分离氯盐溶液中的硝酸和盐酸是关键步骤之一。研究了处理H+/K+/Cl-/H2O-磷酸三丁酯/磺化煤油体系脉冲筛板萃取塔的水力学性能,结果表明分散相液滴直径随脉冲强度的增大而减小,与两相表观流速无关;存留分数随脉冲强度的增大呈现先减小后增大的趋势,随两相表观流速的增大而增大。拟合得到了液滴直径与存留分数的Kumar-Hartland关联式,两者计算值和实验值的平均相对偏差(AARD)分别为4.74%与5.60%。

本文引用格式

潘柏成 , 孙泽 , 马珍 , 张海军 , 董昌吉 , 宋兴福 . 氯盐体系硝酸/盐酸脉冲萃取分离装置水力学研究[J]. 无机盐工业, 2022 , 54(1) : 91 -95 . DOI: 10.19964/j.issn.1006-4990.2021-0140

Abstract

Direct method of nitric acid-potassium chloride can produce potassium nitrate for molten salt at low cost.The se-paration of nitric acid/hydrochloric acid from a solution containing chloride salts by solvent extraction is one of the key steps.The hydraulic performance of the pulsed sieve plate extraction column in the treatment of H+/K+/Cl-/H2O-tributyl phosphate/sulfonated kerosene system was studied.The results showed that the diameter of the dispersed phase drops decreased with the increase of the pulse intensity,and the superficial velocity of the two phases had almost no effect on it.The holdup firstly decreased and then increased with the increase of the pulse intensity,and increased with the increase of the superficial velocity of the two phases.According to the experimental data,Kumar-Hartland correlations of drop diameter and holdup were fitted,and the average absolute relative deviation(AARD) was 4.74% and 5.60%,respectively.

参考文献

[1] 国家市场监督管理总局, 中国国家标准化管理委员会. GB/T36376—2018 太阳能熔盐(硝基型)[S]. 北京: 中国标准出版社, 2018.
[2] 杜芳林, 李江年, 罗华平, 等. 硝酸和氯化钾直接法制取硝酸钾新工艺的开发[J]. 无机盐工业, 1992(6):15-18.
[3] 谢伟胜. 溶剂萃取法制取硝酸钾研究进展[J]. 现代化工, 2008(6):32-36.
[4] 秦炜, 李小松, 李跃, 等. 一种利用硝酸和氯化钾制备硝酸钾的方法:中国,103112876A[P]. 2013-05-22.
[5] 史忠录, 杜佩英, 于雪峰, 等. 硝酸与氯化钾直接制取硝酸钾工艺研究[J]. 无机盐工业, 2019, 51(8):37-39.
[6] WANG H P, ZHOU Z Y, QIN W, et al. Study and modeling of the li-quid-solid equilibrium of the KCl-KNO3-HCl-H2O system at 283.15 K[J]. AIChE Journal, 2020, 66(1).Doi: 10.1002/aic.16750.
[7] 杜芳林, 宫玉臻. 硝酸与氯化钾直接法制取硝酸钾[J]. 磷肥与复肥, 1997(5):13-15.
[8] 马誉景, 金央, 李军, 等. 硝酸和氯化钾直接制备硝酸钾工艺研究及优化[J]. 无机盐工业, 2015, 47(3):31-34.
[9] PORTELA L S. Process for obtaining potassium nitrate from potassi-um chloride and nitric acid:US,4668495[P]. 1987-05-26.
[10] MANOR S, BAR-GURI M, ALEXANDRON A, et al. Process for the manufacture of potassium nitrate:US,4378342[P]. 1983-03-29.
[11] EYAL A, MIZRAHI J, BANIEL A. Potassium nitrate through solvent separation of strong acids[J]. Industrial & Engineering Chemistry Process Design and Development, 1985, 24(2):387-390.
[12] 苏磊, 张海军, 汪瑾, 等. 反应萃取法制备熔盐级硝酸钾工艺探讨[J]. 无机盐工业, 2020, 52(5):35-39.
[13] 费维扬. 萃取塔设备研究和应用的若干新进展[J]. 化工学报, 2013, 64(1):44-51.
[14] 吴秋林, 王俊峰, 张天祥, 等. 核燃料后处理工程溶剂萃取设备[M]. 北京: 中国原子能出版社, 2012.
[15] LADE V G, RATHOD V K, BHATTACHARYYA S, et al. Compar-ison of normal phase operation and phase reversal studies in a pu-lsed sieve plate extraction column[J]. Chemical Engineering Re-search and Design, 2013, 91(6):1133-1144.
[16] SARKAR S, SEN N, SINGH K K, et al. Effect of operating and geo-metric parameters on dispersed phase holdup in pulsed disc and doughnut and pulsed sieve plate columns:A comparative study[J]. Chemical Engineering and Processing:Process Intensification, 2017, 118:131-142.
[17] SEN N, SARKAR S, SINGH K K, et al. Regime transition and hol-dup in pulsed sieve-plate and pulsed disc and doughnut columns:A comparative study[J]. Solvent extraction and ion exchange, 2018, 36(1):66-83.
[18] TORAB-MOSTAEDI M, GHAEMI A, ASADOLLAHZADEH M. Flooding and drop size in a pulsed disc and doughnut extraction column[J]. Chemical Engineering Research and Design, 2011, 89(12):2742-2751.
[19] KHAJENOORI M, HAGHIGHI-ASL A, SAFDARI J, et al. Predic-tion of drop size distribution in a horizontal pulsed plate extraction column[J]. Chemical Engineering and Processing:Process Intensification, 2015, 92:25-32.
[20] YI H, WANG Y, SMITH K H, et al. Hydrodynamic performance of a pulsed solvent extraction column with novel ceramic internals:Holdup and drop size[J]. Industrial & Engineering Chemistry Research, 2017, 56(4):999-1007.
[21] TAN B, LAN M, LI L X, et al. Drop size correlation and population balance model for an agitated-pulsed solvent extraction column[J]. AIChE Journal, 2020, 66(8).Doi: 10.1002/aic.16279.
[22] KHANRAMAKI F, SAFDARI J, SHIRANI A S, et al. Experimen-tal study on hold-up,characteristic and slip velocities in a horizon-tal pulsed sieve-plate column and uranium reactive extraction con-dition in aqueous phase[J]. Progress in Nuclear Energy, 2018, 109:159-170.
[23] WANG F, MAO Z S. Numerical and experimental investigation of liquid-liquid two-phase flow in stirred tanks[J]. Industrial & En-gineering Chemistry Research, 2005, 44(15):5776-5787.
[24] SCHILLER L, NAUMANN A. Fundamental calculations in gravita-tional processing[J]. Zeitschrift Des Vereines Deutscher Ingenieu-re, 1933, 77:320-381.
[25] MORSI S A, ALEXANDER A J. An investigation of particle trajec-tories in two-phase flow systems[J]. Journal of Fluid Mechanics, 1972, 55(2):193-208.
[26] BARNEA E, MIZRAHI J. A generalised approach to the fluid dy-namics of particulate systems part 2:Sedimentation and fluidisa-tion of clouds of spherical liquid drops[J]. The Canadian Journal of Chemical Engineering, 1975, 53(5):461-468.
[27] AUGIER F, MASBERNAT O, GUIRAUD P. Slip velocity and drag law in a liquid-liquid homogeneous dispersed flow[J]. AIChE Jo-urnal, 2003, 49(9):2300-2316.
[28] KUMAR A, HARTLAND S. Gravity settling in liquid/liquid disper-sions[J]. The Canadian Journal of Chemical Engineering, 1985, 63(3):368-376.
[29] 李洲, 费维扬, 杨基础. 液-液萃取过程和设备[M]. 北京: 原子能出版社, 1985.
[30] KUMAR A, HARTLAND S. Prediction of dispersed phase hold-upin pulsed perforated-plate extraction columns[J]. Chemical Engi-neering and Processing:Process Intensification, 1988, 23(1):41-59.
[31] KUMAR A, HARTLAND S. Unified correlations for the prediction of drop size in liquid-liquid extraction columns[J]. Industrial & Engineering Chemistry Research, 1996, 35(8):2682-2695.
文章导航

/