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羟胺二磺酸盐磺化水解生成铵盐的反应过程 II.胺基磺酸盐水解反应动力学 被引量:1

Reaction Process of Ammonium Salt from Hydroxyimidodisulfate II. Kinetics of Hydrolyses of Amino Sulfonate
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摘要 研究了胺基磺酸盐水解反应动力学 ,分析了氢离子对水解反应的催化作用以及水解的盐效应 ,在所研究的离子强度范围内 ,胺基磺酸盐的水解反应呈负盐效应。胺基三磺酸钾 ( NTS)水解反应动力学方程为 :dc NTSdt =k NTSc NTSc H+ ,在 30°C~ 67°C、离子强度 I=0 .0 5 mol/L时 ,k NTS=3.5 77×1 0 9e-5.460× 10 4 / RTL/( mol· s) ;胺基二磺酸钾 ( IDS)的水解反应动力学方程为 :- dcIDSdt=k IDSc H+ c IDS,在32°C~ 72°C、离子强度 I=0 .1 0 mol/L时 ,k IDS=1 .40 5× 1 0 17e-1.0 65× 10 5/ RTL/( mol· min) ;胺基一磺酸钾 ( SA)的水解反应动力学方程为 :- dc SAdt=k SAc H+ c SA,在 5 0°C~ 84°C、离子强度 I=0 .0 5 mol/L时 ,k SA=7.964× 1 0 17e-1.2 77× 10 5/ RTL/( mol·min) The hydrolyses of nitridotrisulfonate, imidodisulfonate, sulfamate in acid aqueous solutions were studied. The ammonium sulfate can be pr oduced by three successive hydrolysis reactions from nitridotrisulfonate. The de pendence of the rate constant k on ionic strength is also investigated. Nega tive salt effect was exhibited in the range of ionic strength studied. The kinet ic of these hydrolyses have been determined as follow: The kinetic equatio n of the acid hydrolysis of potassium nitridotrisulfonate is -d c NTS d t = k NTS c H + c NTS , w here k NTS =3.577×10 9e -5.460×10 4/ RT L/(mol·s) in the temp erature of 30°C ~ 67°C at I = 0.05 mol/L. The rate of the acid hyd rolysis of potassium imidodisulfonate obeys the expression: -d c IDS d t = k IDS c H + c IDS , where k IDS = 1.405 ×10 17 e -1.065×10 5/ RT L/(mol·min) in the temperature of 32°C ~ 72°C at I = 0.10 mol/L. The rate of t he acid hydrolysis of potassium sulfamate can be written as: -d c SA d t = k SA c H + c SA , where k SA =7.964×10 17 ·e -1.277×10 5/ RT L/(mol·min) in the temperature of 50°C ~ 84°C at I = 0.05mol/L.
出处 《华东理工大学学报(自然科学版)》 CAS CSCD 北大核心 2002年第5期472-476,共5页 Journal of East China University of Science and Technology
基金 国家自然科学基金"九五"重点资助项目 (2 963 3 0 3 0 )
关键词 离子强度 液相反应 羟胺二磺酸盐 磺化水解 铵盐 反应过程 胺基磺酸盐水解反应动力学 hydrolysis reaction in liquid phase kinetic model potass ium nitridotrisulfonate potassium imidodisulfate potassium sulfamate
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  • 1朱联锡,卢虹.烟气脱硫脱硝技术进展情况[J].环境科技(辽宁),1993,13(2):86-90. 被引量:3
  • 2Seel V F, Degener E. Kinetik und chemismus der raschigschen hydroxylamin-synthesis [J]. Z Anorg Allg Chem, 1956, 284:101-130.
  • 3Seel V F, Knorre H. Die umsetzung von nitrit mit hydrogensulfit in hydrogensulfit-sulfit-pufferlsungen [J]. Z Anorg Allg Chem, 1961, 313:70-89.
  • 4Oblath S B, Markowitz S S, Novakov T, et al. Kinetics of the formation of hydroxylamine disulfonate by reaction of nitrite with sulfites [J]. J Phys Chem, 1981, 85: 1 017-1 021.
  • 5Oblath S B, Markowitz S S, Novakov T, et al. Kinetics of the initial reaction of nitrite ion in bisulfite solutions [J]. J Phys Chem, 1982, 86: 4 853-4 857.
  • 6Seel V F. Stchiometric und kinetik der umsetzungen von hydroxylamin-N-sulfonaten mit hydrogensulfit [J]. Z Anorg Allg Chem, 1959, 299:122-137.
  • 7Sisler H, Audrieth L F. Potassium nitrilosulfonate [J]. J Am Chem Soc, 1938, 60: 1 947-1 948.
  • 8David L, Abigail R, Chang S G, et al. Kinetics of acid hydrolysis of the nitridotrisulfate ion [J]. Inorg Chem, 1986, 25:4 610-4 611.
  • 9George J D, Norman D. The kinetics of the acid-catalyzed hydrolysis of amine disulfonate ion: The third ionization constant of amine disulfonic acid [J]. J Chem Soc, 1949, 71: 3 491-3 498.
  • 10Maron S H, Berens A R. The kinetics of hydrolysis of the sulfamate ion [J]. J Ameri Chem Soc, 1950, 72: 3 571-3 574.

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  • 1李定邦,刘兆辅,张大年.节能型光解法废气脱硫脱硝技术研究[J].化学世界,2002,43(S1):53-55. 被引量:4
  • 2杜鹏.典型脱硫工艺在火电厂的应用探讨[J].西华大学学报(自然科学版),2002,21(z1):78-80. 被引量:7
  • 3傅军,肖博文,涂晋林.NO_x、SO_2液相反应研究进展——一种同时脱硫脱氮的新思路[J].化工进展,1999,18(1):26-28. 被引量:26
  • 4孙德智.环境工程中的高级氧化技术[M].北京:化学工业出版社,2003.288.
  • 5Lee Tae Gyu,Jeon Myeong Seok,Ju Hyeon Gyu.Optical catalyst reaction/ plasma composite system for processing denitrification or desulfurization[P].Korean,KR 20000017881A,2000-04-06.
  • 6http: // www. zhb. gov. cn/english/SOE/soechina 2000/Chinese/atmospheric_mainc. htm.
  • 7Abboud N E,Chaaban F B, Tabanji W E. Economic evaluation of alternatives to reduce emissions from power plants[J]. Intern J Environ Studies, 2000,57 : 225 ~238.
  • 8Livengood C D. FG technology for combined control of SO2 and NOx [J]. Power Engineering, 1994,98 ( 1 ) : 38~42.
  • 9Hartman M. Sulfur dioxide reactivity of commerial limestones[J]. Chem Commun, 1975, 40:1 466 ~1 477.
  • 10The wet and dry gaseous scrubber divisions of the institute of clean air companies inc (ICAC). Scrubber myths and realities [J]. Power Engineering, 1995, 99(1) :35~38.

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