• Title/Summary/Keyword: $HI_x$solution

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The Phase Separation Characteristics of Bunsen Reaction with HIx Solution in Sulfur-Iodine Hydrogen Production Process (황-요오드 수소 제조 공정에서 HIx 용액을 이용한 분젠 반응의 상 분리 특성)

  • Kim, Hyo-Sub;Hong, Dong-Woo;Han, Sang-Jin;Kim, Young-Ho;Park, Chu-Sik;Bae, Ki-Kwang
    • Transactions of the Korean hydrogen and new energy society
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    • v.21 no.6
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    • pp.479-486
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    • 2010
  • In order to confirm the effect of $HI_x$ solution on Bunsen reaction in Sulfur-Iodine thermochemical hydrogen production process, the reaction was investigated using $HI_x$ solution as a reactant. The phase separation characteristics of reaction with $HI_x$ solution were compared with the reaction using $I_2$ and $H_2O$ as reactants. Firstly, saturation points of $I_2$ in $HI_x$ solution at various temperatures were investigated to determine reaction conditions. With increasing temperature, the amounts of unreacted $I_2$ and $H_2O$ in $HI_x$ solution were increased, while impurities (HI in $H_2SO_4$ phase and $H_2SO_4$ in $HI_x$ phase) in each phase were decreased. The volumes of $H_2SO_4$ phase obtained from Bunsen reaction with $HI_x$ solution was relatively less than those obtained from the reaction with $I_2$ and $H_2O$. The difficulty of phase separation in Bunsen reaction using $HI_x$ solution may be due to the insufficient amount of $H_2O$ existed in $HI_x$ phase after reaction. Therefore, we concluded that the supplement amount of $H_2O$ should be calculated on the basis of the moles of HI and $H_2SO_4$ and added to the reaction system for good phase separation.

The Effect of SO2-O2 Mixture Gas on Phase Separation Composition of Bunsen Reaction with HIx solution (HIx 용액을 이용한 분젠 반응에서 상 분리 조성에 미치는 SO2-O2 혼합물 기체의 영향)

  • Han, Sangjin;Kim, Hyosub;Ahn, Byungtae;Kim, Youngho;Park, Chusik;Bae, Kikwang;Lee, Jonggyu
    • Transactions of the Korean hydrogen and new energy society
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    • v.23 no.5
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    • pp.421-428
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    • 2012
  • The Sulfur-Iodine (SI) thermochemical hydrogen production process is one of the most promising thermochemical water splitting technologies. In the integrated operation of the SI process, the $O_2$ produced from a $H_2SO_4$ decomposition section could be supplied directly to the Bunsen reaction section without preliminary separation. A $HI_x$ ($I_2+HI+H_2O$) solution could be also provided as the reactants in a Bunsen reaction section, since the sole separation of $I_2$ in a $HI_x$ solution recycled from a HI decomposition section was very difficult. Therefore, the Bunsen reaction using $SO_2-O_2$ mixture gases in the presence of the $HI_x$ solution was carried out to identify the effect of $O_2$. The amount of $I_2$ unreacted under the feed of $SO_2-O_2$ mixture gases was little higher than that under the feed of $SO_2$ gas only, and the amount of HI produced was relatively decreased. The $O_2$ in $SO_2-O_2$ mixture gases also played a role to decrease the amount of a impurity in $HI_x$ phase by only striping effect, while that in $H_2SO_4$ phase was hardly affected.

Effects of Solubility of SO2 Gas on Continuous Bunsen Reaction using HIx Solution (HIx 용액을 이용한 연속식 분젠 반응에 미치는 SO2용해도의 영향)

  • KIM, JONGSEOK;PARK, CHUSIK;KANG, KYOUNGSOO;JEONG, SEONGUK;CHO, WON CHUL;KIM, YOUNG HO;BAE, KI KWANG
    • Transactions of the Korean hydrogen and new energy society
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    • v.27 no.1
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    • pp.13-21
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    • 2016
  • The Sulfur-Iodine thermochemical hydrogen production process (SI process) consists of the Bunsen reaction section, the $H_2SO_4$ decomposition section, and the HI decomposition section. The $HI_x$ solution ($I_2-HI-H_2O$) could be recycled to Bunsen reaction section from the HI decomposition section in the operation of the integrated SI process. The phase separation characteristic of the Bunsen reaction using the $HI_x$ solution was similar to that of $I_2-H_2O-SO_2$ system. On the other hands, the amount of produced $H_2SO_4$ phase was small. To investigate the effects of $SO_2$ solubility on Bunsen reaction, the continuous Bunsen reaction was performed at variation of the amounts of $SO_2$ gas. Also, it was carried out to make sure of the effects of partial pressure of $SO_2$ in the condition of 3bar of $SO_2-O_2$ atmosphere. As the results, the characteristic of Bunsen reaction was improved with increasing the amounts and solubility of $SO_2$ gas. The concentration of Bunsen products was changed by reverse Bunsen reaction and evaporation of HI after 12 h.

Characteristics of Bunsen Reaction using Ultrasonic Irradiation in Sulfur-iodine Hydrogen Production Process (황-요오드 수소 제조 공정에서 초음파 조사를 이용한 분젠 반응의 특성)

  • Kim, Hyo Sub;Lee, Dong Hee;Lee, Jong Gyu;Park, Chu Sik;Kim, Young Ho
    • Applied Chemistry for Engineering
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    • v.29 no.1
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    • pp.56-61
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    • 2018
  • In Bunsen reaction section for the integrated operation of sulfur-iodine (SI) process, $I_2$ and $H_2O$ reactants are supplied as dissolved species in an $HI_x$ solution. Most of the $H_2SO_4$ product is found in the $HI_x$ phase when Bunsen reaction is performed using the $HI_x$ solution and $SO_2$ feed, so that the volume ratio of the $H_2SO_4$ phase to the $HI_x$ phase is very low. In this study, we investigated the effects of ultrasound irradiation on Bunsen reaction using the $HI_x$ solution to improve its phase separation performance. With ultrasound irradiation, the amount of $H_2SO_4$ moved to the $H_2SO_4$ phase from the $HI_x$ phase increased by up to 58.0 mol% and the volume of $H_2SO_4$ phase also increased by up to 13.1 vol%. In particular, the effect of ultrasound irradiation on the phase separation was improved with decreasing operating temperature, $I_2$ and $H_2O$ feed concentrations. The ultrasound irradiation induces the formation of additional $H_2O$ molecules by shifting microscopically the reaction equilibrium in the $HI_x$ phase. Afterward, the additionally generated $H_2O$ and isolated $H_2SO_4$ molecules form more $H_2SO_4{\cdot}xH_2O$ (x = 5-6) clusters that can be moved to the $H_2SO_4$ phase.

Crystal Sinking Modeling for Designing Iodine Crystallizer in Thermochemical Sulfur-Iodine Hydrogen Production Process (열화학 황-요오드 수소 생산 공정의 요오드 결정화기 설계를 위한 결정 침강 모델링)

  • Park, Byung Heung;Jeong, Seong-Uk;Kang, Jeong Won
    • Korean Chemical Engineering Research
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    • v.52 no.6
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    • pp.768-774
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    • 2014
  • SI process is a thermochemical process producing hydrogen by decomposing water while recycling sulfur and iodine. Various technologies have been developed to improve the efficiency on Section III of SI process, where iodine is separated and recycled. EED(electro-electrodialysis) could increase the efficiency of Section III without additional chemical compounds but a substantial amount of $I_2$ from a process stream is loaded on EED. In order to reduce the load, a crystallization technology prior to EED is considered as an $I_2$ removal process. In this work, $I_2$ particle sinking behavior was modeled to secure basic data for designing an $I_2$ crystallizer applied to $I_2$-saturated $HI_x$ solutions. The composition of $HI_x$ solution was determined by thermodynamic UVa model and correlation equations and pure properties were used to evaluate the solution properties. A multiphysics computational tool was utilized to calculate particle sinking velocity changes with respect to $I_2$ particle radius and temperature. The terminal velocity of an $I_2$ particle was estimated around 0.5 m/s under considered radius (1.0 to 2.5 mm) and temperature (10 to $50^{\circ}C$) ranges and it was analyzed that the velocity is more dependent on the solution density than the solution viscosity.

ON THE STABILITY OF A BI-JENSEN FUNCTIONAL EQUATION

  • Jun, Kil-Woung;Lee, Yang-Hi;Oh, Jeong-Ha
    • The Pure and Applied Mathematics
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    • v.17 no.3
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    • pp.231-247
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    • 2010
  • In this paper, we investigate the generalized Hyers-Ulam stability of a bi-Jensen functional equation $4f(\frac{x\;+\;y}{2},\;\frac{z\;+\;w}{2})$ = f(x, z) + f(x, w) + f(y, z) + f(y, w). Also, we establish improved results for the stability of a bi-Jensen equation on the punctured domain.

Dimensionless Henry's Constant and Liquid-Vapour Equilibrium of Rosemary Aroma Compounds (로즈마리 향기성분의 기-액 평형과 무차원 헨리의 상수)

  • Yoon, Hyang-Sik;Jeong, Heon-Sang;Min, Young-Kyoo
    • Korean Journal of Food Science and Technology
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    • v.35 no.4
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    • pp.738-742
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    • 2003
  • In order to estimate the mass transfer characteristics of absorption into alcohol solution of aroma compounds such as cineol, myrecene and pinene which are major aroma compounds of rosemary, dimensionless Henry's constant in 70% ethyl alcohol concentration and aroma concentration with different ethyl alcohol concentration were analyzed. From the results of measurement of vapor phase concentration of aroma compounds with different ethyl alcohol concentration, headspace concentrations of all of three aroma compounds were decreased as ethyl alcohol concentration increased. But those patterns were slightly different. Dimensionless Henry's constant equation (Hi) of cineol compound with ethyl alcohol concentration (x) was as follows: $Hi=(-5.75+x)/(-7017.6+257.3{\times}x)$. Dimensionless Henry's constants of cineol, myrecene and pinene in 1 atm, $25^{\circ}C$ and 70% ethyl alcohol concentration were 0.0058, 0.0182 and 0.0365, respectively.

Deposition of NiO on hi-axially textured Ni substrates fort YBCO coated conductor by a MOCVD method (양축정렬된 textured Ni 기판위에 MOCVD법을 이용한 YBCO coated conductor 완충층용 NiO 증착)

  • 선종원;김형섭;박순동;정충환;전병혁;김잔중
    • Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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    • 2002.07a
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    • pp.531-534
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    • 2002
  • NiO buffer layers for YBCO coated conductors were deposited on hi-axially textured Ni substrates by MOCVD(metal organic chemical vapor deposition) method, using single solution source. To establish the processing condition, oxygen partial pressure and deposition temperature were changed. The surface orientation and degree of texture were estimated by X-ray diffraction, X-ray pole figure and atomic force microscopy. The FWHMs of in-plane and out-of-plane of the NiO films were about 10$^{\circ}$. The surface roughness was a function of deposition temperature. The AFM surface roughness of NiO films is in the range of 3∼10 nm, when NiO films was grown at 450∼530$^{\circ}C$.

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