• Title/Summary/Keyword: Ionic Liquid Catalysts

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The Esterification of Oleic Acid Using Acidic Ionic Liquid Catalysts Immobilized on Silica Gel (실리카겔에 고정화된 산성 이온성 액체 촉매를 이용한 올레산의 에스터화 반응연구)

  • Choi, Jae-Hyung;Park, Yong-Beom;Lee, Suk-Hee;Cheon, Jae-Kee;Woo, Hee-Chul
    • Korean Chemical Engineering Research
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    • v.48 no.5
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    • pp.583-588
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    • 2010
  • Esterification of free fatty acid with methanol to biodiesel was investigated in a batch reactor using various solid acid catalysts, such as polymer cation-exchanged resins with sulfuric acid functional group(Amberlyst-15, Dowex 50Wx8), acidic ionic liquids (ILs)-modified silica gels respectively with $-SO_3H$ and $-SO_2Cl$ functional group ($SiO_2-[ASBI][HSO_4]$, $SiO_2-[ASCBI][HSO_4]$) and grafted silica gels respectively with $-SO_3H$ and $-SO_2Cl$ functional group ($SiO_2-R-SO_3H$, $SiO_2-R-SO_2Cl$). The effects of reaction time, temperature, reactant concentration(molar ratio of methanol to oleic acid), and catalyst amount were studied. Allylimidazolium-based ILs on modified silica gels were superior to other tested solid acid catalysts. Especially, the performance of $SiO_2-[ASBI][HSO_4]$ (immobilized by grafting of 3-allyl-1-(4-sulfobutyl)imidazolium hydrogen sulfate on silica gel) was better than that of a widely known Amberlyst-15 catalyst at the same reaction conditions. A high conversion yield of 96% was achieved in the esterification reaction of the simulated cooking oil at 353 K for 2 h. The high catalytic activity of $SiO_2-[ASBI][HSO_4]$ was attributed to the presence of strong Brønsted acid sites from the immobilized functional groups. The catalyst was recovered and the biodiesel product was separated by simple processes such as decantation and filtration.

One-step synthesis of dual-transition metal substitution on ionic liquid based N-doped mesoporous carbon for oxygen reduction reaction

  • Byambasuren, Ulziidelger;Jeon, Yukwon;Altansukh, Dorjgotov;Ji, Yunseong;Shul, Yong-Gun
    • Carbon letters
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    • v.17 no.1
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    • pp.53-64
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    • 2016
  • Nitrogen (N)-doped ordered mesoporous carbons (OMCs) with a dual transition metal system were synthesized as non-Pt catalysts for the ORR. The highly nitrogen doped OMCs were prepared by the precursor of ionic liquid (3-methyl-1-butylpyridine dicyanamide) for N/C species and a mesoporous silica template for the physical structure. Mostly, N-doped carbons are promoted by a single transition metal to improve catalytic activity for ORR in PEMFCs. In this study, our N-doped mesoporous carbons were promoted by the dual transition metals of iron and cobalt (Fe, Co), which were incorporated into the N-doped carbons lattice by subsequently heat treatments. All the prepared carbons were characterized by via transmission electron microscopy (TEM), X-ray diffraction (XRD) and X-ray photoelectron spectroscopy (XPS). To evaluate the activities of synthesized doped carbons, linear sweep was recorded in an acidic solution to compare the ORR catalytic activities values for the use in the PEMFC system. The dual transition metal promotion improved the ORR activity compared with the single transition metal promotion, due to the increase in the quaternary nitrogen species from the structural change by the dual metals. The effect of different ratio of the dual metals into the N doped carbon were examined to evaluate the activities of the oxygen reduction reaction.

Computational Chemistry Study of CO2 Fixation and Cyclic Carbonate Synthesis Using Various Catalysts (촉매를 이용한 이산화탄소 고정화 및 고리형 카보네이트 합성반응에 대한 계산화학적 해석)

  • An, Hye Young;Kim, Min-Kyung;Jeong, Hui Cheol;Eom, Ki Heon;Won, Yong Sun
    • Clean Technology
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    • v.22 no.1
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    • pp.35-44
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    • 2016
  • In this study, a computational chemistry methodology called as molecular modeling was been applied to explain several experiment results mechanistically. The reaction chosen for this study was to remove carbon dioxide, known as a primary greenhouse gas, by an epoxide via the carbon dioxide fixation to produce carbonates. This reaction inherently needs the use of catalysts because it has a significantly high activation barrier (55~59 kcal/mol). Among various types of catalysts, we studied in zeolitic imidazolate framework 90 (ZIF-90)/ionic liquid immobilized ZIF-90 (IL-ZIF-90), polystyrene-supported quaternized ammonium salt, KI/KI-glycine, and dimethylethanolamine (DMEA). First, probable reaction pathways were proposed based on calculated energetics by computational chemistry. The energetics was then used for the thermodynamic interpretation on the activity of catalysts. In the case of ZIF-90/IL-ZIF-90 and KI/KI-glycine, IL-ZIF-90 and KI-glycine showed better yields compared to their counterparts. The calculation proposed interesting results that it is not from the lowering of activation energy but from the unstable intermediates of ZIF-90 and KI-glycine. For DMEA, the calculated activation energy was ~42 kcal/mol, much lower than that of the non-catalytic reaction. A possible reaction pathway was located to confirm the interaction between −NH group from ammonium and oxygen from epoxide for polystyrene-supported quaternized ammonium salt.

A Study on the Synthesis of Tricyclopentadiene Using Ionic Liquid Catalysts (이온성 액체 촉매를 이용한 Tricyclopentadiene 합성에 관한 연구)

  • Kim, Su-Jung;Han, Jeongsik;Jeon, Jong-Ki;Yim, Jin-Heong
    • Applied Chemistry for Engineering
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    • v.26 no.5
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    • pp.593-597
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    • 2015
  • Tricyclopentadiene (TCPD) as a next generation high density fuel was synthesized by Diels-Alder oligomerization reaction of DCPD. TCPD was prepared by ionic liquid (IL) catalysts with combination of cationic and anionic precursors. Two kinds of anionic precursors such as copper(I) chloride (CuCl) and iron(III) chloride ($FeCl_3$) and cationic precursors such as triethylamine hydrochloride (TEAC) and 1-butyl-3-methylimidazolium chloride (BMIC) were used. The preparation of TCPD using IL catalyst was superior to that using Diels-Alder reaction in terms of DCPD conversion and TCPD yield. In addition, TCPD yield was correlated with Lewis acidity by changing the ratio of anionic and cationic precursors. The TCPD yield was higher when using CuCl as anionic precursor than that of using $FeCl_3$. Control of Lewis acidity by changing the molar ratio of anionic and cationic precursors could further improve TCPD yield as well.

Effect of Promoter on the Decomposition of Eco-Frendly Liquid Monopropellant on Cu/hexaaluminate Pellet Catalyst (Cu/hexaaluminate 펠렛 촉매를 이용한 친환경 액체 추진제 분해 반응에 미치는 조촉매의 영향)

  • Kim, Munjeong;Kim, Wooram;Jo, Young Min;Jeon, Jong Ki
    • Clean Technology
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    • v.26 no.3
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    • pp.196-203
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    • 2020
  • In this study, a Cu/hexaaluminate catalyst was prepared by a co-precipitation method, and then a binder was added to form a pellet. A catalyst in which Ni and Ru promoters were added to a Cu/hexaaluminate pellet catalyst was prepared. This study focused on examining the effect of the addition of Ni and Ru promoters on the properties of Cu/hexaaluminate catalysts and the decomposition reaction of ADN-based liquid monopropellants. Cu/hexaaluminate catalysts had few micropores and well-developed mesopores. When Ru was added as a promoter to the Cu/hexaaluminate pellet catalyst, the pore volume and pore size increased significantly. In the thermal decomposition reaction of ADN-based liquid monopropellant, the decomposition onset temperature was 170.2 ℃. Meanwhile, the decomposition onset temperature was significantly reduced to 93.5 ℃ when the Cu/hexaaluminate pellet catalyst was employed. When 1% or 3% of Ru were added as a promoter, the decomposition onset temperatures of ADN-based liquid monopropellant were lowered to 91.0 ℃ and 83.3 ℃, respectively. This means that the Ru promoter is effective in lowering the decomposition onset temperature of the ADN-based liquid monopropellant because the Ru metal has excellent activity in the decomposition reaction of ADN-based liquid monopropellant, simultaneously contributing to the increase of the pore volume and pore size. After the thermal treatment at 1,200 ℃ and decomposition of ADN-based liquid monopropellant were repeatedly performed, it was confirmed that the addition of Ru could enhance the heat resistance of the Cu/hexaaluminate pellet catalyst.

A Study on the Reaction Pathway for Isomerization of Tetrahydrotricyclopentadiene Using Ionic Liquid Catalyst (이온성 액체 촉매를 이용한 Tetrahydrotricyclopentadiene의 이성화 반응 경로에 관한 연구)

  • Kim, Dae Hyun;Han, Jeong-Sik;Jeon, Jong-Ki;Yim, Jin-Heong
    • Applied Chemistry for Engineering
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    • v.26 no.3
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    • pp.366-371
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    • 2015
  • The kinetic behavior of tetrahydrotricyclopentadiene (THTCPD) isomerization was studied by using two kinds of chloroaluminate ionic liquid (IL) catalyst with different Lewis acidity. THTCPD isomerization pathway was discussed under the different temperature and time as reaction parameters using IL catalysts consisting of 1-butyl-3-methylimidazolun chloride $(BMIC)/AlCl_3$ with low acidity and pyridine hydrochloride $(PHC)/AlCl_3$ with high acidity. The conversion of THTCPD isomerization increased with increasing Lewis acidity of IL catalyst. The THTCPD isomerization pathway changed as a function of reaction temperature and catalyst acidity. In the case of $BMIC/AlCl_3$ IL catalyst, THTCPD isomerization pathway was similar to that of using conventional $AlCl_3$ catalyst. However, two different types of additional pathways (endo, exo, endo-NB ${\rightarrow}$ exo, exo, endo-NB ${\rightarrow}$ exo, exo, exo-NB and endo, exo, endo-NB ${\rightarrow}$ exo, exo, endo-NB ${\rightarrow}$ exo, exo, exo-CP) were appeared when using $PHC/AlCl_3$ IL catalyst.

$DeNO_{x}$ Performance of Activated Carbon Catalysts Regenerated by Surfactant Solution (계면활성제 수용액에 의해 재생된 활성탄 촉매의 탈질 성능)

  • Park, Hye-Min;Park, Young-Kwon;Jeon, Jong-Ki
    • Korean Chemical Engineering Research
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    • v.49 no.6
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    • pp.739-744
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    • 2011
  • Activated carbon SCR(CSCR) catalyst that is used to remove $NO_x$ in exhaust gas including boron discharged from the production process of liquid crystal display(LCD) shows deactivation when boron is deposited to block the pores within the catalyst or to cover its active sites. The spent carbon catalyst is regenerated by washing with various surfactants, drying and calcination. For comparison of the physical and chemical properties before and after the regeneration with the variables, type of surfactants and calcination condition, element analysis by ICP, $N_{2}$ adsorption were conducted. $DeNO_{x}$ in SCR with $NH_3$ was carried out in a fixed bed reactor at $120^{\circ}C$. The activated carbon catalyst regenerated through washing with a non-ionic surfactant in $H_{2}O$ at $90^{\circ}C$ and calcination under $N_{2}$ gas at $550^{\circ}C$ shows similar level of surface area and $NO_x$ removal efficiency with those of fresh catalyst.