• Bulletin of the Korean Chemical Society
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• 제28권11호
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• pp.2075-2078
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• 2007

Oligomerization of isobutene has been investigated using a few solid acid catalysts in order to produce efficiently triisobutenes that are useful chemical feedstocks for heavy alkylates and neo-acids. Several reaction conditions such as space velocity and isobutene concentration are evaluated, and a few cation exchange resins with various acid capacities were compared in the reaction. High trimers selectivity and high conversion can be obtained over a catalyst containing high acid capacity at low space velocity and relatively low isobutene concentration. The stability of a catalyst for the reaction is high when the acid capacity of the catalyst is high (for example Amberlyst-35).

• Bulletin of the Korean Chemical Society
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• 제29권2호
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• pp.339-341
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• 2008

Catalytic trimerization of isobutene to produce triisobutenes has been performed over cation-exchange resin and zeolite catalysts. Resin catalysts have the advantage of long lifetime and high trimers selectivity even though the regeneration of an aged catalyst is not satisfactory. On the contrary, zeolite catalysts can be regenerated facilely by simple calcination in air even though the lifetime is short and trimers selectivity is low probably due to small pore size and strong acidity, respectively. It is, therefore highly desirable to develop an inorganic acid catalyst with macro- or meso-pores to show catalytic performances similar or superior to those of macroporous resin catalysts.

• Bulletin of the Korean Chemical Society
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• 제29권1호
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• pp.57-60
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• 2008

Catalytic oligomerization of isobutene to produce triisobutenes has been performed over a cation-exchange resin (Amberlyst-35) by using commercial C4 feeds. The catalytic activity in the oligomerization was retained without deactivation up to 90 h of reaction in a simulated reaction feed without butadiene, but its activity was significantly affected by the presence of butadiene in commercial C4 feeds. The isobutene conversion with time-on-stream was significantly decreased in the presence of butadiene, indicating the catalyst deactivation by butadiene. However, the stable activity for trimerization was accomplished when the oligomerization was carried out after eliminating butadiene by hydrogenation of the feeds. This work demonstrates that butadiene plays a role as a catalyst poison on the solid acid catalyst, so that its removal in the reactant feed is essential for practical application of trimerization.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2004년도 춘계학술대회
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• pp.1945-1950
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• 2004

In this paper, The performance of Kim-Chi refrigerator with three evaporator and one compressor was investigated in employing 55% propane and 45% isobutane (R290/R600a) refrigerant mixture as an alternative refrigerant of R134a. The drop in test was performed by varying both refrigerant charge amount and capillary tube length in order to find both the performance and reliability of a small multi-refrigeration system. As a result, Both the power consumption and COP is increased by about 15% and 10%, respectively as compared to the baseline R134a system. In addition, the propane/isobutene refrigerant mixture system took advantage of the minimization of modification and redesigning of system components because of similar thermodynamic properties with R134a such as saturation pressure, temperature, normal boiling point(NBP) characteristics

• 농약과학회지
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• 제9권3호
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• pp.274-277
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• 2005

살충제 펜피록시메이트는 4-hydroxyimino-5-phenoxypyrazole과 t-butyl 4-chloromethyl benzoate로부터 Williamson 합성을 통하여 합성되고 있다. 그러나 t-butyl benzoate 의 효과적인 합성방법은 여전히 문제점으로 남아있다. 본 연구에서는 t-butyl benzoate를 황산 촉매에서 t-butanol로부터 생성되는 isobutene을 사용하여 4-chloromethyl benzoic acid에 부가하여 합성하였다. 이 방법은 부산물의 생성없이 t-butyl 4-chloromethyl benzoate을 합성할 수 있어 기존에 보고된 방법보다 훨씬 용이하다. 따라서 본 연구는 펜피록시메이트를 대량으로 합성하는 효과적인 방법을 제시하였다.

• 대한화학회지
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• 제21권2호
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• pp.89-93
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• 1977

고령토를 사용하여 합성한 faujasite형 zeolite를 $Zn^{2+},\;La^{3+},\;H^+(NH_4^+)$로 양이온 교환하고 Na-, Zn-, La- 및 H-faujasite의 1-butene의 분해 및 이성화반응에 대한 촉매활성을 조사하였다. $1-Butene{\rightarrow}2-butene$ 반응은 강한 산점이 별로 없는 zeolite에서도 쉽게 일어난다. Isobutene생성에 대한 활성은 La > H > Zn > Na-faujasite의 순으로 La-faujasite가 가장 컸다. Propylene 생성에 대한 활성도 같은 경향을 나타냈으나 여기서는 La-와 H-faujasite의 활성이 거의 같은 정도이었다. 본 실험결과를 보면 zeolite의 산성도(산의 강도 및 량)는 1-butene의 분해 및 이성화 반응에 대한 활성과 직접적인 관계가 있는 것 같다.

• Bulletin of the Korean Chemical Society
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• 제5권2호
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• pp.79-82
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• 1984

This study concerns about catalyic cracking of iso-octane over cation ($Cd^{2+},\;Ca^{2+}\;and\;La^{3+}$) exchange mordenites. It deals with mordenite shape selectivity and with kinetics of this catalytic reaction. The striking feature was that over the region of cracking temperature investigated, 523-665K, the yield of isobutene was predominant, relative to that of larger or smaller carbon chain(s). This permits kinetic analysis of the heterogeneous catalytic system in terms of the modified pulse-version microcatalytic chromatography. The observed activation energy ($E_a,\;KJ\;mol^{-1}$) was found to be 46 for Cd-M, 57 for Ca-M and 59 for La-M, respectively.

• 공업화학
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• 제5권5호
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• pp.825-835
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• 1994

가솔린 옥탄가 향상제인 ETBE(Ethyl Tertiary Butyl Ether)의 기상합성을 성질이 다른 그물구조형 이온교환 수지인 Amberlyst-15와 Amberlyst XN-1010촉매상에서 고정층 상압 유통식 미분형 반응기로 수행하였다. 반응물로는 ethanol과 isobutene을 사용하였고, 반응온도 $70-140^{\circ}C$ 범위에서 실험을 행하여 수지촉매들의 활성을 비교한 결과 Amberlyst-15의 활성이 Amberlyst XN-1010보다 우수하였다. 미분형 반응기로부터 얻은 속도론적 자료를 선형회귀분석하여 적합한 속도모델과 매개변수를 구한 결과 ETBE합성반응은 LHHW(Langmuir-Hinshelwood-Hougen-Waston) 반응기구에 의하여 이루어진 것으로 보여진다. 또한, 각 온도에 따른 표면 반응속도 상수와 반응물들의 흡착평형상수와 표면반응 활성화 에너지를 구하였으며, Amberlyst-15 및 Amberlyst XN-1010의 활성화에너지는 각각 18.64 및 24.19 Kcal/mol이었다.

• Korean Chemical Engineering Research
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• 제46권4호
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• pp.692-696
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• 2008

C4 잔사유 III는 올레핀의 함량이 높음에도 불구하고 이를 활용할 방법이 그리 많지 않다. 대부분 수소화반응을 통하여 부탄으로 전환하여 LPG로 판매하고 있다. C4 잔사유 III는 매우 적은 이소부텐 및 이소부탄을 포함한 2-부텐이 농후한 유분으로, 이 유분 중 2-부텐은 $400{\sim}600^{\circ}C$에서 소성시켜 제조한 에타 알루미나 촉매로 이성화하여 열역학적 평형 수율 근처에서 선택적 위치 이성화시켜 1-부텐으로 전환된다. 전체 공정은 이성화 반응기, 고선택적으로 1-부텐으로 전환시킨 유분을 농축하고 반응물을 제조하는 1-부텐 분리탑과 고순도의 1-부텐 컬럼으로 공정으로 구성되어있다. 1-부텐 생산량은 종래의 분리에 의한 것보다 40~60 wt% 증가한다.

• 대한화학회지
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• 제55권5호
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• pp.812-818
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• 2011

[ $V_{0.9}Sb_{0.1}O_x$ ]systems, bulk and deposited on different supports (five types of ${\gamma}$-aluminas, ${\alpha}$-alumina, silica-alumina, silica gel, magnesium oxide), have been tested in the oxidative dehydrogenation (ODH) of iso-butane. This statement is derived from the data obtained by a set of characterisation techniques(specific surface area measurements, X-ray diffraction, X-ray photoelectron spectroscopy, laser Raman spectroscopy, in situ differential scanning calorimetry and in situ diffuse reflectance-absorption infrared Fourier transform spectroscopy).