• Korean Chemical Engineering Research
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• v.44 no.4
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• pp.393-398
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• 2006

There have been a lot of works in order to develop an excellent adsorbent for separation of olefin and paraffin. In the present work, the adsorption characteristics of mesoporous MCM-41 containing silver ion for 1-butene and n-butane were studied. The adsorption ability for the 1-butene depending on thermal treatment were also investigated.MCM-41 exhibits much higher adsorption amounts for 1-butene as well as n-butane, compared to those of Ag/13X zeolite. In case of MCM-41 containing silver ion, the adsorption amount of 1-butene dramatically increased due to the ${\pi}$-complexation, whereas the adsorption amount of n-butane decrease. The Ag/MCM-41 after the thermal treatment at 373 K under evacuation exhibit the highest 1-butene/n-butane adsorption ratio, expecially at low pressure (100 Torr).

• Applied Chemistry for Engineering
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• v.7 no.4
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• pp.623-632
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• 1996

The reactivity ratios, melting temperature and polymer morphology in propylene/butene-1 and propylene/hexene-1 copolymerization reactions were studied by examining comonomer compositions of resulting polymers. The catalysts used here are different in their supports which are silica(catalyst I) and magnesium(catalyst II). As the content of comonomer(butene-1 and hexene-1) increased in the copolymer, the melting temperature of the copolymer decreased. The morphology of polymer was amorphous in the range of comonomer(butene-1) composition over 40% in the propylene/butene-1 copolymerization and comonomer(hexene-1) composition over 80% in the propylene/hexene-1 copolymerization. The reactivity ratios were obtained by the Fineman-Ross and Kelen-$T{\ddot{u}}d{\tilde{o}}s$ methods.

• Bulletin of the Korean Chemical Society
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• v.22 no.5
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• pp.441-442
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• 2001

• Bulletin of the Korean Chemical Society
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• v.34 no.6
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• pp.1751-1754
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• 2013

3,4-Dihydropyrimidin-2(1H)-ones were efficiently converted into the corresponding pyrimidin-2(1H)-ones in high yields within a short period of time on treatment with aqueous acetonitrile using 1,4-bis(triphenylphosphonium)-2-butene peroxodisulfate. Chemoselective oxidation of 3,4-dihydropyrimidin in the presence of other oxidizable functional groups was also achieved by this reagent.

• Korean Chemical Engineering Research
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• v.46 no.4
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• pp.692-696
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• 2008

There is not much method of using C4 Raffinate III, despite having high olefin contents. The majority of the C4 Raffinate III have been converted into n-butane through hydrogenation, and sold as LPG. The C4 Raffinate III is rich 2-butenes with very low isobutene and isobutene contents. The 2-butenes are converted into 1-butene in the vicinity of thermodynamic equilibrium yield through positional isomerization with n-almumina catalyst calcinated at $400{\sim}600^{\circ}C$. The overall process is composed of isomerization-reactor, de-1-buteneizer to prepare the reactants and to enrich reactive products, and 1-butene column to product a high purity 1-butene. The production of 1-butene increases by 40~60 wt% with the selective positional isomerization from the existing separation method.

• Korean Chemical Engineering Research
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• v.53 no.1
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• pp.116-120
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• 2015

Synthesis of butenes through dehydration of 2-butanol was investigated over HY zeolite catalysts. 2-Butanol dehydration reaction was carried out in a fixed bed catalytic reactor. 2-Butanol conversion was increased with increase of $Si/Al_2$ ratio of HY zeolite catalysts, which can be ascribed to increase of acid strength with increase of $Si/Al_2$ ratio. Selectivities to 1-butene, trans-2-butene, and cis-2-butene were not greatly influenced by the change of the $Si/Al_2$ ratio of HY zeolite. As a result, it was advantageous to use a HY zeolite catalyst with 60 $Si/Al_2$ ratio for maximizing the yield of 1-butene in the dehydration of 2-butanol. The optimal reaction temperature for maximizing the yield of 1-butene was $250^{\circ}C$ over HY (60) catalyst.

• Applied Chemistry for Engineering
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• v.9 no.4
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• pp.523-528
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• 1998

The electrochemical characteristics of $V_2O_5$ as working electrode were studied in the cell (1-butene+$O_2$, $V_2O_5{\mid}YSZ{\mid}Ag$, $O_2$) with a YSZ solid electrolyte. The sintering of Ag as a counter electrode was occurred after calcination, and the structure which has the pores of over $3{\mu}m$ was achieved. In particular, the peak of (010) plane of the working electrode on the XRD spectrum which is responsible for selective oxidation appeared after calcination. The major product of 1-butene oxidation over $V_2O_5$ was butadiene. The technique of SEP (solid electrolyte potentiometry) was used to monitor the chemical potential of chemical species adsorbed on the working electrode. Over a wide range of gas compositions of 1-butene and oxygen, open circuit voltage (OCV) exhibited the mixed potential of surface oxygen activity.

• Applied Chemistry for Engineering
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• v.7 no.5
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• pp.861-868
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• 1996

Skeletal isomerization reaction known as exothermic reaction shows possible maximum yield of i-butene from n-butene at $110^{\circ}C$ over $Pt/MoO_3/SiO_2$. Compared with conventional catalyst such as silica, zeolite, alumina etc., $Pt/MoO_3/SiO_2$ demonstrates higher yield while by-products except 2-butene do not form. Faster H spillover rate over $Pt/MoO_3/SiO_2$ is demonstrated via isothermal reduction experiment at $110^{\circ}C$ compared to the rate over $Pt/MoO_3/Al_2O_3$. Overall isomerization rates are proportional to higher spillover rates from Pt onto $MoO_3$ surface. The skeletal isomerization reaction is composed of two elementary steps. First, carbonium ion formation over Pt crystallites by H spillover. Second, carbenium ion formation over $MoO_3$ followed by formation of i-butene. Moreover, it is suggested that H spillover step from Pt surface onto $MoO_3$ is assumed to be the rate determining step and control the overall isomerization rate.

• Journal of the Korean Vacuum Society
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• v.3 no.4
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• pp.414-419
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• 1994

Surface of Pt/$Al_2O_3$ model catalyst was produced on an aluminum foil with surface area of 1 $cm^2$ The aluminum surface was oxidized under $10 ^5Torr$Torr oxygen and platinum was deposited on top of the oxide layer using a plasma evaporation source. Conversion of I-butene was performed on the model catalyst surface. Isomerization was the major reaction in I-butene conversion on the aluminum oxide layer. Addition of Pt on the aluminum oxide layer induces hydrogenation of I-butene. Selectivity for the hydrogenation increases as the amount of Pt on alumina increases.

• Journal of the Korean Society of Food Science and Nutrition
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• v.24 no.1
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• pp.54-59
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• 1995

Compositional changes in pungent components of Dolsan Leaf Kimchi during fermentation were investigated. Major volatile compounds identified in the kimchi were 3-isothiocyanate-1-propene(allyl isothiocyanate, AITC) di-2-propenyl disulfide, 1-methoxy-2-butanol, 4-isothiocyanate-1-butene and dimethyl trisulfide. The contents of allyl isothiocyanate and 4-isothiocyanate-1-butene decreased, while dimethyl trisulfide increased during fermentation and storage. 1-methoxy 2-butanol increased at the initial stage of fermentation, showing highest at 2~3 days, and decreased thereafter. Di-2-propenyl disulfide decreased after 5 days and increased after 10days of storage. Total glucosinolate content increased by 3days and decreased from 4days of storage.