• Title/Summary/Keyword: DTO reaction

Search Result 10, Processing Time 0.023 seconds

Synthesis of Mesoporous SAPO-34 Catalyst Using Chitosan and Its DTO Reaction (키토산을 이용한 메조 세공 SAPO-34 촉매의 합성 및 DTO 반응)

  • Yoon, Young-Chan;Song, Kang;Lim, Jeong-Hyeon;Park, Chu-Sik;Kim, Young-Ho
    • Applied Chemistry for Engineering
    • /
    • v.32 no.3
    • /
    • pp.305-311
    • /
    • 2021
  • Effects of chitosan as a mesopore directing agent of SAPO-34 catalysts were investigated to improve the catalytic lifetime in DTO reaction. The synthesized catalysts were characterized by XRD, SEM, N2 adsorption-desorption isotherm and NH3-temperature programmed desorption (TPD). The modified SAPO-34 catalysts prepared by varying the added amount of chitosan showed the same cubic morphology and chabazite structure as the conventional SAPO-34 catalyst. As the added amount of chitosan increased to 3 wt%, the surface area, mesopore volume and concentration of weak acid sites of modified SAPO-34 catalysts increased. The modified SAPO-34 catalysts showed enhanced catalytic lifetime and high selectivity for light olefins in the DTO reaction. In particular, the SAPO-CHI 3 catalyst (3 wt%) exhibited the longest catalytic lifetime than that of the conventional SAPO-34. Therefore, it was confirmed that chitosan was a suitable material as a mesopore directing agent to delay deactivation of the SAPO-34 catalyst.

Effects of Acid Treatment of SAPO-34 on the Catalytic Lifetime and Light Olefin Selectivity during DTO Reaction (DTO 반응에서 촉매수명과 경질 올레핀 선택도에 미치는 SAPO-34의 산 처리 효과)

  • Choi, Ki-Hwan;Lee, Dong-Hee;Kim, Hyo-Sub;Park, Chu-Sik;Kim, Young-Ho
    • Applied Chemistry for Engineering
    • /
    • v.26 no.2
    • /
    • pp.217-223
    • /
    • 2015
  • Effects of the post-acid treatment of SAPO-34 sample by hydrochloric acid were investigated to enhance the catalytic performance in DTO reaction. Uniformly sized SAPO-34 samples with cubic-like morphology were prepared by hydrothermal method using TEAOH and DEA as the structure directing agents. It was modified in terms of the HCl concentration and treating time. As a result, the total surface area and micropore volume for the well modified samples increased and the total acid site was somewhat decreased along with the erosion of the external surface. Especially, the catalytic lifetime and light olefins selectivity for acid treated SAPO-0.2 M (3 h) samples were considerably enhanced compared with those of untreated SAPO-34 samples. It indicates that the deactivation by coke formation proceeds mainly at the pore entrance on the external surface. Therefore, the acid treatment was confirmed to be a simple method which can significantly improve the catalytic performance by modifying the external surface of SAPO-34 catalyst.

Effects of Co/Al and Si/Al Molar Ratios on DTO (Dimethyl Ether to Olefins) Reaction over CoAPSO-34 Catalyst (CoAPSO-34 촉매상에서 DTO (Dimethyl Ether to Olefins) 반응에 미치는 Co/Al 및 Si/Al 몰 비의 영향)

  • Kim, Hyo-Sub;Lee, Su-Gyung;Choi, Ki-Hwan;Lee, Dong-Hee;Park, Chu-Sik;Kim, Young-Ho
    • Applied Chemistry for Engineering
    • /
    • v.26 no.2
    • /
    • pp.138-144
    • /
    • 2015
  • Effects of Co/Al and Si/Al molar ratios of cobalt incorporated SAPO-34 catalysts (CoAPSO-34) on their catalytic lifetime were investigated in dimethyl to olefin (DTO) reaction. The property of CoAPSO-34 catalysts was characterized using XRD, SEM, $^{29}Si$ MAS NMR, and $NH_3$-TPD techniques. First, the lifetime of CoAPSO-34 prepared by varying Co/Al molar ratios was improved than that of using the SAPO-34 catalyst, and the optimal Co/Al molar ratio was 0.0025. The total acid site amounts increased from 0.432 to 1.111 mmol/g with increasing Si/Al molar ratios from 0.05 to 0.20 while fixing a Co/Al molar ratio of 0.0025. However, the catalysts with too high acid site amounts were deactivated rapidly with blockages of the pores due to the fast accumulation of polycyclic aromatic hydrocarbons in the cage. Therefore, the CoAPSO-34 catalyst with a proper Si/Al molar ratio of 0.10 was the most superior in terms of the lifetime, which was improved by about 87% as compared with that of the SAPO-34 catalyst.

Synthesis, X-Ray Crystal Structure and Coupling Reactions of 4,5-($1^{\prime},2^{\prime}$-diphenylethylenedithio)-1,3-dithiole-2-thione (dPhEDT-DTT)

  • 이하진;노동윤
    • Bulletin of the Korean Chemical Society
    • /
    • v.19 no.3
    • /
    • pp.340-344
    • /
    • 1998
  • A facile synthesis of 4,5-(1',2'-diphenylethylenedithio)-1,3-dithiole-2-thione (dPhEDT-DTT) is carried out via a Diels-Alder type [2+4] cycloaddition reaction of 1,3-dithiol-2,4,5-trithione oligomer and t-stilbene. Molecular structure of dPhEDT-DTT is determined by x-ray crystallography: space group P1, a=11.694(3) Å, b=12.117(3) Å, c=14.688(3) Å, α=113.12(2)°, β=102.23(2)°, γ=107.02(2)°, V= 1699.1(7) Å3, Z=2. It turns out that dPhEDT-DTT crystallizes as a racemic compound consisting of (R,R) and (S,S) enantiomers. Coupling reaction of dPhEDT-DTO undergone in neat P(OEt)3 yields TTF(SEt)4 instead of ET derivative. When PR3 (R=OEt, OPh, Ph) is used in benzene, toluene or xylene, however, dPhEDT-DTO is decomposed.

Effect of Etching Treatment of SAPO-34 Catalyst on Dimethyl Ether to Olefins Reaction (DTO 반응에 미치는 SAPO-34 촉매의 식각 처리 효과)

  • Song, Kang;Yoon, Young-Chan;Park, Chu-Sik;Kim, Young-Ho
    • Applied Chemistry for Engineering
    • /
    • v.32 no.1
    • /
    • pp.20-27
    • /
    • 2021
  • Effects of the etching treatment of SAPO-34 catalyst were investigated to improve the catalytic lifetime in DTO reaction. The aqueous NH3 solution was a more appropriate treatment agent which could control the degree of etching progress, compared to that of using a strong acid (HCl) or alkali (NaOH) solution. Therefore, the effect on characteristics and lifetime of SAPO-34 catalyst was observed using the treatment concentration and time of aqueous NH3 solution as variables. As the treatment concentration or time of aqueous NH3 solution increased, the growth of erosion was proceeded from the center of SAPO-34 crystal plane, and the acid site concentration and strength gradually decreased. Meanwhile, it was found that external surface area and mesopore volume of SAPO-34 catalyst increased at appropriate treatment conditions. When the treatment concentration and time were 0.05 M and 3 h, respectively, the lifetime of the treated SAPO-34 catalyst was the longest, and was significantly enhanced by ca. 36% (based on DME conversion of > 90%) compared to that of using the untreated catalyst. The model for the etching progress of SAPO-34 catalyst in a mild treatment process using aqueous NH3 solution was also proposed.

The Study on DME (dimethyl ether) Conversion Over the Supported SAPO-34 Catalyst (담지된 SAPO-34 촉매상에서 DME(dimethyl ether) 전환 연구)

  • Lee, Su-Gyung;Yoo, Byoung-Kwan;Je, Han-Sol;Ryu, Tae-Gong;Park, Chu-Sik;Kim, Young-Ho
    • Transactions of the Korean hydrogen and new energy society
    • /
    • v.22 no.2
    • /
    • pp.232-239
    • /
    • 2011
  • DME has received much attention because of its possible use as a fuel and a chemical feedstock. Chemical conversion of DME to olefin (DTO) over various SAPO-34 catalysts was carried out using a fixed bed reactor. Main products of the reaction were light olefins such as ethylene, propylene and butenes. The best reaction conditions for high life time of the catalyst and high selectivity of light olefins were a reaction temperature of $400^{\circ}C$ and a WHSV of $3.54h^{-1}$. In addition, it was found that the deactivation of a SAPO-34 catalyst can be significantly suppressed by the addition of $ZrO_2$ as a supporter.

Purification and Properties of Protease Inhibitor from Streptomyces sp. SK-862 (방선균이 생성하는 단백질 가수분해효소 저해물질의 정제 및 특성)

  • 김중배
    • The Korean Journal of Food And Nutrition
    • /
    • v.11 no.6
    • /
    • pp.678-682
    • /
    • 1998
  • A strain of Streptomyces sp. SK-862, isolated from soil in Wonju city, was able to prodce a biologically active substance that has a strong inhibitory activity against proteolsis by trypsin. The inhyibitory substance was extracted by n-butanol, and then purified by the adsorption chromatography followed by the reverse-phase high performacne liquid chromatography. The purified substance was stable over the pH range from 2 to 10, but was unstable when treated at 8$0^{\circ}C$ for 60 min. This substance was soluble in water, methanol, ethanol nd butanol, but insoluble in chlorofrom and ethylacetate. The Rf value of the purified substance on the thin layer chromatography were 0.56 in n-butanol : methanol : water(5 : 3 : 1v/v) solvent system compare dto 0.23 in ethanol : ammonium hydoxide : water(8 : 1 : 1v/v) solvent system. This substance has maximum absorption at 259 nm. The chemical reaction of the substance was negative for sugar but positive for ninhydrine and iodine reaction.

  • PDF

Effect of Water Addition on the Conversion of Dimethyl Ether to Light Olefins over SAPO-34 (SAPO-34 촉매상에서 디메틸에테르로부터 경질올레핀 제조 및 물의 첨가 효과)

  • Baek, Seung-Chan;Lee, Yun-Jo;Jun, Ki-Won
    • Korean Chemical Engineering Research
    • /
    • v.44 no.4
    • /
    • pp.345-349
    • /
    • 2006
  • Conversion of DME (dimethyl ether) or methanol to light olefins (ethylene, propylene, butenes) over SAPO-34 were systematically studied, where it was observed that DME was dehydrated to light olefins and partially converted to by-products such as CO and $CO_2$ at various reaction temperatures on the time-on-stream. SAPO-34 catalyst during the DTO (dimetyl ether-to-olefins) reaction was significantly deactivated compared with MTO (methanol-toolefins) reaction. By addition of water to the reaction feed, the yield to light olefins was not only increased, but the life time of the catalyst was also prolonged by the suppression of the coke formation by steam.

Conversion of Dimethyl Ether to Light Olefins over a Lead-Incorporated SAPO-34 Catalyst with Hierarchical Structure

  • Kang Song;Jeong Hyeon Lim;Young Chan Yoon;Chu Sik Park;Young Ho Kim
    • Applied Chemistry for Engineering
    • /
    • v.34 no.5
    • /
    • pp.548-555
    • /
    • 2023
  • SAPO-34 catalysts were modified with polyethylene glycol (PEG) and Pb to improve their catalytic lifetime and selectivity for light olefins in the conversion of dimethyl ether to olefins (DTO). Hierarchical SAPO-34 catalysts and PbAPSO-34 catalysts were synthesized according to changes in the molecular weight of PEG (M.W. = 1000, 2000, 4000) and the molar ratio of Pb/Al (Pb/Al = 0.0015, 0.0025, 0.0035), respectively. By introducing PEG into the SAPO-34 catalyst crystals, an enhanced volume of mesopores and reduced acidity were observed, resulting in improved catalytic performance. Pb was successfully substituted into the SAPO-34 catalyst frameworks, and an increased BET surface area and concentration of acid sites in the PbAPSO-34 catalysts were observed. In particular, the concentrations of the weak acid sites, which induce a mild reaction, were increased compared with the concentrations of strong acid sites. Then, the P2000-Pb(25)APSO-34 catalyst was prepared by simultaneously utilizing the synthesis conditions for the P2000 SAPO-34 and Pb(25)APSO-34 catalysts. The P2000-Pb(25)APSO-34 catalyst showed the best catalytic lifetime (183 min based on DME conversion > 90%), with an approximately 62% improvement compared to that of the unmodified catalyst (113 min).

Phase sequence in Codeposition and Solid State Reaction of Co-Si System and Low Temperature Epitaxial Growth of $CoSi_2$ Layer (Co-Si계의 동시증착과 고상반응시 상전이 및 $CoSi_2$ 층의 저온정합성장)

  • 박상욱;심재엽;지응준;최정동;곽준섭;백홍구
    • Journal of the Korean Vacuum Society
    • /
    • v.2 no.4
    • /
    • pp.439-454
    • /
    • 1993
  • The phase sequence of codeposited Co-Si alloy and Co/si multilayer thin film was investigated by differential scanning calormetry(DSC) and X-ray diffraction (XRD) analysis, The phase sequence in codeposition and codeposited amorphous Co-Si alloy thin film were CoSilongrightarrow Co2Si and those in Co/Si multilayer thin film were CoSilongrightarrowCo2Silongrightarrow and CoSilongrightarrowCo2Si longrightarrowCoSilongrightarrowCoSi2 with the atomic concentration ration of Co to Si layer being 2:1 and 1:2 respectively. The observed phase sequence was analyzed by the effectvie heat of formatin . The phase determining factor (PDF) considering structural facotr in addition to the effectvie heat of formation was used to explain the difference in the first crystalline phase between codeposition, codeposited amorphous Co-Si alloy thin film and Co/Si multilayer thin film. The crystallinity of Co-silicide deposited by multitarget bias cosputter deposition (MBCD) wasinvestigated as a funcion of deposition temperature and substrate bias voltage by transmission electron microscopy (TEM) and epitaxial CoSi2 layer was grown at $200^{\circ}C$ . Parameters, Ear, $\alpha$(As), were calculate dto quantitatively explain the low temperature epitaxial grpwth of CoSi2 layer. The phase sequence and crystallinity had a stronger dependence on the substrate bias voltage than on the deposition temperature due to the collisional daxcade mixing, in-situ cleannin g, and increase in the number of nucleation sites by ion bombardment of growing surface.

  • PDF