• 한국수소및신에너지학회논문집
• /
• 제20권5호
• /
• pp.397-403
• /
• 2009

The catalysis of carbon black was investigated for the production of hydrogen by the catalytic decomposition of propane-butane mixture gas in this study. The thermal and the catalytic decompositions of hydrocarbons were performed at the temperature range of 500 - $1100^{\circ}C$, respectively. The conversions of hydrocarbons and the mole traction of hydrogen increased with increasing the reaction temperature and the conversion of hydrocarbons in the catalytic decomposition process was approximately liked with that obtained by the thermal decomposition. However, the mole traction of hydrogen produced in the catalytic decomposition process was higher than that obtained from the thermal decomposition. Therefore, it was concluded that the catalysis for the decomposition of hydrocarbons is occurred over carbon black used as catalyst. The mole traction of hydrogen produced by the catalytic decomposition of hydrocarbons also increased with increasing the mole ratio of $C_3H_8/C_4H_{10}$ in propane and butane mixture gas at $700^{\circ}C$. Therefore, it was concluded that the catalytic decomposition of the high propane mixture gas is more effectively for the production of hydrogen.

• 한국수소및신에너지학회논문집
• /
• 제35권1호
• /
• pp.27-33
• /
• 2024

In this study, we researched Ni-based bead catalysts for the catalytic thermal decomposition of light hydrocarbons. A Ni-based bead-type catalyst was prepared, and catalytic thermal decomposition performance of light hydrocarbons was evaluated. The 30Ni/Al₂O₃ catalyst exhibited the most superior performance, with the presence of both fibrous and carbon black forms on the catalyst surface. Catalytic performance was evaluated for particles sized between 150-250 and 500 ㎛, with excellent catalytic thermal decomposition properties in the 150-250 ㎛ range. After the reaction, carbon removal through collision between catalysts in the fluidized bed was observed. It was confirmed that as the particle size increases, the amount of carbon removed increases.

• 신재생에너지
• /
• 제2권4호
• /
• pp.70-77
• /
• 2006

The butane decomposition over the catalyst is an attractive method for the hydrogen production. The objective of the work was investigated the catalysis of carbon black in butane decomposition reaction. The Butane decomposition was performed over carbon black catalyst in a range of $500-1100^{\circ}C$. The butane conversion of thermal decomposition and catalytic decomposition were increased with increasing the reaction temperature The butane conversion of the thermal decomposition was higher than the butane conversion of the catalytic decomposition. Hydrogen and methane were mostly observed in the butane decomposition over $1000^{\circ}C$. Especially, the hydrogen yield was steadily increased with raising the reaction temperature, It could be known that the hydrogen yield of the catalytic decomposition was higher than one of the thermal cracking because the hydrogen productivity was improved by the catalyst. The deactivation of the catalyst was not observed in the reactivity test. The surface and crystalline of the fresh and used catalysts were characterized by TEM, BET surface area and XRD analysis, respectively. The fresh carbon black particles had mostly smoothly round-shaped surfaces. In the surface of the carbon black after the reaction, the deposited carbon was formed as the protrusion-shaped carbon and the cone-shaped. The proper peaks of carbon black appeared in XRD analysis.

• 공업화학
• /
• 제32권6호
• /
• pp.706-710
• /
• 2021

In the current research, thermal and catalytic thermogravimetric (TG) analysis of polyethylene terephthalate (PET) over natural zeolite (NZ), olivine, bentonite, HZSM-5, and HAl-MCM-41 were investigated using a TG analyzer and model-free kinetic analysis. Catalytic TG analysis of PET was carried out at multi-heating rates, 10, 20, 30, and 40 ℃/min, under nitrogen atmosphere. Apparent activation energy (Ea) values for the thermal and catalytic pyrolysis of PET were calculated using Flynn-Wall-Ozawa method. Although natural catalysts, NZ, olivine, and bentonite, could not lead the higher PET decomposition efficiency than synthetic zeolites, HZSM-5 and HAl-MCM-41, maximum decomposition temperatures on the differential TG (DTG) curves for the catalytic pyrolysis of PET, 436 ℃ over olivine, 435 ℃ over bentonite, and 434 ℃ over NZ, at 10 ℃/min, were definitely lower than non-catalytic pyrolysis. Calculated Ea values for the catalytic pyrolysis of PET over natural catalysts, 177 kJ/mol over olivine, 168 kJ/mol over bentonite, and 171 kJ/mol over NZ, were also not lower than those over synthetic zeolites, however, those were also much lower than the thermal decomposition, suggesting their feasibility as the proper and cost-effective catalysts on the pyrolysis of PET.

• 대한기계학회논문집B
• /
• 제31권4호
• /
• pp.398-404
• /
• 2007

In this paper, thermal characteristics of a nitrous oxide ($N_2O$) catalytic reactor with packed-bed geometry are theoretically and numerically investigated. Several researchers experimentally presented that catalytic decomposition of $N_2O$ in a packed bed generates about 82kJ/mole in the exothermic reaction. Based on the results they have studied the catalytic decomposition of $N_2O$ in a packed bed to use it not only as a mono-propellant thrust for small satellites but also as an igniter system for hybrid rockets. So we aim to identify important parameters existing in an $N_2O$ packed-bed geometry, and to clarify its critical effect on thermal characteristics of the catalytic igniter using a porous medium approach.

• 한국신재생에너지학회:학술대회논문집
• /
• 한국신재생에너지학회 2007년도 추계학술대회 논문집
• /
• pp.93-96
• /
• 2007

Catalytic activities of color and conductive carbon blacks in ethane decomposition for $CO_2-free$ hydrogen production were investigated. The ethane decomposition was carried out in a conventional fixed bed reactor under atmospheric pressure at 973-1173 K for 2 hours. When the decomposition in the presence of carbon black was compared with the non-catalytic thermal decomposition, the former exhibited significantly higher ethane conversion, higher C(s) selectivity and lower ethylene selectivity with small increase of the methane selectivity, which resulted in higher hydrogen yield. This indicates that carbon black is catalytically effective for dehydrogenation of ethane as well as subsequent decomposition of ethylene. All the carbon blacks exhibited stable catalytic activity with time. In durability tests, fluffy N-330 and BP2000 maintained their activities for 36 hours.

• 공업화학
• /
• 제26권2호
• /
• pp.154-158
• /
• 2015

본 연구에서는 $NF_3$의 분해를 위한 ${\gamma}-Al_2O_3$의 촉매활성을 조사하였다. $NF_3$ 분해반응은 고정층 촉매반응기에서 $330{\sim}730^{\circ}C$ 범위의 반응온도와 $3,000{\sim}15,000mL/g-cat{\cdot}h$의 공간속도 조건에서 수행되었고, $NF_3$의 열분해 반응이 촉매분해반응와 비교를 위하여 함께 수행되었다. $400^{\circ}C$의 촉매분해 반응에서 $NF_3$의 전화율은 열분해 반응보다 4배 정도 높았으며, ${\gamma}-Al_2O_3$상에서 $NF_3$의 반응거동은 스팀의 존재에 따라 두 가지 반응경로를 나타내는 것으로 확인되었다. 스팀이 존재하지 않은 조건에서는 기체-고체 반응에 의해서 $NF_3$에 함유된 불소성분은 $AlF_3$로 전이되고, 스팀이 존재하는 조건에서는 가수분해에 의한 촉매적 분해반응이 일어난다. 또한 $NF_3$는 $500^{\circ}C$ 이상에서 NOx와 HF로 완전히 분해되는 것으로 FT-IR분석에서 확인되었다.

• 공업화학
• /
• 제19권3호
• /
• pp.270-276
• /
• 2008

$TiO_2$의 가장 큰 특징은 광촉매적 특성을 들 수 있으나 순수한 $TiO_2$는 자외선 영역에서만 활성을 보이는 단점이 있다. 단점을 보완하고자 본 연구에서는 초고온, 고활성을 이용한 열플라즈마 공정으로 질소가 도핑된 $TiO_2$를 합성하여 $TiO_2$의 광촉매적 특성을 높이고자 하였다. 직류 플라즈마 제트를 이용하여 비금속이온인 질소와 반응 가스인 산소를 $TiCl_4$와 함께 플라즈마 반응기 안에서 반응시켜 질소가 도핑된 $TiO_2$ 나노 분말을 합성하였다. 합성 조건으로 질소의 유량을 변화하였다. 합성 변수에 따른 입자의 상조성, 크기를 분석하였고 아세트알데히드와 곰팡이를 광분해하는 실험을 통해 광촉매 활성을 살펴보았다. 한편 $TiO_2$의 분말 상태와 코팅된 상태의 광촉매 특성을 비교하고자 합성한 분말의 스핀 코팅과 PLD (Pulsed Laser Deposition)을 통해 $TiO_2$를 코팅하였다. 아세트알데히드 분해 실험의 결과 질소가 도핑된 $TiO_2$ 분말의 경우가 순수한 $TiO_2$ 분말에 비해 가시영역에서의 광촉매 활성이 두 배 이상 뛰어난 것을 확인하였으며, 곰팡이 분해 실험 결과 역시 질소가 도핑된 $TiO_2$ 분말에 곰팡이가 분해되는 것을 확인하였다. 분말과 필름을 제조하여 메틸렌블루 광분해 실험한 결과 분말의 경우 100% $TiO_2$입자가 메틸렌블루 분해에 이용되며, 반면 스핀 코팅의 경우 바인더의 함량 때문에 20~30%의 $TiO_2$만이 분해에 이용되기 때문에, 분말의 경우 초기 30 mL 메틸렌블루를 한번에 분해할 수 있었다.

• 한국환경과학회지
• /
• 제17권11호
• /
• pp.1273-1279
• /
• 2008

This study examined the catalytic destruction of 1,2-dichlorobenzene on ${V_2}{O_5}/TiO_2$ nanoparticles. The ${V_2}{O_5}/TiO_2$ nanoparticles were synthesized by the thermal decomposition of vanadium oxytripropoxide and titanium. The effects of the synthesis conditions, such as the synthesis temperature and precursor heating temperature, were investigated. The specific surface areas of ${V_2}{O_5}/TiO_2$ nanoparticles increased with increasing synthesis temperature and decreasing precursor heating temperature. In addition, the removal efficiency of 1,2-dichlorobenzene was promoted by a decrease in heating temperature. However, the removal efficiency of 1,2-dichlorobenzene was decreased by an anatase to rutile phase transformation at temperatures $1,300^{\circ}C$.

• Journal of Advanced Marine Engineering and Technology
• /
• 제28권5호
• /
• pp.818-826
• /
• 2004

The spray-induced mixing characteristics and thermal decomposition of aqueous urea solution into ammonia have been studied to design optimum sizes and geometries of the mixing chamber in SCR(Selective Catalytic Reduction) system. The cold flow tests about the urea-injection nozzle were performed to clarify the parameters of spray mixing characteristics such as mean diameter and velocity of drops and spray width determined from the interactions between incoming air and injected drops. Discrete particle model in Fluent code was adopted to simulate spray-induced mixing process and the experimental results on the spray characteristics were used as input data of numerical calculations. The simulation results on the spray-induced mixing were verified by comparing the spray width extracted from the digital images with the simulated Particle tracks of injected drops. The single kinetic model was adopted to predict thermal decomposition of urea solution into ammonia and solved simultaneously along with the verified spray model. The hot air generator was designed to match the flow rate and temperature of the exhaust gas of the real engines The measured ammonia productions in the hot air generator were compared with the numerical predictions and the comparison results showed good agreements. Finally, we concluded that the design capabilities for sizing optimum mixing chamber were established.