• 공업화학
• /
• 제25권5호
• /
• pp.515-519
• /
• 2014

대두유와 돈지를 이용한 에스테르교환반응실험에서 메탄올과 에탄올의 혼합비율을 조절하여 제조된 바이오디젤의 연료특성을 평가하였다. 메탄올보다는 에탄올에 대한 유지의 용해도가 높았으며 에탄올의 몰비가 증가함에 따라 균질한 바이오디젤 제조가 가능함을 확인하였다. 반응온도 $60^{\circ}C$에서 메탄올과 에탄올의 혼합몰비가 6 : 6일 때 돈지의 경우 가장 우수한 바이오디젤 전환특성을 나타내었다. 또한 대두유의 경우 3 : 3일 때 가장 우수한 바이오디젤 전환특성을 나타내었다. 대두유와 돈지를 원료로 하여 제조된 바이오디젤의 동점도는 $40^{\circ}C$에서 각각 4.17~4.35 cSt, 4.69~4.93 cSt로 측정되었으며, 에탄올의 첨가비가 증가함에 따라 산화안정성과 고위발열량은 증가하였다. 산화안정성은 바이오디젤의 품질기준인 6 h 이상을 만족하였고, 고위발열량은 약 40 MJ/kg으로 나타났다.

• 한국환경과학회지
• /
• 제17권2호
• /
• pp.211-224
• /
• 2008

Characteristics of the esterification reaction between free fatty acid in rice bran oil and methanol was investigated in the presence of catalysts, such as PTS(p-toluene sulfonic acid), Amberlyst 15 dry and SCX(silica gel based strong cation exchange resin). While reaction temperature was kept constant at $65^{\circ}C$, initial feed content of free fatty acid was varied from 100% to 1% by addition of pure free fatty acid which was previously made from rice bran oil. Also, the effect of mole ratio of methanol to fatty acid on the final conversion was examined. When esterification of pure free fatty acid was catalyzed by several acids, final conversions were increased in order of Amberlyst 15 dry, SCX and PTS. Using PTS catalyst, initially the reaction proceeded in homogeneous 2nd oder reaction mechanism. However, phase of reaction mixture changed from homogeneous to heterogeneous along the reaction time and then reaction rate was retarded by mass transfer resistance of methanol. Final conversion of free fatty acid in reaction mixture was depended on initial feed content of free fatty acid, and had maximum value at 30% of initial feed free fatty acid content for all kinds of catalysts used. And the final conversion was increased with mole ratio of methanol by the improvement of reaction rate. When initial feed free fatty acid content below 10% and the reaction was catalyzed by PTS, concentration of free fatty acid in reaction mixture was increased in the middle of reaction time by hydrolysis of triglyceride in reaction mixture. Also, if silica gel was added into the reaction mixture which had initial feed free fatty acid content below 50%, final conversion was increased by the adsorption of moisture produced. The SCX catalyst made the esterification reaction of free fatty acid to progress like in case of PTS catalyst. However, when initial feed free fatty acid content below 10%, concentration of free fatty acid in. reaction mixture was decreased monotonically and not increased in the middle of reaction time on the contrary to the case of PTS. Thus, SCX catalyst accomplished more high value of final conversion than PTS catalyst for the initial feed fatty acid content range from 50% to 5% In case of initial feed free fatty acid content of 1% and mole ratio of methanol was 2, concentration of free fatty acid in reaction mixture increased over the initial feed free fatty acid content for all kind of catalysts used. Although SCX catalyst was added into reaction mixture which had 1% of initial feed fatty acid content, final conversion was hardly raised by mole ratio of methanol.

• 한국환경과학회지
• /
• 제18권2호
• /
• pp.231-238
• /
• 2009

Characteristics of the transesterification reaction between triglycerides in soy bean oil and methanol were investigated in the presence of acid catalysts. such as sulfuric acid and PTS (p-toluene sulfonic acid). Concentrations of diglyceride and monoglyceride which were intermediates in the reaction mixtures, were far below 10% of triglyceride under any reaction conditions. Thus, conversion of the reaction could be determined from the concentration of triglyceride. Dried PTS had more superior catalytic power than sulfuric acid for transesterification reaction between soy bean oil and methanol. When transesterification reaction of soy bean oil was catalyzed by 1 wt% of PTS at methanol stoichiometric mole ratio of 2 and $65^{\circ}C$, final conversion reached 95% within 48 hours. If FAME (fatty acid methyl ester) was added into reaction mixture of soy bean oil, methanol and PTS catalyst, it converted reaction mixture into homogeneous phase, and substantially increased reaction rate. When reaction mixture was freely boiling which had equal volumetric amount of FAME to soy bean oil, methanol stoichiometric mole ratio of 2 and 1 wt% of PTS, final conversion achieved value of 94% and temperature approached to $110^{\circ}C$ within 2 hours.

• 공업화학
• /
• 제29권6호
• /
• pp.746-752
• /
• 2018

본 연구에서는 마이크로웨이브 에너지를 이용하여 폐식용유로부터 바이오디젤을 제조하고, Box-Behnken 설계를 이용하여 공정의 최적화를 설계하였다. Box-Behnken 설계의 계량인자는 메탄올/유지 몰비, 마이크로웨이브 조사세기, 반응시간으로 설정하였고, 계측인자는 FAME 함량이다. 기초실험 결과 산가에 관계없이 계량인자인 메탄올/유지 몰비(8~10)와 반응시간(4~6 min)의 범위는 동일하게 설정하였으며, 마이크로웨이브 조사세기의 경우 산가 1.30 mg KOH/g (8~12 W/g)와 2.00 mg KOH/g (10~14 W/g)로 설정하였다. Box-Behnken 설계에 의해 예측된 바이오디젤 제조공정의 최적조건은 산가 1.30 mg KOH/g인 폐식용유의 경우 메탄올/유지 몰비(7.58), 마이크로웨이브 조사세기(10.26 W/g), 반응시간(5.1 min)이었고, 산가 2.00 mg KOH/g의 경우 메탄올/유지 몰비(7.78), 마이크로웨이브 조사세기(12.18 W/g), 반응시간(5.1 min)로 산출되었다. 이때 예측 FAME 함량은 각각 98.4, 96.3%로 나타났으며, 실제 실험을 통한 오차율은 0.3% 이하로 나타났다. 따라서 마이크로웨이브를 이용한 바이오디젤의 제조공정에 Box-Behnken 설계를 적용할 수 있을 것으로 사료된다.

• 멤브레인
• /
• 제12권4호
• /
• pp.247-254
• /
• 2002

직접메탄올연료전지에 사용가능한 이온교환막을 개발하기 위하여 본 연구에서는 폴리설폰을 설폰화시켜 양이온교환막을 제조하였고 그에 대한 특성을 $150^{\circ}C$에서 열처리 전과 후를 통해 메탄을 투과도, 이온전도도, 이온교환용량 그리고 함수율 등에 대하여 평가하였다. 폴리설폰 고분자의 단량체와 설폰화제의 몰비가 1.4일 때 메탄올 투과도는 $2.87{\times}10^{-7} \;cm^2/s$(열처리 안함), $1.52{\times}10^{-7}\; cm^2/s$(열처리함)과 이온전도도는 1.10{\times}10^{-2}\; S/cm$ (열처리안함), 0.87{\times}10^{-2}\; S/cm$(열처리함)을 각각 보여 주었다. 그 이후의 몰비에서는 거의 증가하지 않았으며, 이러한 경향은 함수율과 이온교환용량에서도 같은 경향을 보여주었다.

• Bulletin of the Korean Chemical Society
• /
• 제16권1호
• /
• pp.42-47
• /
• 1995

Interpolymer complex formation between basic polypeptide poly(L-proline) Form Ⅱ (PLP(Ⅱ)) and acidic polypeptides poly(L-glutamic acid) (PLGA) and poly(L-aspartic acid)(PLAA) has been studied in water-methanol (1:2 v/v) mixed-solvent by viscometry, potentiometry, light scattering and circular dichroism (CD) measurements. It has been found that polymer complexes between PLP(Ⅱ) and PLGA (or PLAA) are formed via hydrogen bonding with a stoichiometric ratio of PLP(Ⅱ)/PLGA (or PLAA)=1:2 (in unit mole ratio) and that PLP(Ⅱ) forms polymer complex more favorably with PLGA than with PLAA. In addition, the minimum (for pH 5.0) and the maximum (for pH 3.2) in reduced viscosity of dilute PLP(Ⅱ)-PLGA mixed solutions are observed at 0.67 unit mole fraction of PLGA (i.e., [PLP(Ⅱ)]/[PLGA]=1/2). These findings could be explained in terms of molecular structure (or conformation) of the complementary polymers associated with the complex formation.

• Korean Chemical Engineering Research
• /
• 제43권5호
• /
• pp.621-626
• /
• 2005

Amberlyst-15 고체 산 촉매를 사용하여 올레산을 메탄올과 반응시켜 바이오 디젤의 성분이 되는 지방산 메틸 에스테르로 전환시켰다. 본 연구에서는 시료의 산가를 측정하고 전환율을 구함으로써 반응 온도, 메탄올 대 올레산의 몰 비 및 촉매의 양이 반응에 미치는 영향을 살펴보았다. 실험 범위 내에서 반응 온도가 $20^{\circ}C$ 상승할 때에 반응 속도는 약 2배씩 증가하였다. 그리고 메탄올 대 올레산의 몰 비가 증가 될 때는 최종 전환율은 증가하였지만, 반응에는 뚜렷한 차이가 없었다. 촉매 역시 반응에 중요한 변수로써, Amberlyst-15의 양을 2배로 증가시켰을 때, 반응속도는 1.2-1.3배 빨라졌다. 실험 데이터를 정량적으로 해석하기 위해 동역학식 연구를 하였으며 모사 균일 혼합물 모델(pseudo-homogeneous model)을 이용한 2차 반응 속도식을 전개하였다.

• Environmental Engineering Research
• /
• 제23권1호
• /
• pp.54-61
• /
• 2018

Biodiesel production parameters and the impact analysis of the potential emissions from both soybean biodiesel and washing water stored in three different environmental conditions were investigated. The effects of the reaction temperature, methanol/oil mole ratio and catalyst concentration on biodiesel yield were considered. And the results showed optimum biodiesel yield of 99% obtained at $54^{\circ}C$, 7 methanol/oil mole ratio and 0.4 wt/wt % catalyst concentration. The potential emissions from both the biodiesel produced and washing water stored (for six weeks) in refrigerator (${\leq}10^{\circ}C$), vacuum (50 kPa) and direct exposure to atmosphere were identified and quantified. Impact analysis of the emissions involved their categorization into: terrestrial acidification, freshwater eutrophication, human toxicity, terrestrial ecotoxicity, climate change and freshwater ecotoxicity. Freshwater ecotoxicity category had the most pronounced negative impact of the potential emissions with $5.237710^{-2}kg\;1,4-DB\;eq$. emissions in Atmosphere, $4.702610^{-2}kg\;1,4-DB\;eq$. emissions in Refrigerator and $3.966110^{-2}kg\;1,4-DB\;eq$. emissions in Vacuum. Climate change had the least effect of the emissions with $6.214106^{-6}kg\;CO_2\;eq$. in Atmosphere, $3.9310^{-6}kg\;CO_2\;eq$. in Refrigerator and $1.6710^{-6}kg\;CO_2\;eq$. in Vacuum. The study showed that the order of preference of the storage environments of biodiesel is vacuum environment, refrigerated condition and exposure to atmosphere.

• 공업화학
• /
• 제22권1호
• /
• pp.72-76
• /
• 2011

본 연구에서는 폐커피가루를 이용하여 커피유를 추출한 후 커피유를 이용한 바이오디젤의 제조특성을 고찰하였다. 커피유의 바이오디젤 제조의 변수로는 메탄올/커피유 반응몰비(6~18), 반응온도($45{\sim}60^{\circ}C$) 등을 선정하여 커피유의 바이오디젤 제조 시 최적조건을 결정하고자 하였다. 제조된 바이오디젤의 성능은 바이오디젤 수율, methyl ester 함량, 점도, 발열량 등을 측정하여 평가하였다. 평가결과 바이오디젤 수율 및 methyl ester 함량을 고려한 최적 반응온도는 $55^{\circ}C$이었으며, 메탄올/커피유 몰비가 12일 경우 가장 우수한 바이오디젤을 제조할 수 있었다. 커피유를 이용하여 제조된 바이오디젤의 발열량을 측정한 결과 39.0~39.4 MJ/kg으로 바이오디젤 기준인 39.3~39.8 MJ/kg을 만족하였다.

• 한국세라믹학회지
• /
• 제24권2호
• /
• pp.186-192
• /
• 1987

ZrO2 powders having high purity were prepared from domestic zircon sand using the caustic fusion method and the soda ash sintering process. In the caustic fusion method, ZrO2 recovery was reached to 96% when 100/140 mesh zircon was reacted with NaOH at the NaOH/Zircon mole ratio 6 and at 650$^{\circ}C$ for 2 hours. And in the soda ash sintering process, ZrO2 was recovered to 88.5% when -325 mesh zircon was reacted with Na2CO3 at the Na2CO3/Zircon mole ratio 1.1 and 1050$^{\circ}C$ for 2 hours. In both cases, Zr component was extracted to ZrOCl2, subsequently crystallized to ZrOCl2$.$8H2O to increase the purity, and converted to ZrO2 by precipitation. And to increase the sinter ability of powder, Cl- ion was removed and strong agglomeration was avoided by methanol distribution of Zr(OH)4 precipitates.