• Title/Summary/Keyword: 기포 생성

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A study of sintering behavior of spray coating in CaO-Al2O3-SiO2 glasses on Al2O3 substrate (CaO-Al2O3-SiO2 계 유리 스프레이 코팅막의 소성 거동에 대한 연구)

  • Na, Hyein;Park, Jewon;Park, Jae-Hyuk;Kim, Dae-Gun;Choi, Sung-Churl;Kim, Hyeong-Jun
    • Journal of the Korean Crystal Growth and Crystal Technology
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    • v.29 no.6
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    • pp.298-307
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    • 2019
  • Two types of CaO-Al2O3-SiO2 (CAS) glass powder applied spray coating on the surface of sintered Al2O3 were researched for sintering behavior; (1) Si-rich, glass containing high content SiO2, (2) Ca-rich, containing high content CaO. Foaming of bubbles remaining inside the Ca-rich glass was produced at a viscosity of approximately 107~109 poise, resulting in decreasing shrinkage (interfering with sintering) and increasing surface roughness. In case of Si-rich glass, there was no serious foaming bubbles phenomenon like Ca-rich below 1000℃, however cristobalite crystals with low density occurred at 1200℃ and then produced re-foaming of bubbles, resulting in abnormal sintering behavior. These phenomenon is considered to be a decrease in viscosity due to an increase in the Ca content of the glass according to the formation of low-density cristobalite crystals. Therefore, in case of CAS glass, it is necessary to consider the increase of surface roughness and the sintering interference because of foaming bubbles phenomenon at low temperature sintering. Especially, when containing high SiO2 content, abnormal foaming phenomenon due to crystallization at high temperature should be predicted.

Hydrodynamic Properties of Interconnected Fluidized Bed Chemical-Looping Combustors (상호 연결된 유동층 매체 순환식 연소로의 수력학적 특성)

  • Son, Sung Real;Go, Kang Seok;Kim, Sang Done
    • Korean Chemical Engineering Research
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    • v.48 no.2
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    • pp.185-192
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    • 2010
  • The chemical-looping combustion(CLC) has advantages of no energy loss for separation of $CO_2$ without $NO_x$ formation. This CLC system consists of oxidation and reduction reactors where metal oxides particles are circulating through these two reactors. In the present study, the reaction kinetic equations of iron oxide oxygen carriers supported on bentonite have been determined by the shrinking core model. Based on the reactivity data, design values of solid circulation rate and solids inventory were determined for the rector. Two types of interconnected fluidized bed systems were designed for CLC application, one system consists of a riser and a bubbling fluidized bed, and the other one has a riser and two bubbling fluidized beds. Solid circulation rates were varied to about $30kg/m^2s$ by aeration into a loop-seal. Solid circulation rate increases with increasing aeration velocity and it increases further with an auxiliary gas flow into the loop-seal. As solid circulation rate is increased, solid hold up in the riser increases. A typical gas leakage from the riser to the fluidized bed is found to be less than 1%.

A Study on Motion of Single Ball with Low Reynolds Number at Performed Interface Layers (액상 계면층을 이용한 저 레이놀즈수 단일강구의 운동연구)

  • 김시영
    • Journal of the Korean Society of Fisheries and Ocean Technology
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    • v.23 no.3
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    • pp.117-126
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    • 1987
  • The author has analysed profile of flow in rear of motion with single ball with low Reynolds number performed interface layers. For each system whose viscosity of the lower phase is as large as or large that of the upper phase, the profile has based on the thickness of the ball in the lower phase is nearly independent of both the ball single and the physical properties of the upper phase of the solution. The examine of the characteristics between Darwin's total displacement of the fluid and data obtained in this study, the averaged volume of each cases was corrected by the viscosity in the lower phase. When the viscosity in the lower phase is less than that of the upper phase, the volume based on the displacement of the fluid in rear region of ball are influenced by both ball size and the viscosity ratio of the upper phase to the lower phase. In the range of the Reynolds number less than a constant values, the volume ratio is influenced by both Reynolds number and Moltion number but mainly Reynolds. In range of Reynolds number over than the value, the volume ratio is independent of Reynolds number, but influenced by Moltion number.

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Interfacial Properties of Propylene Oxide Adducted Sodium Laureth Sulfate Anionic Surfactant (프로필렌 옥사이드를 부가한 소듐 라우레스 설페이트 음이온 계면활성제의 계면 특성에 관한 연구)

  • Jeong Min Lee;Ki Ho Park;Hee Dong Shin;Woo Jin Jeong;Jong Choo Lim
    • Applied Chemistry for Engineering
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    • v.34 no.3
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    • pp.264-271
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    • 2023
  • In this study, ASCO SLES-430 surfactant was synthesized by adducting 3 moles of ethylene oxide and 1 mole of propylene oxide to lauryl alcohol followed by a sulfation process, and the structure of the synthesized ASCO SLES-430 was elucidated by performing FT-IR, 1H-NMR and 13C-NMR analyses. Interfacial properties such as critical micelle concentration, static surface tension, emulsification index, and contact angle were measured, and environmental compatibility indices such as oral toxicity and skin irritation were also estimated for ASCO SLES-430. Both results were compared with ASCO SLES-226 and ASCO SLES-328 SLES surfactants possessing 2 moles and 3 moles of ethylene oxide, respectively. In particular, both foaming ability and foam stability were evaluated for ASCO SLES-430 and compared with ASCO SLES-226 and ASCO SLES-328, which have been widely used in detergent products, in order to test the potential applicability of ASCO SLES-430 in detergent product formulation for a small capacity built-in washing machine.

Basic Characteristics of ALC using Carbon dioxide Conversion Capture Materials (이산화탄소전환탄산화물 혼합 경량기포 콘크리트의 기초 특성)

  • Hye-Jin Yu;Sung-Kwan Seo;Yong-Sik Chu;Woo-Sung Yum;Kuem-Dan Park;Young-Gon Kim;Eun-Sung Yoo
    • Journal of the Korean Recycled Construction Resources Institute
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    • v.12 no.2
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    • pp.121-127
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    • 2024
  • In this study, the applicability of replacing DG(Desulfurized Gypsum) from oil refinery with CCCMs(Carbon dioxide Conversion Capture Materials) as an ALC(Auto-claved LIghtweight Concrete) raw material was examined, and basic properties of ALC was measured. The main chemical components of DG and CCCMs were CaO and SO3, and an increase in LOI(Loss of ignition) due to mineral carbonation reaction was verified. The crystalline phases of CCCMs were CaCO3, CaSO4, Ca(OH)2, and CaSO4·2H2O. When DG, a raw material for ALC production, was replaced with CCCMs, foaming height, pore shape, absolute dry gravity, and compressive strength results measured similar for all binders. In addition, the formation of tobermorite which is main crystalline phase of ALC was shown for all specimens in microstructural analysis.

Air Gasification Characteristics of Unused Woody Biomass in a Lab-scale Bubbling Fluidized Bed Gasifier (미이용 산림바이오매스 및 폐목재의 기포 유동층 Air 가스화 특성 연구)

  • Han, Si Woo;Seo, Myung Won;Park, Sung Jin;Son, Seong Hye;Yoon, Sang Jun;Ra, Ho Won;Mun, Tae-Young;Moon, Ji Hong;Yoon, Sung Min;Kim, Jae Ho;Lee, Uen Do;Jeong, Su Hwa;Yang, Chang Won;Rhee, Young Woo
    • Korean Chemical Engineering Research
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    • v.57 no.6
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    • pp.874-882
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    • 2019
  • In this study, the gasification characteristics of four types of unused woody biomass and one waste wood in a lab-scale bubbling fluidized bed gasifier (Diameter: 0.11 m, Height: 0.42 m) were investigated. Effect of equivalence ratio (ER) of 0.15-0.3 and gas velocity of $2.5-5U_0/U_{mf}$ are determined at the constant temperature of $800^{\circ}C$ and fuel feeding rate of 1 kg/h. The silica sand particle having an average particle size of $287{\mu}m$ and olivine with an average particle size of $500{\mu}m$ were used as the bed material, respectively. The average product gas composition of samples is as follows; $H_2$ 3-4 vol.%, CO 15-16 vol.%, $CH_4$ 4 vol.% and $CO_2$ 18-19 vol.% with a lower heating value (LHV) of $1193-1301kcal/Nm^3$ and higher heating value (HHV) of $1262-1377kcal/Nm^3$. In addition, it was found that olivine reduced most of C2 components and increased $H_2$ content compared to silica sand, resulting in cracking reaction of tar. The non-condensable tar decreases by 72% ($1.24{\rightarrow}0.35g/Nm^3$) and the condensable tar decreases by 27% ($4.4{\rightarrow}3.2g/Nm^3$).

Fluid Inclusions Trapped in Tourmaline from the Daeyou Pegmatite Deposit, Jangsu-Gun, Jeollabukdo (전북 장수군 대유 페그마타이트광산의 전기석에 포획된 유체포유물)

  • Lee, Ju-Youn;Eom, Young-Bo;Nam, Bok-Hyun;Hwang, Byoung-Hoon;Yang, Kyoung-Hee
    • Journal of the Mineralogical Society of Korea
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    • v.20 no.1 s.51
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    • pp.7-19
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    • 2007
  • Four types of fluid inclusions are trapped within tourmaline from Daeyou pegmatite, Jangsu-Gun, Jeonllabukdo. They range $5{\sim}100\;{\mu}m$ in size and are grouped into I, II, III, and IV based on the phase behavior at the room temperature: (1) Type I inclusions are liquid-rich and NaCl equivalent salinity ranged $0{\sim}12\;wt%$, and the homogenization temperatures (Th) ranged $181{\sim}230^{\circ}C$ with eutectic temperatures (Te) $-54{\sim}-22^{\circ}C$. (2) Type II inclusions are vapor-rich and salinity ranged $3{\sim}8\;wt%$ NaCl, and Th ranged $177{\sim}304^{\circ}C$ also showing Te $-54{\sim}-29^{\circ}C$. (3) Type III inclusions contain a halite daughter mineral with $31{\sim}40\;wt%$ NaCl, Th $230{\sim}328^{\circ}C$. More than 90% of Type III homogenize by halite dissolution and are spatially associated with silicate melt inclusions. (4) Type IV inclusions are $CO_{2}$-bearing containing various daughter minerals such as sylvite and/or halite. The density of $CO_{2}$ system within the Type IV is $0.80{\sim}0.75\;g/cm^{3}$, Th $190{\sim}317^{\circ}C$, and salinity $2{\sim}35\;wt%$ NaCl. Type III fluid inclusions, considered as the earliest fluid, formed from the fluid exsolved from the crystallizing pegmatite. It is suggested that Type II fluid in the central part of tourmaline were exsolved earlier than Type I fluids in the margin indicating salinity fluctuation during the growth of tourmaline. It implies the fluctuation of the pressure since the salinity of fluid exsolved from the crystallizing melt is governed by the pressure. The last fluid was Type IV, which may be derived from the nearby limestone and metasedimentary rocks. It is suggested that Daeyou pegmatite containing muscovite without miarolitic cavities was formed by the partial melting resulted from the regional metamorphism. Subsequently, the exsolving fluids from the crystallizing melt were trapped in tourmaline at high pressure condition. The exsolved fluids contain various components such as $CaCl_{2}\;and\;MgCl_{2}$ as well as NaCl and KCl. The exsolution began at least at $2.7{\sim}5.3\;kbar\;and\;230{\sim}328^{\circ}C$ with the pressure fluctuation.

Dyeing on PLA with Disperse Dyes (1) - Effect of Ultrasound (PLA섬유의 분산염료에 의한 염색 (1) - 초음파의 영향)

  • Jeong, Dong-Seok;Cheon, Tae-Il;Lee, Mun-Cheul
    • Proceedings of the Korean Society of Dyers and Finishers Conference
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    • 2011.03a
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    • pp.53-53
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    • 2011
  • Poly(lactic acid)(이하 PLA라 칭함)는 1970-80년대의 초기 연구에서는 높은 제조비용과 희귀성에 의해 봉합사와 약물전달시스템으로 용도가 제한적이었으나 1980년대를 거쳐 1990년 이후 농업의 혁신적인 변화를 거쳐 옥수수의 다양한 측면의 이용의 하나로서 6-7년 전부터 양산화에 성공하여, 의류, 필름 및 플라스틱의 여러 가지 분야에서 적용가능성을 모색하고 있다. PLA의 장점은 석유가 아닌 천연 원료에서 얻을 수 있으며, 기존의 합성섬유와는 달리 일정한 조건하에서 미생물 등에 의해 물과 이산화탄소로 90% 이상 분해되는 친환경적인 소재이다. 합성섬유에서 의류용으로 대부분 사용되는 폴리에스테르(이하 PET라 칭함)와 유사한 물성을 가지고 있는 PLA섬유는 PET섬유와 유사한 분산염료로 염색할 수 있다. 따라서 PLA섬유는 분산염료에 의한 염색법을 중심으로 연구되어지고 있으나, PET 섬유의 융점이 $254^{\circ}C$부근인 반면, PLA섬유는 $160-170^{\circ}C$부근이다. 이로 인해 PLA를 섬유로 용도전개에 있어서 약점으로 작용하고 있다. 그러나 PLA섬유는 특유의 경량감과 새로운 촉감 등의 많은 장점을 지니고 있어 여러 가지 용도전개가 되어지고 있다. 초음파는 사람이 들을 수 없는, 사람마다 한계값은 다르지만, 주파수 약 25kHz이상의 음파를 말하며, 주파수가 높고 파장이 짧기 때문에 강한 진동을 수반한다. 초음파의 이용 원리는 Cavitation이라는 현상으로 생성된 기포가 터지면서 강력한 에너지를 방출한다. 이것은 강력하여 사방으로 퍼져 물질표면이나 내부에 영향을 미친다. 섬유에서는 표면에 뭍은 불순물을 제거하는 세정 등에 응용되고 있으며, 염색분야에서도 다양하게 연구되어지고 있다. 본 연구에서는 초음파에 의한 PLA섬유의 염색성을 조사하였다. PLA섬유를 정련하여 초음파작용의 유무에 따라 염색하여 그 결과를 고찰하였다. 초음파 작용에 따른 분산염료의 표면 색변화는 없었으며, 섬유 표면 색 농도의 차이는 초음파 작용에 의하여 저온에서는 차이가 나타나지만, 고온인 $80^{\circ}C$에서는 오히려 낮아졌다.

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Optimum Conditions for Removal of Hydrogen Sulfide Using Fe-EDTA Complex (Fe-EDTA 착물을 이용한 황화수소 제거의 최적 반응 조건)

  • Jin, Sang-Gi;Cha, Jin-Myeong;Lee, In-Wha;Yoon, Suk-Jin;Kim, Si-Wouk
    • Applied Chemistry for Engineering
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    • v.7 no.1
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    • pp.177-185
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    • 1996
  • The optimum conditions for the removal of hydrogen sulfide by Fe-EDTA complex in the bubble column reactor were investigated. As the concentrations of the complex increased, the conversion rate of hydrogen sulfide increased, while Fe concentration and pH were stably decreased and the amount of elemental sulfur produced was also increased. Hydrogen sulfide was removed efficiently when the concentration of Fe-EDTA complex was maintained more than 0.05M. pH acts as an important factor for the stability of complex in the oxidation of hydrogen sulfide and optimum pH range was 8.5~9.5. As the molar ratio of EDTA : Fe was increased, the conversion rate of hydrogen sulfide became stable. However, the rate was decreased due to the precipitation of FeS when the concentration of EDTA was decreased. As the concentration of EDTA increased, the conversion rate of hydrogen sulfide increased due to the high stability of Fe-EDTA complex.

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A Study on the Development of Superheater Using High-Frequency Resonant Inverter for Induction Heating (유도가열용 고주파 공진형 인버터를 이용한 과열증기 발생장치 개발에 관한 연구)

  • 신대철;권혁민;김기환;김용주
    • The Transactions of the Korean Institute of Power Electronics
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    • v.9 no.2
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    • pp.119-125
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    • 2004
  • This paper is described the indirect induction heated boiler system and induction heated hot air producer using the voltage-fed series resonant high-frequency inverter which can operate in the frequency range from 20〔KHz〕 to 50〔KHz〕. A specially designed Induction heater, which is composed of laminated stainless assembly with many tiny holes and interconnected spot welding points between stainless plates, is inserted into the ceramic type vessel with external working coil. This working coil is connected to the resonant inverter. In the induction heater, it's primary heating section creates low-pressure saturated steam and secondary heating section generates heat distribution evaporating fluid from the turbulence fluid which is flowing through the vessel. The operating performances of this unique appliance in next generation and its effectiveness are evaluated and discussed from the practical point of view.