• Title/Summary/Keyword: 기포 상승 속도

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Study of Hydrodynamics and Reaction Characteristics of K-based Solid Sorbents for CO2 Capture in a Continuous System Composed of Two Bubbling Fluidized-bed Reactors (두 개의 기포유동층으로 구성된 연속장치에서 CO2 회수를 위한 K-계열 고체흡수제의 수력학적 특성 및 반응특성)

  • Kim, Ki-Chan;Kim, Kwang-Yul;Park, Young Cheol;Jo, Sung-Ho;Ryu, Ho-Jung;Yi, Chang-Keun
    • Korean Chemical Engineering Research
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    • v.48 no.4
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    • pp.499-505
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    • 2010
  • In this study, hydrodynamics and reaction characteristic of K-based solid sorbents for $CO_2$ capture were investigated using a continuous system composed of two bubbling fluidized-bed reactors(1.2 m tall bed with 0.11 m i.d.). Potassium-based dry sorbents manufactured by the Korea Electric Power Research Institute were used, which were composed of $K_2CO_3$ of 35% for $CO_2$ absorption and supporters of 65% for mechanical strength. The continuous system consists of two bubbling fluidized-bed reactors, solid injection nozzle, riser, chiller, analyzer and heater for regeneration reaction. The minimum fluidizing velocity of the continuous system was 0.0088 m/s and the solid circulation rate measured was $10.3kg/m^2{\cdot}s$ at 1.05 m/s velocity of the solid injection nozzle. The $CO_2$ concentration of the simulated gas was about 10 vol% in dry basis. Reaction temperature in carbonator and regenerator were maintained about $70^{\circ}C$ and $200^{\circ}C$, respectively. Differential pressures, which were maintained in carbonator and regenerator, were about $415mmH_2O$ and $350mmH_2O$, respectively. In order to find out reaction characteristics of dry sorbents, several experiments were performed according to various experimental conditions such as $H_2O$ content(7.28~19.66%) in feed gas, velocity (0.053~0.103 m/s) of simulated gas, temperature($60{\sim}80^{\circ}C$) of a carbonator, temperature($150{\sim}200^{\circ}C$) of a regenerator and solid circulation rate($7.0{\sim}10.3kg/m^2{\cdot}s$). The respective data of operating variables were saved and analyzed after maintaining one hour in a stable manner. As a result of continuous operation, $CO_2$ removal tended to increase by increasing $H_2O$ content in feed gas, temperature of a regenerator and solid circulation rate and to decrease by increasing temperature of a carbonator and gas velocity in a carbonator.

Effects of Packaging Method on Quality of Chilled Plaice Muscle (포장방법이 냉장어육의 품질에 미치는 영향)

  • 신완철;송재철;최석영;김미숙
    • Journal of the Korean Society of Food Science and Nutrition
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    • v.32 no.8
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    • pp.1292-1296
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    • 2003
  • The purpose of this study is to investigate the changes of physico-chemical properties of chilled plaice muscle, stored at 4$^{\circ}C$ for 0 ∼ 21 days, with different packaging methods (vacuum packaged with PVDC and aerobic packaged with HDPE). pH value in aerobic packaged plaice muscle (APPM) decreased from 6.3 to 6.09 at first 2 day storage, and then increased gradually during storage time. Although pH pattern of vacuum packaged plaice muscle (VPPM) was similar to that of APPM, change of pH value during storage time was slower and lower than APPM. VBN value in aerobic packaged one increased during storage time. Especially it increased significantly after 7 days of storage. While VBN value in VPPM increased only a little to 14 days. TBA value showed significant difference between APPM and VPPM. WHC of APPM was higher than that of VPPM after 7 days of storage. In electrophoretic pattern of myofibril of APPM stored for 14 days hydrolysis of heavy chain and tropomyosin was observed. However, in VPPM, some hydrolysis occurred only in heavy chain. SDS-PAGE analysis showed that hydrolysis of VPPM occurs later than that of APPM.

고무의 가황(加黃) 및 열전도론(熱傳導論) (3(三))

  • Heo, Dong-Seop;Gwon, Dong-Yong
    • Elastomers and Composites
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    • v.10 no.2
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    • pp.136-156
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    • 1975
  • 고무는 불량열전도체(不良熱傳導體)이며 두께가 두꺼우면 내부(內部)가 적정온도수준(適正溫度水準)에 이르기 전까지 가황시간(加黃時間)이 길어진다. 가황온도(加黃溫度)가 상승(上昇)할수록 가황물(加黃物)의 물성(物性)은 열화(劣化)되는 경향(傾向이) 있다. 천연(天然)고무든지 합성(合成)고무든지 간(間)에 과가황(過加黃)에 대(對)한 저항성(抵抗性)이 나쁘므로 특(特)히 고온가황(高溫加黃)에 대(對)해 민감(敏感)하다. 이것은 고온(高溫)에서 단시간(短時間) 가황(加黃)일수록 가속(加速)된다. 평탄가황배합물(平坦加黃配合物)의 경우에서 보더라도 내부(內部)가 적절(適切)히 가황(加黃)되기도 전(前)에 외부(外部)는 과가황(過加黃)이 되는 수가 있다. 근래(近來) 발간(發刊)된 문헌(文獻)에서도 이러한 내용(內容)이 잘 설명(說明)이 되어 있는데 다른 각도(角度)에서 고찰(考察)해 볼것 같으면 정체시간(停滯時間)이 비교적(比較的) 길지 않는 한(限) 가황시간(加黃時間)은 정체시간(停滯時間)과 sheet 가황시간(加黃時間)과의 합(合)이라고 말할 수 있겠다. 예(例)를 들어 설명(說明)하자면 $130^{\circ}C(266^{\circ}F)$에서 정체시간(停滯時間)이 10분(分)이고 sheet 가황시간(加黃時間)이 20분(分)인 제품(製品)은 이 온도(溫度)에서 30분간(分間) 가황(加黃)해야 된다는 것이다. 온도계수(溫度係數)를 2라고 가정(假定)할 경우 $140^{\circ}C(284^{\circ}F)$에서의 가황시간(加黃時間)은 $30\times\frac{1}{2}=15$분(分)이 아니라 $20\times\frac{1}{2}+10=20$분(分)이 된다. 크기가 큰 제품(製品)은 보통(普通) 다음에 있는 여러 방법(方法)들 가운데 한 가지 또는 여러가지를 조합(組合)하여 가황(加黃)시킨다. a) 크기가 작은 것에 대한 것 보다 낮은 온도(溫度)에서 가황(加黃)한다. b) 침투가황-제품(浸透加黃-製品)을 가압하(加壓下)에 두고서 외부가황(外部加黃)은 단속(斷續)시키고 열(熱)이 중심(中心)으로 침투(浸透)하게 한다. c) 단계가황(段階加黃)-처음에는 저온(低溫)에서 시작(始作)하여 일정간격(一定間隔)을 두고 점차(漸次) 온도(溫度)를 상승(上昇)시켜 최종적(最終的)으로 가황온도(加黃溫度)까지 올린다. d) 가능(可能)하다면 metal base나 금형(金型)에서 고무를 증기가황(蒸氣加黃)시킬 경우에 있어서 속이 빈 축(軸)을 사용하여 내부(內部)로 부터 가열(加熱)하면 가황시간(加黃時間)이 단축(短縮)된다. e) 냉각중(冷却中)의 후가황(後加黃)-이것은 가열장치(加熱裝置)에서 끄집어낸 후 제품(製品)의 외부(外部)를 냉각(冷却)시키는 방법(方法)이다. 가열(加熱)된 제품(製品)이 쌓여 있거나 적절(適切)하게 냉각(冷却)되지 않을 때 가황(加黃)이 추가적(追加的)으로 되거나 과가황(過加黃)이 될 우려가 있는 제조공정(製造工程)에서는 흔히들 이 방법(方法)을 무시(無視)하고 있다. 여기서 강조(强調)해 두어야 할 것은 항상 제품(製品)의 외부(外部)를 완전(完全)히 가황(加黃)시킬 필요(必要)는 없다는 것이다. 다공성(多孔性)이나 기포생성(氣泡生成)을 조장(助長)하는 불량가황상태(不良加黃狀態)와 표면(表面)에서의 과가황상태간(過加黃狀態間)의 균형(均衡)을 취(取)해 줘야 하는데 물론(勿論) 이때는 가황시간(加黃時間)을 단축(短縮)시켜야 한다는 경제적(經濟的)인 측면(側面)도 아울러 고려(考慮)해야 한다. 이것은 고무기술자(技術者)가 당면(當面)해야할 과제(課題)에 속(屬)하며 바람직 한것은 본장(本章)의 내용(內容)이 여러 상황하(狀況下)에서 당면(當面)한 문제(問題)에 대(對)해 어떻게 대처(對處)해 야 할지를 모르는 여러 기술자(技術者)들에게 도움이 되었으면 하는 것이다.

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Fluid Inclusion Study of the Samcheonpo Amethyst Deposit of Kyongsangnamdo, Korea (경상남도 삼천포 광산의 자수정에 대한 유체포유물 특성)

  • Bae, Yun-Sue;Yang, Kyoung-Hee
    • Journal of the Mineralogical Society of Korea
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    • v.19 no.3 s.49
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    • pp.153-162
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    • 2006
  • Fluid inclusions in amethyst from the Samcheonpo amethyst deposit of the Waryongsan area, Kyongnam generally grouped into four different types: Type I (liquid-rich and $10{\sim}23wt%$ NaCl, $Th=289{\sim}359^{\circ}C$), Type II (vapor-rich and $2{\sim}10wt%$ NaCl, $Th=304{\sim}365^{\circ}C;$), Type III (halite-bearing, $31{\sim}54wt%$ NaCl, $Th=259{\sim}510^{\circ}C;$), and Type IV ($CO_{2}-bearing\;9{\sim}13wt%\;NaCl,\;126{\sim}277^{\circ}$). Type I, II, and III inclusions are confined in the lower part of the amethyst and Type IV in the upper, which indicates significant hydrothermal activity during the earliest stage of the amethyst growth or the solidus condition of granitic rocks. The earliest fluid exsolved from the crystallizing granitic magma formed Type IIIa which is spatially associated with silicate melt inclusions. The homogenization behavior of Type IIIa inclusions by dissolution of the halite crystal after the bubble disappearance indicates that Type IIIa inclusions were trapped at some relatively elevated pressure. Exsolution of Type IIIb, I, II forming fluids with gradual decrease in their salinity was followed. The last fluid was $CO_{2}-bearing$ fluid (Type IV), which is assumed to be derived by decarbonization reactions with the surrounding sedimentary rocks. It suggests that the fine-grained granitic rocks containing the Samcheonpo amethyst crystallized at the sub-solvus condition saturated with water and exsolved abundant water.