• Title/Summary/Keyword: 탄산화반응

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Research on the Production of CO2 Absorbent Using Railway Tie Concrete Waste (콘크리트 철도 침목 폐기물을 활용한 CO2 포집제 제조 연구)

  • Gyubin Lee;Jae-Young Lee;Hyung-Jun Jang;Sangwon Ko;Hye-Jin Hong
    • Journal of the Korean Recycled Construction Resources Institute
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    • v.11 no.3
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    • pp.260-266
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    • 2023
  • In recent years, excessive emissions of carbon dioxide(CO2) have become the cause of global climate change. Consequently, there has been significant research activity aimed at both removing and utilizing CO2. This study assesses the potential utilization of railway tie concrete waste, generated from railway infrastructure, as a CO2 absorption material and investigates the physicochemical properties before and after CO2 absorption to understand the CO2 removal mechanisms. Railway tie concrete waste primarily consists of Si(26.60 %) and contains 9.82 % of Ca. Compared to samples of Cement and Normal concrete waste, it demonstrated superior potential for use as a CO2 absorption material, with approximately 98 % of the Ca content participating in CO2 absorption reactions. Through Thermogravimetric Analysis(TGA) and X-ray Diffraction(XRD) analysis, it was confirmed that the carbonate reaction, where the Ca in railway tie concrete waste converts into CaCO3 through reaction with CO2 gas, is the primary mechanism for CO2 removal. Furthermore, Scanning Electron Microscopy(SEM) analysis revealed the formation of numerous CaCO3 particles with sizes less than 0.1 ㎛ after the CO2 absorption reaction. This transformation of large internal voids in the CO2 absorption material into mesopores resulted in an increase in the specific surface area of the material.

Numerical Analysis of Molten Carbonate Fuel Cell Stack Using Computational Fluid Dynamics (CFD를 이용한 용융탄산염 연료전지 스택의 수치모사)

  • Lee, Kab-Soo;Cho, Hyun-Ho
    • Journal of the Korean Electrochemical Society
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    • v.8 no.4
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    • pp.155-161
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    • 2005
  • In this paper, commercial CFD program FLUENT v5.3 is used for simulation of MCFC stack. Besides using conservation equations included in FLUENT by default, mass change, mole fraction change and heat added or removed due to electrochemical reactions and water gas shift reaction are considered by adding several equations using user defined function. The stacks calculated are 6 and 25 kW class coflow stack which are composed of 20 and 40 unit cells respectively. Simulation results showed that pressure drop took place in the direction of gas flow, and the pressure drop of cathode side is more larger than that of anode side. And the velocity of cathode gas decreased along with the gas flow direction, but the velocity of anode gas increased because of the mass and volume changes by the chemical reactions in each electrodes. Simulated temperature profile of the stack tended to increase along with the gas flow direction and it showed similar results with the experimental data. Water gas shift reaction was endothermic at the gas inlet side but it was exothermic at the outlet side of electrode respectively. Therefore water gas shift reaction played a role in increasing temperature difference between inlet and outlet side of stack. This results suggests that the simulation of large scale commercial stacks need to consider water gas shift reaction.

Greenhouse Gas Emission Reduction and Economic Benefit Evaluation of Carbon Mineralization Technology using CFBC Ash (순환유동층 석탄재를 이용한 탄소광물화 기술의 온실가스 배출 저감량 및 경제성 분석)

  • Jung, Euntae;Kim, Jeongyun
    • Resources Recycling
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    • v.31 no.3
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    • pp.40-52
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    • 2022
  • This study analyzed the amount of carbon dioxide reduction and economic benefits of detailed processes of CO2 6,000 tons plant facilities with mineral carbonation technology using carbon dioxide and coal materials emitted from domestic circulating fluidized bed combustion power plants. Coal ash reacted with carbon dioxide through carbon mineralization facilities is produced as a complex carbonate and used as a construction material, accompanied by a greenhouse gas reduction. In addition, it is possible to generate profits from the sales of complex carbonates and carbon credits produced in the process. The actual carbon dioxide reduction per ton of complex carbonate production was calculated as 45.8 kgCO2eq, and the annual carbon dioxide reduction was calculated as 805.3 tonCO2, and the benefit-cost ratio (B/C Ratio) is 1.04, the internal rate return (IRR) is 10.65 % and the net present value (NPV) is KRW 24,713,465 won, which is considered economical. Carbon mineralization technology is one of the best solutions to reduce carbon dioxide considering future carbon dioxide reduction and economic potential.

Study on Preparation of High Purity Lithium Hydroxide Powder with 2-step Precipitation Process Using Lithium Carbonate Recovered from Waste LIB Battery (폐리튬이차전지에서 회수한 탄산리튬으로부터 2-step 침전공정을 이용한 고순도 수산화리튬 분말 제조 연구)

  • Joo, Soyeong;Kang, Yubin;Shim, Hyun-Woo;Byun, Suk-Hyun;Kim, Yong Hwan;Lee, Chan-Gi;Kim, Dae-Guen
    • Resources Recycling
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    • v.28 no.5
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    • pp.60-67
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    • 2019
  • A valuable metal recovery from waste resources such as spent rechargeable secondary batteries is of critical issues because of a sharp increase in the amount of waste resources. In this context, it is necessary to research not only recycling waste lithium-ion batteries (LIBs), but also reusing valuable metals (e.g., Li, Co, Ni, Mn etc.) recovered from waste LIBs. In particular, the lithium hydroxide ($LiOH{\cdot}xH_2O$), which is of precursors that can be prepared by the recovery of Li in waste LIBs, can be reused as a catalyst, a carbon dioxide absorbent, and again as a precursor for cathode materials of LIB. However, most studies of recycling the waste LIBs have been focused on the preparation of lithium carbonate with a recovery of Li. Herein, we show the preparation of high purity lithium hydroxide powder along with the precipitation process, and the systematic study to find an optimum condition is also carried out. The lithium carbonate, which is recovered from waste LIBs, was used as starting materials for synthesis of lithium hydroxide. The optimum precipitation conditions for the preparation of LiOH were found as follows: based on stirring, reaction temperature $90^{\circ}C$, reaction time 3 hr, precursor ratio 1:1. To synthesize uniform and high purity lithium hydroxide, 2-step precipitation process was additionally performed, and consequently, high purity $LiOH{\cdot}xH_2O$ powder was obtained.

Study of Separation of carbon dioxide through hollow fiber membrane contactor (중공사막 접촉장치를 통한 이산화탄소 분리에 관한 연구)

  • 염봉열;김민수;이용택;박유인;이규호
    • Proceedings of the Membrane Society of Korea Conference
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    • 1997.10a
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    • pp.61-64
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    • 1997
  • 1. 서론 : 적절한 이산화탄소의 분리는 지구온난화의 가속현상을 늦출 수 있을 뿐만 아니라 각종 탄화수소가스의 원료로 분리 정제된 이산화탄소를 재이용할 수 있으므로 경제적으로 매우 중요하다. 이산화탄소 분리에 사용되던 기존 공정들의 단점을 보완할 수 있는 대체방안으로 최근에 개발되기 시작한 것이 소수성의 다공성 고분자 분리막(hydrophobic porous ploymeric membrane) 방법인데, 이는 모듈의 유효 막 표면적이 상대적으로 크고 기체와 액체의 흐름을 독립적으로 제어할 수 있으므로 범람 등의 현상이 없으나 막 자체의 저항이 비교적 큰 단점을 가지고 있다. Qi와 Cussler는 이러한 특성을 가지는 중공사막 모듈에서의 기-액 흐름에 대한 물질전달 상관관계식을 얻었으며[1], Karoor 등은 여러 가지 중공사막 모듈을 사용하여 순수물과 diethanolamine(DEA) 등의 흡수제에 대한 이산화탄소의 물질전달 거동을 수치모델과 실험을 통하여 고찰하였다[3]. 또한 중공사막 접촉기의 실제적 응용에 대하여 Matsumoto 등은 화력발전소에서 발생하는 연소가스 내의 이산화탄소 흠수에 대한 연구를 수행하였다[4]. 본 연구에서는 중공사막 접촉장치를 사용하여 흡수제를 순수물과 탄산칼륨($K_2CO_3$)을 사용했을 경우의 이산화탄소의 분리 거동을 수치모델과 실험을 통하여 고찰하였다. 수치모델의 경우 이전까지의 연구가 반응이 없는 경우나 반응식을 간략화시킨 경우에 한정되었는데 비하여, 반으이 있는 경우 각각의 반응물질들의 거동을 고려한 반응식을 유도하여 해를 구하고자 하녔다.

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Phase equilibria between coexisting minerals in the talc ores and process of talc formation in the Daeheung Talc Deposits, Korea (대흥활석광상에 있어서 공존하는 광물의 상평형과 활석화 과정)

  • 이상헌
    • The Journal of the Petrological Society of Korea
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    • v.3 no.2
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    • pp.156-170
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    • 1994
  • The talc ore deposits can be divided into chloritic and dolomitic ores according to mineral assemblages. The former is mainly composed of chlorite and talc accompanied with dolomite, muscovite and opaque mineral, and the latter of dolomite and talc with serpentine, calcite and magnesite in places. Talc was originated from chlorite and serpentine. Carbonate minerals were formed either directly from the introduced hydrothermal solution or secondarily as a by-product of steatitization of chlorite and serpentine. The process of talc formation may be governed by the chemical composition of the host rocks and the amount and/or chemical composition of the hydrothermal solution which may be different in places. However, the representative reactions producing talc from chlorite and serpentine are as follows : (1) chlorite+$Mg^{++}+Si^{4+}+H_2O$=talc, (2) chlorite+$Mg^{++}+Si^{4+}+Ca^{++}+CO_2+O_2+H_2O$=talc+ dolomite+ magnesite, and (3) serpentine +$Mg^{++}+Fe^{++}+Si^{4+}+Ca^{++}+CO_2+H_2O$=talc+dolomite. The reactions indicate that the carbonate minerals can be formed when the hydrothermal solution have high $fO_2$ and $fCO_2$. The steatitization might be proceeded by the hydrothermally metasomatic reaction between chlorite schist or chlorite gneiss intercalated in the granitic gneiss and hydrothermal solution accompanied to the wet granitization.

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CO2 Fixation by Magnesium Hydroxide from Ferro-Nickel Slag (페로니켈 슬래그로 부터 제조된 Mg(OH)2를 이용한 CO2 고정화)

  • Song, Hao-Yang;Seo, Jong-Beom;Kang, Seong-Kuy;Kim, In-Deuk;Choi, Bong-Wook;Oh, Kwang-Joong
    • Clean Technology
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    • v.20 no.1
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    • pp.42-50
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    • 2014
  • In this study, the $Mg(OH)_2$ slurry was made form ferro-nickel slag and then used for $CO_2$ sequestration. The experiments were in the order as leaching step, precipitation, carbonation experiments. According to the leaching results, the optimal leaching conditions were $H_2SO_4$ concentration of 1 M and the temperature of 333 K. In the $Mg(OH)_2$ manufacturing step, NaOH was added to increase the pH upto 8, the first precipitation was confirmed as $Fe_2O_3$. After removal the first precipitation, the pH was upto 11, the $Mg(OH)_2$ was generated by XRD analysis. The $Mg(OH)_2$ slurry was used for $CO_2$ sequestration. The pseudo-second-order carbonation model was used to apply for $CO_2$ sequestration. The $CO_2$ sequestration rate was increased by the $CO_2$ partial pressure and temperature. However, $CO_2$ sequestration rate was decreased when temperature upto 323 K. After $CO_2$ sequestrated by $Mg(OH)_2$, the $CO_2$ can be sequestrated stable as $MgCO_3$. This study also presented optimal sequestration condition was the pH upto 8.38, the maximum $MgCO_3$ can be generated. This study can be used as the basic material for $CO_2$ sequestration by ferro-nickel slag at pilot scale in the future.

용융탄산염형 연료전지 분리판 재료의 부식거동

  • 이충곤
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 1998.05a
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    • pp.21-21
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    • 1998
  • 새로운 에너지원으로 각광받고 있는 연료전지는 우주선 동력윈으로서의 이용이래, 보다 실용적인 발전 시스템을 목적으로 많은 연구개발이 시도되고 있다. 이러한 연료전지는 사용하는 전해질의 특성으로 인하여 저온형($<300^{\circ}C$) 과 고온형($500^{\circ}C<$)으로 구분된 수 있는데, 저온형 연료전지의 경우는 전극반응 특성상 귀금속 촉매가 필요한 데 비해, 고온형 연료전지는 이러한 귀금속 촉매가 필요없다는 점등에서 다양한 장점을 가지게 된다. 즉, 저온형에 비해 다양한 연료가 가능하고, 대형화에 유리함며, 고온 페열을 이용할 수 있는 점 등을 들 수 있다. 용융탄산염형 연료전지(MFCFC)는 이러한 고온형 연료진지의 장점을 배경으로 현재 대규모의 개발이 진행되고 있다. 그러나 여기에 주로 사용되는 Li-K, Li-Na와 같은 용융탄신엽은 고부식성 전해질로서 대부분의 금속이 산화물을 형성하는 것으로 알려져 있다. MCFC의 분리판은 셀간을 전기적으로 이어주는 역할, 가스의 유로제공 및 가스 Sealing의 역할을 담당하는 부분으로서, 분리판의 부식은 이러한 특성의 저하 및 전해질의 소모를 유발시켜 MCFC의 내구성에 커다란 영향 을 미치는 요인으로 생각되고 있다. 이러한 배경으로부터 Uchida 그룹은 MCFC의 분라판 재료 의 부식거동을 계동적으로 검토하였다. 먼저 Fe에 Ni 과 Cr을 첨가한 재료를 산화성가스 분위기하에서 $(Li+K)CO_3$에 대하여 검토한 결과, Ni과 Cr 둘다 20wt%이상 첨가시, 내식성융 가지는 결 과를 보고하였다2) 이 경우 보호피막으로서 NiO 와 $LiCrO_2$가 작용하는데, $LiCrO_2$가 용융탄산염 중에서 보다 안정한 것으로 부터, Cr의 첨가가 내식성에 기여하는 것으로 판단하였다. 다음 단계 로서 Fe/Cr재료에 용-융탄산염 중에서 안정한 산화물을 형성하는 Al의 첨가효과를 검토하였다. Al의 첨가는 더욱 내식성을 향상시키는 것이 발견되었고, 약 4wt%의 첨가로 충분한 내식성을 가지 는 것을 보고 하였다. 그러나 이러한 안정한 산화물에 의한 내식성 향상은 전기진도도의 희생을 바탕으로 한 것으로서, 다읍 단계로서 Ti산화물의 반도체적인 특성을 이용하고자 제 4의 원소로서 Ti첨가를 시도하였다. 그러나 Fe/Cr/AVTi재료가 뛰어난 내식성을 가지는 것은 관찰되었으나, 전도도 향상에는 기여하지 못하는 것이 보고되었다. 현재 MCFC는 실용화를 위한 고성능화의 하나로서 가압하에서의 운전을 시도하고 있다. 이 러한 가압하에서의 운전은 기전력의 향상 및 전극반응의 촉진 등으로 출력의 향상을 가져오나. 현재 문제로 되고 있는 Cathode극인 NiO의 용해/석출 현상을 가속화하는 결과를 초래해, 이에대 한 대책으로서 Li-K보다 NiO의 용해가 적은 Li-Na탄산염으로의 전환이 진행되고 있다. 이러한 배경으로부터 Uchida그룹에서 개발한 FeiCr/AVTi재료와 현재 분리판 재료로 사용증인 SUS 310, S SUS 316재료에 대해. 산화성 분위기의 5기압까지의 가압하에서, Li-K, Li-Na탄산염에 대하여 부 식거동을 검토한 결과, 가압하에서 내식성이 향상되는 것이 발견되었다. 이유로서는 가압하에서 용융탄산엽의 증가된 산화력으로 보다 치밀한 내식성 산화물 피막이 형성되기 때문으로 생각되고 있다. 또한 Li-K, Li-Na탄산염에서의 부식의 정도에는 차이가 거의 없었으나, SUS 316의 경우 탄산염에 젖은 부분에서 내식성 피막이 형성되지 않는 이상부식현상이 관찰되었다. 재료간의 내식성 정도에서는 Fe/Cr/Al/Ti이 가장 내식성이 뛰어났으며, SUS 310 또한 뛰어난 내식성을 보였다.

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The Effect of Chloride Additives and pH on Direct Aqueous Carbonation of Cement Paste (시멘트 풀의 직접수성탄산화에서 Chloride 첨가제와 pH의 영향)

  • Lee, Jinhyun;Hwang, Jinyeon;Lee, Hyomin;Son, Byeongseo;Oh, Jiho
    • Journal of the Mineralogical Society of Korea
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    • v.28 no.1
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    • pp.39-49
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    • 2015
  • Recently, carbon capture and storage (CCS) techniques have been globally studied. This study was conducted to use waste cement powder as an efficient raw material of mineral carbonation for $CO_2$ sequestration. Direct aqueous carbonation experiment was conducted with injecting pure $CO_2$ gas (99.9%) to a reactor containing $200m{\ell}$ reacting solution and the pulverized cement paste (W:C = 6:4) having particle size less than 0.15 mm. The effects of two additives (NaCl, $MgCl_2$) in carbonation were analyzed. The characteristics of carbonate minerals and carbonation process according to the type of additives and pH change were carefully evaluated. pH of reacting solution was gradually decreased with injecting $CO_2$ gas. $Ca^{2+}$ ion concentration in $MgCl_2$ containing solution was continuously decreased. In none $MgCl_2$ solution, however, $Ca^{2+}$ ion concentration was increased again as pH decreased. This is probably due to the dissolution of newly formed carbonate mineral in low pH solution. XRD analysis indicates that calcite is dominant carbonate mineral in none $MgCl_2$ solution whereas aragonite is dominant in $MgCl_2$ containing solution. Unstable vaterite formed in early stage of experiment was transformed to well crystallized calcite with decreasing pH in the absence of $MgCl_2$ additives. In the presence of $MgCl_2$ additives, the content of aragonite was increased with decreasing pH whereas the content of calite was decreased.

Characterization of CO2 Biomineralization Microorganisms and Its Mineralization Capability in Solidified Sludge Cover Soil in Landfill (매립지 복토용 슬러지 고화물내 이산화탄소 생광물화 고정균 분석 및 생광물화능 평가)

  • Ahn, Chang-Min;Bae, Young-Shin;Ham, Jong-Heon;Chun, Seung-Kyu;Kim, Chang-Gyun
    • Journal of Korean Society of Environmental Engineers
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    • v.35 no.8
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    • pp.598-606
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    • 2013
  • This study was performed to determine whether biomineralization microbes were actively present underneath landfill cover soil producing biocalcification. From this, various types of microbes were observed. Among them, two species were dominantly found; Bacillus megaterium and Alkaliphilus metalliredigens that were known as biominerlization bacteria. With those microbes, $CO_2$ was more highly consumed than without bacteria. In response, the calcium carbonate mineral was produced at 30% (wt) greater than that of the control. At the same time, TG-DTA was successfully used for quantification of $CO_2$ consumed forming calcium carbonate minerals resulting from biocalcification. It was decided that the presence of solidified sewage sludge cake utilized as a cover soil in the landfill could efficiently contribute to possible media adaptably and naturally sequestering $CO_2$ producing from the landfill.