• 제목/요약/키워드: Chlorination

검색결과 335건 처리시간 0.02초

Cl2+CO 혼합가스에 의한 합성루타일 염화반응의 속도론적 연구 (Chlorination Kinetics of Synthetic Rutile with Cl2+CO Gas)

  • 홍성민;이소영;손호상
    • 자원리싸이클링
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    • 제29권3호
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    • pp.3-10
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    • 2020
  • 일메나이트의 선택염화를 통해 제조한 합성루타일을 유동층에서 CO와 Cl2 혼합가스를 이용하여 염화시켜 TiO2의 염화반응 속도에 미치는 반응 온도, 시간, CO가스와 Cl2가스의 분압 비($p_{Cl_2}/p_{CO}$)의 영향에 대하여 조사하였다. $p_{Cl_2}/p_{CO}$가 높을 때 TiCl4의 전환율은 감소하였으며, 화학양론 계산결과와 실험결과를 비교하였을 때 Cl2가스 보다 CO가스의 분압이 더 큰 영향을 미친 것으로 판단되었다. 따라서 실험 결과를 입자의 기공을 고려한 모델에 대입하였을 때 합성 루타일의 염화반응은 화학반응율속으로 결정되었고, 활성화에너지는 53.77 kJ/mol로 계산되었다.

PVC에 의한 일메나이트 광석 중 선택염화에 의한 Fe의 제거 (Removal of Iron from Ilmenite through Selective Chlorination Using PVC)

  • 손용익;링리에;손호상
    • 자원리싸이클링
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    • 제25권3호
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    • pp.74-81
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    • 2016
  • 고정층 반응기에서 PVC를 염화제로 사용하여 일메나이트 광석 중 철을 선택적으로 제거하기 위한 염화반응에 대하여 조사하였다. 철의 제거율에 미치는 PVC첨가량과 반응온도의 영향에 대하여 조사하였다. 철의 제거율은 PVC 첨가량과 온도가 증가할수록 상승하였다. PVC에서 생성된 HCl가스와 반응한 후의 시편 표면에는 많은 기공이 관찰되었다. 이러한 기공에 의해서 일메나이트 입자의 중앙부분에 있는 철과 반응할 수 있었던 것으로 생각된다. 선택적 염화반응을 속도론적 모델에 의해 조사한 결과 입자 계면에서의 화학반응에 의해서 율속되는 것으로 생각된다. PVC를 사용한 일메나이트의 선택적 염화반응에서 활성화 에너지는 20.47 kJ/mol로 계산되었다.

상수 염소 소독에 의한 클로로페놀 생성에 관한 연구 (A Study on Production of Chlorophenols by Chlorinaion of Drinking Water)

  • 정용;권숙표;박하영
    • 약학회지
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    • 제24권2호
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    • pp.87-95
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    • 1980
  • Chlorination to polluted water can produce chlorocompounds which may impair human health. It has been discussed that chlorophenols would be one of undesirable substances in drinking water. This study was undertaken to investigate the production mechanism of chlorophenols by chlorination in the disinfection of water and to determine pollution levels of phenols as precursor of chlorophenols and chloropbenols in some sewage, stream water and tap water in the vicinity of Seoul from January to September, 1979. By chlorination with hyperchlorite to phenols in distilled water, o-chlorophenol was predominantly produced at the concentration of less than 10ppm of free chlorine. o-Chlorophenol, 2,6-dichlorophenol and 2,4-dichlorophenol were also produced by chlorination with the concenration from 20 to 100ppm of free chlorine. From the concentration of 100ppm of free chlorine to 200ppm, o-Chlorophenol was vanished and 2,6-dichlorophenol and 2,4-dichlorophenol were determined. Phenols originated from night soil, municipal sewage and stream were determined at 49.15 ppm. 0.095 ppm and 0.003 ppm in average respectively. About 87 and 88 percent of phenols in sewage and night soil were biodegradated by aeration for 10 days and 74 and 51 percent of phenols in sewage and night soil by spontaneous settling for 10 days. From the tap water in Seoul during summer, 1979, chlorophenols were identified; they were average 0.042 ppb of o-chlorophenol, 0.033 ppb of 2, 6-dichlorophenol and 0.003 ppb of 2, 4-dichlorophenol respectively. With the above result and discussion, it is considered that chlorophenols should be controlled from the source as well as chlorination in water purification.

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Chlorination of TRU/RE/SrOx in Oxide Spent Nuclear Fuel Using Ammonium Chloride as a Chlorinating Agent

  • Yoon, Dalsung;Paek, Seungwoo;Lee, Sang-Kwon;Lee, Ju Ho;Lee, Chang Hwa
    • 방사성폐기물학회지
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    • 제20권2호
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    • pp.193-207
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    • 2022
  • Thermodynamically, TRUOx, REOx, and SrOx can be chlorinated using ammonium chloride (NH4Cl) as a chlorinating agent, whereas uranium oxides (U3O8 and UO2) remain in the oxide form. In the preliminary experiments of this study, U3O8 and CeO2 are reacted separately with NH4Cl at 623 K in a sealed reactor. CeO2 is highly reactive with NH4Cl and becomes chlorinated into CeCl3. The chlorination yield ranges from 96% to 100%. By contrast, U3O8 remains as UO2 even after chlorination. We produced U/REOx- and U/SrOx-simulated fuels to understand the chlorination characteristics of the oxide compounds. Each simulated fuel is chlorinated with NH4Cl, and the products are dissolved in LiCl-KCl salt to separate the oxide compounds from the chloride salt. The oxide compounds precipitate at the bottom. The precipitate and salt phases are sampled and analyzed via X-ray diffraction, scanning electron microscope-energy dispersive spectroscopy, and inductively coupled plasma-optical emission spectroscopy. The analysis results indicate that REOx and SrOx can be easily chlorinated from the simulated fuels; however, only a few of U oxide phases is chlorinated, particularly from the U/SrOx-simulated fuels.

Chiral 2-Amino Alcohol Derivatives Catalyze the Enantioselective α-Chlorination of β-Ketoesters

  • Zhang, Baohua;Guo, Ruixia;Liu, Sijie;Shi, Lanxiang;Li, Xiaoyun
    • Bulletin of the Korean Chemical Society
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    • 제35권6호
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    • pp.1759-1762
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    • 2014
  • The enantioselective ${\alpha}$-chlorination of cyclic ${\beta}$-ketoesters catalyzed by chiral 2-aminoalcohol derivatives (2f) has been developed. For the optically active ${\alpha}$-chlorinated products, the isolated yields are in the range of 85-94% and the enantiomeric excesses are up to 84% ee.

염소화 반응조건이 SBR의 표면마찰 특성에 미치는 영향 (The Effects of Chlorination on the Friction Properties of SBR)

  • 박차철;김호정
    • 한국의류산업학회지
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    • 제10권1호
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    • pp.101-105
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    • 2008
  • This study was concerned with the influence of reaction conditions on the surface friction properties of Syrene-Butadiene Rubber(SBR) sheet when it was chlorinated by chemical treatment method using the sodium hypochlorite and sulfuric acid. The results of this study were as follows. SEM photographs of chlorinated SBR surface showed uneven etching caused by the chlorination. In the FTIR spectra, the intensity of C=C peak of SBR was decreased with increasing the concentration of sodium hypochlorite. Otherwise there was no trace of C=C peak in spectrum of SBR treated with 5 wt% NaOCl with pH 0.1 for 90 seconds. EDX spectra showed that relative content of chlorine of SBR was increased with increasing the amount of sodium hypochlorite, and also affected with pH condition of acid solution. Friction angle and friction coefficient of SBR were influenced with concentration of sodium hypochlorite, but were not with pH condition of acid solution.

염소처리에 의한 Microcystin의 제거 (Removal of microcystin by chlorination)

  • 이태관;진정숙
    • 한국물환경학회지
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    • 제18권3호
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    • pp.321-326
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    • 2002
  • On this study, removal method for microcystin, toxic substance released from the blue-green algae, using chloride was investigated. 82 ~ 98% of Microsystin were removed within 1 hr when sample had microsystin only. However, if the sample had algae cell removal efficiency was decreased to 50%, except the concentration of chloride $10Cl-mg/{\ell}$. As a result, intermediate-chlorination which dose chloride after coagulation process is considered the optimum method for the removal of microcystin because most of algae cell could remove during the coagulation process.

항생제 내성 제어를 위한 소독 기법간의 비교 ; 염소, 오존 및 전자빔 (The Comparison of Disinfection Technologies for Managing Antibiotic Resistance ; Chlrorination, Ozonation and Electron Beam)

  • 오준식;김성표
    • 상하수도학회지
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    • 제27권6호
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    • pp.797-803
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    • 2013
  • Recently, a number of countries are now considering the reuse of effluents from wastewater treatment for various water applications. To improve the reuse of wastewater effluent, the development of appropriate micro-pollutant removal technology is necessary. Although several researche have been studied for removing micro-pollutants in water, little study has been conducted for the removal of emerging contaminant such as antibiotic resistant genes (ARGs) by disinfection processes. Therefore, the aim of this study is to compare the capacity of disinfection technologies such as chlorination, ozone, and electron beam, for removing antibiotic resistant bacteria (ARB) and ARGs. Based on this study, better ARG removal can be achieved by ozonation and electron beam. Relatively, high CT values of chlorination or ozonation are needed to remove ARB and ARG compared to conventional pathogens.

수영장 관리 (Management of Swimming Pool)

  • 김경호
    • 환경위생공학
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    • 제4권1호
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    • pp.37-42
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    • 1989
  • Management of Swimming pool is focused on Swimming pool samitation in relation with chlorination of swimming water and potable water, disposal of waste and excrement within the boundry of swimming pool that may be summerised as follows: 1. Chlorination of Swimming Water Residual chlorine must be kept within the range of $0.4\~0.6 mg/l$ and in case of chloramine should be $0.7\~1.0mg/l$ while swimming pool is in operation 2. Chlorination of potable Water Residual chlorine must be kept within the rangs of $0.2\~04 mg/l$ at all time 3. Disposal of litters must be kept in the water tight waste bin with fitted lid, and waste should not be overflow -out of the bin. When waste in landfilled, the sufficient amount of cover material should be used daily. 4. Disposal of excrement Toilet must be water-flush type. However, The establishment of pit latrine is unavoidable the excrement must be covered with lime or dirt so that excrement should not be exposed to air.

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음용수내 발암물질인 염소 소독부산물의 전기화학적 제거 특성 (Electrochemical Removal Characteristics of Disinfection By-products by Chlorination in Drinking Water)

  • 권순우;이종대;신장식
    • 한국응용과학기술학회지
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    • 제21권4호
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    • pp.364-369
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    • 2004
  • It has been confirmed that some Trihalomethanes (THMs) suspected as carcinogens, can be formed during chlorination for water supply through the reaction of chlorine and humic substances in water. The electrochemical characteristics on activated carbon fiber filter (ACF) electrode were investigated to remove the THMs in the chlorination process of drinking water. The electrochemical removal efficiency depended on the applied voltage and flow rate. In this study, the best result showed that the removal efficiency of THMs was higher than 99%.