• 한국재료학회지
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• 제32권5호
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• pp.280-286
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• 2022

Corrosion is a natural, inevitable process, and is one of the world's most serious problems. Losses incurred due to corrosion are extremely expensive for society. Several technological strategies have been explored and implemented to address these losses. The use of inhibitors to prevent corrosion is a common and efficient method to reduce corrosion losses. This review covers Al and Al-composite corrosion inhibitors in chloride-containing solutions, because of their popularity in a broad array of industrial applications. A vast number of studies in the literature detail the common tendency of Al and Al-composites with reinforcements to deteriorate. Accordingly, it is worthwhile to employ inhibitors to protect them, as discussed in the present work. The emphasis is on selecting the smartest corrosion inhibitor and evaluating its performance. According to the study, the most commonly used corrosion inhibitors are 1,4-naphthoquinone (NQ), 1,5-naphthalene diol, 3-amino-1,2,4-triazole-5-thiol (ATAT), ammonium tetrathiotungstate, clotrimazole, amoxicillin, antimicrobial and antifungal drugs. Electrochemical impedance spectroscopy (EIS), potentiodynamic (PDP), and weight loss were among the most commonly used modern electrochemical technologies to test inhibitors' efficacy under environmental conditions.

• 한국응용과학기술학회지
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• 제27권2호
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• pp.208-215
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• 2010

EAF dust which is contained around 30% of zinc, 15% of iron and 3% of lead individually, is chemically treated by ammonium chloride, ammonia water, ammonia gas and carbon dioxide, and also tested and identified the ratios of the recovery of In by applied the variations of particle size, pH and heating temperature as well, in order to getting optimized recovery of the In metal after performing all of those processes. Experimental results showed that the rate of Zn recovery is 97% when the mixture of 1.3 of $NH_4Cl$/EAF is heated to the temperature of $400^{\circ}C$ and leached by water, and 95% recovery of In when ammonia gas and carbon dioxide is added simultaneously and adjust the 9.5 of pH to the same mixture above. For the purpose of remove the impurities in the mixed sample, which is prepared by the two samples, indicated above showing as the ratio of 95% and 97% recovery, in case of applied the cementation process to it, and also by electrolytic process, produced the In plate of 95~97%, and acquired 99-99.5% of In metal ingot finally by applied the heating process at $470{\sim}500^{\circ}C$.

• 한국표면공학회지
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• 제30권2호
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• pp.104-110
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• 1997

Conventional hexavlent chromium electroplating baths deposit the matal at low cathode efficiency and have poor covering and throwing power. The processs also generate hazardous wastes. To overcome many of the disadvantages of hexavalent chromium plating the use of trivalent chromium has advocted. After Yoshida, who first studied trivalent chromium plating, using ammonium sulfate and urea, there are numerous report describing the trivalent chromium electropating process using complexing agents. This study investigaten trivalent chromium plating electrolyte solutious containing formate as a complexing agent and ammouim chloride for conducting agent. The effects of composition and operating conditions on deposits and current efficiencies were investigated in trivalent chromium plating baths by analyzing the relationship pulse conditions and surface morphology The surface morphology of the deposits was observed by SEM. pulse electrolysis has been effective on obtaining a smooth with high current efficiency comparing with D.C. electrolysis in trivalent chromium solution.

• 한국수소및신에너지학회논문집
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• 제25권5호
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• pp.475-481
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• 2014

Ammonia borane ($NH_3BH_3$), as a source material for energy generation and hydrogen storage, has attracted growing interest due to its high hydrogen content. We have investigated the synthesis of ammonia borane from sodium borohydride ($NaBH_4$) and ammonium chloride ($NH_4Cl$) utilizing a low-temperature process. From our results, we obtained a maximum synthetic yield of 98.2% of ammonia borane complex. The diammoniate diborane (DADB) was detected in about 5~10mol% with in the solid ammonia borane by solid-state $^{11}B$-NMR analysis. The synthesized solid ammonia borane products were studied to characterize hydrogen release upon thermal dehydrogenation.

• 한국건설순환자원학회논문집
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• 제3권4호
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• pp.366-373
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• 2015

재건축 재개발 사업 등으로 인하여 증가하는 건설폐기물을 효율적이고 친환경적으로 처리하기 위하여 건설폐기물을 재활용하여 사용하고 있다. 대표적으로 순환골재가 있으며, 이는 수산화칼슘에 의하여 높은 강알칼리성을 나타내며 많은 환경문제를 발생시키고 있다. 따라서 본 연구는 순환골재의 pH를 저감하기 위해 인산나트륨계암모늄염을 사용하여 순환골재의 강알칼리성을 감소시키기 위한 연구이다. 또한, 순환골재 pH 저감제의 현장적용 가능성을 평가하였다. 그 결과 pH 저감제 비율이 증가할수록 pH가 감소하는 것을 확인할 수 있었으며 순환골재 생산과정 중 pH 저감제를 이용한 침지, 분사 등의 방법으로 현장적용이 가능할 것으로 판단된다.

• 자원리싸이클링
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• 제7권4호
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• pp.64-75
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• 1998

본 연구의 목적은 분무배소법에 의해 조성과 입도분포가 매우 균일하고 고순도인 Fe 산화물과 Mn 산화물의 복합산화물 또는 Mn 페라이트 분말을 제조하는데 있다. 본 연구에서는 우선 염산 용액에$SiO_2$, P, Al, Ca, Na 등의 불순물들을 다량 함유하고 있는 Fe와 Mn 성분을 정해진 조성으로 용해시킴으로써 분무배소의 원료용액을 제조하였다. Na와 Ca를 제외한 대부분의 불순물들은 원료 산 용액의 pH를 약 3이상으로 유지시킴으로써 공침현상에 의해 효과적으로 제거되었으며 Na와 Ca 성분은 분말제조 후 수세에 의해 제거가 가능하였다. 반면 PVA, resin amine 등의 고분자 응집제들은 불순물 제거에 거의 효과가 없는 것으로 확인되었다. 본 연구에서는 불순물들이 효과적으로 제거된 정제된 산 용액을 노즐을 이용하여 고온의 배소로 내로 분무시킴으로써 Fe 산화물과 Mn 산화물의 복합 산화물 또는 Mn 페라이트 분말을 제조하였다. 이때 생성된 분말들은 매우 균일하게 혼합되어 있었으며, 배소로 내에서의 반응온도가 증가할수록 생성된 분말의 입도는 증가하였다.

• 공업화학
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• 제7권2호
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• pp.379-386
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• 1996

광 이량화 특성을 나타내는 1-methyl-4-[2-(4-diethylacetylphenyl)ethenyl] pridinium methosulfate(SbQ-A염)를 dimethyl sulfate, terephthalaldehyde mono-(diethyl acetal) 및 4-picoline을 이용하여 합성하였다. 합성된 SbQ-A염을 PVA와 반응시켜 동일(MW=77,000-79,000g/mol) 분자량을 가진 PVA내 SbQ의 함량이 다른 PVA-SbQ-H 시료 및 SbQ의 함량은 약 1.3mol%로 같으나 PVA의 분자량이 다른 PVA-SbQ-L들을 합성하였다. Gray scale(GS)법을 이용하여 측정된 PVA-SbQ 수용성 감광성 고분자의 상대감도는 PVA내 SbQ의 함량이 증가함에 따라 증가하였으며, PVA의 분자량이 낮아질수록 감소하였다. PVA-SbQ-H의 경우 SbQ 함량이 2.63mol%인 시료는 PVA에 ammonium dichromate가 혼합된 기존시료보다 90배 증가된 감도를 나타내었다. PVA-SbQ를 사용하여 형광체 슬러리를 제조하고 사진식각공정을 거쳐 형광체의 미세패턴을 형성하였다. 형광체 슬러리 제조시 양이온 계면활성제인 cetyltrimethyl ammonium chloride를 첨가제로 사용하면 형광면의 해상도가 증가됨을 알았다.

• 한국지하수토양환경학회지:지하수토양환경
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• 제9권4호
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• pp.24-31
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• 2004

유류오염토양을 건설재료로 재활용할 수 있는 방안으로써 Cold Mix Asphalt(CMA) 처리를 제시하였고 디젤 및 디젤화합물로 오염된 토양의 CMA 처리특성을 고찰하였다. 양이온성 또는 음이온성 또는 비이온성 계면활성제를 함유하고 있는 5가지 아스팔트 이멀젼을 이용해서 디젤 오염토양의 처리능을 고찰한 결과 첨가된 계면활성제의 차이에 의한 성능의 차이는 확연하게 드러나지 않았으나, 토양과의 친밀성 및 흡착계수를 고려하여 Lauryl Dimethyl Benzyl Ammonium Chloride (LDBAC)를 포함한 이멀젼을 오염토양 처리에 적합한 아스팔트 이멀젼으로 선정하였다. 아스팔트 이멀젼 LDBAC에 의한 세가지 디젤화합물의 처리능은 docosane, pentadecane, undecane의 순으로 높은 것으로 나타났다. 아스팔트 이멀젼 LDBAC를 이용하여 CMA처리된 토양에 대한 용출실험결과 비교적 고농도인 10,000 mg/kg 의 디젤로 오염된 토양도 CMA처리 가능함을 확인하였다. 공시체로부터 디젤의 용출은 초기 4일까지는 확산에 의한 거동을 보여 주었고 그 이후로는 용출속도가 감소하여 총 용출가능양의 $50\%$ 이상이 유출되었다고 판단되는 depletion의 거동을 보여 주었다. CMA처리된 오염토양으로부터 3가지 디젤화합물의 총용출량은 undecane > pentadecane > docosane의 순서로 높은 것으로 나타났으며, pentadecane의 경우 CMA 처리시 양생속도가 상대적으로 더딘 것으로 밝혀졌다.

• 한국재료학회:학술대회논문집
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• 한국재료학회 2003년도 춘계학술발표강연 및 논문개요집
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• pp.135-135
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• 2003

This paper presents the preparation of SnO$_2$ films by Sol-Gel process and using spin coating method, and their sensing properties in CO gas. Experimental procedure consisted of following steps: (1) Tin chloride(SnCl$_4$) and Ammonium hydrogen carbonate (NH$_4$HCO$_3$) were used as precursors; (2) the Sol solution with concentration of about 10wt% SnO$_2$ was prepared from washed Gel-precipitate for spin coating step; (3) thereafter, the coating solution was dropped onto the alumina (Al$_2$O$_3$) substrate that was then spun, the spin coating was carried out with total 10 times; (4) finally, the films were calcined for 3 hours at 50$0^{\circ}C$ or higher temperature (600, 700, 800 or 90$0^{\circ}C$) in order to obtain various gram sizes. The average grain size was calculated by Scherrer's equation using main peaks in XRD spectra; meanwhile the thickness, microstructure and surface morphology of the films were observed by FE-SEM.

• 상하수도학회지
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• 제25권4호
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• pp.503-510
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• 2011

Ammonia in water which is toxic to human, its concentration is regulated below 0.5 mg/L in drinking water. Current study aimed to develop appropriate models for ammonia stripping using hollow fiber membrane contactor. Two different models were developed during the study. Model 1 was assumed only free ammonia ($NH_3$) transfer in stripping process, whereas the Model 2 was assumed with total ammonia ($NH_3+{NH_4}^+$) transfer. Ammonium chloride ($NH_4CI$), sodium hydroxide(NaOH) were used to make ammonia solution, which was concentration of 25 mg as N/L at a pH of 10.5. The experimental conditions were such that, the liquid flow was in tube-side in upward direction and t he gas flow was on shell-side in downward direction a t room temperature. The experimental and modeling results showed that marginal difference were observed at low gas flux. However the difference between the both models and experimental value were increased when the gas flux was increased. The study concludes that the Model 1 with free ammonia is more appropriate when both models were compared and useful in ammonia stripping process at low gas flux.