• Journal of Environmental Science International
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• v.17 no.2
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• pp.225-232
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• 2008

The objectives of this study were conducted to determine the effects of two chemical amendments on volatile fatty acids (VFA) and nitrogen contents in poultry litter after broiler chicks were raised in poultry houses for 6 weeks. Two different additives were applied as a top dressing to the litter at a rate of $AlCl_3{\cdot}6H_2O$ (200 g)+$CaCO_3$ (50 g) or Alum (200 g)+$CaCO_3$ (50 g)/kg of rice bran; untreated litter served as controls. Application of $AlCl_3+CaCO_3$ and Alum+$CaCO_3$ reduced total VFA contents by 67% and 51% at 6 weeks, respectively, compard to the control groups. The decrease in litter pH with two chemical treatments results in decreased proportion of VFA and increased nitrogen contents of the litter. These results indicate that treating $AlCl_3+CaCO_3$ and Alum+$CaCO_3$ to poultry litter offers the potential for reducing an environmental impact.

• Korean Journal of Poultry Science
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• v.31 no.3
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• pp.171-176
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• 2004

The objectives of this study were to determine the effect of applying two different additives to the litter on broiler performance and the carbon dioxide gas production in poultry cages. In two different experiments, the carbon dioxide gas production in poultry litter used for 42 days was measured. The chemical additives were applied to the litter at a rate of 200 g aluminum chloride(A1Cl$_3$ㆍ6$H_2O$) or 200 g aluminum sulfate [Al$_2$(SO$_4$)$_3$ㆍ14$H_2O$, Alum] + 50 g carbon carbonate per kg litter. There was no effect on broiler performance by the litter additives, but the values of carbon dioxide gas produced from broiler litters which were treated with chemical additives were significantly lower(P < 0.05 and 0.01) than that of the control. This study showed that carbon dioxide gas production can be reduced by chemically treating the litter with A1Cl$_3$ or Alum + CaCO$_3$.

• Journal of Environmental Science International
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• v.18 no.12
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• pp.1437-1442
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• 2009

Recent studies have shown that alum addition to litter results in many environmental and economic advantages, such as reductions in metal runoff, lower ammonia emission and improved poultry performance. However, no research has been conducted to evaluate the effects of different types of alum on soluble metals in poultry litter. The objective of this study was conducted to investigate changes in soluble metal from poultry litter with different types of aluminum sulfate (alum) under laboratory condition. The treatments used in this study, which were mixed in the upper 1 cm of litter or sprayed onto the litter surface, were 4 g alum, 8 g alum, 8.66 g liquid alum, 17.3 g liquid alum, 11.2 g A7 (high acid alum), and 22.4 g A7 (high acid alum)/100 g litter. Applying different types of alum to poultry litter reduced (P<0.05) concentrations of soluble Fe (9 to 54%), Cu (9 to 49%) and Zn (11 to 40%), relative to untreated litter, whereas it increased Ca and Mg (P<0.05). Mean soluble Fe and Cu levels in poultry litter from different types of alum decreased in the order: 22.4 g A7 (54% and 49%) > 17.3 g liquid alum (48% and 42%) > 8 g alum (48% and 31%) > 4 g alum (28% and 10%) > 8.6 g liquid alum (10% and 9%) > 11.2 g A7 (8.6% and 9%). Additionally, the high reduction in soluble Zn concentration was 4 g alum (40%), followed by 8 g alum (26%), 22.4 g A7 (25%), 17.3 g liquid alum (23%), 8.66 g liquid alum (18%), and 11.2 g A7 (11%), respectively. In conclusion, the current studies suggest that treating poultry litter with different types of alum can be applied to reduce soluble metal (Fe, Cu, and Zn) and to develop a production to merchandise for poultry litter that would result in reduction in pollutants from these materials. Furthermore, in order to improve environmental management in the poultry industry, the use of alum, liquid alum and high acid alum all should be provided a valid means of reducing negative environmental impact.

• Korean Journal of Mineralogy and Petrology
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• v.36 no.1
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• pp.19-32
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• 2023

This study was conducted to remove fluorine (F) (initial concentration of 9.5 mg/L) from leachate of reclaimed mine waste dump site via different methods: (1) co-precipitation using Ca-based materials; (2) adsorption using activated carbon and fly ash; and (3) coagulation and sedimentation using alum. The F removal efficiencies of each case were estimated as 65.6% (Ca co-precipitation), 27.9% (adsorption of activated carbon), 71.5% (adsorption of fly ash), and 96.6% (alum coagulation and sedimentation). In addition, the applicability of the continuous treatment process using alum coagulation was evaluated by lab-scale experiments using simulated mine drainage containing F of lower (6.4 mg/L) and higher (15.7 mg/L) concentrations, and it was confirmed that the treatment of both cases met the domestic standard (below 3 mg/L) for discharged water in clean areas. Furthermore, the results of bench-scale field tests indicated that the water quality standard of discharged water could be satisfied with the proper operation and management of the process.

• Journal of environmental and Sanitary engineering
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• v.16 no.3
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• pp.96-103
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• 2001

This study was carried out to investigate the major factors for the removal of NOMs (Natural Organic Matters) by alum ferric chloride and blended coagulants that consisted of alum and ferric chloride. Investigated factors were pH, the dosage of coagulant, alkalinity, hardness and bloc strength. The particle size contained in the test water came from the Han River was also measured. DOC(Dissolved Organic Carbon) removal at pH 6 was two to three times higher than at pH 8.5. The blended coagulant showed 9 to 10 percent higher DOC removal efficiency and 2 to 4 percent higher turbidity under the same condition. Alkalinity consumption of alum, ferric chloride and blended coagulant was 81%, 90% and 86% of theoretical value, respectively. The limit concentration of alkalinity to avoid pin floe was 10 mg $CaCO_3/L$ when alum was used. Hardness had no apparent effect on coagulation. The residual turbidity and $UV_{254}$ showed a tendency of increasing with floc strength($sec^{-1}$) increase. The order of floe strength was the following; alum >blended coagulant > ferric chloride. The particle counter test showed 89 percent of the small particle size(SPS, $1~5{\;}{\mu}textrm{m}$) and 11 percent of the medium to large particle size(M.LPS, $5~125{\;}{\mu}textrm{m}$). At PH7.85, the particle removal efficiencies of SPS($1~5{\;}{\mu}textrm{m}$) and M.LPS($5~125{\;}{\mu}textrm{m}$) in the coagulation process were 81% and 95%, respectively.

• Journal of Korean Society of Environmental Engineers
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• v.36 no.8
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• pp.561-569
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• 2014

This study was carried out to get the characteristics of anaerobic digestion for chemical/biological sludge produced from municipal sewage treatment plant for phosphorus. Anaerobic mesophilic batch tests showed that the ultimate biodegradability of waste activated sludge showed 31%, PACl sludge 24%, Alum sludge 26%, respectively. At the S/I 1.0, 75% of total biodegradable volatile solids (TBVS) of waste activated sludge was degraded with an initial rapid decay coefficient, k1 of $0.1129day^{-1}$ and 74% of TBVS of PACl sludge with k1 of $0.0998day^{-1}$, and 76% of TBVS of Alum sludge with k1 of $0.1091day^{-1}$ for 20 days. During the operation of SCFMRs, the 3 reactor (Control, PACl, Alum) pH maintained 6.7~7.0 and the reactor alkalinity maintained 1,800~ 2,200 mg/L as $CaCO_3$. The average biogas production rates of SCFMRs fed with PACl sludge and Alum sludge were 0.089 v/v-d and 0.091 v/v-d, respectively, which was 27~28% lower than that of the control (0.124 v/v-d) at an HRT (hydraulic retention times) of 20 days. And the methane content during the operation ranged 70~76% in 3 reactor. The average TVS removal efficiency of SCFMRs fed with PACl sludge and Alum sludge were 19.6% and 19.9%, respectively, at an HRT of 20 days, which showed 4% lower than that of the control (23.8%). The average BVS removal efficiency of SCFMRs fed with PACl sludge and Alum sludge were 25.8% and 26.9%, respectively, at an HRT of 20 days, which was 8~9% lower than that of the control (34.5%).

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2001.02a
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• pp.29-48
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• 2001

일반적인 폐수처리 시 여러 광물들이 사용되는 데 예를 들면, 수산화칼슘 및 탄산나트륨은 중화제, 점토는 응집제, 알룸(alum) 및 염화철은 인 제거제로 사용되고 있다. 산성광산배수인 경우에는 알칼리성의 중화제로 석회 (CaO), 석회석 (CaCO$_3$), 가성소다 (NaOH), 탄산나트륨 (NaCO$_3$) 등이 사용된다. 그러나, 설비비 및 유지비가 많이 들어 몇 십년 동안 계속해서 침출되는 산성광산배수를 처리하기에는 문제가 있다. 산성광산배수 (Acid Mine Drainage, AMD)는 pH가 6.0 미만이고 총산도 (totalacidity)가 총알카리도 (total alkalinity)를 초과하는 물로서 노천광이 가행되었던 지역, 가행중이거나 휴광 또는 폐광된 광산에서 유출된다. 또한 도로사면 절개부나 지하철 터널에서도 황철석(pyrite)이나 백철석 (marcasite)을 함유하는 층이 공기 중에 노출되면 산성수가 침출되어 나오기도 한다. 산성광산배수에 의한 하천수의 오염이 매우 극심하여 때로는 미생물마저도 그 속에 살 수 없게 된다. 산성광산배수에 의해 오염된 하천수의 오염범위는 산성수의 양, 농도, 하천에 유입되는 산성수의 분포, 상류에서 흘러드는 오염되지 않은 물의 양, 지류에서 유입되는 물의 양에 따라 좌우된다. 산성광산배수 오염이 문제시되고 있는 나라는 미국을 포함하여 호주, 일본, 한국, 러시아, 남아연방 등이다. 산성광산배수는 환원환경에서 생성된 석탄층 및 접촉교대 또는 열수에 의해 생성된 금속광이 공기 및 물에 노출되어 생성되는 자연적인 현상이다. 그러나 국지적인 지역에서 인간이 이 광상들을 환경영향을 고려하지 않고 대규모로 개발할 때 인간 생활에 심각한 영향을 미치는 것이다. 광산산성배수를 처리하기 위해 상기와 같이 여러 기술이 도입 적용되었으며 일부 기술들은 현재도 사용되고 있다. 각 기술마다 일장일단이 있으므로 경비의 과다, 유지 및 관리에 대한 지속성 여부, 공간의 확보 여부, 지역적 특수성에 맞춰 가장 적합한 방법을 채택하여야 하며 꾸준히 채택한 기술의 개량 및 새로운 기술의 첨가가 요구되고 있다. 따라서, 산성광산배수 오염지대에 대해 획일적으로 같은 처리방법을 채택하여 사용하는 것보다 각 지역 또는 광산산성폐수가 유출되어 나오는 광산폐기물의 특성 등을 고려하여 거기에 맞는 기술들을 복합적으로 또는 단독으로 사용하되 처리방법 채택 시 신중을 기할 것이 요망된다.

• Journal of the Korea institute for structural maintenance and inspection
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• v.9 no.3
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• pp.120-128
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• 2005

In the construction industry, due to the cost rise of raw material for concrete, we have looked into recycling by-products which came from foundry. When using the Ground Granulated Blast-Furnace Slag(SG), it is good for enhancing the qualities of concrete such as reducing hydration heat, increasing fluidity, long-term strength and durability, but it has some problems : construction time is increased or the rotation rate of form is decreased due to low development of early strength. In this study, therefore, to enhance the early strength of SG mortar, we used some alkali activators(KOH, NaOH, $Na_2CO_3$, $Na_2SO_4$, water glass, $Ca(OH)_2$, alum. This paper deals with reacted products, setting time, heat evolution rate, flow and the strength development of SG cement mortar activated by alkali activators. From the results, if alkali activators were selected and added properly, SG is good for using as the materials of mortar and concrete.

• Journal of Korean Society of Environmental Engineers
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• v.32 no.12
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• pp.1087-1093
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• 2010

Autotrophic denitrification is known as an effective and economical alternative for heterotrophic denitrification using external carbon sources such as methanol. In this study, we evaluated design and operation parameters for a sulfur denitrification reactor (SDR) treating high strength nitrogen wastewater. The SDR was filled with spherical sulfur media in connected to a pilot-scale nutrient removal process (daily flow rate, $Q=18\;m^3/d$) using moving spongy media. Total nitrogen (TN) concentration of the final effluent was below the 7.0 mg TN/L because nitrate was additionally removed through autotrophic denitrificationin without adding alkalinity (initial alkalinity was $169.4{\pm}20.8\;mg$ $CaCO_3$/L). During the test period, 60~80% of nitrogen in the influent was removed even in low temperature (below $15^{\circ}C$). The alkalinity consumption for nitrate removal in SDR was $4.09{\pm}1.29$ g $CaCO_3/g$ ${NO_3}^-$-N, and the residual alkalinity of influent of SDR was higher than that of theoretical requirements for full conversion of nitrate. The consumption of sulfur was 943.8 g S/d and it was 2.4 times higher than theoretical value (400.1 g S/d) due to abrasion and loss of sulfur media in backwash, etc.