• Title/Summary/Keyword: Waste Oyster Shell

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Characteristics of Melting Slag Using Sewage Sludge by Inorganic Additives (무기성 폐기물 첨가제 혼합에 따른 하수슬러지의 용융특성)

  • Bae, Jung-Suk;Lee, Sang-Won;Cha, Jae-Hwan;Kim, Hyo-Su;Kim, Chang-Won
    • Journal of Korean Society of Environmental Engineers
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    • v.30 no.11
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    • pp.1116-1122
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    • 2008
  • The existing technology which is for recycling aggregate using dried swage sludge have been limited for practical application, because the properties of aggregate are not regular and don't meet the recycling aggregate standard. In this research, an innovative slag-producing technology is developed by addition of oyster shell, waste cast-sand and iron-rust as inorganic waste additives. The mixed slag with the additives was evaluated at the various ratio of CaO/SiO$_2$, SiO$_2$/Al$_2$O$_3$ and Fe$_2$O$_3$/SiO$_2$. When the waste sludge was melted at 1,400$^{\circ}C$ during 20 minutes, the optimal ratio of CaO/SiO$_2$ for the slag added the oyster shell, SiO$_2$/Al$_2$O$_3$ for added the waste cast-sand and Fe$_2$O$_3$/SiO$_2$ for added the iron-rust were 1.00, 3.00 and 0.60, respectively. At the optimal condition, the bulk density of the slag was 2.24 g/cm$^3$, 2.45 g/cm$^3$ and 2.73 g/cm$^3$, And the 24 h water adsorption was 4.72%, 1.44% and 0.37%, respectively. Therefore it is proved that adding the waste additives to the process of the slag production contributed for elevation of recycling aggregate properties. And also it is expected that production cost can be reduced by decreased melting temperature.

The Effects of Calcium-type Catalysts on the Pyrolysis Reaction of Raw Material Resin for Producing from Waste Vinyl to Fuel-oil (폐 농업용 비닐 수지에서 연료유 생성을 위한 원료 수지의 열분해반응에서 칼슘계 촉매의 영향)

  • Bak, Young-Cheol;Choi, Joo-Hong;Cho, Tae-Ho
    • Journal of Energy Engineering
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    • v.17 no.1
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    • pp.8-14
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    • 2008
  • The effects of calcium type catalysts addition on the thermal decomposition of low density polyethylene (LDPE) and ethylene vinyl acetate (EVA) resin have been studied in a thermal analyze. (TGA, DSC) and a small batch reactor. The calcium type catalysts tested were calcinated dolomite, lime, and calcinated oyster shell. As the results of TGA experiments, pyrolysis starting temperature for LDPE varied in the range of $330{\sim}360^{\circ}C$ according to heating rate, but EVA resin had the 1st pyrolysis temperature range of $300{\sim}400^{\circ}C$ and the 2nd pyrolysis temperature range of $425{\sim}525^{\circ}C$. The calcinated dolomite enhanced the pyrolysis rate in LDPE pyrolysis reaction, while the calcium type catalysts reduced the pyrolysis rate in EVA pyrolysis reaction. In the DSC experiments, addition of calcium type catalysts reduced the melting point, but did not affect to the heat of fusin. Calcinated dolomite reduced 20% of the heat of pyrolysis reaction. In the batch system experiments, the mixing of calcinated dolomite and lime enhanced the yield of fuel oil, but did not affect to the distribution of carbon numbers.

Investigation of Waste Shell Fine Aggregates on the Material Characteristics of Cement Mortars (패각 잔골재가 시멘트 모르타르 재료 특성에 미치는 영향 분석)

  • Oh, Seo-Eun;Choi, Seung-Ha;Kim, Kyuwon;Han, Soo-Ho;Chung, Sang-Yeop
    • KSCE Journal of Civil and Environmental Engineering Research
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    • v.44 no.1
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    • pp.33-39
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    • 2024
  • This study explores the utilization of common marine wastes, specifically seashells, such as oysters and cockles, as alternative fine aggregates in construction materials. The considered seashells were cleaned and pre-processed for use as a substitute for aggregate in mortar. Cement mortar specimens were prepared under different conditions, such as substitution ratios and the cleaning status of the seashells. The compressive strength of the mortars specimens was evaluated, and the solid and porous structures of each specimen were analyzed using microstructure analysis methods such as XRD, SEM, and micro-CT. The results confirmed that oyster and cockle seashells are composed of different calcium carbonate polymorphs, and their microstructural characteristics influence the mechanical properties of the cement mortar specimens.

Nitrogen Removal from Synthetic Domestic Wastewater Using the Soil Column (토양컬럼을 이용한 합성하수 중의 질소제거)

  • Cheong, Kyung-Hoon;Lim, Byung-Gab;Choi, Hyung-Il;Park, Sang-Ill;Moon, Ok-Ran
    • Journal of Environmental Science International
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    • v.16 no.6
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    • pp.707-714
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    • 2007
  • A laboratory experiment was performed to investigate nitrogen removal by the soil column. The addition of 20% waste oyster shell to the soil accelerated nitrification in soil column. The $NO_3^--N$ concentration in the effluent decreased with the decrease of HRT(Hydraulic Retention Time). When methanol and glucose added as carbon sources, the average removal rates of T-N(Total Nitrogen) were 82% and 77.9%, respectively. The $NO_3^--N$ removal by methanol supplementation in soil column can likely be attributed to denitrification. In continuous removal of nitrogen using the soil column, the COD(Chemical Oxygen Demand) and $NH_4^+-N$ removed simultaneously in organic matter decomposing column. The greater part of $NH_4^+-N$ was nitrified by the percolated through nitrification column, and the little $NH_4^+-N$ was found in the effluent. The T-N of 87.4% removed at HRT of 36 hrs in denitrfication column. Because of nitrified effluents from nitrification column are low in carbonaceous matter, an external source of carbon is required.

Synthesis of Pure and Porous CaO·Al2O3 Clinker by Burning of Hydrates (수화물 소성에 의한 고순도 다공성 CaO·Al2O3 클링커의 합성)

  • Kim, Du-Hyouk;Song, Tae-Woong
    • Journal of the Korean Ceramic Society
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    • v.47 no.5
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    • pp.401-406
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    • 2010
  • For the lower-temperature preparation of calcium monoaluminate(CA, C:CaO, A:$Al_2O_3$) clinker which is hard to synthesize purely within its melting point, an equimolar hydrate was obtained and then used as a starting raw material of clinker burning. The hydrate was prepared from a mixture of waste oyster shell and industrial aluminium hydroxide by heating to $1200^{\circ}C$, grinding and mixing with water. The hydrate was composed of amorphous aluminium hydroxide and $C_3AH_6$(H:$H_2O$) formed by resolution-precipitation mechanism of the system C-A-H. By heating the hydrate, nearly pure and porous calcium monoaluminate clinker was formed at $1400^{\circ}C$ which is fairly lower temperature than that of its melting point. The formation of calcium monoaluminate was performed mainly by the reaction between amorphous alumina and $C_{12}A_7$ caused by the decomposition of $C_3AH_6$. The immediate and earlier formation of $C_{12}A_7$ seemed to be accelerated by not only high surface area and instability of the thermally decomposed hydrate but also the catalytic effect of water decomposed from the hydrate. The final calcium monoaluminate clinker was very porous because of the influence of highly porous shape of the thermally decomposed hydrate.

A Short Composting Method by the Single Phase Composter for the Production of Oyster Mushroom (느타리버섯 배지 제조기를 이용한 배지의 제조 연구)

  • Lee, Ho-Yong;Shin, Chang-Yup;Lee, Young-Keun;Chang, Hwa-Hyoung;Min, Bong-Hee
    • The Korean Journal of Mycology
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    • v.27 no.1 s.88
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    • pp.10-14
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    • 1999
  • A single phase composter was constructed by modifying the conventional mixer of sawdust for the cultivation of oyster mushroom Pleurotus ostreatus. The machine was designed on the basis of 3-phase-1 system which was controlled in prewetting, pasteurization and fermentation processes. In composting 200 kg of straw and cotton waste in the machine, it took 20 minutes in prewetting step and also to hours at $65^{\circ}C$ in pasteurization process. Postfermentation by aerothermophiles was completed by treating the compost at $45^{\circ}C-50^{\circ}C$ for 48 hours which was shorten 24 hours from the conventional method. In the postfermentation at high temperature, forced aeration and/or vigorous mixing process(es) played a great role in the improvement of spawn quality. The growth of mycelium of oyster mushroom was excellent in the culture combinated with 3 parts of surface inoculation and 7 parts of mechanical mixing.

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