• 한국버섯학회지
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• 제13권3호
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• pp.250-255
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• 2015

버섯 수확 후 배지의 수도용상토의 부재료로써 활용가능성을 확인한 결과 버섯 수확 후 배지는 유기물함량이 60.72%이었으며 질소-인산-칼륨이 1.39-0.89-0.81%의 화학적 특성을 확인할 수 있었다. 버섯 수확 후 배지의 안정화과정에서는 온도는 20일 경과시점에서 pH의 상승과 온도하강이 이루어졌으며 발아지수도 77로 확인되어 버섯 수확 후 배지를 수도용 상토의 재료로 활용 시에는 20일 이상의 안정화과정이 필요할 것으로 조사되었다. 벼 종자의 발아특성에서는 일반적인 수도용상토 재료로 제조된 대조구와 비교시에 버섯 수확 후 배지가 10% 이내로 혼합된 실험구들이 발아율은 82%이상이었으며 평균 발아일수와 발아세에도 통계적 유의차가 없거나 대조구보다 양호한 수준으로 확인되었다. 초기생육에서도 버섯 수확 후 배지가 10% 이내로 혼합된 처리구의 지상부건물중과 묘소질이 대조구보다 높은 것으로 확인되어 버섯 수확 후 배지는 수도용상토의 재료로서 활용가능성이 높을 것으로 판단되었다.

• 플랜트 저널
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• 제6권2호
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• pp.70-77
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• 2010

This study investigated the characteristics of co-combustion of mixed anthracite (domestic and Vietnam) and bituminous coal (Sonoma, Australia) at circulating fluidized bed boiler in Donghae thermal power plant when mixing ratio of bituminous coal is variable. Co-combustion of bituminous coal contributes to improvement in general combustion characteristics such as moderately retaining temperature of furnace and recycle loop, reducing unburned carbon powder, and reducing discharge concentration of NOx and limestone supply owing to improvement in anthracite combustibility as the mixing ratio was increased. However, bed materials were needed to be added externally when the mixing ratio exceeded 40% because of reduction in generating bed materials based on reduction in ash production. When co-combustion was conducted in the section of 40 to 60% in the mixing ratio while the supplied particles of bituminous coal was increased from 6 mm to 10 mm, continuous operation was shown to be possible with upper differential pressure of 100 mmH2O (0.98 kPa) and more without addition of bed materials for the co-combustion of mixed anthracite and bituminous coal (to 50% or less of the ratio) and that of domestic coal and bituminous coal (to 60% of the ratio).

• 식물병연구
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• 제24권4호
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• pp.257-264
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• 2018

딸기 수경재배시스템은 국내에서 매년 증가추세에 있다. 대부분의 딸기농가는 수경재배에서 베드를 멀칭하여 9월 초순 딸기묘를 정식한다. Fusarium oxysporum f. sp. fragariae에 의한 시들음병과 점박이응애 Tetranychus urticae는 정식 후 높은 온도조건에서 발생이 증가하는 경향이 있다. 따라서 베드 녹색 polyethylene(PE)필름 멀칭과 무멀칭처리에서 시들음병과 점박이응애 발생을 비교하기 위해 시험을 실시하였다. 녹색 PE필름 멀칭처리에서 시들음병 발생은 10월 초순부터 시작되었고 무멀칭처리보다 더 증가하였다. 녹색 PE피름 멀칭 처리는 점박이응애의 피해율이 무멀칭처리보다 높았다. 녹색 PE필름 멀칭처리의 상토내 온도는 무멀칭처리보다 증가했지만 대기내 상대습도는 감소하였다. 이런 결과로 딸기 수경재배에서 베드의 무멀칭처리는 시들음병과 점박이응애 발생을 낮추는 효과가 있다고 판단된다.

• 대한전기학회:학술대회논문집
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• 대한전기학회 1998년도 하계학술대회 논문집 B
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• pp.722-724
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• 1998

One of the major concerns of our time is the need to use energy economically and rationally while at the same time, protecting the environment. Circulating Fluidized Bed(CFB) Boilers represent a proven, very attractive clean coal technology, with the added advantage of an unusual fuel flexibility CFB boiler is the best available compromise between cost and environment for fossil fuel power plant. This paper briefly describes CFB process and 200MW CFB boiler for Tonghae power plant. Also, discussed are differences between the control process of fluidized bed and conventional boilers, and applied control process for Tonghae power plant.

• 한국해양공학회지
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• 제17권2호
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• pp.8-13
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• 2003

Soil, ground water, and sea bed are exposed to a continuous accumulation of polluted materials, causing serious environmental damage. It has been reported that such pollution causes a massive mortality of fish stock in rivers due to the resuspension of toxic chemicals, occurring during strong wind conditions. Therefore, it becomes apparent that there is an immediate demand for the restoration treatment of polluted river bed (or sea bed) sediment layers. Pollution levels of major rivers and ports, such as Paldang, Kyungan rivers, and Masan port, are becoming of great public concern, and are posing a serious environmental threat. In particular, the pollution of the Shi-hwa river has become a nation wide issue for the last few years. In spite of such public concern, the pollution levels of such rivers or ports are worsening everyday. In this study, an environmentally sound engineering package is introduced that helps to restore the polluted river bed or sea bed sediments. This engineering package consists of a suction facility, followed by a series of mechanical, chemical, and biological treatment units. The suction facility is designed to minimize secondary pollution that occurs from the resuspension of toxic materials during suction. The sea bed cleaning engineering package is designed to be installed on the top of a floating barge. Such a combination of environmental plant and shipbuilding technology provides a cost-effective solution, minimizing the transportation between suction and treatment facilities.

• Journal of Biosystems Engineering
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• 제37권3호
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• pp.155-165
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• 2012

This study was performed to offer the data for design of the seedling bed transfer equipment to make the automation of working process in a plant factory. The seedling bed transfer equipment pushing the seedling bed with bearing wheels on the rail for interconnecting each working process by a pneumatic cylinder was made and examined. The examined transfer force to push the seedling bed with a weight of 178.9 N by the pneumatic cylinder with length of 60 cm and section area of 5 $cm^2$ was measured by experiments. The examined transfer forces was compared with theoretical ones calculated by the theoretical formula derived from dynamic system analysis according to the number of the seedling bed and pushing speed of the pneumatic cylinder head at no load. The transfer function of the equipment with the input variable as the pushing speed $V_{h0}$(m/s) and the output variable as the transfer force f(t)(N) was represented as $F(s)=(V_{h0}/k)(s+B/M)/(s(s^2+Bs/M+1/(kM))$ where M(kg), k(m/N) and B(Ns/m) are the mass of the bed, the compression coefficient of the pneumatic cylinder and the dynamic friction coefficient between the seedling bed and the rail, respectively. The examined transfer force curves and the theoretical ones were represented similar wave forms as to use the theoretical formular to design the device for the seedling bed transfer. The condition of no vibration of the transfer force curve was $kB^2>4M$. The condition of transferring the bed by the repeatable impact and vibration force according to difference of transfer distance of the pneumatic cylinder head from that of the bed was as $Ce^{-\frac{3{\pi}D}{2\omega}}<-1$, where ${\omega}=\sqrt{\frac{1}{kM}-\frac{B^2}{4M^2}}$, $C=\{\frac{\frac{B}{2M}-\frac{1}{kB}}{\omega}\}$, $D=\frac{B}{2M}$. The examined mean peak transfer force represented 4 times of the stead state transfer force. Therefore it seemed that the transfer force of the pneumatic cylinder required for design of the push device was 4Bv where v is the pushing speed.

• 상하수도학회지
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• 제26권3호
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• pp.409-421
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• 2012

Ethanolamine (ETA) is mainly used to prevent corrosion of pipe in secondary cooling system of nuclear power plant. Condensed ETA in wastewater could increase COD and T-N when it was emitted to natural water system. Compared to conventional treatments, electrochemical oxidation process using packed bed bipolar electrodes was adopted to treat COD and T-N. According to arrangement of feeder electrode, single packed bed bipolar electrode reactor and multi-paired packed bed bipolar reactor were developed and conventional zero-valent iron (ZVI) was selected as conducting bipolar electrode. Bipolar electrodes were coordinated three-dimensionally in the reactor. The experimental results showed that COD and T-N was little removed in unit system at different pH condition (pH 8 and 11) on 100V. However, in multi-paired system that applied 600V, COD was eliminated 80.85% (anode-cathode-anode, A-C-A) and 85.11% (cathode-anode-cathode, C-A-C), respectively. T-N was also removed 96.88% (A-C-A) and 90.63% (C-A-C), simultaneously. Current efficiency was estimated both single and multi-paired system. At unit bipolar packed bed reactor, current efficiency was almost zero, however in multi-paired system, current efficiency was 300~500% at A-C-A and 250~350% at C-A-C. Current efficiency was over 100% hence it was confirmed that this system is more effective than conventional electrochemical oxidation system.

• 한국자원식물학회:학술대회논문집
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• 한국자원식물학회 2002년도 제9차 국제심포지움 및 추계정기학술발표회
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• pp.8-8
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• 2002

• 한국작물학회지
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• 제13권
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• pp.77-81
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• 1973

대두의 근계에 관한 연구의 제1보로 3개품종을 상토와 모래의 2개토양에서 각시기별로 재료를 채취하여 몇 개형질에 대한 조사측정을 하고 통계처리를 한 바 그 결과를 요약하면 다음과 같다. 1. 경직경의 비대는 발육초기 1개월까지는 완만하며 8월하순이후부터 급격하여지고 모래보다 상토에서 그 비대정도가 높았다. 2. Top의 길이의 신장도 발육 1개월이후부터 급격하여지고 모래보다 상토에서 더욱 신장이 잘된다. 3. Top길이보다 Root길이가 발육초기 1개월까지는 길고 Root의 길이는 반대로 상토보다 모래에서 신장이 잘된다. 4. Top무게도 발육초기 1개월까지는 완만히 증가하고 모래보다 상토에서 무겁게 나타나나 Top길이보다 Top무게의 경우에 그 증가의 정도가 완만하다. 5. Top무게보다 Root무게는 발육초기 1개월까지는 무거우며 상토에서 모래보다 무겁게 나타난다. 6. 5개형질 상호간에는 모래, 상토, 전체에 있어서 어느것이나 높은 상관관계를 보이고 Root길이와의 관계를 보면 Top무게, Top길이, Root무게, 경직경의 순서로 높은 상관계수를 나타내었다. 7. Root무게와의 관계를 보면 경직경, Top무게, Top길이, Root길이의 순서로 상관계수가 높았다.

• Membrane and Water Treatment
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• 제11권4호
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• pp.247-255
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• 2020

Sand filter is a key unit process for particle removal in water purification treatments. Its long-standing use is due to on-site customized retrofit. Proper selection of filter media is one of the retrofit approaches to improve filter performance. This study described a series of controlled laboratory column tests and examined the effects of media property on filtration and backwash. When sand media of 0.51 mm in effective size was replaced by sand of 0.60 mm, the filter run increased up to 5 times in the given bed depth. The change of media property required an increase of backwash rate by 0.05 m/min to satisfy the requirement of bed expansion, more than 20%. When the anthracite was changed with lower effective size and uniformity coefficient, correlation with sand in the filter bed could be satisfied within the permissible error between media and bulk characteristics. Besides, this selection resulted in a well-stratified configuration of media layers after bed expansion. The column study showed that the correlation of property between the dual media had a significant effect on the filter productivity and backwash interval.