• Journal of IKEEE
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• v.7 no.1 s.12
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• pp.9-15
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• 2003

An optimized finite-field multiplier is proposed for encryption and error correction devices. It is based on a modified Linear Feedback Shift Register (LFSR) which has lower power consumption and smaller area than prior LFSR-based finite-field multipliers. The proposed finite field multiplier for GF(2n) multiplies two n-bit polynomials using polynomial basis to produce $z(x)=a(x)^*b(x)$ mod p(x), where p(x) is a irreducible polynomial for the Galois Field. The LFSR based on a serial multiplication structure has less complex circuits than array structures and hybrid structures. It is efficient to use the LFSR structure for systems with limited area and power consumption. The prior finite-field multipliers need 3${\cdot}$m flip-flops for multiplication of m-bit polynomials. Consequently, they need 6${\cdot}$m latches because one flip-flop consists of two latches. The proposed finite-field multiplier requires only 4${\cdot}$m latches for m-bit multiplication, which results in 1/3 smaller area than the prior finite-field multipliers. As a result, it can be used effectively in encryption and error correction devices with low-power consumption and small area.

• Journal of Bio-Environment Control
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• v.12 no.3
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• pp.107-113
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• 2003

This study was carried out to improve the performance of pre-developed heat recovery devices attached to exhaust-gas flue connected to combustion chamber of greenhouse heating system. Four different units were compared in the aspect of heat recovery performance; A-, B-, and C-types are exactly the same with the old ones reported in previous studies. D-type newly developed in this experiment is mainly different with the old ones in its heat exchange area and tube thickness. But airflow direction(U-turn) and pipe arrangement are similar with previous three types. The results are summarized as follows; 1. System performances in the aspect of heat recovery efficiency were estimated as 42.2% for A-type, 40.6% for B-type, 54.4% for C-type, and 69.2% for D-type. 2. There was not significant improvement of heat recovering efficiency between two different airflow directions inside the heat exchange system. But considering current technical conditions, straight air flow pattern has more advantage than hair-pin How pattern (U-turn f1ow). 3. The main factors influencing on heat recovery efficiency were presumably verified to be the total area of heat exchange surface, the thickness of ail-flow pipes, and the convective heat transfer coefficient influenced by airflow velocity under the conditions of allowable pipe durability and safety. 4. Desirable blower capacity for each type of heat recovery units were significantly different to each other. Therefore, the optimum airflow capacity should be determined by considering in economic aspect of electricity required together with the optimum heat recovery performance of given heat recovery systems.

• Proceedings of the Korea Institute of Fire Science and Engineering Conference
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• 2011.04a
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• pp.393-396
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• 2011

설치의 법적규제가 없는 수배전반용 개별식 자동소화장치의 경우, 소화약제량 산정시 설계자마다 체적당 소요가스량, 개구부 면적, 개구면적당 가산량을 다르게 적용하여 같은 크기의 panel 인데도 소화약제량이 다르게 산정되는 경우가 있다. 따라서, 본 논문에서는 수배전반 및 전동기 기동반용 개별식 자동소화장치를 위한 청정소화약제량(HFC-227ea)을 산정하기 위해 NFPA, NFSC를 비교분석하여 최적의 소화약 제량 산정식을 도출하였다.

• Proceedings of the Korean Vacuum Society Conference
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• 2012.02a
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• pp.514-514
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• 2012

면방전 구조의 대가압 DBD플라즈마 소스를 제작하여 Ar과 N2 기체를 유입하여 미생물인 Fungi의 변화를 관찰하였다. 면방전 구조의 DBD플라즈마 소스는 유리기판위에 포토리소그라피 공정으로 미소전극을 형성하여 고밀도의 방전셀을 형성하였다. 방전시 발생하는 열에 의한 효과의 제어를 위하여 냉각장치를 장착하였다. 또한 유리기판과 포토리소그라피 공정은 방전영역에 제한없이 다양한 크기의 소스제작이 가능하다. 셀 피치가 $400{\mu}m$이며 $cm^2$ 당 200여개의 방전 셀로 구성되어 있어서 기존 메쉬타입의 DBD플라즈마 장치에 비해 균일하게 플라즈마를 조사할 수 있으며 플라즈마 제트 장치에 비해서는 넓은 면적을 동시에 조사할 수 있게 되었다. Ar 과 N2기체를 3 L/min의 유량으로 방전공간에 유입하면서 1 kV의 구동전압으로 플라즈마를 발생하였다. 이 경우 플라즈마의 조사시간을 20 s, 40 s, 60 s 간격으로 변화를 주며 Fungi의 변화를 관찰하였다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.34 no.1
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• pp.27-34
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• 2010

In a test duct with closed configuration, particle removal performance of an edge-plate type electrostatic precipitator (ESP) was evaluated at a high flow rate in $CO_2$ rich environments by changing gap distances between collection plates, concentrations of $CO_2$, particle sizes, types of electrodes, and types of power supplies. At the same experimental conditions, collection efficiency of particles with the mean particle size, 300 nm, decreased as the gap distance and $CO_2$ concentration increased because of low electrostatic force and low discharged current. In addition, as the particle size increased, the efficiency increased because of high charging rate of the large particles. With the electrode type which has higher surface area of a discharging plate and with the power supply which applied 25 kHz-pulsed DC voltages, the removal efficiency was high even in rich $CO_2$ condition due to high electrostatic force at the same power consumption.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.17 no.3
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• pp.699-707
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• 2016

This paper proposes a low-complexity central processing unit (CPU) that is suitable for deeply embedded systems, including Internet of things (IoT) applications. The core features a 16-bit instruction set architecture (ISA) that leads to high code density, as well as a multicycle architecture with a counter-based control unit and adder sharing that lead to a small hardware area. A co-processor, instruction cache, AMBA bus, internal SRAM, external memory, on-chip debugger (OCD), and peripheral I/Os are placed around the core to make a system-on-a-chip (SoC) platform. This platform is based on a modified Harvard architecture to facilitate memory access by reducing the number of access clock cycles. The SoC platform and CPU were simulated and verified at the C and the assembly levels, and FPGA prototyping with integrated logic analysis was carried out. The CPU was synthesized at the ASIC front-end gate netlist level using a $0.18{\mu}m$ digital CMOS technology with 1.8V supply, resulting in a gate count of merely 7700 at a 50MHz clock speed. The SoC platform was embedded in an FPGA on a miniature board and applied to deeply embedded IoT applications.

• Journal of Energy Engineering
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• v.13 no.4
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• pp.311-318
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• 2004

In the present study, the combustion characteristics of methane and hydrogen-supplemented methane as alternative fuels for automotive vehicles were investigated at various hydrogen substitution rate, ignition position and ignition methods in a CVCC. The main results obtained from the study can be summarized as follow. In case of center ignition and neat methane-air mixture, the flame propagation processes are propagated with an elliptical shape, but they are changed an instable elliptical shape flame with very regular cells and higher velocity by increasing the hydrogen supplement rate. In case of side, 0.5R ignition and neat methane-air mixture, the flame propagation processes are propagated with an instable elliptical shape flame, but they are changed from an instable elliptical shape to wedge shape flame with very irregular cells and higher velocity by increasing the hydrogen supplement rate. Although the flame propagation shape with ignition position and ignition devices was not differ, the flame area of MSCDI device was a little larger than it of CDI device at the same time.

• Proceedings of the Korea Water Resources Association Conference
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• 2021.06a
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• pp.123-123
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• 2021

도시하천유역이나 복합유역 등 지역적 성향을 고려한 도달시간 산정에 관한 연구는 현재까지도 미흡한 실정이다. 소규모 유역의 홍수량을 산정할 경우 유하시간보다 유입시간 비중이 상대적으로 크다. 그러나 유하시간만을 고려하여 도달시간을 산정할 때, 소규모 유역의 경우 하도가 없고 유역면적이 5km² 내외 또는 하도의 저류 효과를 기대할 수 없는 경우 도달시간이 짧아 홍수량이 과대 산정된다. 이를 극복하고자 재해영향성평가등의 협의 실무지침에서는 도달시간 이외에 매개변수인 저류상수를 인위적으로 증가시키는 방법을 제안하고 있다. 하지만 이 방법 역시 유역의 물리적인 특성을 나타내는 변수를 왜곡한다는 근복적인 문제를 완전히 해결하지 못하였다. 이에 본 연구에서는 기존 중·대규모 하천을 대상으로 수행된 연구결과를 바탕으로 제안된 홍수 도달시간 산정방법의 한계를 극복하고, 유입시간이 지배적인 소규모 복합유역에 적용 가능한 도달시간 산정방안을 제시하고자 한다. 이를 위해 실증실험을 통해 기존 유입시간 산정식을 개선하고, 도시수문 모니터링 시범유역에 적용하여 정확성을 평가하고자 하였다. 먼저, 홍수도달 시간 측정을 위한 강우유출 실내 실험장치를 제작하였다. 실험장치는 본체(길이3m×폭1.2m×높이0.8m)와 경사조절 장치(0~15도)를 포함하고 있다. 본체 전면부를 타공(ø10mm)하고 상·하단에서 지표와 기저유출을 집수하여 티핑버킷으로 유량을 측정하였고, 토체 내에는 토양수분센서를 설치하여 강우유출 발생시간 동안 토양수분 변화를 측정하였다. 본 연구에서는 하도흐름인 유하시간(Kraven 공식)을 계산하여 도달시간을 산정하기 보다 지표면 흐름인 유입시간(Kerby 공식)에 보정계수를 도입하여 도달시간을 산정하는 방안을 검토하였다. 실험 결과, 불투수 면적비율이 증가함에 따라 도달시간은 감소하고, 불투수 유역이 하류에 위치할수록 유출발생시간이 빨라졌다. 실증실험 결과를 바탕으로 도시수문 모니터링 시범유역에 적용하여 기존 유하시간과 저류상수를 보정하는 도달시간 산정방식(연속형 Kraven)과 유입시간을 보정한 도달시간 산정(수정 Kerby)으로 도출된 유출량을 실측 유량과 비교하였다. 그 결과 제안된 홍수도달시간 산정식에서 모의된 홍수량이 기존 방식과 유사하거나 우수한 첨두홍수량을 보였으며, 설계자 임의성이 배제된 일관성있는 해석값을 제시해 줄 것으로 판단된다.

• Resources Recycling
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• v.9 no.3
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• pp.13-21
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• 2000

This study describes to analyze the heat transfer characteristics of waste solvent recovery system using a double pipe heat exchanger heating solvent by the hot oil. The solvent recovery system consists of the feeding pump, the double pipe heat exchanger, the vacuum spray chamber, and the condenser. A double pipe heat exchanger consists of the first section to conduct the heating of solvent to the thermal saturated point and the second section to evaporate the saturated solvent. The heat transfer area for vaporization of water, benzene and alkylbenzene was predicted by the heat balance modelling and experimentally measured from the temperature distribution as a function of solvent flow rate and heating temperature. The required heat transfer area for vaporization was increased with increasing solvent flow rates and with decreasing heating temperatures due to decreased quantity of transferred heat per the unit area. Theoretical modelling of the heat transfer area for solvents vaporization in the pipe showed good agreement with experimental results. Results showed to be suitable for the waste solvent recovery using a double pipe heat exchanger.

• Proceedings of the Korean Institute of Navigation and Port Research Conference
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• 2004.11a
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• pp.183-188
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• 2004

This paper presents a method for designing layout on the yard and evaluating alternative designs of the layout by applying simulation. The design method is based on the concepts of the conventional port container terminal with yard layout, In general, yard design of the container terminal is consists of the two major parts. One is to divide yard area between the number of sections and the number of runs and the other is to decide the number of equipment that is the yard truck and yard crane. In the past days, this design was depended on the experience of the terminal operator and the reproduction of the conventional terminal layout because it is a very complex decision problem. In this paper, we suggest the method of yard design as a conceptual procedure and estimate the efficiency of the container crane and the optimal number of equipment using simulation. In the experiment results, the number of sections and runs on yard area, the number of yard truck per container crane and the number of yard crane per run are decided. In addition, the traffic flow among blocks on yard layout is estimated in terms of rate.