• Journal of Electrical Engineering and Technology
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• 제10권4호
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• pp.1432-1440
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• 2015

A dynamic economic dispatch and control method is proposed to minimize the overall generating cost for a stand-alone microgrid in DongAo Island, which is integrated with wind turbine generator, solar PV, diesel generator, battery storage, the seawater desalination system and the conventional loads. A new dispatching strategy is presented based on the ranking of component generation costs and two different control modes, in which diesel generator and battery storage alternate to act as the master power source to follow system power fluctuation. The optimal models and GA-based optimization process are given to minimize the overall system generating cost subject to the corresponding constraints and the proposed dispatch strategy. The effectiveness of the proposed method is verified in the stand-alone microgrid in DongAo Island, and the results provide a feasible theoretical and technical basis for optimal energy management and operation control of stand-alone microgrid.

• Membrane and Water Treatment
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• 제3권3호
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• pp.201-209
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• 2012

Membrane separation technologies have some of advantages are considered a better alternative to traditional methods. Research of novel membranes is very vital for covering the higher required of membrane in several purposes like water desalting technology. In this work polyamide-6/cellulose acetate (PA-6/CA) blend membrane was developed according to the wet phase inversion system. The structures of the prepared membranes were examined by scanning electron microscopy (SEM). SEM images showed uniform particles distribution in the prepared membranes. Moreover, SEM images revealed that the membranes have relatively uniform surface (PA-6/CA). PA-6/CA blend membranes systems are evaluated by using synthetic NaCl solution. The separation performance showed that salt rejection increased with increasing of heat treatment of the casted films and it was improved with increasing of operating pressure.

• Environmental Engineering Research
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• 제24권2호
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• pp.347-353
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• 2019

Although membrane distillation (MD) has great promise for desalination of saline water sources, it is crucial to improve its thermal efficiency to reduce the operating cost. Accordingly, this study intended to examine the thermal energy efficiency of MD modules in a pilot scale system. Two different modules of hollow fiber membranes were compared in direct contact MD mode. One of them was made of polypropylene with the effective membrane area of $2.6m^2$ and the other was made of polyvinylidene fluoride with the effective membrane area of $7.6m^2$. The influence of operation parameters, including the temperatures of feed and distillate, feed flow rate, and distillate flow rate on the flux, recovery, and performance ratio (PR), was investigated. Results showed that the two MD membranes showed different flux and PR values even under similar conditions. Moreover, both flow rate and temperature difference between feed and distillate significantly affect the PR values. These results suggest that the operating conditions for MD should be determined by considering the module properties.

• 멤브레인
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• 제28권1호
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• pp.75-82
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• 2018

정삼투법을 이용한 해수담수화는 역삼투 공정에 비해 에너지 절감이 가능하여 해수담수화 차세대 기술로 주목받고 있다. 막을 기반으로 하는 수처리 분야에서 분리 성능을 향상시키고 새로운 기능을 부여하기 위해, 고분자 매트릭스에 필러인 나노물질을 삽입하는 박막 나노복합체 분리막(thin film nanocomposite, TFN) 개발에 대한 연구가 요구되고 있다. 본 연구에서는 딥 코팅(dip coating) 방법을 기반으로 한 다층박막적층법(Layer-by-layer, LBL)을 이용하여 산화그래핀(graphene oxide, GO)의 나노 적층구조를 제어하여, 정삼투 공정에서의 높은 안정성 및 높은 수투과도 및 염 제거, 낮은 염 역확산을 갖는 그래핀 나노복합체 분리막을 개발하고자 하였다. 정삼투 공정의 성능 향상을 위한 산화그래핀의 환원 반응시간과 LBL 딥코팅 적층 수의 최적화를 통해, 수투과도 2.51 LMH/bar, 물분자 선택성 8.3 L/g, 염 제거율 99.5%를 갖는 나노복합체 분리막을 개발하였다. 이는 상용화된 CTA FO 분리막보다 수투과도는 10배, 물분자 선택성은 4배 높게 향상되었으며, 염 제거율은 비슷한 수준으로 나타났다.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2007년도 하계학술발표대회 논문집
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• pp.59-59
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• 2007

• Journal of Advanced Marine Engineering and Technology
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• 제41권3호
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• pp.182-190
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• 2017

모든 액체는 소량의 기체성분들이 녹아있으며, 액체에 용해되는 기체의 양은 액체에 작용하는 주위압력에 기여하는 각 기체성분의 분압에 비례한다는 헨리의 법칙을 따른다. 따라서 다단증발식 해수담수화설비의 경우, 각 증발단의 운전온도와 압력은 다르며, 이 운전조건에 비례하여 해수에 용해되어 있던 기체들이 증발과정에서 방출되는데 주성분은 불응축기체인 이산화탄소, 질소, 산소 및 아르곤이다. 대류열전달의 입장에서는 불응축기체는 증발증기를 응축시키는 냉각기의 성능을 저하시키는 주요한 원인이기 때문에 증발과정에서 방출되는 불응축기체의 평가는 증발식 해수담수화설비에서 중요한 설계인자 중의 한가지이다. 증발식 해수담수화공정의 경우, 대부분의 증발기는 진공압력으로 유지되기 때문에 진공유지장치의 설계를 위해서는 증발과정에서 해수로부터 방출되는 불응축기체의 방출량을 평가하는 것이 매우 중요다. 본 연구는 불응축기체의 방출량을 정량적으로 계산하기 위해 수행하였으며, 연구결과에 따르면 불응축가스의 방출량은 후단으로 갈수록 감소하며, 담수생산량에 비례함을 알 수 있었다.

• 유체기계공업학회:학술대회논문집
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• 유체기계공업학회 2003년도 유체기계 연구개발 발표회 논문집
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• pp.482-486
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• 2003

A high-efficiency turbo steam compressor has been successfully developed for the MVR desalination system, first one in Korea. The state-of-the-art design methods using real gas properties were applied to get all the aerodynamic design results. Bull and pinion gear trains, tilting-pad bearings and investment cast impellers were developed also to be integrated into the integral gear-driven turbo steam compressor. System tests show highly efficient performance.

• Membrane and Water Treatment
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• 제8권3호
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• pp.279-292
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• 2017

This study was aimed at ultrafiltration (UF) as a pretreatment before reverse osmosis (RO) within the scheme of hybrid reverse osmosis-multistage flush (RO-MSF) desalination. Seawater at elevated temperature (after MSF heat-exchangers) was used as a feed in this process. The pretreatment system was represented as a set of functionally-linked technological segments such as: UF filtration, backwashing, chemical- enhanced backwashing, cleaning, waste disposal, etc. The process represents the sequences of operating cycles. The cycle, in turn, consists of the following unit operations: filtration, backwashing and chemical-enhanced backwashing (CEB). Quantitative assessment was based on the following indicators: normalized permeability, transmembrane pressure, specific energy and water consumption, specific waste generation. UF pre-treatment is accompanied by the following waste streams: $W1=1.19{\times}10$ power of $-2m^3$ (disposed NaOCl with 0.0044% wt.)/$m^3$ (filtrate); $W2=5.95{\times}10$ power of $-3m^3$ (disposed $H_2SO_4$ with 0.052% wt.)/$m^3$(filtrate); $W3=7.26{\times}10$ power of $-2m^3$ (disposed sea water)/$m^3$ (filtrate). Specific energy consumption is $1.11{\times}10$ power of $-1kWh/m^3$ (filtrate). The indicators evaluated over the cycles with conventional (non-chemical) backwashing were compared with the cycles accompanied by CEB. A positive impact of CEB on performance indicators was demonstrated namely: normalized UF resistance remains unchanged within the regime accompanied by CEB, whereas the lack of CEB results in 30% of its growth. Those quantitative indicators can be incorporated into the target function for solving different optimization problems. They can be used in the software for optimisation of operating regimes or in the synthesis of optimal flow- diagram. The cycle characteristics, process parameters and water quality data are attached.

• 상하수도학회지
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• 제30권3호
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• pp.271-278
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• 2016

Recently, reverse osmosis (RO) is the most common process for seawater desalination. A common problem in both RO and thermal processes is the high energy requirements for seawater desalination. The one energy saving method when utilizing the osmotic power is utilizing pressure retarded osmosis (PRO) process. The PRO process can be used to operate hydro turbines for electrical power production or can be used directly to supplement the energy required for RO desalination system. This study was carried out to evaluate the performance of both single-stage PRO process and two-stage PRO process using RO concentrate for a draw solution and RO permeate for a feed solution. The major results, were found that increase of the draw and feed solution flowrate lead to increase of the production of power density and water permeate. Also, comparison between CDCF and CDDF configuration showed that the CDDF was better than CDCF for stable operation of PRO process. In addition, power density of two-stage PRO was lower than the one of single-stage. However, net power of two-stage PRO was higher than the one of single-stage PRO.

• 한국태양에너지학회 논문집
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• 제34권2호
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• pp.73-81
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• 2014

Ocean thermal energy conversion(OTEC) is a power generation method that utilizes temperature difference between the warm surface seawater and cold deep sea water of ocean. As potential sources of clean-energy supply, Ocean thermal energy conversion(OTEC) power plants' viability has been investigated. Therefore, this paper evaluated the thermodynamic performance of solar-OTEC convergence system for the production with electric power and desalinated water. The comparison analysis of solar-OTEC convergence system performance was carried out as the fluid temperature, saturated temperature difference and pressure of flash evaporator under equivalent conditions. As a results, maximum system efficiency, electric power and fresh water output show at 40, 10, 2.5 kPa of the flash evaporator pressure, respectively. And their respective enhancement ratios were approximately 6.1, 18, 8.6 times higher than that of the base open OTEC system. Also, performance of solar-OTEC system is the highest in the flash evaporator pressure of 10 kPa.