• Title/Summary/Keyword: dry-FGD

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Optimization of In-Line Dry Scrubbing FGD process using Calcium Hydroxide and Effect of Additives (소석회를 사용한 In-Line형 건식탈황공정의 최적화와 첨가제의 영향)

  • 박재만;신창섭
    • Journal of the Korean Society of Safety
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    • v.12 no.2
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    • pp.102-111
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    • 1997
  • An In-line dry scrubbing FGD process was investigated. Calcium hydroxide was entrained in flue gas and the SO$_2$ removal efficiency by humidity and additives were examined. The range of reaction temperature was $200^{\circ}C$~$500^{\circ}C$ and the concentration of $SO_2$ was around 900ppm. By the increase of humidity in flue gas, the removal efficiency was increased. The effect of NaOH as a additive was very high and got high conversion of $Ca(OH)_2$, however in case of RH 90%, it was reverse. The effect of particle size and flow rate were examined. And the reaction rate constant and effective diffusivity also calculated.

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Numerical Analysis for Improving of SOx Removal Efficiency in the DSI(Dry Sorbent Injection Technique) of FGD System(I) (배연탈황 공정 중 DSI 공법의 탈황효율 향상을 위한 전산 유체 역학적 연구(I))

  • Chung, Jin-Do;Kim, Jang-Woo;Kim, Byung-Hwan;Park, Young-Moon
    • Journal of Korean Society of Environmental Engineers
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    • v.29 no.1
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    • pp.47-53
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    • 2007
  • The aim of this study is to research applicable possibility or Dry Sorbent Injection Technique(DSI) in sox removal process using Computational Fluid Dynamics(CFD) software package. It will be applied for 500MW in capacity coal-fired thermal power plant operated by South Korea N. Power Co., Ltd. The DSI process is adapted between a preheater and an EP process in the technological assembly. The numerical analysis performs in predicting and optimizing of DSI process's characteristics, which consists of structure of duct, position of injection nozzles, injection speed, and dispersion of sorbent. Computing results are shown that degree of sorbent dispersion depends on structure of duct and position of injection nozzles strongly. The highest dispersion efficiency was obtained when we set a Lobed-plate inside the duct and 6 injection nozzles on the duct(4 injection nozzles at the corners and 2 injection nozzles on upper and under walls as a rectangle duct shape). We also know that change of injection speed of sorbent doesn't have an large effect on the sorbent dispersion but it can effect to drop pressure.

Feed Water Flow Control of Super Critical Once Through Boiler in Korea Standard Power Plant (한국표준형 초 임계압 관류형 보일러의 급수제어)

  • 김은기;장용창;조수현
    • 제어로봇시스템학회:학술대회논문집
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    • 2000.10a
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    • pp.251-251
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    • 2000
  • Tangjin Power Plant is modern Korean standard plant which is made up Once Through Super Critical Boiler, Turbin, Generator and Flue Gas Desulfarization System. INFI-90 system fur control of the 500 MW Korean standard super critical once through boiler Mark-V for Turbine, EX-2000 fer Generator, WDPF for FGD were installed in Tangiin thermal power plant. There were two BFPTs, BFPM, 25% control valve, 35% control valve to control boiler feed water flow. It is very difficult to tune the Separator Tank level control system and change the mode from Wet to Dry. This paper focuses on test results and modification control logic for feed water control system in Tangjin power plant.

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Preparation and Characterization of Porous Filters from Ca(OH)2 and CaCO3 for SO2 Removal in Dry-FGD Process (건식 FGD 공정에서 SO2 제거를 위한 Ca(OH)2 및 CaCO3 원료의 다공성 필터 제조 및 특성)

  • Han, Yo-Seop;Kim, Hyun-Jung;Park, Young-Goo;Park, Jai-Koo
    • Applied Chemistry for Engineering
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    • v.16 no.6
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    • pp.772-777
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    • 2005
  • Porous hydrated lime and limestone filters were prepared by foaming and gelcasting method, and their physical properties were evaluated. Through these analyses, it has been found that with the increased porosity and pore size of the filters, majority of pores in the filters were inter-connected by windows. Also, $SO_2$ removal efficiency for the filters was investigated. As the porosity and the reaction temperature increased, $SO_2$ removal efficiency also increased. Especially, unlike the variation of entrance concentration, the entrance flow rate had great influence on the removal efficiency. In case of the filters with an equal porosity, the hydrated lime filter had superior removal efficiency compared to the limestone filter. From these results, it was shown that the high conversion ratio to CaO from the hydrated lime filter was a result of facilitated formation of $CaSO_4$ by $SO_2$.

A Numerical Study of $SO_2$ Efficiency Improvement in the DSI process of FGD (Vortex에 의한 DSI공정 중 혼합효율 향상에 관한 연구)

  • Chung, J.D.;Kim, J.W.
    • Journal of ILASS-Korea
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    • v.14 no.1
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    • pp.1-7
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    • 2009
  • This study carried out numerical analysis of flow field of combustion gas and sorbent to test sorbent efficiency of DSI process. To provide rapid mixing for increase utilization rate of sorbent, streamwise vorticity can be introduced into the flowing streams by other means; for example, by installing vortex generators immediately downstream of the wavy trailing edge. Computing results show that the degree of sorbent dispersion depends strongly on duct structure. Highest dispersion efficiency received when vortex generator was installed inside of duct. The results presented in this study a optimum condition for the development of practical DSI process.

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Properties and Mock-up Test of Lightweight Foamed Concrete Based on Blast Furnace Slag by Crack Reducing Admixture (팽창성 균열저감제를 이용한 고로슬래그 미분말 기반 경량기포 콘크리트의 특성 및 목업실험)

  • Han, Sang-Yoon;Han, Min-Cheol
    • Journal of the Korea Institute of Building Construction
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    • v.17 no.6
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    • pp.507-515
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    • 2017
  • This study is to develop a high quality lightweight foamed concrete that can be applied in the field using EXFG by cracking reducing agent combined with FGD and ALS. First, to increase the volume of foam, the flow and density of the mixture was increased and decreased, respectively. At this time, the effect of substitution ratio of EXFG on fluidity was negligible. The fraction of foam was the highest at EXFG 1%, and the settlement was found to be prevented by the expansion reaction at EXFG 1%. At this time, the ratio of foam was 65%. In the compressive strength, the strengths were similar or decreased when the substitution ratio of EXFG was more than 1%. The apparent density satisfied the KS 0.5 type at the bubble contents was 65%. In case of EXFG substitution, dry shrinkage was decreased by about 10%. As the substitution ratio of EXFG increased, the thermal conductivity increased proportionally.

Model Development of Spray Dryer Absorber FGD Process (Spray Dryer Absorber 배연탈황공정의 모델 개발)

  • Jang, Sun-Hee;Oh, Eui-Kyung;Lee, Hyung-Keun;Kim, Sun-Geon
    • Clean Technology
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    • v.2 no.1
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    • pp.80-95
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    • 1996
  • A mathematical model has been developed for simulating the spray dryer absorber (SDA) used in semi-dry flue gas desulfurization process. Fundamental equations include the component mass and heat balances in both gas and droplet phases and the equation of motion for a single droplet. The model developed described the pilot-plant data much better than the existing SPRAYMOD-M model. The effect of the process variables, whose values were chosen within the operation limits of the actual pilot plants, on % $SO_2$ removal or conversion of the sorbent were calculated, and discussed in terms of $SO_2$ absorption rate, the residence time of flue gas, the velocity and drying time of droplets. Finally, the % $SO_2$ removal was calculated with two independent process variables and the results were shown on three-dimensional or two-dimensional diagrams with the lines of constant % $SO_2$ removal, so that they can be easily applied to preliminary design of the SDA.

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Evaluation of SO2 Absorption Efficiency for Calcined Oyster Shell Slurry Using a Simulated Spray Type-flue Gas Desulfurization (FGD) System: A Comparative Study with Limestone Slurry (모사 Spray Type 배연탈황설비를 이용한 소성패각 슬러리의 SO2 흡수능 평가: 석회석과의 비교연구)

  • Kim, Seok-Hwi;Hong, Bum-Uh;Lee, Jin-Won;Cha, Wang-Seok;Kim, Kangjoo;Moon, Bo-Kyung
    • Economic and Environmental Geology
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    • v.52 no.2
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    • pp.119-128
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    • 2019
  • About 300,000 tones of oyster shell are annually produced in Korea and, thus, a massive recycling plan is required. Many desulfurizing studies using oyster shells with chemical composition of $CaCO_3$ have been performed so far; however, most of them have focused on dry desulfurization. This study investigates the possibility of using oyster shells for wet desulfurization after calcination. For this, a simulated wet desulfurization facility of spray type was devised and compared the SOx-stripping characteristics of calcined oyster shell with those of limestone. The calcined oyster shell slurry indicate a better desulfurizability than the slurries of raw shell or limestone because the oyster shell transformed to a more reactive phase ($Ca(OH)_2$) by the calcination and hydration. Because of this reason, when the calcined oyster shell slurries were used, the reaction residue showed the higher gypsum ($CaSO_4{\cdot}2H_2O$) contents than any other cases. In the continuous desulfurization experiments, calcined oyster shell slurry showed a wider pH variation than limestone or raw oyster shell slurries, another clear indication of high reactivity of calcined oyster shells for $SO_2$ absorption. Our study also shows that the efficiency of wet desulfurization can be improved by the use of calcined oyster shells.