• 제목/요약/키워드: pretreatment process

검색결과 724건 처리시간 0.026초

GTA-GMA 하이브리드공정에 따른 자동차용 아연도금강판의 용접부 기공감소 (I) - 선행 GTA의 영향 (Porosity Reduction during Gas Tungsten Arc-Gas Metal Arc Hybrid Welding of Zinc Coated Steel Sheets (I) - Effect of Preceding Gas Tungsten Arc)

  • 강민정;안영남;김철희
    • Journal of Welding and Joining
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    • 제34권4호
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    • pp.40-47
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    • 2016
  • The Zn coating on automotive galvanized steel sheets can improve corrosion resistance. However, the boiling temperature of Zn is lower than the melting temperature of steel and it causes well-known spatter and porosity problem. One of most prominent solutions is a pretreatment of Zn coating by an additional welding arc prior to the main welding process. In this research, GTA and GMA are selected as heat sources for pretreatment and main welding processes, respectively. The authors suggested three possible mechanisms to reduce weld defects by the GTA pretreatment: (1) Formation of gap between the sheets; (2) Evaporation of Zn layer; (3) Oxidation of Zn layer. Among them, Zn Oxidation is the most important mechanism to reduce weld defects in the GTA-GMA hybrid process.

저탁도 해수원수 특성에 적합한 응집 - 여과 공정의 최적화 (Optimization of Coagulation and Media Filtration Process for Low Turbidity Seawater)

  • 손동민;조명흠;김정숙;강임석
    • 대한환경공학회지
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    • 제36권4호
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    • pp.251-257
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    • 2014
  • 본 연구는 RO 해수담수화 전처리 공정으로써 응집 및 여과공정에 대하여 수행되었다. RO 시스템은 충분하고 안정적인 전처리를 통하여 RO 막오염을 완화 할 수 있는 우수한 수질을 공급할 수 있어야 한다. 본 실험은 RO 막 공정의 전처리로서 다양한 응집제 주입량, 응집 교반 강도 및 시간, 탁도, 여과속도 실험 조건을 사용하여 응집과 여과공정의 효과를 조사하기 위하여 수행되었다. 본 연구 결과 적합한 RO 공급수로 적절한 SDI 값을 나타내기 위한 최적 전처리 조건은 응집 pH 6.5, 탁도 4 NTU 이상 그리고 여재 충진 높이가 550 mm 이상인 것으로 나타났다. 그러나 응집교반 강도, 응집제 주입농도와 여과속도는 여과효율에 비교적 큰 영향을 미치지 않은 것으로 나타났다.

Ag 코팅 Cu 플레이크의 제조에서 전처리 및 Ag 코팅 공정 변화의 효과 (Effects of Pretreatment and Ag Coating Processes Conditions on the Properties of Ag-Coated Cu Flakes)

  • 김지환;이종현
    • 한국재료학회지
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    • 제24권11호
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    • pp.617-624
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    • 2014
  • To elucidate the effects of a pretreatment process on the uniformity of Ag electroless plating on Cu flakes, pretreatment time was mainly considered with a mixed solution of 0.15 M ammonium hydroxide and 0.0375 M ammonium sulphate. Optical inspection of Ag-coated Cu flakes determined that the optimal pretreatment time is 120 s. Repetition of the sequence in which Ag plating was done immediately after the pretreatment of 120 s clearly enhanced the plating uniformity. Scanning electron microscopy revealed that holes were formed irregularly on some Cu flakes during the period from the asdropping of an Ag precursor solution to 5 min. The hole formation was judged to be due to continuous removal of Cu on the local surfaces by the repetitive formation and elimination of $Cu_2O$ or $Cu(OH)_2$ layers. However, the increase of the amount of Ag coating suppressed the hole creation and increasingly enhanced the antioxidant property.

Improvement of sugar recovery from Sida acuta (Thailand Weed) by NaOH pretreatment and application to bioethanol production

  • Siripong, Premjet;Doungporn, Premjet;Yoo, Hah Young;Kim, Seung Wook
    • Korean Journal of Chemical Engineering
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    • 제35권12호
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    • pp.2413-2420
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    • 2018
  • Sida acuta, a common type of weed in Thailand, contains relatively high cellulose (42.7%) content. We pretreated NaOH to improve glucose recovery from S. acuta. The effect of pretreatment temperature and NaOH concentration was fundamentally investigated based on hydrolysis efficiency with recovery of solid fraction. The pretreatment condition was determined to be 3% NaOH at $60^{\circ}C$ for 9 h, which showed the highest glucose recovery. The hydrolysates obtained by enzymatic hydrolysis of S. acuta were applied to the fermentation of Saccharomyces cerevisiae K35, and a theoretical yield of 97.6% was achieved at 18 h. This indicated that the hydrolysates medium without detoxification had no negative effects on the fermentation. The production of biomass into bioethanol was evaluated based on the material balance of 1,000 g basis. Following this estimation, approximately 28 g and 110 g bioethanol could be produced by untreated and pretreated S. acuta, respectively, and this production was improved about 3.9-fold by NaOH pretreatment. These results again show the importance of pretreatment in biorefinery process.

열적-알칼리성 전처리 유무에 따른 폴리하이드록시부티레이트의 고온 혐기성 소화 영향 연구 (Thermophilic Anaerobic Digestion of Polyhydroxybutyrate with and without Thermo-alkaline Pretreatment)

  • 이지현;이준엽
    • 한국환경과학회지
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    • 제33권2호
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    • pp.121-129
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    • 2024
  • The study investigated the effect of thermo-alkaline pretreatment on the solubilization of polyhydroxybutyrate (PHB) and its potential to enhance of thermophilic anaerobic digestion, focusing on biochemical methane potential (BMP) and methane production rate, using two different particle sizes of PHB (1500 ㎛ and 400 ㎛). Thermo-alkaline pretreatment tests were conducted at 90 ℃ for 24 hours with varying NaOH dosages from 0-80% (w/w). BMP tests with untreated PHB exhibited methane production ranging from 150.4~225.4 mL CH4/g COD and 21.5~24.2 mL CH4/g VSS/d, indicating higher methane production for smaller particle sizes of PHB, 400 ㎛. Thermo-alkaline pretreatment tests achieved a 95.3% PHB solubilization efficiency when 400 ㎛ PHB particles were treated with 80% NaOH dosage at 90 ℃ for 24 hours. BMP tests with pretreated PHB showed substantial improvement in thermophilic anaerobic digestion, with an increase of up to 112% in BMP and up to 168% in methane production rate. The results suggest that a combined pretreatment process, including physical (400 ㎛ PHB particles) and thermo-alkaline (90 ℃, 40-80% NaOH dosage, and 24 hours reaction time), is required for high-rate thermophilic anaerobic digestion of PHB with enhanced methane production.

정밀여과법 하수재이용 공정에서 오존의 전처리 효과에 관한 연구 (Effect of Ozonation in Microfiltration Membrane for Wastewater Reuse)

  • 문성용;안세혁;이상협;박종훈;홍석원;최용수
    • 상하수도학회지
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    • 제20권4호
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    • pp.535-543
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    • 2006
  • The Ozone oxidation process was applied to increase the efficiency of reuse process when treating the secondary effluent by the membrane system. This paper focus on decreasing efficiency of membrane fouling, because of membrane fouling reduction by ozone and evaluation of application of the ozone oxidation. The feed water was secondary effluent from BNR process. The result shows that the ozone pretreatment can reduce membrane fouling effectively. Also, the improvement of treated water quality was obvious. The reduction of the membrane fouling led decrease of following pollutant and increase of lnner adsorptive ability of hydrophilic organic matter and decrease of molecular weight. MF membrane process alone can meet the domestic reuse water standards. And ozone pretreatment process also can increase the removal rates of turbidity, COD, nitrogen, and color.

당 생산을 위한 카놀라 부산물의 암모니아 침지 전처리 공정의 최적화 (Optimization of soaking in aqueous ammonia pretreatment of canola residues for sugar production)

  • 유하영;김성봉;이상준;이자현;서영준;김승욱
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2011년도 추계학술대회 초록집
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    • pp.114.1-114.1
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    • 2011
  • Bioenergy production from lignocellulosic biomass and agriculture wastes have been attracted because of its sustainable and non-edible source. Especially, canola is considered as one of the best feedstock for renewable fuel production. Oil extracted canola and its agriculture residues are reuseable for bioethanol production. However, a pretreatment step is required before enzymatic hydrolysis to disrupt recalcitrant lignocellulosic matrix. To increase the sugar conversion, more efficient pretreatment process was necessary for removal of saccharification barriers such as lignin. Alkaline pretreatment makes the lignocellulose swollen through solvation and induces more porous structure for enzyme access. In our previous work, aqueous ammonia (1~20%) was utilized for alkaline reagent to increase the crystallinity of canola residues pretreatment. In this study, significant factors for efficient soaking in aqueous ammonia pretreatment on canola residues was optimized by using the response surface method (RSM). Based on the fundamental experiments, the real values of factors at the center (0) were determined as follows; $70^{\circ}C$ of temperature, 17.5% of ammonia concentration and 18 h of reaction time in the experiment design using central composition design (CCD). A statistical model predicted that the highest removal yield of lignin was 54% at the following optimized reaction conditions: $72.68^{\circ}C$ of temperature, 18.30% of ammonia concentration and 18.30 h of reaction time. Finally, maximum theoretical yields of soaking in aqueous ammonia pretreatment were 42.23% of glucose and 22.68% of xylose.

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세라믹 분리막의 분산형 용수공급 시스템 적용을 위한 전처리 연계공정의 고플럭스 평가 (Evaluation of High Flux Combined with Pretreatment Process for Application of Decentralized Water Supply System with Ceramic Membrane)

  • 강준석;박서경;이정은;강소연;이정준;쿠엔 보;김성수;김한승
    • 한국수처리학회지
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    • 제26권6호
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    • pp.61-72
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    • 2018
  • In this study, applicability of the decentralized water supply system were investigated by the high flux evaluation using ceramic membrane with combined pretreatment process. A) filtration process increased the transmembrane pressure of 1.4 kPa and 89.5 kPa on 2 and $5m^3/m^2{\cdot}d$ of filtration flux, respectively, the physical backwashing recovery rate were less than 28.6%. The (B) Coag./Floc. - Sedi. combined process with 4 mg / L of A-PAC showed that the transmembrane pressure increased to within 6 kPa, the physical backwashing recovery rate was over 37.9 % higher than (A) Filtration process. (C) Coag./Floc. combined process showed an increase of transmembrane pressure compared with (B) Coag./Floc. - Sedi. combined process, physical backwashing recovery rate was over 84%. As a result of the membrane fouling analysis using the resistance in series model, the combined pretreatment process showed that the cake resistance (Rc) was more than 92% at membrane filtration flux of $2m^3/m^2{\cdot}d$. In the (C) Coag./Floc. combined process, cake resistance(Rc) was over 86% on high flux conditions. The coagulation floc contained in influent was removed by the membrane, and the cake layer formed with the removed floc was identified as reversible fouling resistance which could be recovered by physical backwashing. The decentralized water supply system, which has the limitation of site area and installation space, is considered to could be operation of high flux of ceramic membrane by applying (C) Coag./Floc. combined process without sedimentation process.

The Structure and Electrical Characteristics of CNTs Depending on the Hydrogen Plasma Treatment

  • Uh, Hyung-Soo;Lee, Soo-Myun;Jeon, Pil-Goo;Kwak, Byung-Hwak;Park, Sang-Sik;Cho, Euo-Sik;Lee, Jong-Duk;Kwon, Sang-Jik
    • 한국정보디스플레이학회:학술대회논문집
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    • 한국정보디스플레이학회 2003년도 International Meeting on Information Display
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    • pp.855-858
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    • 2003
  • Carbon nanotubes (CNTs) were grown on Ni-coated TiN/Si substrate by microwave plasma chemical vapor deposition using mixture gas of $H_2/CH_4$ at low temperature of 500 $^{\circ}C$. Average diameter of CNTs could be easily controlled by $H_2$ plasma pretreatment time before CNTs growth. The turn-on voltages of CNT emitters were varied from 3.5 $V/{\mu}m$ to 9 $V/{\mu}m$ according to the hydrogen pretreatment conditions. The close relationship between electron emission characteristics and pretreatment time indicates that pretreatment condition can be a key process parameter in CNTs growth for field emission displays..

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Bleaching of Hardwood Kraft Pulp by Xylanase Pretreatment

  • Cho, Nam-Seok
    • Journal of the Korean Wood Science and Technology
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    • 제27권4호
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    • pp.65-71
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    • 1999
  • This study was carried out to investigate the effect of xylanase pretreatment of the unbleached hardwood kraft pulp during the conventional Chlorine-Extraction- Hypochlorite (CEH) bleaching on pulp property. Optimum bleaching condition was evaluated by using Novozym produced from the fungus Humicola insolens. Also the effect of chelating agent prior to enzyme treatment was analyzed. The kappa number of enzymatic bleached pulp at the enzyme charge 10 IU/ml was slightly similar to that of bleached pulp without enzyme. By enzyme treatment, the chlorine charge in conventional CEH bleaching process of hardwood KP could be reduced by 17%, while no adverse effect on pulp yield and strength was. The optimum condition for enzyme pretreatment was 10 IU/ml xylanase charge, 3 to 4 hrs treatment, and 2% pulp consistency. In sugar composition in the enzyme pretreated pulp, arabinose and mannose were not much different, but more xylose was retained. This high content of hemicellulose in pulp seems to play an important role in pulp properties. The pulp pretreatment by chelating agent prior to enzyme treatment could improve the enzyme activity and enhance the bleaching effect at 0.2% diethylenetriamine pentaacetic acid (DTPA) charges.

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