• 상하수도학회지
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• 제25권5호
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• pp.777-782
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• 2011

The residual treatment facilities in WTP(water treatment plant) play an important role in solid-liquid separation. At present, it is difficult to solve problems related with thickening and dewatering of WTP sludge, and discharging waste water to river. The quantity of residuals generated from water treatment plants depends upon the raw water quality, dosage of chemicals used, performance of the treatment process, method of sludge removal, efficiency of sedimentation, and backwashing frequency. Sludge production by the physical separation of SS(Suspended Solid) occurs under quiescent conditions in the primary clarifier, where SSs are allowed to settle and to consolidate on the clarifier bottom. Raw primary sludge results when the settled solids are hydraulically removed from the tank. In this study, Drawing characteristics of the sludge thickening in the thickener of Water Treatment Plants was simulated by Using CFD(Computational Fluid Dynamics.

• 펄프종이기술
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• 제33권2호
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• pp.68-73
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• 2001

This experiment was executed to clarify the optimum condition of reductive bleaching for 100% color papers. The reductive bleaching of the color paper was desirable to be done under such conditions as high temperature over $60^{\circ}C$ and high consistency within possibly short time. The FAS bleaching like the sodium hydrosulfite required oxygen-free condition. Especially, as the mixture between pulps and chemicals was favored in case of the high consistency, it was actively recommended. Therefore, it is desirable to control the dosage with the type of the dyes, the nature, the dye content, the paper compositions, and the targeting initial and final brightness.

• Environmental Engineering Research
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• 제20권3호
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• pp.285-289
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• 2015

Complicated and expensive seawater desalination technology is a big challenge in boron removal process. Conventional seawater desalination process of coagulation utilized for pre-treatment is difficult to remove boron. Boron can be removed more effectively in Reverse Osmosis (RO) process than any other processes. In this study, a coagulant with the name Mineral Cluster was examined its boron removal ability. Boron removal efficiency of Mineral Cluster depended on pH value and Mineral Cluster dosage. Desalination process combines the pre-treatment process with Mineral cluster diluted at the ratio of 1:2500 and the RO membrane process. The original sea water could be desalinated to drinking water quality, 1 mg/L, without any pH adjustments. Therefore, if the Mineral cluster is added without any other chemicals for adjusting pH, the desalination process would be much safer, efficient and economical.

• 펄프종이기술
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• 제48권1호
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• pp.100-110
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• 2016

Alkaline Peroxide Mechanical Pulping (APMP) of Pinus densiflora harvested from domestic mountains was explored. APMP contributes to various advantages including pulp quality, elimination of the need for a bleaching process, and energy savings. Sequential treatment of impregnation of bleaching chemicals and refining not only overcome the concern of alkaline darkening of wood chips during chemical impregnation, but it also brightens the chips to the desired brightness levels suitable for writing and printing papers. APMP pulping from Pinus densiflora was greatly influenced by the dosage levels of hydrogen peroxide and sodium hydroxide. Alkaline peroxide treatment was carried out by applying one of three levels of hydrogen peroxide (1.5, 3, and 4.5% based on the oven-dried weight of the wood chips) and one of three levels of sodium hydroxide (1.5, 3, and 4.5% based on the oven-dried weight of the wood chips). Other chemicals including a peroxide stabilizers and metal chelation were constantly added for all treatments. Chemical treatment with a liquor-to-wood ration of 9:1 was carried out in a laboratory digestor. Compared to BTMP, APMP pulping displayed outstanding characteristics including the less requirement of refining energy, the better improvement of tensile strength, the more reduction of shives, and the greater increase of pulp brightness. In particular, when 4.5% of hydrogen peroxide with impregnation during 90 minutes was used, the brightness of APMP reached 64.9% ISO. Even though bulk of APMP was decreased with the increase of sodium hydroxide, a better and improved balance could be achieved between optical and strength properties. The spent liquor obtained from the discharge of the impregnation process at the dosage level of 4.5% hydrogen peroxide exhibited an equal level of residual peroxide with BTMP. In conclusion, APMP pulping showed successful results with Pinus densiflora due to its better response to the development of optical and physical properties compared to TMP pulping.

• 공업화학
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• 제9권3호
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• pp.336-341
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• 1998

II형 무수석고의 평균 입경과 치환율이 시멘트페이스트의 유동성에 미치는 영향에 대해 비교하였다. 나프탈렌계(NSF)와 폴리카르본산계(NT-2) 등 2가지 고유동화제의 첨가량을 0~2.0wt%으로 변화시켰을 때 3종으로 구분한 II형 무수석고의 평균입경(4, 14, $35{\mu}m$)과 치환율(3, 5, 10, 15wt%)의 변화에 따른 영향을 측정하였다. 이들 변수들에 따른 영향을 측정하기 위하여 시멘트페이스트의 초기 유동성 및 경과시간별로 겉보기 점도를 관찰하였다. 시멘페이스트의 초기유동성은 II형 무수석고의 평균입경에 의한 영향보다는 II형 무수석고의 치환율 증가에 의한 영향이 더욱 큰 것으로 나타났다. II형 무수석고의 치환율을 10wt%로 고정시 NT-2, 1.0wt% 첨가로 시멘트페이스트의 유동성은 동일 첨가량의 NSF보다 크게 향상되었다. 이는 측정된 변수들의 범위 중에서 가장 우수한 시멘트 페이스트의 유동성을 보여주는 경우이다. NT-2, 1.0wt% 첨가에서 II형 무수석고의 치환율 증가에 따라 시멘트 페이스트의 겉보기 점도가 현저하게 감소되었다. 이로부터 시멘트 페이스트의 유동성 향상을 위해서는 NT-2의 첨가와 더불어 시멘트를 II형 무수석고로 일정비율 치환하는 것이 더욱 효과적임을 알 수 있었다.

• Applied Biological Chemistry
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• 제30권3호
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• pp.227-233
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• 1987

Aniline 유도체(誘導體)로부터 thiocyanation에 의(依)해 2-aminobenzothiazole 유도체(誘導體)를 합성(合成)하였고, 이어서 mothylisocanate의 부가반응(附加反應)에 의(依)하여 3-(benzothiazol-2-yl)-1-methyl urea 유도체(誘導體) 6종(種)을 합성(合成)하여 IR, NMR, GC/MS 등(等)에 의(依)하여 물질(物質)의 구조(構造)를 확인(確認)하였다. 합성(合成)한 화합물(化合物)들의 바랭이, 강아지풀의 화본과(禾本科) 잡초(雜草)와 쇠비름, 명아주의 광엽(廣葉) 잡초(雜草)에 대(對)하여 50g, 200g, 800g a.i/10a로 발아전처리(發芽前處理)를 하여 살초효과(殺草效果)를 조사(調査)한 결과(結果)는 다음과 같다. 합성(合成)한 화합물(化合物) 6종(種) 모두 발아전처리제(發芽前處理劑)로서 800g a.i/10a 살포량(撒布量)에서 화본과(禾本科) 또는 광엽(廣葉) 잡초(雜草)에 대(對)하여 살초효과(殺草效果)가 인정(認定)되었다. 화합물(化合物) 번호(番號) ACRI-S-8416, ACRI-S-8411 및 ACRI-S-8413은 800g a.i/10a의 살포량(撒布量)에서 광엽(廣葉) 잡초(雜草)에 효과(效果)가 있었으며 ACRI-S-8412는 화본과(禾本科) 잡초(雜草)에 선택적(選擇的) 살초효과(殺草效果)가 인정(認定)되었다. 화합물(化合物) 번호(番號) ACRI-S-8414 즉(卽), 3- (6-ethylbenzothiazol-2-yl)-1-methyl urea는 6종(種)의 화합물(化合物) 중(中) 가장 강력(强力)한 살초효과(殺草效果)를 나타내었으며 50g a.i/10a의 살포량(撒布量)에서도 화본과(禾本科) 잡초(雜草)에 60%의 선택적(選擇的) 살초효과(殺草效果)가 인정(認定)되었다.

• 상하수도학회지
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• 제21권2호
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• pp.243-252
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• 2007

Effects of alum dosage on the particle growth were investigated by monitoring particle counts in a rapid mixing process. Kaolin was used for turbid water sample and several other chemicals were added to adjust pH and ionic strength. The range of velocity gradient and mixing time applied for rapid mixing were $200{\sim}300sec^{-1}$ and 30~180 sec, respectively. Particle distribution in the synthetic water sample was close to the natural water where their turbidity was same. The number of particles in the range of $10.0{\sim}12.0{\mu}m$ increased rapidly with rapid mixing time at alum dose of 20mg/L, however, the number of $8.0{\sim}9.0{\mu}m$ particles increased at alum dose of 50mg/L. The number of $14.0{\sim}25.0{\mu}m$ particles at alum dose of 20mg/L was 10 times higher than them at alum dose of 50mg/L. Dominant particle growth was monitored at the lower alum dose than the optimum dose from a jar test at an extended rapid mixing time(about 120 sec). The number of $8.0{\sim}14.0{\mu}m$ particles was lower both at a higher alum doses and higher G values. At G value of $200sec^{-1}$ and at alum dose of 10-20mg/L, residual turbidity was lower as the mixing time increased. But at alum dose above 40mg/L and at same G value, lower residual turbidity occurred in a short rapid mixing time. Low residual turbidity at G value of $300sec^{-1}$ occurred both at lower alum doses and at shorter mixing time comparing to the results at G value of $200sec^{-1}$.

• 유기물자원화
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• 제26권1호
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• pp.47-53
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• 2018

유기성 폐기물 소화공정의 발효액에서 젖산(lactic acid)을 회수하기 위해 화학침전법을 평가하였다. 젖산(lactic acid)의 회수율을 높이기 위하여 화학침전제 종류와 교반속도 및 침전시간 등 반응조건이 회수율 향상에 미치는 영향을 살펴보았다. 화학침전제의 종류에 관계없이 주입양이 증가할수록 젖산(lactic acid) 회수율이 증가하는 경향을 보였으며, CaO가 $Ca(OH)_2$와 $CaCO_3$에 비하여 높은 회수율을 나타냈다. CaO를 사용한 반응조건 최적화 실험결과, 교반속도 180 rpm, 침전시간 24 h, ethanol 주입량 25%(v/v)에서 회수율이 48%로 가장 높게 나타났다. 본 연구에서는 발효액 내 젖산(lactic acid)의 농도만 고려하여 주입할 침전제의 양을 계산하였기 때문에 실제 적용을 위해서는 발효액의 유기산 종류 및 농도를 고려하여 침전제의 투입량을 결정해야할 것이다. 유기물의 정성적 분석(FEEM, SEC) 결과로 볼 때 침전공정은 유기산의 특성에 큰 영향을 미치지 않았다.

• 펄프종이기술
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• 제43권3호
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• pp.106-112
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• 2011

The effects of alkaline treatment on the WRV, crystalline structure and sheet structure of softwood and hardwood bleached kraft pulp were investigated. Sodium hydroxide and sodium carbonate were used as chemicals for alkaline treatment and two levels of alkali dosage (5%, 10%) were applied respectively. Alkali treated and untreated pulp were refined to three levels (550, 450 and 350 mL CSF). WRV of the alkali treated pulps depended on the alkaline type and concentration. It was found that the crystalline structures of softwood and hardwood pulp were not changed by refining. Sodium carbonate and lower concentration of sodium hydroxide treatment did not caused any modification of cellulose crystalline structure, while higher concentration of sodium hydroxide treatment caused the partial modification of cellulose crystalline structure. Alkaline treatment of hardwood bleached kraft pulp led to the shrinkage of fiber diameter and bulky structure of sheet. Alkaline treatment of softwood bleached kraft pulp did not cause the significant change in fiber shrinkage and bulk of sheet.

• Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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• 제2권2호
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• pp.115-121
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• 1998

Train of chemical and biological processes was investigated to treat leachate from industrial waste landfill. Organics and nitrogen concentrations of landfill leachate studied in this research were high and their BOD/COD ratio was 0.3. Biological process should be combined with chemical process for optimum treatment of leachate. PAC(Polyaluminium chloride) was the best coagulant among three chemicals tested, and the optimum condition of PAC coagulation was pH 6 and 1,250 mg/L of dosage. When SBR was operated for simultaneous removal of organics and nitrogen, removal efficiency of COD and T-N reached over $82\%,\;71\%,$ respectively and time distribution of 2/4/2/1 was most effective for one cycle of anoxic/aerobic/anoxic/aerobic.