PUKYONG

한외여과(UF) pilot plant를 이용한 낙동강원수의 처리

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Alternative Title
Treatment of the Nakdong river water using pilot-scale ultrafiltration
Abstract
This study focuses on the removal efficiency of dissolved and particulate matters with applying pretreatments, such as ozone-coagulation performance and ozone-coagulation-Roughing filter(Gravity Flow Fiber Filter) performance to UF membrane separation process. Also, it signifies the changes of permeate flux and fouling of membrane with pretreatment, thus suggests the appropriation of ozone-coagulation performance and ozone-coagulation-Roughing filter performance as the membrane filtration pretreatment process.
After applying pre ozone-coagulation settling and pre ozone-coagulation-Roughing filter to hollow fiber UF as the pretreatment performance in 4 months, the result shows that the turbidity range of feed water is from 0.3245 NTU to 22.22 NTU, and that the average turbidity is 1.0 NTU in the beginning of the operation. However, the turbidity of the feed hits high level from 56 days to 79 days approximately after the initial operation. This is because of typhoon and heavy rainfall which become the cause of the temporary destabilization in settling basin in water treatment plant. Nevertheless, the quality of treated water always remains less than 0.1 NTU, much lower than the 0.5 NTU, the drinking water standard, and the average is less than 0.05 NTU in 4 months.
The permeate fluxes are 148 LMH(L/㎥·hr at 20℃) and 149LMH(L/㎥·hr at 20℃). This result indicates that no matter how the quality of raw water differs, the permeate flux is not affected if the quality of membrane feed water fulfills a certain level with the pretreatment of coagulation-settlement and roughing filter. In the case of pre ozone-coagulation settling and pre ozone-coagulation-Roughing filter applied to hollow fiber UF membrane as the pretreatment process, KMnO4 and TPC of final treated water are 70.36 % and 99.9 % and 73.66 % and 99.91 %, the high removal efficiency.
In the case of Al, Fe, and Mn, which can not be removed by membrane, the values with applying pre ozone-coagulation settling as the pretreatment procedure are 97.51 %, 100 %, and 60.27 %, and those with pre ozone-coagulation-Roughing filter are 90.67 %, 100 %, and 100 %, also the high remove efficiency.
Therefore, the application of pre ozone-coagulation settling operation and pre ozone-coagulation-Roughing filter operation as the pretreatment method can be highly efficient to increase permeate flux and remove particulate matter and inorganic matter in practice plant.
Author(s)
장형욱
Issued Date
2007
Awarded Date
2007. 2
Type
Dissertation
Keyword
UF Ozone Roughing filter Flux Membrane fouling
Publisher
부경대학교 대학원
URI
https://repository.pknu.ac.kr:8443/handle/2021.oak/3699
http://pknu.dcollection.net/jsp/common/DcLoOrgPer.jsp?sItemId=000001953626
Alternative Author(s)
Jang, Hyung-Wook
Affiliation
부경대학교 대학원
Department
대학원 환경공학과
Advisor
강임석
Table Of Contents
제 1 장 서론 1
제 2 장 문헌연구 3
2.1 여과 메카니즘 3
2.1.1 급속여과 메카니즘 3
2.1.2 섬유사 여과의 특성 4
2.2 응집공정 6
2.2.1 응집 메카니즘 6
2.2.2 천연유기물질의 응집 mechanism 9
2.3 분리막에 의한 정수공정 13
2.3.1 막공정의 특성과 종류 13
2.3.2 MF 및 UF 막분리 공정의 원리 14
2.3.3 막여과 메카니즘 16
2.3.4 UF 막을 이용한 입자상 물질 제거 17
2.3.5 막 여과 방식 19
2.3.6 오존처리가 막 오염에 미치는 영향 20
제 3 장 재료 및 방법 27
3.1 실험장치 및 방법 27
3.1.1 응집 실험장치 27
3.1.2 오존 발생장치 28
3.1.3 회분식 막 장치 29
3.2 Pilot-Plant의 UF 막 여과 장치 31
3.3 수질분석방법 32
제 4 장 결과 및 고찰 35
4.1 전처리공정(오존 및 응집)이 UF공정에 미치는 영향 35
4.1.1 오존처리에 의한 입자상 및 용존유기물 특성의 변화 35
4.1.2 저탁도시 오존처리 및 응집이 막 오염저감에 미치는 영향 39
4.1.3 고탁도시의 오존처리 및 응집이 막 오염 저감에 미치는 영향 45
4.2 오존-응집-침전공정을 적용한 UF pilot-plant의 운전특성 47
4.2.1 오존-응집-침전공정에 따른 막여과 장치의 운전 및 처리특성 47
4.2.2 오존-응집-침전공정에 따른 막여과 장치 처리수의 수질평가 51
4.3 오존-Roughing filter를 적용한 UF pilot-plant의 운전특성 57
4.3.1 오존-Roughing filter의 전처리공정에 따른 막 여과 장치의 운전 및 처리특성 57
4.3.2 오존-오존-Roughing filter에 따른 막 여과 장치 처리수의 수질 평가 61
제 5 장 결론 66
참고문헌 68
Degree
Master
Appears in Collections:
산업대학원 > 환경공학과
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