PUKYONG

열적 전처리 공정에 의한 하수슬러지의 가용화

Metadata Downloads
Alternative Title
Solublization of wastewater treatment sludge by using thermal pretreatment
Abstract
An increase of the population and urbanization has contributed to
a significant increase of generated sewage sludge. The annual
production of sewage sludge is constantly growing and will continue
to grow in the future.
An important process among facilities that can secure energy in a
sewage treatment plant is an anaerobic digester. The pretreatment
process for he anaerobic digester was used increasing gas
production and reducing sludge in wastewater treatment plant.
The pretreatment technology of the anaerobic digester includes
physicochemical treatment consisting of ultrasonication, high
pressure treatment, microwave, high voltage, mechanical grinding
and thermal treatment etc..
The main operating factors of the thermal treatment process in the
anaerobic digestion pretreatment process are temperature, pressure
and time. By applying heat, the substrate structure changes from
insoluble to soluble, increasing the biodegradability of the substrate,
breaking the chemical bonds in the cell wall and releasing
intracellular water. The release of water within the cell
consequently contributes to the improvement of the dewaterability
of the sludge.
The purpose of this study is that the thermal pretreatment of
sewage sludge contributes to the solubilization of soluble COD,
which is used as an indicator for improving the efficiency of the
digester, and the reduction of energy required for mixing and
sludge transfer in the anaerobic digester. The purpose of this study
is to present data that thermal pretreatment contributes to the
increase in the efficiency of the anaerobic digestion tank and the
energy independence of sewage sludge by analyzing the effect on
the capillary suction time expressing phosphorus sludge dewatering
properties.
The thermal pretreatment process of sewage sludge affects the
increase rate of soluble COD, which is an indicator of improving
the efficiency of the digester, the decrease in viscosity of the
sludge that contributes to energy reduction in the sludge mixing
and transport process, and the capillary suction time, which is an
indicator of dewaterability of sludge . The temperature and reaction
time selected as independent variables of the thermal pretreatment
process of sewage sludge were designed with central composite
design (CCD) among surface reaction analysis methods, and the
experimental results are as follows.
In the application of sewage sludge in the thermal pretreatment
process, the SCOD solubilization rate(%) increased in proportion to
the temperature and reaction time in the heat treatment
temperature range of 90 – 150 ℃ and the reaction time of 60 – 90
minutes, and the maximum solubilization rate of the primary sludge
was determined by the heat treatment temperature. It was found to
be 15.3% at 140 ℃ and reaction time of 80 minutes, and the
maximum solubilization rate of the secondary sludge was 37.8% at a
heat treatment temperature of 150 ℃ and reaction time of 60
minutes, and the solubilization rate of the secondary sludge was
higher than that of the primary sludge.
In the thermal pretreatment process of sludge, the SCOD
solubilization rate, the decrease rate of capillary suction time, and
the decrease rate of viscosity showed a positive correlation with
each other. It was found that the increase in solubilization rate by
thermal pretreatment affects the decrease in viscosity and increase
in sludge solubilization.
Author(s)
임정용
Issued Date
2021
Awarded Date
2021. 8
Type
Dissertation
Keyword
solublization
Publisher
부경대학교
URI
https://repository.pknu.ac.kr:8443/handle/2021.oak/1222
http://pknu.dcollection.net/jsp/common/DcLoOrgPer.jsp?sItemId=200000506578
Alternative Author(s)
Joung Young Im
Affiliation
부경대학교 산업대학원
Department
산업대학원 환경공학과
Advisor
손윤석
Table Of Contents
제 1 장 서 론 1
제 2 장 문헌연구 3
2.1 하수슬러지 3
2.2 슬러지 전처리 기술 6
2.2.1 슬러지 전처리 기술 개요 6
2.2.2 열적 전처리공정 7
1) 열적 전처리공정 개요 7
2) 열가수분해 목적 10
3) 열가수분해 연구동향 12
4) 온도의 영향 13
5) 반응시간의 영향 15
2.3 혐기성소화 16
2.3.1 혐기성소화의 정의 16
2.3.2 혐기성소화의 원리 16
2.4 반응표면분석법(RSM, Response Surface Methodology) 18
2.4.1 실험계획법 18
2.4.2 반응표면분석-중심합성계획법 19
제 3 장 실험재료 및 방법 22
3.1 실험설계 22
3.2 실험 슬러지 및 가열장치 26
3.3 슬러지 분석방법 29
3.3.1 COD 29
3.3.2 점도 29
3.3.3 모세관 흡입시간(CST: capillary suction time) 30
3.3.4 슬러지 가용화율 32
제 4 장 실험결과 및 고찰 33
4.1 열적 전처리에 의한 슬러지 가용화율 변화 특성 33
4.1.1 1차 슬러지의 열적 전처리에 의한 가용화율 변화 특성 33
4.1.2 2차 슬러지의 열적 전처리에 의한 가용화율 변화 특성 40
4.2 열적 전처리에 의한 슬러지 모세관흡입시간 변화 특성 46
4.3 열적 전처리에 의한 슬러지 점도 변화 특성 54
4.4 열적 전처리에 의한 슬러지 가용화율과 모세관 흡입시간 및 점도 감소율의 상관관계 60
제 5 장 결 론 65
참 고 문 헌 68
Degree
Master
Appears in Collections:
산업대학원 > 환경공학과
Authorize & License
  • Authorize공개
Files in This Item:

Items in Repository are protected by copyright, with all rights reserved, unless otherwise indicated.