국내 가축분뇨 혐기소화시설 현황 및 운영실태 분석

정광화,김중곤,한덕우,곽정훈,Jeong, Kwang-Hwa,Kim, Jung-Gon,Han, Duk-Woo,Kwag, Jung-Hun 한국축산환경학회 2014 한국축산시설환경학회지 Vol.20 No.1

This study was conducted to survey and inspect the currently operating anaerobic digestion facilities for animal manure. Recently, the number of anaerobic digestion facility for livestock manure is on the rise thanks to growing interest in developing alternative energy. A anaerobic digestion system has been constructed in large scale farms or animal manure public resource center. Currently, most animal manure anaerobic digestion facilities in operation are producing biogas from the pig slurry which contains 97% water. Methane gas can be used to operate a engine generator which then produces electricity. Anaerobic digestate, a by-product of digestion, is mostly utilized as a liquid fertilizer after curing processing. Only in a few cases, it can be discharged after wastewater treatment process. The problem of anaerobic digestate treatment is the imbalance of C/N ratio. The content of N was too high to keep it into normal process.

돼지분뇨에 마이크로파 반응시간에 따른 호기성 퇴비화 과정에서 수분증발량 및 특성변화에 관한 연구

곽정훈,정광화,최동윤,김중곤,한덕우,한만희,유용희,라창식,Kwag, Jung-Hoon,Jeong, Kwang-Hwa,Choi, Dong-Yoon,Kim, Jung-Gon,Han, Duk-Woo,Han, Man-Hee,Yoo, Young-Hee,La, Chang-Six 한국축산환경학회 2013 한국축산시설환경학회지 Vol.19 No.2

In this experiment, we hypothesized that pre-conditioning pig manure with microwave radiation can effectively eliminate moisture and consequently, cut down a need for expensive sawdust. For the experiment, pig manure/sawdust mixture of water content 79% was divided into 4 groups and each of them were treated with microwave for predetermined time periods, 5, 10, 15, 20 minutes. Subsequently, they were transferred to chambers (20 L) and aerobically composted. During the 2 weeks composting, air was supplied using blower (150 L per $1m^3$) and temperature and other variables were monitored continuously. When the data were analyzed, it was found, (1) moisture content was significantly decreased as radiation period extended. (2) weight reduction of compost after completion of composting was noticeably bigger in 15 min radiated group(31%), compared with 5 min (24.6%), 10 min (21.4%), 20 min (27.2%) radiated groups.

돼지분뇨 슬러리 액비화시 폭기가 액비특성 및 슬러지 형성에 미치는 영향

정광화,이명규,김중곤,한덕우,곽정훈,Jeong, Kwang-Hwa,Khan, Modabber Ahmed,Lee, Myung-Gyu,Kim, Jung-Gon,Han, Duk-Woo,Kwag, Jung-Hun 한국축산환경학회 2013 한국축산시설환경학회지 Vol.19 No.1

Two types of reactors were set to investigate the change of characteristics of pig slurry by aeration during fertilization period. One system was equipped with air diffuser to supply oxygen to pig slurry for liquid fertilization, but there was no air diffuser in the other system. Air supply to the experimental systems was regulated by air flow meter. The reactors were set up in the laboratory to protect the pig slurry from external condition such as temperature and humidity changes. Maintaining optimal pH range in the experimental reactors is an important factor for liquid fertilization of pig slurry. In this study, pH ranges of aerobic reactor and anoxic reactor was 7.04~7.19 and 7.34~7.81, respectively. The temperature of aerobic reactors was $2{\sim}3^{\circ}C$ higher then indoor temperature. The amount of sludge accumulated at the bottom layer of non-aerated reactors was 4~5 times more than that of aerated reactors.

국내 가축분뇨 처리시설 형태별 특성조사 분석

정광화(Kwang-Hwa ,Jeong),김중곤(Jung-Kon Kim),Modabber Ahmed Khan,한덕우(Duk-Woo Han),곽정훈(Jung-Hoon Kwag) 유기성자원학회 2014 유기물자원화 Vol.22 No.4

국내 경제성장에 힘입어 최근 30여 년 간에 걸쳐서 축산물 소비가 급격하게 늘어나고 있다. 이에 따라 국내 가축 규모는 전업화, 대형화 되는 추세에 있다. 가축 사육두수의 증가는 필연적으로 가축분뇨발생량 증가를 초래하게 되었다. 농림축산 통계에 따르면 2013년 말 기준으로 약 47,235천 톤의 가축분뇨가 발생되었다. 이 분뇨를 처리하기 위해서 퇴비화, 액비화, 정화 그리고 혐기소화와 같은 다양한 가축분뇨 처리방법이 적용되고 있다. 가축분뇨를 퇴비화 처리 하는 시설에 있어서는 에스컬레이터식,패들식, 스크루식 또는 로타리식 등의 4가지 종류의 교반시설이 적용되고 있다. 가축분뇨 액비화 시설의 경우에는 호기적 방법과 무산소적 방법 등의 2가지 시설이 운영되고 있다. 가축분뇨를 액비화하기위해서 전국에 약 8천기에 달하는 액비화 시설이 설치, 운영되고 있다. 가축분뇨 정화처리 시설에서는 고액분리 처리, 2차 처리 그리고 고도 처리의 3가지 단계의 기술을 적용하고 있다. 2012년 말 기준으로 볼 때 혐기소화 처리방법에 의해서 처리된 돼지분뇨 슬러리는 약 21천 톤에 달한다. 가축분뇨 처리를 위해서 퇴비, 액비, 정화 시설, 혐기소화 시설 등을 선택함에 있어서 악취제거 효율을 높이는 것이 대단히 중요한 사안이 되었다. 본 연구에서는 국내에 설치된 가축분뇨처리 시설의 특징과 운영방식을 6년간에 걸친 시설 설치관련 서류 검토와 현장조사를 통하여 분석하였다 Due to development of the national economy growth, livestock goods consumption has rapidly increased over the past 30 years. It has led livestock breeders to increase their livestock numbers. An increased number of livestock have consequently resulted in an increasing animal feces generation. According to the agricultural statistics provided by the Bureau of Statistics, livestock manure amounts to 47,235 thousand tons in 2013. To treat livestock manure, various types of treatment facilities like composting, liquid fertilization, purification, and anaerobic digestion facilities are being applied. In composting facility, there are four kinds of agitation system: escalator, paddle, screw and rotary type. In case of liquid fertilization process, there are two types of system: aeration and anoxic type. There are about 8,000 liquid fertilization facilities for treatment livestock manure in Korea. For purification of livestock manure, the treatment process is divided by three steps: Solid/Liquid separation process, Secondary purification process and advanced oxidation process. About 21 thousand tons of livestock manure was treated by anaerobic digestion facility in 2012. In every type of facility for livestock manure treatment, it is very important to choose the optimal deodorization equipment for the livestock manure treatment facility. In this study, the investigation has been carried out for six years to analyse the characteristics of livestock manure treatment facilities and related technique of Korea.

현수, 배관 내 혼합 폭기방식 적용이 돼지분뇨 슬러리의 액상비료화에 미치는 영향

정광화(Kwang Hwa-Jeong),김중곤(Jung-Kon Kim),Modabber Ahmed Khan,곽정훈(Kwag Jung-Hoon),한덕우(Han Duk-Woo) 유기성자원학회 2014 유기물자원화 Vol.22 No.4

폭기방식에 따른 돼지분뇨 슬러리의 액비화 효과를 분석하기 위하여 3 가지 형태의 산기방식을 적용하였다. 첫 번째 형태는 기존에 일반적으로 사용되는 산기방식으로서 바닥부분에 고정식으로 설치된 산기장치를 통해 공기를 상향식으로 공급하는 방식이다. 두 번째 방식은 기존 바닥부분 고정 설치식 산기장치를 현수식으로 적용하여 시험용 반응조 바닥으로부터 약 10 cm정도 띄워서 설치하였다. 세번째 방식은 액비조 내의 돼지분뇨 슬러리를 펌프로 흡입하여 다시 액비조로 보내는 순환용 배관에 벤추리 방식의 공기 공급부를 설치하여 배관 내를 흐르는 액비에 공기를 혼합하는 방식의 반응조이다. 고액분리한 돈분뇨 슬러리를 시험용 반응조에 주입 후 1 주일간 정치시켜 고형물을 침전시킨 다음에 폭기 시험을 개시하였다. 바닥 고정식 폭기방식의 반응조에 투입된 원 슬러리 중의 유기물과 T-N,T-P, BOD 농도는 각각 1.82%, 4,400 mg/L, 360 mg/L, 13,542 mg/L 이었으며 폭기 실시 후 채취한슬러 중의 유기물과 T-N, T-P, BOD 농도는 2.01%, 4,400 mg/L, 420 mg/L, 16,824 mg/L 수준이었다. 본 연구에서 시험용으로 제작, 사용된 배관 내 혼합방식의 시험구에서의 상기 수질분석 항목의 농도는 각각 1.58%, 3.700 mg/L, 260 mg/L, 15,735 mg/L 에서 1.96%, 4,000 mg/L, 340 mg/L, 18,098 mg/L 수준으로 변화하였다. 바닥 폭기방식과 배관 내 혼합방식의 두 가지 폭기조의 중층 부분에서의 측정한 상기 수질분석 항목의 농도는 변화정도는 각각 10.4%, 0%, 16.7%, 24.2%와 24.0%, 8.1%, 30.8%, 15.0% 인 것으로 분석되어 배관 내 혼합방식에서의 혼합효과와 액비조 내 액비성분의 균질도 정도가 상대적으로 더 높은 것으로 분석되었다. 폭기조 표면에 생성되는 거품 층의 두께는 배 관 내 혼합방식이 더 얇게 형성되는 결과를 보였다 Three types of diffuser systems were manufactured and applied to investigate the effect of liquid fertilization of pig manure slurry by application of aeration processes. In the first type reactor, commonly used diffuser system, which diffuse air upward by diffusing aerator fixed at the bottom of the reactor is installed. In case of the second type, air diffuser is installed 10 cm above of the bottom of a reactor. In the third type reactor, the venturi-type air diffuser is installed at circulation pipe, which return pig slurry in the reactor(mixing-in-pipe process). The pig manure slurry separated to solid / liquid was flowed into the experimental reactor, and left as it for one week to precipitate solids. The concentration of organic matter, T-N, T-P and BOD in the raw pig manure slurry flowed into the reactor of bottom-fixed type aeration process were 1.82%, 4,400 mg/L, 360 mg/L and 13,542 mg/L, respectively. After aeration the concentration of organic matters, T-N, T-P and BOD in the slurry were 2.01%, 4,400 mg/L, 420 mg/L and 16,824 mg/L, respectively. The concentration of organic matter, T-N, T-P and BOD in the mixing-in-pipe type changed from 1.58%, 3,700 mg/L, 260 mg/L and 15,735 mg/L to 1.96%, 4,000 mg/L, 340 mg/L, and 18,098 mg/L, respectively. Changes of the concentration of organic matter, T-N, T-P and BOD of the pig manure slurry collected from the middle layers of two aeration reactors; bottom aeration process and the mixing-in-pipe process, were 10.4%, 0%, 16.7% and 24.2% and 24.0%, 8.1%, 30.8% and 15.0%, respectively. The thickness of foam layer generated on the surface of pig manure slurry in aeration tank was thinner in mixing-in-pipe reactor than bottom-fixed type aeration reactor.