생물학적 고정막(biological fixed-film)을 이용한 REMSMAS공법이 개발되었다. REMSMAS 공법에서 유기물질 제거속도에 관한 수학적 model는 CMAS공법과는 많은 차이점이 있었으며, 유기물질 제거속도에 대한 동력학적 해석은 screen media에 부착된 활성미생물과 부유상태의 미생물에 근거를 두어 해석하였다. 단일폭기 CMAS공법은 steady-strate에 도달된 후 연속적으로 공칭체류시간이 4.5, 6, 9.5 및 12시간으로 운전되었고 REMSMAS 공법은 공칭체류시간이 6시간 및 12시간으로 운전되었으며 운전초기는 nonsteady-state상태였다. 또한 시수는 원액을 약 18배 희석하여 COD값이 950mg/l, BOD값이 450mg/l 되도록 하였다. 부유상태의 미생물에 근거를 둔 설계인자들은 단일폭기 CMAS공법 의하여 구하여 졌으며 이 값들은 REMSMAS공법의 유기물 제거속도에 대한 동력학적 상수를 구하는 이용되었다. 단일폭기 CMAS공법에서 얻어진 $Y_2,;K_d,(mu_{max})_s;and;K_s$ 및 $K_s$값은 각각 0.78, 0.27/hr, 1.1/hr, 95mg/l였다. REMSMAS공법에서 단위표면적당 유기물 부하량상수 값은 $9.1mg/cm^2-day$였고 포화상수(Kg)값은 평균 53.5mg/l였다. REMSMAS공법은 steady-state 운전될 때는 유기물 제거율은 단일폭기 CMAS법 보다 높게 나타났으나 한계운전 기일에 도달됨에 따라 감소 한다.
It is preented the removable moving screen media-activated sludge (REMSMAS) process by using the biological fixed-film systems. The substrate removal kinetic difference between the aeration-only completed mixing activated sludge (CMAS) process and REMSMAS process were observed. The substrate removal kinetics were developed based on the attached and suspended microbial growths. The units of the aeration-only CMAS process were continously operated with the normal detention time of 4.5, 6, 9.5 and 12 flours studies after steady-state condition and the operating of the REMSMAS units conducted with the normal detention time of 6 and 12 hours studies in nonsteady-state condition. The feed solution was diluted 18 times to the raw starch wastewater in of order to maintain the proper COD (950mg/l) and BOD (450mg/l) concentration. Design parameters related to the suspended microbial growths were caculated by the equations used in the aeration-only CMAS model and these parameters used to evalute the kinetic constants in the REMSMAS process. The kinetic constant values of $Y_2,;K_d,(mu_{max})_s;and;K_s$ from Monod equations were respectively 0.78, 0.027/hr, 1.1/hr and 95mg/l in the aeration-only CMAS process. The value of the aera capacity (F) appeared to be $9.1;mg/cm^2-day$ and the mean value of the saturation constant $(K_g)$ appeared to be 53.5 mg/l in the REMSMAs process. Also, the substrate removal .ate of the REMSMAS process was higher than that of the normal activated sludge process when this system was operated in steady-state condition. However, the rate was reduced as the critical operating day was approached.
