高校化学工程学报
高校化學工程學報
고교화학공정학보
JOURNAL OF CHEMICAL ENGINEERING OF CHINESE UNIVERSITIES
2014年
4期
701-706
,共6页
单从云%罗勇%初广文%邹海魁%陈建峰
單從雲%囉勇%初廣文%鄒海魁%陳建峰
단종운%라용%초엄문%추해괴%진건봉
并流旋转填充床%整体式SiC填料%气相压降%关联式
併流鏇轉填充床%整體式SiC填料%氣相壓降%關聯式
병류선전전충상%정체식SiC전료%기상압강%관련식
co-current rotating packed bed (CO-RPB)%structured SiC packing%gas pressure drop
以空气-水为研究体系,在并流旋转填充床内采用整体式碳化硅(SiC)填料,利用单因素法,分别考察了转速、气量对干床压降的影响以及转速、气量、液量对湿床压降的影响。实验结果表明,对于干床压降,压降随转速的增大而减小,随气量增大而增大。当气量为183 m3?h-1、转速为1400 r?min-1时,压降为-140 Pa左右;对于湿床压降,压降随转速增大而减小,随气量增大而增大,液量变化对湿床压降影响不大。当气量为183 m3?h-1、液量为340 L?h-1、转速为1400 r?min-1时,湿床压降为-160 Pa左右。通过对实验数据的关联,分别得到了干床和湿床压降的关联式,与实验结果的偏差均在±15%以内。
以空氣-水為研究體繫,在併流鏇轉填充床內採用整體式碳化硅(SiC)填料,利用單因素法,分彆攷察瞭轉速、氣量對榦床壓降的影響以及轉速、氣量、液量對濕床壓降的影響。實驗結果錶明,對于榦床壓降,壓降隨轉速的增大而減小,隨氣量增大而增大。噹氣量為183 m3?h-1、轉速為1400 r?min-1時,壓降為-140 Pa左右;對于濕床壓降,壓降隨轉速增大而減小,隨氣量增大而增大,液量變化對濕床壓降影響不大。噹氣量為183 m3?h-1、液量為340 L?h-1、轉速為1400 r?min-1時,濕床壓降為-160 Pa左右。通過對實驗數據的關聯,分彆得到瞭榦床和濕床壓降的關聯式,與實驗結果的偏差均在±15%以內。
이공기-수위연구체계,재병류선전전충상내채용정체식탄화규(SiC)전료,이용단인소법,분별고찰료전속、기량대간상압강적영향이급전속、기량、액량대습상압강적영향。실험결과표명,대우간상압강,압강수전속적증대이감소,수기량증대이증대。당기량위183 m3?h-1、전속위1400 r?min-1시,압강위-140 Pa좌우;대우습상압강,압강수전속증대이감소,수기량증대이증대,액량변화대습상압강영향불대。당기량위183 m3?h-1、액량위340 L?h-1、전속위1400 r?min-1시,습상압강위-160 Pa좌우。통과대실험수거적관련,분별득도료간상화습상압강적관련식,여실험결과적편차균재±15%이내。
Gas pressure drop was studied in a co-current rotating packed bed (CO-RPB) filled with structured SiC by an air-water system. According to the single factor method, effects of rotational speed, gas flow rate on the gas pressure drop were examined in the dry CO-RPB, while effects of rotational speed, gas flow rate, liquid flow rate on the gas pressure drop were investigated in the wet CO-RPB. Experimental results show that the gas pressure drop decreases with the increase of rotational speed and increases with the increase of the gas flow rate in the dry CO-RPB. When the gas flow rate is 183 m3?h-1 and rotational speed is 1400 r?min-1, the dry bed gas pressure drop is about-140 Pa. In the wet CO-RPB, the gas pressure drop decreases with the increase of the rotational speed and increases with the increase of the gas flow rate. However, the gas pressure drop is almost constant with the increase of liquid flow rate. When the gas flow rate is 183 m3?h-1 and liquid flow rate is 340 L?h-1 with a rotational speed of 1400 r?min-1, the wet bed gas pressure drop is about-160 Pa. Two empirical correlations for estimating the gas pressure drop in the dry and wet CO-RPB are proposed. The deviation of gas pressure drop predicted from the two correlations is within ±15%of the experimental data.