高校化学工程学报
高校化學工程學報
고교화학공정학보
JOURNAL OF CHEMICAL ENGINEERING OF CHINESE UNIVERSITIES
2013年
4期
547-554
,共8页
季丰%苏宝根%邢华斌%鲍宗必%苏云%杨亦文%任其龙
季豐%囌寶根%邢華斌%鮑宗必%囌雲%楊亦文%任其龍
계봉%소보근%형화빈%포종필%소운%양역문%임기룡
干气%吸附分离%乙烯%丙烯%活性炭%吸附%脱附
榦氣%吸附分離%乙烯%丙烯%活性炭%吸附%脫附
간기%흡부분리%을희%병희%활성탄%흡부%탈부
dry gas%adsorption separation%ethylene%propylene%activated carbon%adsorption
为了建立干气中乙烯、丙烯的吸附分离方法,搭建了考察乙烯、丙烯在活性炭上动态吸附和脱附特性的实验装置,测定了温度为298~333 K、压力为0.2~1.0 MPa条件下,干气中甲烷、乙烯、乙烷、丙烯、丙烷等组分在活性炭上的动态吸附容量,获得各组分的吸附等温线并计算乙烯/丙烯的分离因子,确定活性炭对乙烯、丙烯有很好的吸附选择性。采用升温和惰性气体吹扫相结合的方式进行活性炭的再生,考察了温度和吹扫气流速对再生效果的影响,得到最佳再生条件:温度为373 K,氢气流速为60 mL×min-1,吹扫时间为35 min。活性炭经过多次吸附和再生后,各组分的吸附容量没有显著下降。
為瞭建立榦氣中乙烯、丙烯的吸附分離方法,搭建瞭攷察乙烯、丙烯在活性炭上動態吸附和脫附特性的實驗裝置,測定瞭溫度為298~333 K、壓力為0.2~1.0 MPa條件下,榦氣中甲烷、乙烯、乙烷、丙烯、丙烷等組分在活性炭上的動態吸附容量,穫得各組分的吸附等溫線併計算乙烯/丙烯的分離因子,確定活性炭對乙烯、丙烯有很好的吸附選擇性。採用升溫和惰性氣體吹掃相結閤的方式進行活性炭的再生,攷察瞭溫度和吹掃氣流速對再生效果的影響,得到最佳再生條件:溫度為373 K,氫氣流速為60 mL×min-1,吹掃時間為35 min。活性炭經過多次吸附和再生後,各組分的吸附容量沒有顯著下降。
위료건립간기중을희、병희적흡부분리방법,탑건료고찰을희、병희재활성탄상동태흡부화탈부특성적실험장치,측정료온도위298~333 K、압력위0.2~1.0 MPa조건하,간기중갑완、을희、을완、병희、병완등조분재활성탄상적동태흡부용량,획득각조분적흡부등온선병계산을희/병희적분리인자,학정활성탄대을희、병희유흔호적흡부선택성。채용승온화타성기체취소상결합적방식진행활성탄적재생,고찰료온도화취소기류속대재생효과적영향,득도최가재생조건:온도위373 K,경기류속위60 mL×min-1,취소시간위35 min。활성탄경과다차흡부화재생후,각조분적흡부용량몰유현저하강。
In order to study the method of separating ethylene and propylene in dry gas by adsorption separation, the dynamic breakthrough experimental device used to investigate the adsorption-desorption characteristics of ethylene and propylene on activated carbon was established. Adsorption isotherms of methane, ethylene, ethane, propylene, propane were determined at temperature from 298K to 333K and total pressure range between 0.2MPa to 1.0 MPa. The adsorption capacities of above components and the separation factor of propylene and ethylene were also obtained. The result indicates that the activated carbon has excellent adsorption selectivity to ethylene and propylene. The method combining with heating and inert gas purging was used to regenerate the activated carbon, and the effects of temperature and flow velocity on regeneration were evaluated. The optimal regeneration was obtained when using hydrogen as purging gas with the velocity of 60 mL×min-1 for 35 min at 373 K. It was observed that the adsorption capacity of all components on activated carbon has no significant decrease after several adsorption–regeneration cycles.