当代化工
噹代化工
당대화공
Contemporary Chemical Industry
2015年
11期
2569-2571
,共3页
付秋红%张宝国%张艳侠%包洪洲%段日
付鞦紅%張寶國%張豔俠%包洪洲%段日
부추홍%장보국%장염협%포홍주%단일
1,4-丁二醇%环状缩醛 2-(4′-羟基丁氧基)-四氢呋喃%镍%催化剂
1,4-丁二醇%環狀縮醛 2-(4′-羥基丁氧基)-四氫呋喃%鎳%催化劑
1,4-정이순%배상축철 2-(4′-간기정양기)-사경부남%얼%최화제
1,4- butanediol%Cyclic acetal 2- (4 '- hydroxy butoxy) - tetrahydrofuran%Nickel%Catalyst
采用浸渍法制备镍系催化剂,应用于1,4-丁二醇生产过程中副产物环状缩醛2-(4′-羟基丁氧基)-四氢呋喃的加氢转化工艺,在小型固定床加氢装置上分别考察了催化剂中活性组分镍含量和催化剂焙烧温度对加氢性能的影响。800 h 运转实验结果表明,催化剂中活性金属镍含量在30%左右、催化剂焙烧温度为基准时催化剂具有较好的加氢活性、选择性和稳定性,同时,催化剂有较好的抗水性能。
採用浸漬法製備鎳繫催化劑,應用于1,4-丁二醇生產過程中副產物環狀縮醛2-(4′-羥基丁氧基)-四氫呋喃的加氫轉化工藝,在小型固定床加氫裝置上分彆攷察瞭催化劑中活性組分鎳含量和催化劑焙燒溫度對加氫性能的影響。800 h 運轉實驗結果錶明,催化劑中活性金屬鎳含量在30%左右、催化劑焙燒溫度為基準時催化劑具有較好的加氫活性、選擇性和穩定性,同時,催化劑有較好的抗水性能。
채용침지법제비얼계최화제,응용우1,4-정이순생산과정중부산물배상축철2-(4′-간기정양기)-사경부남적가경전화공예,재소형고정상가경장치상분별고찰료최화제중활성조분얼함량화최화제배소온도대가경성능적영향。800 h 운전실험결과표명,최화제중활성금속얼함량재30%좌우、최화제배소온도위기준시최화제구유교호적가경활성、선택성화은정성,동시,최화제유교호적항수성능。
According to the hydroconversion process of cyclic acetal 2 - (4 '- hydroxy butoxy) – tetrahydrofuran in 1,4-butanediol production, Ni-based acetal hydrogenation catalyst was prepared with the impregnation method. The effect of nickel content and calcination temperature on catalyst performance was studied in the small fixed bed hydrogenation unit. The results of 800-hour running experiment show that, when the nickel content is about 30%,and the catalyst calcination temperature is the benchmark, prepared catalyst has good hydrogenation activity, selectivity, stability and water resistance.