化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2015年
7期
2505-2513
,共9页
张因%赵丽丽%张鸿喜%李海涛%刘盼盼%盖媛媛%赵永祥
張因%趙麗麗%張鴻喜%李海濤%劉盼盼%蓋媛媛%趙永祥
장인%조려려%장홍희%리해도%류반반%개원원%조영상
加氢%催化剂%催化剂载体%镍%二氧化锆%二氧化硅%氧化铝
加氫%催化劑%催化劑載體%鎳%二氧化鋯%二氧化硅%氧化鋁
가경%최화제%최화제재체%얼%이양화고%이양화규%양화려
hydrogenation%catalyst%catalyst support%nickel%zirconia%silica%alumina
分别以ZrO2、SiO2与Al2O3为载体,采用等体积浸渍法制备了Ni质量分数为15%的催化剂,考察了其催化顺酐液相加氢性能,并利用BET、XRD、H2-TPR以及TPO-MS等表征手段对催化剂进行了详细表征。结果表明,随载体不同各催化剂的加氢活性及选择性存在较大差异,Ni/Al2O3催化剂的 CC键加氢活性最高,但其几乎没有CO加氢活性,催化顺酐加氢主产物为丁二酸酐。Ni/ZrO2催化剂具有最高的CO加氢活性,催化顺酐加氢主产物为γ-丁内酯,在反应温度为483 K,氢气压力为5 MPa的条件下反应8 h时,Ni/ZrO2催化剂的γ-丁内酯选择性达79.20%。催化剂的套用实验表明,Ni/ZrO2与Ni/SiO2催化剂具有高的使用稳定性,Ni/Al2O3催化剂则在套用过程中快速失活。顺酐加氢至γ-丁内酯的中间产物——丁二酸酐与催化剂间的相互作用是影响催化剂加氢选择性及使用稳定性的主要原因。
分彆以ZrO2、SiO2與Al2O3為載體,採用等體積浸漬法製備瞭Ni質量分數為15%的催化劑,攷察瞭其催化順酐液相加氫性能,併利用BET、XRD、H2-TPR以及TPO-MS等錶徵手段對催化劑進行瞭詳細錶徵。結果錶明,隨載體不同各催化劑的加氫活性及選擇性存在較大差異,Ni/Al2O3催化劑的 CC鍵加氫活性最高,但其幾乎沒有CO加氫活性,催化順酐加氫主產物為丁二痠酐。Ni/ZrO2催化劑具有最高的CO加氫活性,催化順酐加氫主產物為γ-丁內酯,在反應溫度為483 K,氫氣壓力為5 MPa的條件下反應8 h時,Ni/ZrO2催化劑的γ-丁內酯選擇性達79.20%。催化劑的套用實驗錶明,Ni/ZrO2與Ni/SiO2催化劑具有高的使用穩定性,Ni/Al2O3催化劑則在套用過程中快速失活。順酐加氫至γ-丁內酯的中間產物——丁二痠酐與催化劑間的相互作用是影響催化劑加氫選擇性及使用穩定性的主要原因。
분별이ZrO2、SiO2여Al2O3위재체,채용등체적침지법제비료Ni질량분수위15%적최화제,고찰료기최화순항액상가경성능,병이용BET、XRD、H2-TPR이급TPO-MS등표정수단대최화제진행료상세표정。결과표명,수재체불동각최화제적가경활성급선택성존재교대차이,Ni/Al2O3최화제적 CC건가경활성최고,단기궤호몰유CO가경활성,최화순항가경주산물위정이산항。Ni/ZrO2최화제구유최고적CO가경활성,최화순항가경주산물위γ-정내지,재반응온도위483 K,경기압력위5 MPa적조건하반응8 h시,Ni/ZrO2최화제적γ-정내지선택성체79.20%。최화제적투용실험표명,Ni/ZrO2여Ni/SiO2최화제구유고적사용은정성,Ni/Al2O3최화제칙재투용과정중쾌속실활。순항가경지γ-정내지적중간산물——정이산항여최화제간적상호작용시영향최화제가경선택성급사용은정성적주요원인。
Nickel-based catalysts supported on ZrO2, SiO2, and Al2O3 supports, were prepared by incipient impregnation method and evaluated using liquid phase hydrogenation of maleic anhydride. BET,XRD,H2-TPR and TPO-MS were employed to characterize these catalysts. Their catalytic performance varied with supports used. Among all the catalysts, Ni/Al2O3 catalyst exhibited the highest activity for C C hydrogenation, while there was the lowest activity for C O hydrogenation. Ni/ZrO2 catalyst had the highest C O hydrogenation activity, and maleic anhydride conversion and γ-butyrolactone selectivity were 100% and 79.2% respectively under the reaction condition of 483 K, 5 MPa of H2 and 8 h of reaction time. The re-use experiment of catalyst demonstrated that the stability of catalyst in liquid phase hydrogenation of maleic anhydride was better for Ni/ZrO2 and Ni/SiO2 than Ni/Al2O3. Both selectivity and stability of catalysts could be explained by the interaction between succinic anhydride and catalyst.