天然气化工(C1化学与化工)
天然氣化工(C1化學與化工)
천연기화공(C1화학여화공)
Natural Gas Chemical Industry
2015年
4期
24-28,48
,共6页
Pt-Sn-K/Al2O3催化剂%异丁烷%脱氢%硫化合物
Pt-Sn-K/Al2O3催化劑%異丁烷%脫氫%硫化閤物
Pt-Sn-K/Al2O3최화제%이정완%탈경%류화합물
Pt-Sn-K/Al2O3 catalyst%isobutane%dehydrogenation%sulfur compound
在固定床反应器中考察了常见硫化合物对Pt-Sn-K/Al2O3催化剂催化异丁烷脱氢活性的影响。实验结果表明,在温度580℃、压力0.1MPa、进料组成V(H2):V(i-C4H10)=2:1、总空速GHSV=2000h-1和GHSV(i-C4H10)=667h-1的条件下反应,乙硫醇、乙硫醚和二硫化碳使Pt-Sn-K/Al2O3催化剂的异丁烷转化率下降,异丁烯选择性上升;且随原料中硫含量的增加,异丁烷脱氢活性下降的程度增大。在原料硫质量分数为200×10-6的条件下,硫化合物对Pt-Sn-K/AI2O3催化剂的异丁烷脱氢毒性大小顺序为:噻吩>EtSH≈Et2S≈CS2≈PrSH≈H2S。硫化合物导致的Pt-Sn-K/Al2O3催化剂中毒为可逆中毒。
在固定床反應器中攷察瞭常見硫化閤物對Pt-Sn-K/Al2O3催化劑催化異丁烷脫氫活性的影響。實驗結果錶明,在溫度580℃、壓力0.1MPa、進料組成V(H2):V(i-C4H10)=2:1、總空速GHSV=2000h-1和GHSV(i-C4H10)=667h-1的條件下反應,乙硫醇、乙硫醚和二硫化碳使Pt-Sn-K/Al2O3催化劑的異丁烷轉化率下降,異丁烯選擇性上升;且隨原料中硫含量的增加,異丁烷脫氫活性下降的程度增大。在原料硫質量分數為200×10-6的條件下,硫化閤物對Pt-Sn-K/AI2O3催化劑的異丁烷脫氫毒性大小順序為:噻吩>EtSH≈Et2S≈CS2≈PrSH≈H2S。硫化閤物導緻的Pt-Sn-K/Al2O3催化劑中毒為可逆中毒。
재고정상반응기중고찰료상견류화합물대Pt-Sn-K/Al2O3최화제최화이정완탈경활성적영향。실험결과표명,재온도580℃、압력0.1MPa、진료조성V(H2):V(i-C4H10)=2:1、총공속GHSV=2000h-1화GHSV(i-C4H10)=667h-1적조건하반응,을류순、을류미화이류화탄사Pt-Sn-K/Al2O3최화제적이정완전화솔하강,이정희선택성상승;차수원료중류함량적증가,이정완탈경활성하강적정도증대。재원료류질량분수위200×10-6적조건하,류화합물대Pt-Sn-K/AI2O3최화제적이정완탈경독성대소순서위:새분>EtSH≈Et2S≈CS2≈PrSH≈H2S。류화합물도치적Pt-Sn-K/Al2O3최화제중독위가역중독。
The influence of sulfur compounds on the performance of Pt-Sn-K/Al2O3 catalyst for isobutane dehydrogenation reaction was investigated in a fixed-bed reactor. The results showed that, under the reaction conditions of 580℃, 0.1MPa, V (H2)/V(i-C4H10) of 2 in the feedstock, GHSV for total feedstock of 2000h-1, and GHSV for i-C4H10 of 667h-1, the addition of ethanethiol, diethyl sulfide and carbon disulfide led to a decline of isobutane conversion and a rise of isobutene selectivity; and the higher the concentration of sulfur compounds in the feedstock was, the larger the decline of the dehydrogenation activity of the catalyst was. When the mass fraction of sulfur from the sulfur compounds in feedstock was 200 ×10-6, the toxicity of different sulfur compounds on the dehydrogenation activity of Pt-Sn-K/AI2O3 catalyst was as follows: C4H4S (thiophene)>EtSH≈Et2S≈CS2≈PrSH≈H2S. The poisoning of Pt-Sn-K/Al2O3 catalyst caused by sulfur compounds was reversible.