化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
3期
993-1002
,共10页
丁路%周志杰%赵冰%霍威%于广锁
丁路%週誌傑%趙冰%霍威%于廣鎖
정로%주지걸%조빙%곽위%우엄쇄
滴管炉%水蒸气气化%碳转化率%气焦比
滴管爐%水蒸氣氣化%碳轉化率%氣焦比
적관로%수증기기화%탄전화솔%기초비
drop tube furnace%steam-gasification reaction%carbon conversion%steam/char ratio
在滴管炉内对煤焦与水蒸气气化反应进行了实验研究,考察了煤阶、气化温度、水蒸气与进料煤焦质量比(气焦比)对气化气体产物释放特性以及煤焦转化率的影响。实验温度为1100、1200、1300和1400℃,气焦比分别为0.4:1、0.6:1和1:1。研究发现:滴管炉内不同煤焦的水蒸气气化气体产物以H2含量最高,CH4含量最低。不同煤阶热解焦、气化温度以及气焦比的变化影响滴管炉内水蒸气气化产物气体组成和转化率的高低。随气化温度的升高,神府煤焦和北宿煤焦气化气体产物中H2和CO产率不断增大,H2/CO的比值则逐渐减小,碳转化率有不断增加的趋势。在气化温度大于1200℃的条件下,当气焦比从0.4:1增至0.6:1,神府煤焦和北宿煤焦的碳转化率变化幅度不大(5%以内);当气焦比从0.6:1增至1:1,北宿煤焦的碳转化率略微降低,而神府煤焦的碳转化率增幅则在15%以上。
在滴管爐內對煤焦與水蒸氣氣化反應進行瞭實驗研究,攷察瞭煤階、氣化溫度、水蒸氣與進料煤焦質量比(氣焦比)對氣化氣體產物釋放特性以及煤焦轉化率的影響。實驗溫度為1100、1200、1300和1400℃,氣焦比分彆為0.4:1、0.6:1和1:1。研究髮現:滴管爐內不同煤焦的水蒸氣氣化氣體產物以H2含量最高,CH4含量最低。不同煤階熱解焦、氣化溫度以及氣焦比的變化影響滴管爐內水蒸氣氣化產物氣體組成和轉化率的高低。隨氣化溫度的升高,神府煤焦和北宿煤焦氣化氣體產物中H2和CO產率不斷增大,H2/CO的比值則逐漸減小,碳轉化率有不斷增加的趨勢。在氣化溫度大于1200℃的條件下,噹氣焦比從0.4:1增至0.6:1,神府煤焦和北宿煤焦的碳轉化率變化幅度不大(5%以內);噹氣焦比從0.6:1增至1:1,北宿煤焦的碳轉化率略微降低,而神府煤焦的碳轉化率增幅則在15%以上。
재적관로내대매초여수증기기화반응진행료실험연구,고찰료매계、기화온도、수증기여진료매초질량비(기초비)대기화기체산물석방특성이급매초전화솔적영향。실험온도위1100、1200、1300화1400℃,기초비분별위0.4:1、0.6:1화1:1。연구발현:적관로내불동매초적수증기기화기체산물이H2함량최고,CH4함량최저。불동매계열해초、기화온도이급기초비적변화영향적관로내수증기기화산물기체조성화전화솔적고저。수기화온도적승고,신부매초화북숙매초기화기체산물중H2화CO산솔불단증대,H2/CO적비치칙축점감소,탄전화솔유불단증가적추세。재기화온도대우1200℃적조건하,당기초비종0.4:1증지0.6:1,신부매초화북숙매초적탄전화솔변화폭도불대(5%이내);당기초비종0.6:1증지1:1,북숙매초적탄전화솔략미강저,이신부매초적탄전화솔증폭칙재15%이상。
The steam-gasification reaction characteristics of coal char was studied in a drop tube furnace (DTF). The effects of various factors, such as coal type, gasification temperature and mass ratio of steam to char(steam/char ratio) on the properties of gas products and carbon conversion had been investigated. The experiment temperatures were1100, 1200, 1300 and 1400℃, steam/char ratios 0.4:1, 0.6:1 and 1:1, respectively. The results showed that, for all coal char studied, H2 content in gaseous products was the largest and CH4 content did the smallest. The char from coal with different coal ranks, change of gasification temperature and steam/char ratio had effects on gas composition and carbon conversion for DTF steam-gasification. At steam/char ratio of 0.4:1, 0.6:1 and 1:1, for Shen-fu’ and Bei-su’char, CO and H2 yield increased continuously and H2/CO ratio decreased gradually when gasification temperature went up. The carbon conversion showed an increasing tendency with temperature increased. At gasification temperature higher than 1200℃, the change of carbon conversion of Shen-fu’ and Bei-su’char was not bigger 5%, although steam/char ratio increased from 0.4:1 to 0.6:1. But the ratio increased from 0.6:1 to 1:1, the carbon conversion of Bei-su’char had a little decreasing, in contrast, for Shen-fu’char the increase of carbon conversion was higher than 15%.