东北电力大学学报
東北電力大學學報
동북전력대학학보
JOURNAL OF NORTHEAST DIANLI UNIVERSITY
2013年
5期
6-9
,共4页
页岩油泥%催化剂%产油率%馏程
頁巖油泥%催化劑%產油率%餾程
혈암유니%최화제%산유솔%류정
Oil shale sludge%Catalyst%Oil yield%Boiling ranges
在管式反应器上,考察了页岩油泥在不同催化剂( Al2 O3、K2 CO3、Fe2 O3)及比例(质量比为13、15、110)下的热解行为,着重研究了催化剂对产油率和热解油馏程的影响。结果表明:油泥催化热解效果良好,碳酸钾在15时,产油率达到44.08%,氧化铝在13时,产油率达到45.42%,与无催化剂相比,分别提高了28.97%和32.89%。对馏程的促进方面,氧化铁表现突出,在15和110时,均使得重、柴油含量下降,汽油含量上涨。催化热解是按碳正离子机理进行的,重质油发生裂化反应,烷烃出现聚合反应,均提高轻质油的产量。
在管式反應器上,攷察瞭頁巖油泥在不同催化劑( Al2 O3、K2 CO3、Fe2 O3)及比例(質量比為13、15、110)下的熱解行為,著重研究瞭催化劑對產油率和熱解油餾程的影響。結果錶明:油泥催化熱解效果良好,碳痠鉀在15時,產油率達到44.08%,氧化鋁在13時,產油率達到45.42%,與無催化劑相比,分彆提高瞭28.97%和32.89%。對餾程的促進方麵,氧化鐵錶現突齣,在15和110時,均使得重、柴油含量下降,汽油含量上漲。催化熱解是按碳正離子機理進行的,重質油髮生裂化反應,烷烴齣現聚閤反應,均提高輕質油的產量。
재관식반응기상,고찰료혈암유니재불동최화제( Al2 O3、K2 CO3、Fe2 O3)급비례(질량비위13、15、110)하적열해행위,착중연구료최화제대산유솔화열해유류정적영향。결과표명:유니최화열해효과량호,탄산갑재15시,산유솔체도44.08%,양화려재13시,산유솔체도45.42%,여무최화제상비,분별제고료28.97%화32.89%。대류정적촉진방면,양화철표현돌출,재15화110시,균사득중、시유함량하강,기유함량상창。최화열해시안탄정리자궤리진행적,중질유발생열화반응,완경출현취합반응,균제고경질유적산량。
Aimed at studying on the relationship between catalysts and oil yield and boiling ranges,pyrolysis of oil shale sludge was carried out in a tubular electric furnace with different catalysts ( Al2 O3、K2 CO3 and Fe2 O3 ) and mixing ratios ( 1 3、1 5、1 10 ) . The results showed that the effect of catalytic pyrolysis of oil shale sludge was good,the addition of K2 CO3 at 1:5 leaded to the increase of the total oil yield up to 44. 08%, when the mass fraction of Al2 O3 in oil sludge was 33%,the yield of shale oil increased to 45. 42%. Compared with Catalyst-free,the oil yield respectively increased by 28. 97% and 32. 89%. In the aspect of catalysts im-proving the quality of shale oil,Fe2 O3 appeared stronger catalytic role than other metal oxides. When the mass fraction of Fe2 O3 in oil shale sludge was 10~20%,the yield of gasoline increased sharply. Catalytic pyrolysis is abide by carbocations mechanism. Both the cracking of heavy oil and polymerization of paraffin could im-prove the yield of gasolene.