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| ±¾Ìû²úÉú 1 ¸ö ·ÒëEPI £¬µã»÷ÕâÀï½øÐв鿴 | ||
ankang276½ð³æ (ÕýʽдÊÖ)
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ÔÚ¸ßѹ΢·´×°ÖÃÉÏ£¬ÒÔÕýÊ®¶þÍéΪģÐÍ»¯ºÏÎ¶ÔPt/ZSM-22¡¢Pt/ZSM-23ºÍPt/ZSM-22/ZSM-23´ß»¯¼Á½øÐÐÁ˼ÓÇâÒì¹¹·´Ó¦»îÐÔÆÀ¼Û£¬½á¹û±íÃ÷£¬ÔÚPt/ZSM-22¡¢Pt/ZSM-23ºÍPt/ZSM-22/ZSM-23´ß»¯¼ÁÉÏ£¬ÕýÊ®¶þÍéµÄ¼ÓÇâÒì¹¹·´Ó¦×ª»¯ÂÊ¡¢ÁѽâÎï²úÂÊ¡¢¶àÖ§Á´Òì¹¹ÌåÊÕÂʾùËæ×Å·´Ó¦Î¶ȵÄÉý¸ßÖð½¥Ôö´ó£¬Ò칹ʮ¶þÍé²úÂʺ͵¥Ö§Á´Òì¹¹ÌåÊÕÂÊÏÈÔö¼Óºó¼õÉÙ£¬ÓëPt/ZSM-22ºÍPt/ZSM-23´ß»¯¼ÁÏà±È½Ï£¬Pt/ZSM-22/ZSM-23´ß»¯¼Á¶Ô³¤Á´Õý¹¹ÍéÌþ±íÏÖ³ö¸üºÃµÄ¼ÓÇâÒì¹¹»¯Ñ¡ÔñÐÔ£¬²úÎï·Ö²¼ÒÔµ¥Ö§Á´Òì¹¹ÌåΪÖ÷¡£ÔÚ200ml¼ÓÇâÆÀ¼Û×°ÖÃÉÏ£¬ÒÔʯÀ¯»ù200SNÍÑÀ¯ÓÍ¡¢650SN¿·È©¾«ÖÆÓÍ¡¢À¯ÏÂÓÍ¡¢¼ÓÇâÁÑ»¯Î²ÓÍ¡¢À¯¸àºÍ»·Íé»ùVGOΪÔÁÏÓÍ£¬½øÒ»²½Ñо¿ÁËPt/ZSM-22/ZSM-23´ß»¯¼ÁµÄ¼ÓÇâÒì¹¹»îÐÔ¡¢Ñ¡ÔñÐÔºÍÎȶ¨ÐÔ£¬2500СʱµÄ·´Ó¦ÆÀ¼Û½á¹û±íÃ÷£¬Pt/ZSM-22/ZSM-23´ß»¯¼Á¾ßÓнϺõÄÔÁÏÊÊÓ¦ÐԺͻîÐÔÎȶ¨ÐÔ£¬Äܹ»½«²»Í¬À¯º¬Á¿µÄÔÁÏÓÍת»¯³ÉµÍÇãµã¡¢¸ßÕ³¶ÈÖ¸ÊýÉõÖÁÊdz¬¸ßÕ³¶ÈÖ¸ÊýµÄÈó»¬ÓÍ»ù´¡ÓÍ¡£ On the high-pressure microreactor device, n-dodecane as a model compound, the hydroisomerization activity evaluation of Pt/ZSM-22, Pt/ZSM-23, and Pt/ZSM-22/ZSM-23 catalyst was carried on, the results indicated that , for the three catalysts, the convertion ratio, yield of cracking products and multi-branched isomers all increased with the increase of reaction temperature,but the yield of i-dodecane and mono-branched isomers first increased and then decreased, compared with Pt/ZSM-22 and Pt/ZSM-23 catalysts, Pt/ZSM-22/ZSM-23 catalyst showed better hydroisomerization selectivity for long chain n-alkanes, products distribution was mainly mono-branched isomers. Hydroisomerization activity,selectivity and stability of Pt/ZSM-22/ZSM-23 catalyst were investigated using the paraffinic 200SN ketone-benzol dewaxing oil, 650SN furfural refined oil , hydrocracking tail oil, foots oil, cerate and naphthenic VGO as feedstocks. The 2500 hours evaluation results indicated that Pt/ZSM-22/ZSM-23 catalyst showed super catalytic performances, including high activity, high hydroisomerization selectivity and broad adaptability to feedstocks. We could obtain low-freezing base oils with high viscosity index or ultrahigh viscosity index in high yield with various wax feedstocks. |
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8814402
ÖÁ×ðľ³æ (Ö°Òµ×÷¼Ò)
- ·ÒëEPI: 509
- Ó¦Öú: 18 (СѧÉú)
- ¹ó±ö: 0.381
- ½ð±Ò: 12916.1
- É¢½ð: 47
- ºì»¨: 16
- Ìû×Ó: 4183
- ÔÚÏß: 357.8Сʱ
- ³æºÅ: 1184404
- ×¢²á: 2011-01-06
- רҵ: Ò©ÎïѧÆäËû¿ÆÑ§ÎÊÌâ
¡¾´ð°¸¡¿Ó¦Öú»ØÌû
| The hydroisomerization activities of Pt/ZSM-22, Pt/ZSM-23, and Pt/ZSM-22/ZSM-23 catalysts were evaluated on the high-pressure microreactor device with n-dodecane as a model compound. It is indicated that , for the three catalysts, the convertion ratio, yield of cracking products and multi-branched isomers all increased with the increase of reaction temperature, while the yield of i-dodecane and mono-branched isomers increased and then decreased with the increase of reaction temperature, and that Pt/ZSM-22/ZSM-23 catalyst showed better hydroisomerization selectivity for long chain n-alkanes than Pt/ZSM-22 and Pt/ZSM-23 catalysts, and the main products were mono-branched isomers. Hydroisomerization activity, selectivity and stability of Pt/ZSM-22/ZSM-23 catalyst were then investigated on 200ml hydrogenation evaluation device with the paraffinic 200SN ketone-benzol dewaxing oil, 650SN furfural refined oil , hydrocracking tail oil, foots oil, cerate and naphthenic VGO as starting materials. It is indicated from the 2500 hours evaluation results that the Pt/ZSM-22/ZSM-23 catalyst showed preferable catalytic performances, including high activity, high hydroisomerization selectivity and good adaptability to starting materials, and that low-freezing base oils with high viscosity index or even ultrahigh viscosity index can be obtained from various wax starting materials with the Pt/ZSM-22/ZSM-23 catalyst. |
2Â¥2012-05-03 08:13:46
8814402
ÖÁ×ðľ³æ (Ö°Òµ×÷¼Ò)
- ·ÒëEPI: 509
- Ó¦Öú: 18 (СѧÉú)
- ¹ó±ö: 0.381
- ½ð±Ò: 12916.1
- É¢½ð: 47
- ºì»¨: 16
- Ìû×Ó: 4183
- ÔÚÏß: 357.8Сʱ
- ³æºÅ: 1184404
- ×¢²á: 2011-01-06
- רҵ: Ò©ÎïѧÆäËû¿ÆÑ§ÎÊÌâ
¡¾´ð°¸¡¿Ó¦Öú»ØÌû
¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï ¡ï
ankang276: ½ð±Ò+30, ·ÒëEPI+1, ¡ï¡ï¡ïºÜÓаïÖú 2012-05-03 13:36:22
ankang276: ½ð±Ò+30, ·ÒëEPI+1, ¡ï¡ï¡ïºÜÓаïÖú 2012-05-03 13:36:22
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The hydroisomerization activities of Pt/ZSM-22, Pt/ZSM-23, and Pt/ZSM-22/ZSM-23 catalysts were evaluated on the high-pressure microreactor device with n-dodecane as a model compound. It is indicated that , for the three catalysts, the convertion ratio, yield of cracking products and multi-branched isomers all increased with the increase of reaction temperature, while the yield of i-dodecane and mono-branched isomers increased and then decreased with the increase of reaction temperature, and that Pt/ZSM-22/ZSM-23 catalyst showed better hydroisomerization selectivity for long chain n-alkanes than Pt/ZSM-22 and Pt/ZSM-23 catalysts, and the main products were mono-branched isomers. Hydroisomerization activity, selectivity and stability of Pt/ZSM-22/ZSM-23 catalyst were then investigated on 200ml hydrogenation evaluation device with the paraffinic 200SN ketone-benzol dewaxing oil, 650SN furfural refined oil , hydrocracking tail oil, foots oil, cerate and naphthenic VGO as starting materials. It is indicated from the 2500 hours evaluation results that the Pt/ZSM-22/ZSM-23 catalyst showed preferable catalytic performances, including high activity, high hydroisomerization selectivity and good adaptability to starting materials, and that base oils with low pour points and high viscosity index or even ultrahigh viscosity index can be obtained from various wax starting materials with the Pt/ZSM-22/ZSM-23 catalyst. ×îºóÒ»¾äÓиöС¸Ä¶¯ |
3Â¥2012-05-03 08:24:08














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