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renfangshu
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wypward(½ð±Ò+1):лл²ÎÓë 2010-09-06 21:30:25
wypward(½ð±Ò+1):лл²ÎÓë 2010-09-06 21:30:25
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Ï©Ìþ±¥ºÍ ¼ÓÇâת»¯ Íé»ù»¯ ˫ϩÌþ Äܸø³öÕ⼸¸öרҵÃû´ÊµÄÓ¢Óïµ¥´ÊÂ𣿠|

2Â¥2010-09-06 17:23:16
smartlijia
½ð³æ (СÓÐÃûÆø)
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- ½ð±Ò: 3185.1
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- Ìû×Ó: 177
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feimi-china(½ð±Ò+10, ·ÒëEPI+1): 2010-09-11 10:44:32
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ÎÒËѵ½µÄרҵ´Ê»ã¼°ÆäÀý¾äÈçÏ£¬Ï£Íû¶ÔºóÀ´ÕßÓÐÓá£ÎÒÊÇѧ»úеµÄ£¬ËùÒÔ²»¸ÒÍý×ԷƱ¡£¬»¹Íû¼ûÁ¡£ Ï©Ìþ±¥ºÍ olefin saturation The hydrodesulfurization result showed that at 230 ¡æ, the olefin saturation degree of LH 01G catalyst was 68.4%; ¼ÓÇâÍÑÁò½á¹û±íÃ÷ :ÔÚ 2 30¡æÊ± ,LH 0 1G´ß»¯¼ÁµÄÏ©Ìþ±¥ºÍÂÊΪ 6 8.4% ¼ÓÇâת»¯ Hydro-Conversion Reactive Mechanism,Preparation and Property Appraisal of the New-typeMo-Co/TiO2 Hydro-Conversion Catalyst (Non-Presulfurizing Process) ÐÂÐÍ(²»Ô¤Áò»¯)Mo-Co/TiO_2¼ÓÇâת»¯´ß»¯¼ÁµÄ·´Ó¦»úÀí¡¢ÖÆ±¸ºÍÐÔÄÜÆÀ¼Û Íé»ù»¯ alkylate Analytical Case for Alkylate Raw Material Pre-hydrogenation Process Íé»ù»¯ÔÁÏÔ¤¼ÓÇ⹤ÒÕÓ¦Ó÷ÖÎö ˫ϩÌþ diolefin The amount of C5/C9+ distillates in pygas, the amount of unsaturated hydrocarbon, mono - olefin and diolefin in C5 distillate, and the typical composition of C9+ are presented. ½éÉÜÁѽâÆûÓÍÖÐC5£¯C9+µÄÊýÁ¿; C5Áó·ÖÖв»±¥ºÍÌþµÄº¬Á¿¼°µ¥Ë«Ï©ÌþµÄÁ¿¡£ |
3Â¥2010-09-07 01:28:28
renfangshu
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- ×¢²á: 2007-06-16
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feimi-china(½ð±Ò+1): 2010-09-13 13:38:13
ringzhu(½ð±Ò+4): 2010-11-22 14:54:45
feimi-china(½ð±Ò+1): 2010-09-13 13:38:13
ringzhu(½ð±Ò+4): 2010-11-22 14:54:45
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the Hydro-Conversion of ÓлúÁò»¯Îïand olefin saturation which is the raw Material for making Hydrogen The diolefin is Selectively Removaled from Alkylate Raw Material in Refinery ²»ÊÇѧÕâ¸öרҵµÄ£¬¿ÉÄܲ»¹»×¼È·¡£ |

4Â¥2010-09-08 15:18:30













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