Tham khảo tài liệu 'phân tích eclectron trong hóa phân tích phần 5', kỹ thuật - công nghệ, hoá học - dầu khí phục vụ nhu cầu học tập, nghiên cứu và làm việc hiệu quả | Table 2 Summary of results for fixed bed run Fll-09-1348. Catalyst 3 40 g . Ridirchcmle LP 33 81 Diluent g Glass beads Cnlnlyst volume Ct Diluent Volume rr Period r Ỉ 2 3 4 5 6 Dale 5 15 88 5 HỰ88 5 10 88 5 18 88 5 10 88 5 20 88 Time on stream Balance Duration 1 Average Temperature C 235. 235. 231. 250. 220. 235. Maximum A Temperature C k Pressure MPa 1 48 lli co Feed Ratio .080 .080 .080 .080 .080 .080 Space Velocity Nl g-cnl-h Space Velocity Aff g-Fe-h 3 55 G1ISV h- r 238. 484. 238. 238. 238. 476. CO Conversion ll co Conversion II co Usage .850 STY moh 11 4 CO g-cat A 4 .044 .001 .044 .054 .023 .065 Pco Pl co P l o .704 .800 415 .487 Weight of Outlet 11 4 85 11 0 7 24 CO CO 365 Hydrocarbons Oxygenates .731 .575 .787 .805 .617 .613 Wax r .43 Yield g NmP. H 1 CO Converted 4 c llr Cj-C i Hydrocarbons C5-C11 Hydrocarbons C Hydrocarbons too. 155. 120. 107. 107. Wax nil. 144. r Oxygenates 15 5 Total 228. 251. 200. 205. 204. 155. 1 2 olefins n-paraflin Ratio c c3 C-4 4 7 1 . 3 26 c8 C1D Based on unreduced catalyst Maximum axial temperature diOercnce Rased on reactor volume J Balances 1 2 6 Unanalyzed products collected from hot trap balances 3-5 Unrecovered products from wax analysis. Table 2 coni ll . Summitry of results for llxcil bed run FH-DQ-1348. Period i -1 2 .3 .
