the prime minister and i korean drama episode 1 eng sub

... performed with STD NMR. Combined with trNOE information one can obtain a 3D picture with the binding residues of the ligand identified in their relative orientation in space and thus efficiently optimize ... there is a different flexibility in the N-terminal and the C-terminal parts of the molecule due to interactions with the protein. This is i n full agreement with the STD determination of the binding epitope ... id entify the binding epitope of ligands to a protein receptor [ 21] . This feature can be used to quickly identify the binding contribution from either peptide or carbohydrate, especially in the...

Ngày tải lên: 21/02/2014, 15:20

... nucleotide substitutions in HIV -1 isolated from both treated and untreated individuals. Numbers of nucleotide substitutions in RT and PR in treated individuals, excluding positions responsible ... received nucleoside reverse transcriptase inhibitors (NRTIs) (Figure 2); the dis- tribution of treatments in these individuals is described in the Table 1. The mean of GA transitions was 8 .1 (95% CI, ... the M18 4I substi- tution which commonly occurs prior to M184V.[ 21] However, M18 4I is rare in clinical samples and the switch from isoleucine to valine results from a AG transition. Consideration...

Ngày tải lên: 20/06/2014, 08:20

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

Ngày tải lên: 21/07/2014, 21:21

... Christesen for her coordinating efforts and abilities in pulling this all together for us. xii 2 Design of GAS-HANDLING Systems and Facilities Figure 1 -1. Gas field facility ... Cylinder/Packing Lubrication System 316 Pipe Sizing Considerations, 317 Foundation Design Considerations 319 , Industry Standard Specifications 320, Fugitive Emissions Control 3 21 Example ... Inhibitors and Anti-Agglomerators, 10 7 CHAPTER S LTX Units and Line Heaters 10 9 LTX Units, 11 0 Line Heaters, 11 2 Heat Duty, 11 3 Fire-Tube Size, 11 5 Coil Sizing, 11 6 Choose Temperatures ...

Ngày tải lên: 06/08/2014, 02:20

... 26.78 Sot. Vapor v g 3306 2947 2444 2036,4 17 03.2 12 06.7 867,9 633 .1 468.0 350.4 265.4 203.27 15 7.34 12 3, 01 97.07 77.29 62.06 50.23 40.96 33.64 27.82 26.80 Enthalpy Sat. Liquid 0.00 3.02 8.05 13 .06 18 ,07 28.06 38.04 48,02 57.99 67.97 77.94 87.92 97.90 10 7.89 11 7.89 12 7.89 13 7.90 14 7.92 15 7.95 16 7.99 17 8.05 18 0.07 Evap. hfg 10 75,8 10 74 .1 10 71. 3 10 68,4 10 65.6 10 59.9 10 54.3 10 48.6 10 42.9 10 37.2 10 31, 6 10 25.8 10 20.0 10 14 .1 1008.2 10 02.3 996.3 990.2 984 .1 977,9 9 71. 6 970,3 Sat. Vapor kg 10 75.8 10 77 .1 1079.3 10 81. 5 10 83.7 10 88.0 10 92,3 10 96.6 11 00.9 11 05.2 11 09.5 11 13.7 11 17.9 11 22,0 11 26 .1 113 0.2 11 34.2 11 38 .1 1 14 2.0 1 14 5.9 11 49.7 1 1. 50.4 Entropy Sat. Liquid Sf 0.0000 0.00 61 0. 016 2 0.0262 0,03 61 0.0555 0.0745 0.0932 0 .11 15 0 .12 95 0 .14 71 0 .16 45 0 .18 16 0 ,19 84 0. 214 9 0.2 311 0.2472 0.2630 0.2785 0,2938 Evap. % 2 .18 77 2 .17 09 2 .14 35 2 ,11 67 2.0903 2.0393 1. 9902 1. 9428 1. 8972 1. 85 31 1. 810 6 1. 7694 1. 7296 1. 6 910 1. 6537 1. 617 4 1. 5822 1, 5480 1. 514 7 1, 4824 0.3090 ... .746 10 .044 8.628 7.444 6.449 5.609 4.896 4.289 3.770 3.324 2.939 2.606 2. 317 2.06 51 Sot Vapor v s 23 .15 19 .382 16 .323 13 .8 21 11. 763 10 .0 61 8.645 7.4 61 6.466 5.626 4, 914 4.307 3.788 3.342 2.957 2.625 2.335 2.0836 Enthalpy Sat. Liquid hf 18 8 .13 19 8.23 208.34 216 .48 228.64 238.84 249.06 259. 31 269.59 279.92 290.28 300.68 311 .13 3 21. 63 332 .18 342,79 353.45 364 .17 Evap. Hfg 965.2 958.8 952.2 945.5 938.7 9 31. 8 924.7 917 .5 910 .1 902.6 894.9 887.0 879.0 870,7 862.2 853.5 844.6 835.4 Sat. Vapor h s 11 53.4 11 57.0 11 60.5 11 64.0 1 16 7.3 1 17 0.6 11 73.8 11 76.8 1 17 9.7 11 82.5 11 85.2 11 87.7 11 90 .1 1 19 2,3 11 94.4 11 96.3 11 98 .1 1 19 9.6 Entropy Sat. Liquid Sf 0.3239 0.3387 0.35 31 0.3675 0.3 817 0.3958 0.4096 0.4234 0.4369 0.4504 0.4637 0.4769 0.4900 0.5029 0. 515 8 0.5286 0.5 413 0.5539 Evap. % 1. 42 01 1.39 01 1.3609 1. 3323 1. 3043 1. 2769 1. 25 01 1 ... / -X4 % % /i /'4 ;/4 ã% /&apos ;i 3/; | s I i 1 1 1 1 B.W.G. Gauge 22 24 26 27 18 20 22 24 16 18 20 22 12 13 14 15 16 17 18 19 20 10 11 12 13 14 15 16 17 18 20 8 10 11 12 13 14 15 16 Thickness In. .028 .022 . 018 . 016 .049 .035 ,028 .022 .065 .049 .035 .028 .10 9 .095 .083 .072 .065 .058 .049 .042 .035 ,13 4 .12 0 .10 9 .095 .083 .072 .065 .058 .049 .035 .16 5 .13 4 .12 0 .10 9 .095 .083 .072 .065 internal Area !n. 2 .0295 .0333 .0360 .0373 .0603 .07 31 .0799 .0860 .10 75 .12 69 .14 52 .15 48 .13 01 .14 86 . ...

Ngày tải lên: 06/08/2014, 02:20

... Design of GAS-HANDLING Systems and Facilities I -in. and 1- in. OD on l!4-in. For triangular patterns these are %-in. OD on %-in., M-in. OD on 1- in., and 1- in. OD on 1/ 4-in, In ... burning inside a piece of pipe which is in turn surrounded by the process fluid. In this situation, there is radiant and convective heat transfer from the flame to the inside ... transfer improved if it is placed in the shell. It is harder to clean the shell than it is the tubes, so the non-fouling fluid should be put in the shell. If boiling service is ...

Ngày tải lên: 06/08/2014, 02:20

Ngày tải lên: 06/08/2014, 02:20

Ngày tải lên: 06/08/2014, 02:20

Ngày tải lên: 06/08/2014, 02:20

Ngày tải lên: 06/08/2014, 02:20

Ngày tải lên: 06/08/2014, 02:20