the prime minister and i korean drama episode 1 eng sub
Tài liệu Báo cáo Y học: NMR-based determination of the binding epitope and conformational analysis of MUC-1 glycopeptides and peptides bound to the breast cancer-selective monoclonal antibody SM3 pptx
Ngày tải lên :
21/02/2014, 15:20
... 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...
- 12
- 717
- 0
báo cáo hóa học:" Substitutions in the Reverse Transcriptase and Protease Genes of HIV-1 Subtype B in Untreated Individuals and Patients Treated With Antiretroviral Drugs" potx
Ngày tải lên :
20/06/2014, 08:20
... 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 GA 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 AG transition.
Consideration...
- 6
- 286
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps
Ngày tải lên :
06/08/2014, 02:20
... 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
...
- 25
- 362
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc
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
.
...
- 25
- 383
- 0
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps
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
...
- 25
- 348
- 0
