jaeri-tech 96-053 - iaea
TRANSCRIPT
JAERI-Tech—96-053 JP9702030
JAERI-Tech96-053
Japan Atomic Energy Research Institute
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This report is issued irregularly.Inquiries about availability of the reports should be addressed to Research
Information Division, Department of Intellectual Resources, Japan Atomic EnergyResearch Institute, Tokai-mura, Naka-gun, Ibaraki-ken 319-11, Japan.
©Japan Atomic Energy Research Institute, 1996
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JAERI-Tech 96-053
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JAERI-Tech 96-053
Preliminary Design of Steam Reformer in Out-Pile Demonstration
Test Facility for HTTR Heat Utilization System
Katsuhiro HAGA, Ryutaro HINO, Yosiyuki INAGAKI,
Kazuhiko HATA, Hideki AITA,Kenji SEKITA,
Tetsuo NISHIHARA, Seiya YAMADA * and Yukio SUDO
Department of Advanced Nuclear Heat Technology
Oarai Research Establishment
Japan Atomic Energy Research Institute
Oarai-machi, Higashiibaraki-gun, Ibaraki-ken
(Received October 30,1996)
One of the key objectives of HTTR is to demonstrate effectiveness
of high-temperature nuclear heat utilization system. Prior to connecting
a heat utilization system to HTTR, an out-pile demonstration test is
indispensable for the development of experimental apparatuses,
operational control and safety technology, and verification of the
analysis code of safety assessment. For the first heat utilization system
of HTTR, design of the hydrogen production system by steam reforming is
going on. We have proposed the out-pile demonstration test plan of the heat
utilization system and conducted preliminary design of the test facility.
In this report, design of the steam reformer, which is the
principal component of the test facility, is described. In the course of
the design, two types of reformers are considered. The one reformer
contains three reactor tubes and the other contains one reactor tube to
reduce the construction cost of the test facility. We have selected the
steam reformer operational conditions and structural specifications by
analyzing the steam reforming characteristics and component structural
strength for each type of reformer.
Keywords:Nuclear Heat Utilization, HTTR, Demonstration Test, Steam
Reformer, Hydrogen Production, Reactor Tube, Design
* Mitsubishi Heavy Industries, Ltd.
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JAERI-Tech 96-053
Contents
1. Introduction 1
2. Outline of Out-of-pile Demonstration Test and Test Facility 1
2.1 Main Items of Out-of-pile Demonstration Test 2
2.2 Thermal and Hydraulic Conditions of Out-of-pile Demonstration Test ••• 3
2.3 Components of Out-of-pile Demonstration Test Facility 5
3 . Structure of Steam Reformer 9
3 .1 Principle of Basic Design 9
3 . 2 Structure Design 9
4. Performance of Steam Reformer 15
4.1 Optimization of the Method to Promote Heat Transfer of Reactor Tube ••• 15
4.2 Analysis Model 20
4.3 Analysis Condition 26
4 .4 Influence of the Approach Temperature 27
4 . 5 Influence of Feed Gas Constitution to Heat and Mass Transfer 28
5. Structure Design Calculation 47
5.1 Consideration for Design Condition 47
5 . 2 Design Condition 48
5.3 Calculation Results 48
6. Arrangement of Measuring Instrument 60
7. Specification 65
8 . Compensation Heater Block 67
8.1 Inst allation Purpose 67
8.2 Optimization of Heater Capacity 67
8 . 3 Optimization Result 68
9 . Conclusions 70
Acknowledgments 70
References 71
(4)
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JAERI-Tech 96-053
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JAERI-Tech 96-053
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JAERI-Tech 96-053
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JAERI-Tech 96-053
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JAERI-Tech 96-053
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JAERI-Tech 96-053
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JAERI-Tech 96-053
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JAERI-Tech 96-053
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26
JAERI-Tech 96-053
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JAERI-Tech 96-053
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U
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36.33
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28 —
JAERI-Tech 96-053
(2) turn*
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<y > X Table 4. 3
9
(3)
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(b)
(c)
(d)
(e)
(f)
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(Nn'/s)
(Nn'/s)
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(kf)
(kf)
(Table 4.
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X.
0.00861
0. 00478
37.10% / 5. 44%
0.0328
14.49
9.41
41.32
26.66
173
282
281
135
0
0
36.
0
. 00773
. 00466
74% / 5. 36%
.03215
14.57
9.92
40.80
26.40
176
283
281
135
t
29 —
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ISWA'AEiXM'/ttiP
AftfiftffftlftP&SIADJttt$ft4fffiftpftl9$tfi'P
Mi t tSAPJUJBSSfttJ P
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CO3£fi£j-7 htliPffiHAP
^fitA'^/ttffiSfHj P7)X#l l t8§APt) ^^"iHSftiiP (CH4)jtf 5 Xt 8§ tb P7K^i$flP7"f>APJSJ4A' JOD^^ >A P?l/7*WAP
*'J91»J)' Jl^XPSSAP^'JOA^'XJTJJPSSUJP
i£fi£Jf'X?T>*P$AP^/dt*'A?ntnSfUJP^fiE^'^HlffiSSAP^/$j)*x,"jaf6titt!P
^'1SMM>5WP
ftHNO.
HIH2H3H4H5H6H7H8H9H1OH11H12H13H13H14H14
S1S2S3S4S5S6
R1R2R3R4R5R6R7R8R9RIOR11R12R13R14R15R16
P1P2P3P4P5P6P7P8P9P10P11P12P13P14P15P16P17
C1C2C3C4C5C6
N1N2
;£/£ (°C
100.0100.0920.0880.0605.0605.0554.0554.0280.0280.0280 0132.3132.31323100.0100.0
20.0240.8240.8258.82588400.0
40.040.040.040.0
350.0350.0350.0350.0350.0350.0350.0350.0350.0450.0450.0450.0
620.0620.0525.7525.7464.3464.3200.0200.0260.0260.0100.0100.0100.0100.0100.0100.0100.0
20.050.020.050.020.050.0
E^(atg)
40.340.340.240.039.839.839.839.839.839.739.739.739.739.739.639.5
47.047.046.046.046.046.0
47.047.047.047.047.046.346.246.146.046.045.345.345.345 345.045.0
39.639.539.539.439.439.339.239.139.038.938.838.70.5
38.738.70.50.5
5.05.05.04.75.04.9
1 *
0.06900. 06900.06900.06900.06900 06900.06900.06900.0690
00.06900.06900.06900.06900.06900.0690
0.05580.05580.05580.05580.04520.0452
0.00620.0036
00.00980.00980.00980.00980.00980.00980.04520.0550
00.05500.05500.05500.0550
0.05500.05500.05500.05500.05500.05500.05500.05500.05500.05500.05500.05500.00340.00370.00020.00360.0035
0.09210.09210.32890.32890.21220.2122
00
100.0100.0920.0880.0605.0605.0554.0554.0282.8282.8282.8136.6136.61323100.0100.0
20.0240.8240.8258.8258.8400.0
40.040.040.040.0
350.0350.0350.0350.0350.0350.0350.0350.0350.0450.0450.0450.0
620.0620.0525.7525.7464.3464.3200.0200.0260.0260.0100.0100.0100.0100.0100.0100.0100.0
20.050.020.050.020.050.0
E^(atg)
40.340.340.240.039.839.839.839.839.839 739.739.739.739.739.639.5
47.047.046.046.046.046.0
47.047.047.047.047.046.346.246.146.046.045.345.345.345.345.045.0
39.639.539.439.439.439.339.239.139.038.938.838.70.5
38.738.70.50.5
504.95.04.65.04.9
i f i * (kg/s)
0. 20700.20700.20700 20700.20700. 20700.20700.20700.2070
00.20700.20700.20700 20700. 20700. 2070
016560.16560.16560.16560. 13560. 1356
0.01850.0109
00.02940.02940.02940.02940.02940.02940.13560.1650
00. 16500.16500.16500.1650
0.16500. 16500.16500.16500.16500.16500.16500.16500.16500.16500.16500.16500.01030.01110.00070.01090.0104
0.27630.27630.98670.98670.63660.6366
00
(kcal/kR)
21247.8247.8668.4668.4765.1
H e
100100100100100100100100100100100100100100100100
000000
0000000000000000
00000000000000000
000000
00
CH4
0000000000000000
000000
10069.0786.2286.2286.2286.22862286.2286.22
018.7018.7018.7018.7018.7018.70
5.445.445.445.445.445.446.306.306.306.309.509.50
1000.130.13
69.070.13
000000
00
H 2 0
0000000000000000
100100100100100100
000000000
10078.3078.3078.3078.3078.3078.30
47.7847.7847.7847.7847.7847.7839.5439.5435.4535.452.602.60
00000
100100100100100100
00
RI-Tech 96-053
at£
0.30.30.20.09.89.89.89.89.89 79 79.79.79.79.69J>j
7.07.06.06.06.06.0
7.07.07.07.07.06.36.26.16.06.05.35.35.35.35.05.0
9.69.59.49.49.49.39.29.19.0B.9B.88.70.5B.7B.7D.50.5
5.04.9
5J4.65.04.9
5*t4(kg/s)
0.20700.20700.20700.20700.20700.20700. 20700. 20700.2070
00 20700. 20700.20700 20700. 20700. 2070
0.16560.16560.16560. 16560. 13560. 1356
0.01850.0109
00.02940.02940.02940.02940.02940.02940.13560.1650
00.16500.16500.16500.1650
0.16500.16500.16500.16500.16500.16500.16500.16500.16500. 16500.16500.16500.01030.01110.00070.01090.0104
0.27630.27630.98670.9867
_ 0.63660.6366
00
I'/Mfc' -(kcal/kg)
21247.8247.8668.4668.4765.1
He
100100100100100100100100100100100100100100100100
000000
0000000000000000
00000000000000000
000000
00
CH4
0000000000000000
000000
10069.0786.2286.2286.2286.22862286.2286.22
018.7018.7018.7018.7018.7018.70
5.445.445.445.445.445.446.306.306.306.309.509.50100
0.130.1369.070.13
000000
00
H 2 O
0000000000000000
100100100100100100
000000000
10078.30783078.3078.30783078 30
47.7847.7847.7847.7847.7847.7839.5439.5435.4535.452.602.60
00000
100100100100100100
00
H 2
0000000000000000
000000
030.6313.6513.6513.6513.6513.65
. 13.6513.65
02972.972.972 972.972 97
37.1037.1037.1037.1037.1037.1042.9542.9547.0447.0470.9870.98
098.9198.9130.6398.91
000000
00
CO
0000000000000000
000000
00.300.130.130.130.130.130.13013
00.030.030.030.030.030.03
3.923.923.923.923.923.924.544.540.450.450.680.68
00.960.960.300.96
000000
00
CO2
0000000000000000
000000
0000000000000000
5.765.765.765.765.765.766676.6710.7510.7516.2316.23
00000
000000
00
N2
0000000000000000
000000
0000000000000000
00000000000000000
000000
100100
31 ~ 32
JAERI-Tech 96-053
Table 4.3
M0«'x)io»8AnMMJUntttfttiP*&«i&KSfAP
ITSffiP§AP
miuJADSUP
7k^tt»AP7k^WMttiP
MMJ'Jl&iflSAP
*mrjit f t*&*An
* ^ W » A P7k?ftftllttP
.£4aSADftttiP
&*tifi&«AP**iii«ft«Hip
flUM'XttffiKttP{&**** aEW^ffiPJKIftttffilloSfclln' <n* XJlftfillffflJjoWiKAP
K4«l«fflfrlto**M* <fn" *£3fEKt«l*AP
MlMlMl
^ttijyi»li5i*4A'XAPi/BttSTkJKfcAPW * • * « « * » £
ffifMnKlln'ta'jlff»ftDlft»AnM*4to»*fajp
* f c * » ^ $ * A P
7kffi«&K«ttiP
ffifMnttwiipra»fflHDM»AD
SfiM'XftlPllAP^/fcft'x&jflSftupCOfcrtn^APCQXtiLizimai^'A^fgKAa£fil*'x.'tttt»tta^»M«AP#*tt»l»ttiP(CH4)
MMl
*3»ftD7OAPM'JUSHMftAP
MXMAQ
*M»'*ft»ttAPAWA»'A»»»ttlPSfiU'JltftfMlAP£/£*'*&lPSf ffi PSfftft'ttttftttAP£tt»'a»ffitlttJP
«fcB*MUlPS**'JUH**HJP
HIH2H3H4H5H6H7K8H9momiH12H13HI 3H14H14
S1S2S3S4S5S6
R1R2R3R4R5R6R7R8R9RIOR11.R12R13R14R15R16
PIP2P3P4P5P6P7R8P9P10P11P12P13P14P15P16P17
C1C2C3C4C5C6
N1N2
;s^ cc:
100.0100.0920.0880.0609.5609.5558.5558.5280.0280.0280.0129.8129.8129.8100.0100.0
20.0240.8240.8258.8258.8400.0
40.040.040.040.0
350.0350.0350.0350.0350.0350.0350.0350.0350.0450.0450.0450.0
623.8623.8528.3528.34631463.1200.0200.0260.0260.0100.0100.0100.0100.0100.0100.0100.0
20.050.020.050.020.050.0
Eifc(atg)
40.340.340.240.039.839.839.839.839.839.739.739.739.739.739.639.5
47.047.046.046.046.046.0
47.047.047.047.047.046.346.246.146.046.045.345.345.345.345.045.0
39.639.539.539.439.439.339.239.139.038.938.838.70.5
38.738.70.50.5
5.05.05.04.75.04.9
Stt(kB/$)
0.06900.06900.06900.06900.06900.06900.06900.06900.0690
00.06900.06.900.06900.06900.06900.0690
0.05670.05670.05670.05670.04520.0452
0.00640.0035
00.00990.00990.00990.00990.00990.00990.04520.0551
00.05510.05510.05510.0551
0.05510.05510.05510.05510.05510.05510.05510.05510.05510.05510.05510.05510.00330.00370.00020.00350.0035
0.08520.08520.32480.32480.21010.2101
00
&£ cc:
100.0100.0920.0880.0609.5609.5558.5558.5285.0285.0285.0137.5137.5129.8100.0100.0
20.0240.8240.8258.8258.8400.0
40.040.040.040.0
350.0350.0350.0350.0350.0350.0350.0350.0350.0450.0450.0450.0
623.8623.8528.3528.3463.1463.1200.0200.0260.0260.0100.0100.0100.0100.0100.0100.0100.0
20.050.020.050.020.050.0
Estate;
40.340.340.240.039.839.839.839 839 839 739.739.739.739.739.639.5
47.047.046.046.046.046<0
47.047.047.047.047.046.346.246.146.046.045.345.345.345.345.045.0
39.639.539.539.439.439.339.239.139.038.938.838.70.5
38.738.70.50.5
5.04.95.04.65.04.9
3SE*(kB/s)
0.20700. 20700.20700.20700.20700. 20700. 20700. 20700. 2070
00. 20700. 20700. 20700. 20700. 20700. 2070
0.16700.16700.16700.16700. 13560. 1356
0.01910.0105
00.02970.02970.02970.02970.02970.02970.13560.1652
00.16520.16520 16520. 1652
0.16520.16520.16520.16520.16520 16520.16520.16520.16520.16520.16520. 16520.01000.01100.00050.01050.0105
0.25550.25550.97440.97440. 63030. 6303
00
i>m' -(kcal/ke)
21247.8247.8668.4668.4765.1
H e
100100100100100100100100100100100100100100100100
000000
0000000000000000
00000000000000000
000000
00
CH4
0000000000000000
000000
90.0673.4382.5682 5682.5682.5682.5682.5682 56
016.4416.4416.4416.4416.4416.44
5.365.365.365.365.365 366.216.216.216.219.349.34
1000.130.13
73.430.13
000000
00
C 2H
4.
2.2.2.2.2.2.2.
0.0.0.0.0.0.
1
Tech 96-053
H e
100100100100100100100100100100100100100100100100
000000
0000000000000000
00000000000000000
000000
00
CH4
0000000000000000
000000
90.0673.4382.5682.5682.5682.5682.5682.5682.56
016 4416.4416.4416.4416.4416.44
5.365.365.365.365.365.366.216.216.216.219.349.34100
0.130.1373.430.13
000000
00
C2H
4.
2.2.2.2.2.2.2.
0.0.0.0.0.0.
6
0000000000000000
000000
930717171717171710545454545454
00000000000000000
000000
00
C3 H
I
3.
0.0.0.00.0.
8
0000000000000000
000000
300818181818181810363636363636
00000000000000000
000000
00
nC4H10
0000000000000000
000000
0.960
0.530.530.530.530.530.530.53
00.110.110.110.110. 110.11
000000Q0000000000
000000
00
*flf$ (K)iC4H10
00000000000ft0000
000000
0.750
0.410.410.410.410.410.410.41
00.080.080.080.080.080.08
00000000000000000
000000
00
H 20
0000000000000000
100100100100100100
000000000
10080.0680.0680.0680.0680.0680.06
47.7947.7947.7947.7947.7947.7939.5139.5135.2435.242.602.60
00000
100100100100100100
00
H 2
26.11.11.11.11.11.11.11.
2.2.2.2.2.2.
36.36.36.36.36.36.42.42.46.46.70.70.
98.98.26.98.
0000000000000000
000000
030868686868686860383838383838
747474747474575783834444086863086
000000
00
CO
0.0.0.0.0.000.
0.0.0.0.0.0.
4.4.4.4.4.4.4.4.0.0.0.0.
1.1.0.1.
0000000000000000
00000*0
027121212121212120030303030303
090909090909747447477171001012701
000000
00
CO
6666666611111616
2
0000000000000000
000000
0000000000000000
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000000
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0000000000000000
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100100
2- 33 ~ 34
JAERI-Tech 96-053
Table 4.4
B:(B-A)/A
°C°C°C°C°Ckcal/kg°Ckcal/kg°Ckg/skg/sKW
620526350450173
0.6680.6290.0550.05514.49
624528350450
. 1760.6610.6310.0550.05514.56
1.85%
0. 48%
P<C
°Ckcal/kg°Ckcal/kg°Ckg/skg/sKW
526464
40350282
0.6650.7390.0550.0109.41
52846340
350283
0.6590.7720.0550.0109.91
0.46%
5.38%
°C°C°C°C
kcal/kgt:kcal/kg°Ckg/skg/sKW
464200
2050
2810.679
10.0550.32941.32
4632002050281
0.6721
0.0550.32540.80
-0.17%
-1.25%
°C°C°C
°Ckcal/kg'Ckcal/kgt:kg/skg/sKW
2601002050
1350.723
10.0550.21226.66
2601002050135
0.7151
0.0550.21026.40
0.00%
-0.99%
— 35
JAERI-Tech 96-053
(a) (C)
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36
JAERI-Tech 96-053
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Av
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41 —
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(7LUD/6>|)
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JAERI-Tech 96-053
40.
35.
30.
25.
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0.5 6
(m)
Fig.4.11
__ 46 —
JAERI-Tech 96-053
5. 1
q= In (
T-T4
T2=T1-qIn (r2/rL)
2nLXi2
In (r3/r2) 1( 2nr3La
(5.1)
Tl
T4
rl
r2
r3
X 12
A 23
a
T2
CO
(m)
(m)
(m)
# $ (kcal/hm°C)
m (kcal/hm°C)
(°C)
' 1 ^
8 8 0
4 0
0. 2 3 5
0 . 4 5
0 . 4 8
0. 6 4
1 7 . 3
1 0
1 8 5
4 0 0
8 8 0
4 0
0 . 4 0 5
0 . 6 5
0 . 6 9
0 . 6 4
1 7 . 3
1 0
1 8 0
4 0 0
4 o o ° c4 0 0°C
— 47
JAERI-Tech 96-053
8 8 0°C
9 0 0 °C
5. 2
Fig. 5.
5 . 3
(1)(a)
m
__--
kg/cm2
kg/cm2
kg/cm2
°C
°C
°C
'Ml ^A^X
5 0
5 0
7
4 0 0
4 0 0
9 0 0
t
CDCD :
t«=PDi/ (200a 1.2P)
Di
at.
SCMV4
5 Okg/cm2
4 0 0°C
9 0 0mm
1 1 . 9 kg/mm2
3 0 mm
1 . 0
2 . 5 mm
— 48 —
U
JAERI-Tech 96-053
: 1 9 . 4 Omm
: 1 9 . 4 0 mm
(2)(a)
(b)
(200<7.T? -0.2P)
K=l/6[2KD/2/h)"2]
: t
t .
t ,t2
SCMV4
5 0 kg/cm2
4 0 0°C
4 0 0mm
2 2 5mm
1
1 1 . 9 kg/mm2
3 0 mm
1 . 0
2 . 5 mm
1 8 . 9 9mm
1 8 . 9 9mm
(3)(a)
( 2 0 0 c r . 77 -
Di
SFVAF22B
5 0 kg/cm2
4 0 0°C
2 3 7 . 2 mm
1 2 . 1 kg/mm2
3 0 mm
1 . 0
5 . 0 3 mm
SFVAF22B
5 0 kg/cm2
4 0 0°C
5 0 0mm
1 2 . 1 kg/mm2
3 0 mm
1 . 0
1 0 . 6 0 mm
49
JAERI-Tech 96-053
(4)
mwi} n 12 & g 211J I S B 8 2 4 3 W £ S 2 7 7 > iS
77>yfffi^ SFVAF 2 2 B
SCMV4
S N B 1 6
Mi©ff2tfc 1 a
•BXfsj utl/TjQ_yj r V.K5/CU1 /
sow*®
^ Zm. <7 f » ( k g / m m 2 )
fi^^fflimJ^cr r (kg/mm2)
& Zmt7a (kg/mm2)
Sr^^f f lZm^<7b (kg/mm2)
^ Zm<7 n , (kg/mm2)
ftSffifflSSla. (kg/mm2)
5 0
4 0 0
1 3 . 3
1 2 . 1
1 5 . 4
1 5 . 4
1 3 . 1
1 1. 9
*OUh4i,C>R©iIg
77-XT-y hWS&S
A
B
cG
(mm)
(mm)
(mm)
(ram)
1 3 8 0
9 6 0
1 2 6 0
1 0 4 4 . 0 6
50
JAERI-Tech 96-053
7 =7 y :J1%lm<-
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ii7,*r»j bWi
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jfxTy bmc
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(mm)
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(mm)
(mm)
(kg)
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M
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(kg)
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(kg
(kg
0 0
9 7
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• mm)
• mm)
M D
Me
MT
5
7
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=
5
8
0
9
/
3
6
5
1
6
1
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9
8
8
8
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h
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9
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1 0
5 2 9
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7 1
0 0
mm)
3 2 0
5 4 8
2 0 5
7 3
8 0
7 5
— 51
JAERI-Tech 96-053
% Wi h / h o
& £fc gi / g o
^7-it^^IE^^ f
& £fc F& £* T
^ *fr V
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{£ ££ Z
££ *& d
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0 . 8 8 3 9
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(kg/miD2)
= 8 . 7
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§•£
1.
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5
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(kg/mm2)
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1 2. 1
(kg/mm2)
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1 9. 6
1 3 . 3
1 3 . 3
1 3 . 3
1 3 . 3
52 —
JAERI-Tech 96-053
(5)
(a) r#£i£ii4&«!flijj mu&m- -.t i = P D o / (200O-.7? - 0 . 8 P )
t .
7 kg/cm2
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4 0 O°C
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4 0 mm
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2 8 . 2 mm
2 8 . 2 mm
53 —
JAERI-Tech 96-053
(2)(a)(b)
t*=PDK/ ( 2 0 0 < J . ?? -0.2P)
K=l/6[2+(D/2/h)"2]
tfcH-fflffi
g D
t K
t ,
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5 0 kg/cm2
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1
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(3)
(a)
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5 0 kg/cm2
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5 0 kg/cm2
4 0 0°C
5 0 Omm
1 2 . 1 kg/mm2
4 0 mm
1. 0
1 0 . 6 0 mm
— 54
JAERI-Tech 96-053
(4)
J I S B 8 2 4 3 7 5 >iS
S F V A F 2 2 B
SCMV4
S N B 1 6
iI©M 1 a
MuZj&ffiEtl P (kg/cm2)
"£ iSa (»(kg/mm2)
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Sf?{^fflS^ab (kg/mm2)
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117**r "j hW/$)fcl G (mm)
1 8 2 0
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55 —
JAERI-Tech 96-053
77>yfic
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(mm)
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mm)
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8 5 2
4 5
9 8
0 0
— 56 ~
JAERI-Tech 96-053
& & h/ho
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•f? ^r IT
££ $[ V
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1
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— 57 —
JAERI-Tech 96-053
(5)
(a)t i = P D 0 / ( 2 0 0 a . ?? - 0 . 8 P )
£ Dc
t,
-f X R
7 kg/cm2
9 0 0°C
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1. 0
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58
JAERI-Tech 96-053
Fig. 5.1
59
JAERI-Tech 96-053
6. ftffiiJ,£
(l)
(3)
(2) M/h U
Table
— 60
JAERI-Tech 96-053
CO
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JAERI-Tech 96-053
CO
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JAERI-Tech 96-053
'&y??&z$&&&}&&y?&&&$$#S8&ivXi&
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Fig.6.
— 64
JAERI-Tech 96-053
7 . ft
en
kf/i 96kg/cm2G 7/50
°C 900/400
kg/s 0. 055/0. 069
AP °C 450/880°C 620/605
CH4 (AP/ tUP) wet 18. 7/5. 44H20 wet mol% 78. 3/47. 8
H2 (AP/WP) wet mol% 2. 97/37.1CO (AP/WP) wet mol% 0. 03/3. 92
C02 (AP/tUP) wet 0. 0/5. 75kg/cm2 5. 40 /0 .18
mm 360x5
mm 960x30
mm 165.2x16
mm 76.3x3mm 17.3x3mm 185.2x5mm 0. 5HxQ. 5Wxl0pitch
mm8770Hx28.45gap
S V Nm3/m3h 31501
mm 370x5013000H
14 800 HSCMV4
800 HX ij - SUS304TP
8oo H
65 —
JAERI-Tech 96-053
(2)
ttm
kW/; 288kg/cm2G 7/50
CM'J/JPfJ) °C 900/400
flftj kg/s
A P °C°C
CH4 ( A P / W P ) wet rnolXH?0 ( A P / t H P ) wet molXH, wet molX
CO (AP/WP) wet molXCO, ( A P / t H P ) wet mol%
kg/cm2
0.165/0.207450/880
620/605
18. 7/5. 4478. 3/47. 82. 97/37. 1
0. 03/3. 920. 0/5. 75
5.40/0. 18
mmmm
mm
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3
mm 8770HX28. 45gapSV Nm3/m3h 3150
710x5013000H
800 HSCMV4
> z i p - r 800 HSUS304TP
8oo H
66
JAERI-Tech 96-053
8.
8.
f f c ^
^>o (Fig. 8.
8. 2 b
T,-T4
In (rz/ri) In (r3/r2) 1
2nraLa
q
Ti
r.
&ft (kcal/h)
S (m)
8. 2»l^f o
67
JAERI-Tech 96-053
r2 9Vm
r3 9\-W\
A .2 Hfrfft
A 2 3 ?m
a 9\-Wi
L fe^
F*l« (m)
H^?l (m)tf^fe#$ (kcal/hm°C)mfc^ (kcal/hm°C)vmrnmimm (kcai/hm2ooMMg. ( m )
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q
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0. 4 8m
0. 6 4kcal/hm°C
1 7 . 3kcal/hm°C
1 0 0 0kcal/hm2OC
9m
4 6 7 0 Okcal/h ( 5 4 kW)
9 OkW
A : ,
A 23
L
q
8 8 0°C
37°C ( 3 2 - 4 2 )
0. 4 0 5m
0. 6 5m
0 . 6 9m
0. 6 4kcal/hm°C
1 7 . 3kcal/hm°C
1 0 0 0kcal/hm2oC
9m
6 4 1 0 Okcal/h ( 7 5 kW)
1 2 OkW
— 68 ~
JAERI-Tech 96-053
ISi^~'^"
Fig.8.1
Fig.8.2
— 69
JAERI-Tech 96-053
9.
IS: btz
c , HEND
— 70 —
JAERI-Tech 96-053
(1)
P^MMMiOWM \ N JAERI-Review 95016(1995).
(2) HTTRig^^Pf^^ : MM (msMmm^^m¥ $ 6 ^ 1 2/3 2 6 B)
(3) K. HADA et al. : "Plant Arrangement and Operational Procedure of HTTR with Heat
Utilization System", 1st Research Coordination Meeting for the Coordinated Research
Programme of Design and Evaluation of Heat Utilization Systems for the HTTR, Tokai
Research Establishment of the JAERI, 9-11 Nov.(1994).
(4) S. Saito et al. : "Design of High-Temperature Engineering Test Reactor (HTTR)".
JAERI 1332(1994).
(5) mm-Bit: B^m+tt^Mk, 38> 834. (1996)(6) rmmn-~iMfo(D^m'mmi. a*mm¥£, P.35-59(1991).(7) M7E3S0J : .'^^mmm^y h V ^ J W,2WL, P672 — 673, 675—676(1994).
(8) Gnielinski,v : Forsch.-Ing-Wes. 41(1975)Nr. 5. S. 145/153
(9) \^$&- W YfrifcfomX] . S * ^ « ^ ^ . p53~55(1980).
(10) Vornehm,L :Z. VDI 80(1936)22 S. 702.
(11) mit^m : i~!ft£&£ta:H-^> h V y ^ J m2m, P968~972(1994).
(12) m.lt$t&) : l^mmm^y h V y ^ J m2m, P674~678(1994).
(13) r>ffc1*X^fcEj &tl$.1&. it^H^W,^, P261.P337C1992).
(14) -gtemfc: r f i ^ f t | § M / K I I ^ ^ ! i S O 3 £ a # t t J ^m^^m, Vol25,No. 4, P261(1982).
(is) [*mm&Wtmmm%k^-'7 (HENDED
©HIIE^MJ B^^T-^W^Pir. JAERI 1333, P18, 41-44(1995).(16) r ^ X ^ J I J ejcITSHg. it^JL^m^, P242(1992).(17) <^m : \^Z^mm^y HVy^J m2KS. P675-676(1994).(is) rxmffi&Wt^mmmji-?0
(HENDED
(Dmmmi a*m::£tiWRffi* JAERI 1333, PIS,41-44(1995).
(19) MTyfclB : "fi^JftlSt9:fh^> h V y ^ J ^2HS> P672-673(1994).
(20) r ^ ^ X ^ j g m j *H5)iS, ^ ^ X ^ m ^ s P355-356(1992).
(21) rAM*i&«HSHIiE^tt;U-r (HENDEL)
(D^mm] B*m?tlW2ffix> JAERI 1333, P41-44(1995).
(22) AIChE Journal, Vol.35, No. 1, plOO~plOK1989), Fig. 3, Fig. 5
71 —
m