planta de relicuefaccion en buque metanero

7/13/2019 Planta de Relicuefaccion en Buque Metanero

1/152


2/152


3/152

Q aac a a aa,

aba.

Ea aac a E Q, ca,

ca a aa ca c a a aa

cb aa c. A aac a cabac a L M

M, cc R, cc aaa a ca a

a ca aa a ac.

P aac a ca a C Naca Ea a

a c, ca a Ma A, a cca

a c a c, Rc P, bca a

cc a, aba aa a ba ac, Ica P

cac c L M, Saa G aac aa a

acc.


4/152

I

R Abac ........................................................................................................ VII

DOCUMENTO 1 MEMORIA

Ca 1 OBJETIVO Y ALCANCE ...................................................................................... 2Ca 2 ANTECEDENTES ............................................................................................... 3

2.1 Mca GNL ..................................................................................................... 3

2.1.1 Icc ..................................................................................................... 32.1.2 La a a aa .............................................................................. 32.1.3 Sac ca ...................................................................................... 6

2.2 B a .................................................................................................. 92.3 Tca cacc ............................................................................... 11

2.3.1 Pc aca .......................................................................................... 122.3.2 E cc Ba I .................................................................................. 132.3.3 Vaa aa ................................................................................... 15

Ca 3 SELECCIN ..................................................................................................... 173.1 Dcc caaa a aa cacc ................................... 17

3.1.1 Jaa ............................................................................................................... 18

3.1.2 Tacb ......................................................................................................... 203.1.3 Ma I .............................................................................................................. 223.1.4 EcR ............................................................................................................. 243.1.5 Ma III ............................................................................................................ 253.1.6 HGS LabGI .................................................................................................... 27


5/152

II

3.1.7 TGE LabGI..................................................................................................... 283.2 Pc cc ............................................................................................. 29

3.2.1 C cc ..................................................................................... 293.2.2 Sa caa ..................................................................................... 333.2.3 Jcac a cc ............................................................................. 35

Ca 4 SIMULACIN .................................................................................................. 394.1 Dcc a ac ................................................................................. 394.2 Da aa a ac ....................................................................................... 42

4.2.1 Vaa ............................................................................................................... 434.2.2 Icaba cacaa b .............................................................. 444.2.3 C ................................................................................................... 444.2.4 Icaba aca aa .............................................................. 444.2.5 Oa ccac .................................................................................... 45

4.3 Cac aca ................................................................................. 454.4 Cac a a ................................................................................ 484.5 Cac caa ....................................................................................... 504.6 Acaac b a a ................................................................................ 51

Ca 5 DISEO ........................................................................................................... 545.1 Dcc .................................................................................... 54

5.1.1 C BOG ......................................................................................... 545.1.2 C/a ................................................................ 565.1.3 Vaa ............................................................................................................... 585.1.4 Icaba cc ............................................................................. 595.1.5 Icaba cacaa b .............................................................. 615.1.6 Saa a/ a ............................................... 62


6/152

III

5.2 Dcc a aac ................................................................................. 635.2.1 Dc ...................................................................................................... 635.2.2 Sa c ......................................................................................... 665.2.3 Raca ................................................................................................... 67

Ca 6 CONCLUSIONES ............................................................................................. 69Ca 7 REFERENCIAS Y BIBLIOGRAFA....................................................................... 70

7.1 Rca cca ....................................................................................... 707.2. Bbaa ........................................................................................................... 727.3 Dcc cca ....................................................................................... 75

DOCUMENTO 2 ESTUDIO ECONMICO

Ca 1 PRESUPUESTO ............................................................................................... 77Ca 2 AHORRO ECONMICO................................................................................... 79

DOCUMENTO 3 ANEXOS

A A TABLA DE COMPARACIN ................................................................................ 85

A B SIMULACIONES Y RESULTADOS ........................................................................ 88

A C SIMULACIN DE LA PLANTA

A D INFORMACIN DE LOS EQUIPOS


7/152

IV

DOCUMENTO 1 MEMORIA

Fa 1: R bca a aa a a Ibca 5

Fa 2: C a a aa c a aca 6

Fa 3: Iac a aa Eaa 8

Fa 4: Cc Ba aaa T 14

Fa 5: Daaa a aa Jaa 19

Fa 6: Daaa a aa Tacb 21

Fa 7: Daaa a aa Ma I 23

Fa 8: Daaa a aa EcR 25

Fa 9: Daaa a aa Ma III 26

Fa 10: Daaa a aa HGS LabGI 27

Fa 11: Daaa a aa TGE LabGI 29

Fa 12: Daaa T aa cc a ac 41

Fa 13: Ra c GNL a c 46Fa 14: C cc a cc BOG 47

Fa 15: Vaac a a GNL 49

Fa 16: Vaac caa 50

Fa 17: Vaac caa aa 51

Fa 18: T c caa a 55

Fa 19: Ca aa a c/a 57

Fa 20: Ca aa c Ma I 58

Fa 21: Icaba cc aca aa 60

Fa 22: B MOSS 63

Fa 23: Paa b 64

Fa 24: Va aa b 65


8/152

V


Fa 1: C ca b a aa 19, 20 21 80


9/152

VI

DOCUMENTO 1 MEMORIA

Taba 1: Tca cacc b 13

Taba 2: Caac cca cca cacc b 17

Taba 3: DAFO ca cacc 34

Taba 4: Cc cca aa a ac 43

Taba 5: Cc BOG 46

Taba 6: Cc cca ac aa a ac 48


Taba 1: I ca 78

Taba 2: Da aa c ac 81

Taba 3: C ca c cbb 82

Taba 4: A cc a a a 83


10/152

VII

E c caa a aa cacc b a, ac

a ca , a c caacca ca cca ca. La ca a

A (ASPENTECH), ca c c a aab. Baa

caac, a a a a cacc

aaa a a a, c aa aca

aa b a cca.

T c ca ac ba LNG , a a

c a , a c a

a a cc caacc. T c a a A

(ASPENTECH), ca c a aab. Ba

ca , a ac ba

c c aa aaa aa a

ca .


11/152


12/152

2

1

E b c a a aa cacc a a ac A (ASPENTECH), a cc a aab

cca cca aa aac a b b a.

Paa aac caa a a ca cca a

aa ca ca c a c aa aa

aaa c a.

S aa a ba bbca a ac ca

cca ac a c, cba a aca

a c caa a ac, a c a aaa

c ac, ca, ba a a a

aca ac b: a caa, a caa.

Paa aa ca a ba cc cb a aaa

c a DAFO (ba, aaa, aa, a).

S aa a aaa c

aa, c a aca a ac, cba

c baac c.

S aa a ca c aa,

cc a a a a aa aa b

a MOSS aa cca (140 000 3) ca a.


13/152

3

2

2.1.1

E ac aca a c aca a a aa a ba. La

c a ca a ca aa ca a

c c aa a a a [1].

E acab, cab, a aa a a aa a

ca a ca c. E a aa abc c a

aaa, ca a a caa a baa,

a cc a ca a a a aa

c cbb baa aa .

Paa a ac c a a ca baaa a bab a

a caba a ca ca a ac

cbb caa c aca a aaa,

aca c aca a ca ca a c

ab.

2.1.2

E a aa aca c a aa a cc a

cca. S aa a a ca aa abaaa c

a a aac.


14/152

4

La aac a ca a aa ca GNL ca

a acaaa a ca ba. E a cc aa

c a caa cc a c aa cc,

a aaca.

E a c ac a a cc

ac aa.

Na a c cc c aa a

ac a aa . Paa aa a ac a

cc aa a a aa cacc, a aa

163 C a a a aca, c cab a a a

a . E a a ca aaca a a cc a a

a a aa. La c a a aca

a aaca b a a aa ca

cc ( a aa) 630 c a a

aa caa caa cbb c aa aca.

Paa a a b a aa aa

aa GNL a ba aa. L b caa

aa a a cacc, c a aa

a (12 aba). Ua caa, aca a a

aca a a a cca. Ca a a

caa a a caa a a a acac.

E Eaa a a acac, aa a ccc

a . E ca a c a ac

cbb. E a a 1 a a a aa acac

ca aca a a a a, c a

ac a ca.


15/152

5

FEE: C E, 2009 2

F 1: I

L b aaca a ca a aa caa c

a a cc cc ca, a 40 000

150000 , a a ca aaa 12 000 /. La ba accaa aa a c c c GNL. D

aaca, a aa ccaa. Gaca a

aa aa a cb a, GNL a aa

a a aa bc a a a c.

La aa a GNL a a ac c

aa ca aa a a a aca. P a c a

aac a ca, b c a a

a c ba ac. E a a 2 a caa

c.


16/152

6

FEE: G I 3

F 2: C

A, a cca c a aa ba a ca a

c. P caba a a a a

ca a aacc.

Ua a GNL c aa

aa a. E GNL aab a aa

a cc. P , bca a a c Eaa ca c

a ca aa cc a ac cc.

2.1.3

E a 2008 a a cacc cca a Sa Ga

Ma. E c a H Hb, c ca a EE UU,

c 58 % a [4].


17/152

7

A a a ac c, a cab a c ca

a aa. E a aa 24 % c a aa 2009

25,5 % a a. Ua a GNL a

a ca ca 8 %, a cc ac a

. E GNL c a acaa 28 % ca aca

a aca ac a ca ba, aa

aca a c Ea [6].

La c a Ucaa a a a a a a ca

a, ca ac a

a. E c, a c (Pa Ibca) c GNL a aca [7]. Eaa 2008 a a

ac GNL a . A a Eaa 75,03 %

a b a c GNL [8].

La cc GNL a a a a a aa baa a

a c, c a aa aca, a a cca

c aa c c a a GNL,

a c caaca aa cacc. La cc 2008

ca 20 % a a ac, a ca aca a ccc

a aa acac aa M (Aa), T La

Paa (Ia Caaa). La caaca aaca a a GNL

aa acaa 2 487 000 a ccc 12 a

150 000 caa [2].

S caa 2008 a 28,7 10() aa 494

b, ca ac, c a . E

2009 a caa 27 10(), ac aa c

ac [6].

E a a a a a Eaa cc

c a, c a c c a Ea.


18/152

8

Eaa cb caa ac c Aa, c a ca

35,4 % a ca 42,8 % c c GNL, a CORES. Oa

Na, Pa G, Ta Tba, E ca a a

a a aa c a ca 55 %, ca ac

GNL c aa aa cbb [9]. A, 2009

ca ca ac Na Ga

Ecaa a a Eaa a a c GNL [8]. La

a 3 ca a aa 2010 cca.

FEE: C , 2010 9

F 3: I E


19/152

9

2.2

La cc ca a aaca a aa ac

a c.

E GNL aa a 163 C b c cac b, a aa

ca aa aa a cc. A a aaca,

a b a a a a a a aca a

aa a, a [3]. E cab, a

ca a ab ba, a .

P a ca a b a c b

cc ca ca a, a aa

c a ac b cac a a caa. L aa

a ca ca.

E ac c a b a b a baa

aa aa a a a cc a aac ca ac c a baa aa.

A, aa c a caa GNL

aa a ccca a aa ca a cc.

P a b aa a ca acaa cbb a

aa. E ca ba aa ca c,

cc c aac aa . E c a

( aa aa BOG), a a a a cbb

ca, aa a a aa

a a a. E a a a a a acac BOG

a a cab. E a acaa, a cc a

ca 0,15 % a caa aa b a a, a caa

a a 0,3 % a.


20/152

10

La aac c ca a. Da a caa

caa GNL a a, aa a cc

a a ca a a

a caa aa a c , a a a caa.

E ca a: a baa. L

a aa a ca a

b aa . L a a ca bac aa

a cca a aaca a

cc BOG a (0,1 % a) a a aa c a a

.

L b aaca Eaa ca 25 000

270 000 caaca. D , b 270 000

a a acaa a a aa acac

aca. E Eaa cb aa a.

C a a BOG, b a a a

aa caa ac a aa a , c a aa

a ba aca BOG c cbb aa

aa b a. EL BOG b a

c. La aa a a b

ba a a aca, caba cbb

ba a. E ab a ba a ba a, c

b a a, aca a ca c

aa a .

Oa c a a a ca a

cbb baa, a ca ac, aaca

caa. E a a cca ca. E cab

c a a bac a a aa. A,

BOG a a ca aca.


21/152

11

P ab a a cc, c

cb a. E BOG a a cbb baa

a a. E a a a ca a ca b,

a c c a BOG a c.

S ba, ba a ca aca a a cbb

a baa a c c, a b a a

aa a ca BOG. Ea a a ba a cc

a ca ca a cc

a. La a a ac ca

ca BOG aa ca a a.

La c a aa a a aaca, a ca

c a a ca a a caa caa aa

a, aca c cbb a a

c aa a .

2.3

La ca a cacc a ac a 70, a

b GNL, a c. Ea

ca aa a aba a aba c

cc ca aa ba, a 0,3 W/ [11].

P a c aca a ca a

cc a cc ca c aaa a

a . S c a a, cc cacaa

cc ca . S cc aba aa a aa

ca ca a a c caa a aac.


22/152

12

D c a a a ca c c cc a

aa a ca. La cac c aa

aa a aac aa b a a a a a

acac a b a 2000.

2.3.1

S a aa a c a aca a ba

ca. L a b QF (210 000

) QMa (270 000

) ca ab aa cacc aca BOG a

c c a a c c a

ac a.

S ba, b aa a aa cacc LNG Jaa

a 2000, ca aa aa a a O c Ja Ca

11 000 . E b caba a a ac a MOSS cc a, a a

c aaaa c [10].

Ca a ca cacc, acc a a

ca abca a a a aa, a

aba a aba 1 b aa aa a aac b a

aa Eaa.

E a a a a cc aa ca a

aa ca a aa b. A, a a abca

a a ca aa cac a ca ac

c.


23/152

13

1:

Licencia Empresa Ao Proceso

JamalOsaka Gas 2000 Brayton inverso

Tractebel Tractebel 2004 Brayton inverso

Mark IHamworthy 2006 Brayton inverso

EcoRelCryostar 2008 Brayton inverso

Mark IIIHamworthy 2008 Brayton inverso

Mark III Laby-GIHamworthy 2009 Brayton inverso

TGE Laby-GITractebel 2009 Cascada

La aba 1 a a ca ca a ac a c

a cc Ba a c a.

C c a c a c ca, cc cacaa

c a a cc. E cab, c

a aca ba a cc b, b ca a

a a a a c ac c.

2.3.2

E cc Ba a a c, caa a

a ba aa a c, c aba. E c cab a a aa a aba a

c a acc ca.

La a 4 a cc Ba aaa aaa

c. Saa a a a ca caca c aaa.


24/152

14

FEE: H 14

F 4: C B

E a aa 1 2 c a a a 4 aa a c

aa a c aa a a. La c

a a aa a a ca c a ac.

P a c a a a cac (aa 2 3) c

a aaa c ac a

aa a , aa a a a 4 aaa a a 4. E

a a a ca a a aca c a,

aa aba a aa a c.

E a ca aca a a , ca aba

baa . E a cc aab a

, cbb, c bc ca ba

a.


25/152

15

2.3.3

La aa a a aa cacc a ba c a

b aac a ac aa b.

P aa c cc c cbb a a

a, aca cbb baa c.

S ac cca a a caa, a

ca a caa aa a. La caa a GNL

aa a a a c.

A, c GNL c c aca a

bc c ba a a a. E

a ca a , aa a a

a cc , ca a ca

Ea U, a a aa c ca a ca c

a acac.

La aa c c , c

cc b ab ca a a c . La ac a

a ca b a a Ha, c a aa a ca

b QF QMa, a a ca ab aa

ca c a c cca a BOG a

b.

La a Qaaa 2 EMb c a a aa a aac a

aa ca c a Ma I, a

b QFL. Paa QMa b c,

a a a Ha.

S a ba c cc a c c a a a

ca caa a, a c a aa ab a ca. E b a


26/152

16

a aa a a a b a

a a ca a a c.

E cab, a a a b, aa, a a

a.

E , aa a a cc a a b

c, acca a ca a c ca aaa aa a

c b aa.


27/152

17

3

3.1

La aac a caac a a ca a c caa a

a a abca bca aca a a cca

b.

Paa a a cca a aa a caac a

cc a caa a a aba 2. La ac baa

b a ca c abca a aa

a . La aba ca c a a

ac. E A A c a aba ca, a a aca

ca a: c a .

2: C

TECNOLOGAS Jamal TGE Mark I EcoRel Mark III HGSLaby-GITGE

Laby-GI

CONSUMO DEPOTENCIA (MW) 3 4,875 5,8 6 4,9 6 -

Consumo unitario(fabricante) (kWh/t) 1000 780 852,94 857,14 720,59 882,35 -

Consumo unitario(simulacin) (kWh/t) 1193,1 666,5 824,3 917,4 937,8 1013,1 1741,67

Diferencia19,31% -14,55% -3,36% 7,03% 30,14% 14,82%

SISTEMA DEPROPULSIN

Turbinasde vaporde hlicesimple

Turbinasde vaporde hlicesimple

Motordiesel debajavelocidadde hlicedoble



Motor decombustindual

Motor decombustindual

BOG (t/h mx.) 3 6,25 6,8 7 6,8 6,8

FEE: D 10,11, 13,15,18


28/152

18

La ac caa c, a a ac a a, a

aa c a c a c caa c a

c abca. E a ca c c aa

caa a. Dca ac a aa ab aa

ca ca c, caa aa a

bc a aa bca, a c

A B, ab c a caa ac.

3.1.1

E b LNG Jaa a aac a ca. Uaba

c ca cc Ba aba a

aac a.

E a ca a ac a ba a a aa, aa ca

a caa cca aa ab a . E ca a BOG ccaa aca a caa aa a

aa a ba. E cc a BOG ca a a a aa

a caa a cbb c baa.

E c ac cca BOG a aaca aca a

c c cca aa a BOG aca a caa

ca a. L c cca aa,

a ac cca a cc a. E

cc a caa c ca . E ca

a b aa c a a a c c. La

c aa a a a ba a

a caa caa.


29/152

19

E a a c c caba

, a a aa ca. Paa aca ca a aa

a.

Ua c a c a , caa a,

ca a aa cc. Ea c cc:

a , ca ba GNL. E

a ca aa a a 3,5 MPa aa 0,65 MPa.

P cc aca a caa a a cac.

E aaa a a a 5.

FEE: EAMA, H 10

F 5: D J

E BOG c aa 0,45 MPa ca. D aca

aa a/ aa. E GNL a


30/152

20

a ba a a a cac

ca caba , aa ac c a,

acc a aa a cb a caa a.

E c ca a a caa aa a b

ab a a caa aa a a aa c

. La ca aa aa c c a. E ba

a a c cc , a c a

aca aa a aa a aa a a ba.

P c a aa a aca aca aa

a aa, a ca c BOG, a a

aa c cca. E cab, a caa a a

a aca ca b cca.

3.1.2

E c ab baa cc Ba c c

ccca a cc a a ca

ca. La aa a a aa b 228 000 .

E BOG c a c aa 0,3 MPa 0,6 MPa, c

c cca, c caa, ca

caba ca. E caba ca a a caa a c a c ba ca aa 50 C

170 C. C a baa, a cac BOG aa a

c aa aa, ac a a

ca c.

E c b a a cc aa a caba, a

b aca c a aa, a ac a


31/152

21

a caa a BOG ca. P a

a a ca a a.

La a 6 a aaa c.

FEE: GEDMEE, KD. 11

F 6: D

E c b c aa c ac

a caba cacaa b aa aa ab c aa

a. S c caba cc aa acaa

aa 80 C 110 C.

E a a aca a ba a ca a a

a ca aa c a La aa


32/152

22

acaa a 170 C. Ic a c a

a caa a.

Tab a aa aa a a aa a a

c. E BOG c a aa caa

ca GNL, a ca a aa

a aa. E ca ca a a a a aa a aa,

a ba a abc a aaca. E

a c ac a a b LNG Jaa aa c a

aa a.

La aca ca aca 5 %

a . E cab, caba cc a

25 % c cca a c cc,

, b a a a c cc. S ca

c BOG aca, . S a a aaa

ca a, a ca a aac a a cb

ca a aa a a ab.

3.1.3

Ea aa aa c a ca b QF 210 000

aaca. E c cabac a caa Qaaa 2

EMb bcaba a a ca b

a a a ca, cb c a

b c a baa ca.

E c c BOG aa aa a a a caa a. A

a c a aa a aa ca ca

a a ba acca a, ca a a aa. E


33/152

23

c aa cc aa aa a

a a c.

E a a 7 aaa .

E GNL aa ca c a aa BOG. E BOG ca a ca

c caba cc ca, a a

aa a a a, a ca c a, GNL

a a . La caa a ca c:

caba cc, ca aa a/.

E c aa 5,8 MPa a aa c

a aa 110 C. E a a a c aa 1,55 MPa a

aa aa 163 C.

FEE: ADE, . 15

F 7: D M I


34/152

24

E c a aca ca aa a, c

cca a aa b b a aca. A c a

a cb a a c aa. Ua

a a cb (CGU, ) a aaa aa ca

ca c BOG c a caa a aa

a aa a aa.

3.1.4

La aa EcR, a a a a, aa aa cb a ca

caba a a Qaaa 2 EMb aa a

a, QF QMa. Ea cc aa aa b QMa,

266 000 caaca, a a Ca.

E BOG ca c aa aa, ca c

ac a a cc c ca

caba, aa a a cca ba. E c a

caba ac ab cacaa b

ca caba cc. A, caba ac

ab a b cab aa, a

b a a a a aa aa a.

E c caba ca a caa a,

a aa ca. E cab

c BOG c caba a ca c

aa , aa a aa .

Paa a aac c a a a a 8.


35/152

25

FEE: C 16

F 8: D E

E a ba a a a

a ca a, aa. Paa caa c a

c a aa, a aa a aa a aa, a

ca a ca aca aa aa

a c a a CGU.

3.1.5

Ea aa a a a a Ma I c a c c c

ca aa c aaa aa b QMa ab

a.


36/152

26

E a a c c BOG aca a caa

caba ca caa aa c ca c aa

a. Paa a acac ca caba cacaa

b, a a c aa caa a aa BOG a

c.

E BOG a aa ab caba caa ca, a

a a a caa a.

P a aa a a caacca a a Ma I. S

a a a 9.

FEE: H 13

F 9: D M III


37/152

27

3.1.

La a aa a aa a cb a,

ca c c a a, aa a ca ca

a a cbb a c ca

ca Bca.

La aa ca a a Ma III, c a cc c

a BOG c a aa aa a. Db

a c c ca a.

E aaa a a 10.

FEE: MA B& 18

F 10: D HG LGI


38/152

28

3.1.

Ea aa a caacca ca a cc Ba,

c cacaa c a cca ca.

La aa, a a HGS LabGI, aa c a c a

cb a a c ca a. Pa

BOG a a aa a aa a aa ca.

Paa aa c aaa a a a 11.

E ca cc cacaa . E c

c , a c aa a aa 40 C,

a aa ca. D c

caba aa a a c aa c

c LabGI aa 30C. Ua a acaa a aa

c aa aa ca c baa . Ma, BOG

aca c LabGI aa c 3 aa aa. E ca c aa a BOG aa ca a

100 C 0,45 MPa. E BOG baa a a a aa ca

aa G/L aa.


39/152

29

FEE: MA B& 18

F 11: D GE LGI

C ccca cab a c c

ca, c a

a cc Ba a a cbb c a. A,

aa ac a a c cc

a .

3.2

3.2.1

Paa a cc acaa a aa cacc b a

ab c a caaca a cac


40/152

30

a a aab cc ac a aa. La ca

ba a aa , caac c a

a aca, ca c cab aa

cc a a ccaca a a .

E a aa cacc a a a c a cc

a a cca ca c. E a ca, a a

ac baa aba a c caa a

ca. E cab, b a a ac a aac aa

b a aa a, a a a cc ccaa

a ac b .

E b a ac a ac

ca. Paa a cc a aa b, a

a c c ac. L c b

a a ac a a b acc a a a

a c c.

E c a a

cca, a ac caca a aa. E cab, a ca

ac c a aa

a a a acaa a aa ca a ccaa

.

L c c a c cc c

cacaa. E 0,5 0,4 W/ GNL c, cab,

a c a 0,8 W/. La cca c

ac a a caaca c aa a aa

a .

S ba, a a a a

c, ca a a a a a. C

ccca ac a a a


41/152

31

aa acac. T caa ac ca aa a

aac a aa. P ca, a c N

c.

E a a a 30 a a bca a

cc ca a a ba aa a aac a

aaa acaa aa a. Aa aac a

caa a cca c a a (c ),

a a a aac c a (, a,

c.), a GNL aa aa aa caa. E cab,

a cc a , c a cba aaa a aa b.

La a ac a b a. E a a

cbb a a ca a a a a. Paa a

cc a aa acaa a a ca a ac

a a aab. E a c

a c a aca a

a c, ac cac a, a

. Cc a aa

acab c a cc a c

ac .

La aa ab a aa ba a

aa. Faca aa a aa a c

a a a ca b aba. La

aab aca a a aac ca ab ca

ca caa a aa.

La ba a ac ab aa cc ca

a a. La caa caa aaa b caba a

cc a aa aca a a cc aba a aa,

b ab a cc ca.


42/152

32

Ua cc a c a aa a

ba a, aa a aa aa a b.

Ua a aa a caba aca aa c

caba cc a c ab

aa cc, b a a a c, c

aa . La aa a aa aca a a ca

caba a caa aa b a a.

E acab a a abca c aa ca

ca aa cc aab, c aa

a c aa aaa. Ua a cc ab acc a aba a aa c. C

ccca, ac a a cc a ac

aa a a aa a ca b.

S b a ac a a acac ca , c

baac a bac ca a a, b ca aa

c a aa.

C a c c c c aca

b a (IGC c), a caa Qaaa 2 a EMb ca a

ca aa a cc a aaa [15]. E c, b

a a c cca a c c a

, ca cc ca aa c.

E c a aa a caa a cacc ca

a aa a aa c a c aa ca a

a a ba aca a. E

c a b a aa b cca, c,

0,16 % a . A, a aa b c c a

a aca aa aa b a a aa, ca

ca a a a c (c,

bba ba) 2100 % a.


43/152

33

C a aca, a c aa a aa a c,

a ca a c a ,

ab a a aa cb a, aac a

a c BOG c ac a.

3.2.2

A a a a a aa acaa aa b a a a

a aba DAFO (aba 3) ac a cc c aca ca

a a aca caa .

La cc a, c c a, a aa c a a

b a aa , 140 000 .

E a a aa a ca caa c LabGI, ab

a a b a aa cca a .

Aaa c TGE LabGI, a c cacaa, cbac

c c LabGI bca a aa a. E c

a BOG c cbb aa cb

c a baa. HGS LabGI ab a c,

ca c c Ma III. Ab ca c a aa

a c b c a

a ba ca a cbb aa ca. E

a c a BOG c c caa .

Caa c a ba a, c c

aa a aa, c a aa

aac b a , a 210000 , caa BOG c aa a c.


44/152

34

3: DAF

TECNOLOGAS Debilidades Amenazas Fortalezas Oportunidades

Jamal

Alto consumo Poca flexibilidad Pocos equiposPuesto enfuncionamiento

Muchas tuberasDiseo para un

buque pequeoEquipos conocidos

Utiliza tecnologasadicionalesespecializadas

Ligero Aprovechable parapropulsin

No muy compacto

Tractebel

Utiliza un sistemacomplejo pararegular el gas deflash

Poca flexibilidad Muy bajo consumo Equipos conocidos

Diseo para grandesbuques

No aprovechablepara propulsin Pocos equipos

Ligero

Compacto

Mark I

Diseo para grandes

buques

Bajo consumo Puesto en

funcionamientoCompacto Equipos conocidos

Flexibilidad con GNL

Aprovechable parapropulsin

EcoRel


Equipos pococonocidos

Compacto Puesto enfuncionamiento

No aprovechablepara propulsin

Flexibilidad connitrgeno

Mark III

Mucho volumenMejora el consumode Mark I

Mejora flexibilidad deMark I

Utiliza muchosequipos Equipos conocidos


Aprovechable parapropulsin

HGS Laby-GI

Alto consumo Alterna con otrocombustibleDiseo para grandesbuques

Equipos conocidos

Mucho volumen

TGE Laby-GI

Alto consumo Alterna con otrocombustible


Equipos conocidos

Mucho volumen

Ofrece pocaseguridad

E c TGE LabGI cacaa, a a a cbb

a a aca, c a cc cc

ac. E c a a c aca a a

a, ac a aac a c

a a ac cc. N aca aa a aac

b aa, a a c.


45/152

35

Ab c LabGI, a a c cc aa a ac BOG

b c ca a aa a aac b

cca. E c c a a

a BOG ca c,

baa a ac c c a caa

BOG a a aa c a aca a b

aa.

3.2.3

E c Jaa, a caacca c

a aa b 135 000 caaca ac a ba

aaa cc. Cab aca a aa ca a aa a

cc, a aa a a a a b a. E b

aca 2001 a aa cca a baa aa

a aa.

La aa aa aa aa baa c BOG. E c

c cbb ca aca aaaa. Ea

cac a aa b c aca a ba

a a aa b. A a c ca a aa a

c a c a

c, c a a ca aaa

ca b c a aa a c.

La c c ab a aa a, a

c a a cbb baa

ca c, c a c c b QF

QMa a ca.


46/152

36

S ba, a a a cc c c,

baa a aa a aa a ca, a aa ba a ac.

E BOG a caba aca ca, a

c caba a a, , a ca

BOG bcaa c a a a caa. E ba ab

a a aa Tacb ca a cc.

E ab a a c a aa caa c

aa. S ba, a a a b a

ca b, aa ba a ba

a ca.

E c Tacb a c cc , a a

ccca a a a aa c, a a c

c ca, a c caba ca,

c c a a ca. E a a ca c

a ba cc aa aaaa ba ba a a

ac c, EcR Ma I.

Ma I EcR aa aca aa c, ca

a aa a a ba. La aa EcR a caba

cacaa b a c a aa BOG a caba

cc. C ccca, c a aa

caba ac, , ca a aa a

a ba a a aac. E c Ma I a ab

a ca c GNL c a c, c a

a aa a c ca a a aa aa. E a

c a a ba aca ca cab

ab c.

L a ba aaa aa a ac a aa aa

b aa cc, cac b a a ba. E

c ba ca a, Ca a


47/152

37

aa a c aa aa EcR. L a aa

aa a a ba ac a aa

a c. E cab, ca c a ca

GNL cabaa cc.

Paa c a a ac a c a

GNL, a b aa aca a a acac,

c a a ba ca c a aa ba. E

a ca ac a a ca a,

abaca a b ac. E c a

aa a a c a aa a aa c a aa aab a a ac c GNL.

P c ca Ma III a ,

c Ma I c . La c 15 %

c cc ca abca ac b a

bac a a . A, a cba

c a a a ac.

P b aa abaa c a aac Ma I, caa

c c a a aa a a a

ac c cca baa a ac caca

a aa, ba . La aa ca Ma I a a

ba cca b a abaa a c

aca aa a aac, a ca a baa abca a

b aa Qaaa EMb cc cca .

L c c a c ca

a aac cb c a

a cc ab a. E a ,

a .


48/152

38

A, a ab a, cc

ca a cac c, , c Ba

c c a, a caca

ac a caa. E b a ac

a a c a ba aca a caba. L

c a a ac aca c a a aa caba,

a aa ac a caa c, a

ab a aa c c a b.


49/152

39

La ac a aa a a a cab a A P. La aa abaa c c c aa c

a a c ac c aa cc a

ca a aa.

C a a c a a a aa ca, acaa a a

caacca b aa , a aa b a

a aa a cc.

E c ca c a ba ca

ca a b aa a 140000 caaca GNL, aaa a a a a aa, c a

caa BOG a 80 aa aa ac a a

a. L b a a Eaa ca 40 000 caaca

aa 270 000 c, ca ca

aa cacc .

E A C aaa c a c a. La

aa ca aba baaa c Ma I a a

aac a ca a aa a aac b

aa.

E a aa, BOG c a (BOG01) aa c

(C101). S a a aa a a caacca caa BOG

0,95 /. Pa a a c a a aa

a a aa ca a a a aa


50/152

40

caba. La ac a a cab a aa ca (M101),

a a GNL c c (LNG03).

A c a BOG a a aa c a a aa

cab c. E GNL a a aa a

ac ca c a c BOG a c

caba. E BOG a, c c c

(C101) c aa 400 Pa, ac c

aa. L c a ac a

c a ba a a. E c a a a

aa GNL a a aa (M101). La a (S202) c a aaa aa c (C101) caba ca

cc aca aa (E202).

C a c, a c BOG c c (BOG04)

c caba ca (E202) a 400 Pa 100,6 C. E a ac

caba ca aa a a a aa

a aa (E201, E202, E203). E caba aca aa c

ca aa b a c a caa a

caba.

E BOG (BOG06) a caba (E203) a 160 C c ca

a ca aac a/ (S201). A aac a a c

a a (FLASH) a c GNL (LNG01), a ca a cca

(LNG03) aca caba ca (E101) a aa cc a

aa a a (LNG02). La GNL 150 Pa,

a a a, a a aa.

E GNL cc a 166,5 C aca a aaca. Q a

ac ac a ba bc cb a

caa c a a ( ca) GNL

a ba.


51/152

41

Paa cc ca a ca 11,8 /, c aa aa

a cacc c c c. La a 12 ba

aaa T aa cc a.

F 12: D

C a ca, cc Ba c aa aa

aa 5,75 MPa. La c (N201) a

c (C301) c c a 1,6:1,

c caba cacaa b (E301) a c aa

aa (H2O03).

E aa c a (H2O01) a a 25 C 1 a ba caa 45 /

bba (P301) aca caba c aaa (H2O03, H2O04,

200

10

100

0

0

0

100

10

2000 100 1000 00 0


52/152

42

H2O05). E ca aa c a aa aa a

ac a aa a ca 40 C

a a ca ca a 15 C a aa a a (H2O09).

E aa a a aa c ac aa

acaa a aa a aa 35 C (N2O07). D ca

c caba ca cc (E201, E202) a aa

118 C (N209). Ea c cc a a ba a (T301)

aa ca aa 163 C 1,3 MPa.

E a (N210) c a cac

caba cc (E203, E202, E201), a ac ca

BOG c c c (BOG04)

(N209)

La ac c cc c

c cc 716.6 W/ a aa 82 aa aa a

aa, caa c a c aca cca. E

cc c COP 1,13, 13 % ca a

a ca.

Paa a ac a ca a caacca a

a a aca aba. La cc a a

aba 4.


53/152

43

4: C

Buque 140 000 m3

BOR 0,14 % al da Gas natural

BOG 0,95 kg/s

temperatura -140 C Componente % mol

presin 1,15 bar

Metano 87,88

Nitrgeno Etano 0,01

caudal 11,8 kg/s Nitrgeno 12,11

Agua

caudal 45 kg/s

temperatura 25 C

presin 1 atm

La caaca b ca 140 000 , aa Eaa. S a

ca a aa c 0,14 % BOG a a, c a,

b a 0,95 /. M aa a a

a , ca aa ca ac a a

a caa.

4.2.1

A c, c a aa a a aa c a

a 160 C aa a c a aa 60 C. La caa

a 15 Pa c BOG a

aaa a 100 Pa 160 C.


54/152

44

4.2.2

E ca a caba c aa a, a a a ca ca

a aa aa a aa a 10 C, aa

35C aaa. A , a caa caa caba a a ca a 50 Pa.

4.2.3

T c cc c 0,8. E ca a a ba

a a a: 0,85.

E a c a 1,6. Aa

ca a 1,4 ca ca a a ba,

a abaa c a.

4.2.4

E caba a a c aa a

c aa aa a aab. Ca a aa

aa aca a ac cca a a abca.

E c 3 C a a caa 50 Pa aa caa

c a a a c.

E caba cc b a ca aa

b ab a c. S a acac abca ALPEMA, a

ca aa b 50 C, ,


55/152

45

ca c cab a, a ca a a a

[25].

E ca, caba c a

a, a cab a aa ca a aa. E

ca a cc b a.

4.2.5

S ca a bba aa a aa a

75 % a a 300 Pa a cc a. La c

aa c a, caba cca

ca caa caba acc a.

E aa a/ a 150 Pa aa, aa a

c a ccac aa. E ca a a aac a acc a aa

caba, a c c b caa c 93,3 %

ca aca a, , a a acc

6,7 % a aa a acac BOG.

La ca bc c ca a

a a a ccac a a a BOG. D a aa

c ca 0,84 / GNL c a ccac a a a

ca acaa 92,6 % a. E a a 13 a c.


56/152

46

F 13: GL

La ac a aa c ca ca c

a. C ccca, ca ca

a caba cc. Paa a ac ca c 0,95 /

BOG a 140 C 115 Pa, a a 11,8 /,

ca aa a aa c. E caa aa

ca aa a ca aa aa a 15 K.

C a a aba 5, a ca a aa,

a a cc a, c 87,88 % a a

12,11 % a aa a ac a.

5: C BG

GAS NATURAL LICUADO Ligero Medio Pesado

Etano 97,86 87,88 67,61 % mol

Propano 0 0,01 0,01 % mol

Nitrgeno 2,14 12,11 32,38 % mol

FEE: EL, E. 20

0%

10%

20%

30%

0%

0%

0%

0%

0%

0%

100%


57/152

47

E c a aa aca aa a a ac,

b a caaca a ca a cab, ccca

a a a ca aac (a a) c

, aa bc ca GNL Eaa.

La aac a cc aca ca a c cc a aa,

c a a a 14. Ua cc ca a caacca

a c c cc

cca a caaca caca a. La cc a a, 15 %

, a c aa ca b.

F 14: C BG

La cca GNL cca a cc a BOG b aca a a

aa. Db a a a a a cacc a ca

GNL Eaa ca a caa cb a a

cbb a caa.

1..

1103.2

. . .112.12 2.1

32.3

0.0

200.0

00.0

00.0

00.0

1000.0

1200.0

/. % %


58/152

48

E a a aa a aac aa c ca

a a GNL aca a a acac. M a

ab ca a cc a b aa cc

a aca a a cacc.

Da a ca a a caa GNL aa ca a ,

a BOG caa a a. E b

a cc aa BOG aa c ca

cab c a a acac a caa

cbb , caa a a ba.

E BOG a a , 0,06 % a, a a

aa acaa 70 C, a cc a

b. E a aba 6 a a cc a b a a

aa aa aa ac, ca

, aa a a GNL.

6: C

Temperatura (C) BOR ratio (kg/s)nitrgeno

(kg/s) agua (kg/s)Apertura de

vlvula

Cargado -160 0,16% 1,02 11,6 54 0%

Lastrado -100 0,06% 0,41 5,6 23 19,7%

La cc a caa b a

caa aa, a c caa GNL a a

caba a c c. E ac aa

cca b a a ca aa c

ac .


59/152

49

La a 15 a c b aa a aa a a a GNL

ca aca caba a ca c a

aa a a a aa c aa aa a aa a

a aa caba cc ca 100 C.

F 15: GL

La a aa aba c c a aac a

c a aa BOG a a aa c. S a a ab

a ca a ac ca c a a aa

caba cc. N ab a a c ab a

ca ca aa a aa, aca a a a b a

ba .

Ea caacca acaa a cc BOG. A

c ca a, a c ac abb ca

a c c a, abb ca a

c cab a.

10%

%

0%

%

10%

1%

20%

2%

30%

10 10 120 100

()


60/152

50

Ca caa BOG c ab c a (a ), a a

c b a c caa GNL. La

aac caa a ca a aa cab

10 C a a aa c. E cab, a a

caa GNL, a aac a aa c a ab

a a c , a ca a b

ca a a c cc 70 % a a.

Ia, ab b aa a cc a

aa ac. A , a a 16 a c b aa

a a 17 c caa aa aa caa BOG a a

aa c, aa a aa ca c aa

a a aa a c.

F 16:

10

11

12

13

1

0. 0. 1 1.2


61/152

51

F 17:

E a a aac caa aa a a ,

aa a a abb ca aa,

b ca a a ca aa caa c

a caa aa. S a a aa aa

ba 40 C, aa ca a cc aba. E cab,

caa aca ca a c c,

a c c a aa a.

E a ac a aa aa c, a ba a ac a

a aa Ma I a a Ha. E a a c a

aa a aa .

La aa c c bc a c aa a cc

aac b, c a a ca. E a aac caca, a

c a aa a. N ba, a

30

3

0

0

0. 0. 1 1.2


62/152

52

ca a aa c a a aac

a c c aa a.

E a ac aaa c c. Ma I a

, ca a c c, c a

a caa b c c caa BOG. U a

a caa BOG c.

E a ac ca c c aa a ac,

a c a a aa c caa

a . S a ca c c

abaaa c c ca, a a

.

La aa ca ca ab c acca a a aa a

a a a c GNL ca aa a ca. C a

, a aa ca a a a aa c a a

c b a a ba a aa,

caba cc a a cac. D a aa

ca a aa a caba aca aa, b a a

ca ca c, a a aa c.

S a a c EcR, a caba

cacaa b c, a c ,

b a GNL a cc a a cc,

a a a a ca a, a GNL c a

caa a a a ac cca a

c. E a EcR a caba ca a , c

c c ca c

c b .

E c aa ab ca a a a a

caba c a aa ca, aca a c c. N


63/152

53

c a , ac c a aca a

c. U a aa ca a aa acaa

ab a caba cc a c, a

aa baac aa caba.

S ca a a aa c c a caaca a a ca

cab a cc ca a ac a a,

cc a a a ca. E ca a a

c c a aa ca, a

cc ac.

P a, aa c a aa a c

c aa a a ba a a aa ab

aa a cc aa a a aa a cc a aa

a c, aa c ca a ca c

aa a/ c a.

E caa ab a a a

ca a aac a

ba, c a aa a a

c b cca. La aa ccac a a

caa ca cabaa caba aca aa, ca

c, ab ccaa a cc a aa.


64/152

54

5.1.1

E c BOG c c cca aa

a BOG aca caba cc a aa.

E c a ab ca a aa a aa a

BOG a a caa, c ac b cca, a a aa

a ba, a a cb aa a.

La aac caa a 1 600 / (1 /) b a aa

b, a ca 4:1. E a a 18 a a

ac c c a aab aa a aca Aa Cc. La c

acaa a c SC 6. E a c a

250000 EUR aa 1,3 a, 3 a 2 ac, c 3 900 .


65/152

55

FEE: A C 21

F 18:

S ba c abcac ac a aa aac.

Tab c a a a aa a a cc

a ca a aa a, ac

b abaa c.

A a a a a aa, b a a ac

ac a a a, a cc c caac

a cbb aa aca a ba a, c a

a a aca aa a caa cb,

a a ca a a aa aa c.


66/152

56

5.1.2 /

Ea a c aa c a a cc

ca a a a cca c a aa. E

a c 2 500 W a a a ca

ac aa.

La aa a aa aa

.

Ca a aa a a aa c

a c c c aa, a a c

aa c c a a aa a a aca a a

a a a aa c . L c a ba

c a ab cca, aa

c aa a a a.

E (a 19) a ca a ca ca aa c a a aa c ca aa a ba a,

ac c b a. C ccca a , a

ba aca c , a aa c a accaa c

cc aba a ba a.


67/152

57

FEE: A C 22

F 19: C /

Ta caa aa c a c aa aa

caba cacaa b, a a cacaa aa b

aa aa a aa aca a. E caba a

a c, c caa a a

19, c a 100 / aa caa . E A D cca

caa a caacca cca caba.

La acaa c a caa

a a 20, ca a aa c Ma I.


68/152

58

FEE: H

F 20: C M I

L ca c a 3 a, 7 a 4

ac, 45 000 , a ,

caba c aa. S c ca a

600000 EUR.

5.1.3

Ua aa ab ( ) baa c c

a a c a ca c aa


69/152

59

a ca a cc aa, acc a caa a a aa

.

L c b ca c aaa a

a aab . D , caba aca

aa a ca aa aa ca

c a aca a c.

E a a b a aa aa ca a a

c ca a a a aa.

5.1.4

L c cc aca c a ba cc

aa a ac. La caacca caca a caba

ac aab aa aa ac c a aac. T aa

20 % caba ac cacaa b, a baa

.

La aac aa a a a cab c

c. E a ac a a c cab

b a a ac aa a c a aca. E b a

a 21.

L abca c aa aaa a a a aa, a ca

aa a caba. E caba ca a aa

c a caaca aca c a a a.


70/152

60

FEE: C E & C 24

F 21: I

La a cca caba ba a a a c

cab c a a , aa

aa, a a a ac 1 400 /aaa.

S aa cac a c a:

cac, c caa aa.

Paa a aa caba aa, ca a a

1,9 c a cc 0,3 0,4 , c a c a ca

a 751 , ac a ac 3 300 / a. S c

ca a 200 000 EUR. E caba b ca a


71/152

61

aa c aa aa. Aca ccac

a A D.

C aba, caba a a (caa a)

ac a cab a aa (a). E a aaa cca

aa c ba, aa a aaa, a caca c

aa, aa cc . E ca ca

caba aca aa, aa a ba caa. La caa

a 3 ac, 2 a 6 a, a. E

caba aa caa a a

b.

Ta ca b a a a caba

caa cc, ba a c

aca ca b aa, b ca a cc

aca ca a ab c c. La

a a a c ca a c a c ba a

ac a c, aa c caba

a ca ca a a aa.

5.1.5

L caba a c TEMA

( , 6 ., 1978). L

a TEMA ca R a aa acac

c aca.

Paa a ac a a aa c

caba ca b ca c aa a aa a

aa. S a aa caba c aa a

, aab, c a a


72/152

62

caacca. S a a a a aa

b. L caba ac a cab a c 154 b

5,4 , 15 19 . La

a caba 6,35. E ca a aa aacaa caba.

E ca a a a a aa a a b aa

a a c. L a cacac TEMA AEL,

c cba ab, c a a cacaa ba a ab c

a cba, aca a a abaaa a a .

5.1. /

E a ca aa a, aaca acca

acaa aa a a. E acab ca a

a aa aa a a a c aa a. U a aca 7 a

0,5 .

E aa c a a cc aa a a b acc

cab c ccca a ac. E a

c a a acca a a aa a aa a a

CGU aa a. E ab, a aa ca aca

b a ca a.


73/152

63

5.2.1

La aac b baa baa ca cca a aa a

cba bac. E ba a ca ca b MOSS

a a aa. La aac ca

aca aaa ac b a a a a ac

cba.

Paa a aa a caca b MOSS,

a a c aac a aa aaa caa,

ac c a c GNL, c a a

a 22 a cba bac.

FEE: () AG 23

F 22: B M


74/152

64

E ac c c a c aa aba

a aa c c c a ca. E a a 23 a a 24

a a b bc a aa b a MOSS

aa aba a aa Jaa, ca

a a aa aa.

F 23:

E c a b c, aa c a ca a

aca , ca aca ac,

c cac c aa a aa a

a a b.

La a 24 a a a aa a aa a a ac c

aa a ba a. E c a a aa

aa aca a a a ba a, ca a a

a a. E cab a aca

a ba.


75/152

65

F 24:

E c caa cac a cac

aa a Jaa. E ca a caba

cacaa b aa a, ca aa a ac acaca aa . A ca aa a aca aa

c a a aca a a caa a.

L caba aca aa, c aa, aa

c a caa a, aa aa aa ca a

cac. La aa GNL ca aa cca a caa a a

c, aa aca acc c a a aa

ca.

E a, ca , aa, c BOG, caa a

aa c a a bac MOSS, c a

aca ac a aa a cac.


76/152

66

5.2.2

Paa aac a a bac a a ac a a

cab , c a a caa (aa,

a caa), aa a a aac, aa ca

a a b: a, a aa c a caa

a c . L a cca

c aa c.

E cab a aaca c a

aa c a a a a. E aa

a ba a bca a a caba a a

c aca a aa cab a a.

A, a a a a a a a c

a ba a ba caa.

S aca a ac a a aa a

c c a ca c ca a a

b a a c a a , a a a a a

a c ba b a a a a

. Na a aac aa a a c c

caa a aac c aa

a.

La aac cca b, b ca c

a bac c b . L

a c c a c ca aa a

a baac bac. L c

caba cacaa b aa a aa a

bac GLP GNL aa baa a

aa.


77/152

67

E caba aca aa, cc aab aa a

aac, a cca bac aa a cca bac

b, c aca c a bac cac aba

ba. A, a ca a a

c caba a, b a a cac a a a

caba ca.

5.2.3

C ab, a aa b c c a

ca a a c a aa.

C a aa cacc a aa ca c

a c a c a aac aa, a aa aa

ca , a a ba ca aa aaa,

ca aa a a c, BOG ba a a a

a ca a ba a a aa a .

Paa aa a aa aba a aa ca c c b

b ca c: b ca a aa aa b a

aca a, b aa a a

c a, aa aac a

ac, c a a cab caa aacaa b.

E c a a a aca a.

Paa c c, a a aaa aa a a

cb a CGU c a aca aca aa a aa. E c

aca b a (IGC, ) a

aca a c aa a c a

a, b aaa a a a

cb a. E ca a ba a c


78/152

68

a CGU a caa, c BOG aca a

caa cb a c cbb.

E c a a CGU c cab c caa

a ca, c c a caaca a caa,

baa a aca 1100 % aa a aa cacc c a CGU,

c aa aac a aa GNL, a a a

a a b a c aca a.


79/152

69

La c a a c c a a a a cc a aa cacc

a bac aca, a a a ac

aa aa a a a ca

aaa a BOG aa c a a.

Eca a a aca a aacc c aa a ca

ca ca ca a a,

ca aba a a ac [12]. A, c bc

cc a cca a a caa c, c

a ca.

S ba, aa a a aa aba, ca c

cbb aa a BOG a aa a a ac a

ba a. E ca ca, a a ca ca

a aa, a aaa c caa .


80/152

70

[1] OECD/EIA (2009): W , c.

[2] CNE (2009): Iac bca c a a.

[3] QUEROL, E (2007): Ga cbb, a a.

[4] RHL, C (2009): BP aca , c.

[5] RHL, C (2010): BP aca , c.

[6] BP (2010): BP aca , aa a.

[7] SEDIGAS (ca. 2009): E a .

[8] SEDIGAS (ca. 2009): E a Eaa.

[9] CORES (2010); B ac cab 146 (), aaa 4.

[10] HATANAKA, N; YONEYAMA, Hac; IRIE, Ta; MIHASHI, Taa; OKA,

Maa OHMORI, M (ca. 2001): A ca aac LNG a

21 c LNG Jaa: N LNG ca ac a.

[11] GERDSMEYER, KD.; HARRY ISALSKI, W. (ca.2004): Oba ac

LNG .

[12] RICHARDSON, A J.; ALSULAITI, Aba (ca. 2006): Cc a

ac ' a LNG .

[13] HAMWORTHY GAS SYSTEMS AS (ca. 2008): LNG a aca.


81/152

71

[14] HAMWORTHY GAS SYSTEMS AS (2009): O a ca Ba

a cc a LNG aca.

[15] ANDERSON, Ta N.; EHRHARDT, Ma E.; FOGLESONG, Rb E.; BOLTON,

T; JONES, Da RICHARDSON, A J.(2009): Sba ac a

LNG ca.

[16] CRYOSTAR (2007): Sca ac EcR Ca

Maa 10 ().

[17] HAMWORTHY GAS SYSTEMS AS (ca. 2010): LNG a .

[18] MAN DIESEL (ca. 2009): MEGI a MAN B&W : A cca,

aa a cc b a.

[19] TGE MARINE GAS ENGINEERING (ca. 2010): F a c a c b

a ac a LNG ca.

[20] QUEROL, E.; GONZALEZREGUERAL, B.; GARCATORRENT, J. GARCAMATNEZ,

M.J. (2010): B a (BOG) aa Sa aa a (LNG)a, b ..c/ca/a

[21] ATLAS COPCO (2208): SC a TP : c ca

c.

[22] ATLAS COPCO (2009): Ma .

[23] AGNCHILE (2004): Acac b a aa: a aaca.

[24] CHART ENERGY & CHEMICAL, INC. (2009): Iaa, a, a

aac c ca ba a a a ca, c

a a .

[25] ALPEMA (2000): T aa ba a a a ca

aac aca, a c.


82/152

72

[26] CNE ( a) 20100301: I a ca

aa a, (a).

[27] MAN B&G ( a) ca. 2010: LNG ca b ME a

ac.

[28] KWANG PIL, Ca; RAUSAND, Ma VATN, J ( a) 2007: Rab

a ac LNG ca, b

..c/ca/.

Ta a bbaa cac cc

AIR PRODUCTS AND CHEMICALS, INC. (2008): LNG c, b

://.ac.c

ATLAS COPCO (2008): GT a T : c ca c,

b ://.aacc.c//

ATLAS COPCO (2008): LNG : a a ba a.

ATLAS COPCO (2008): P : ca c a b.

ATLAS COPCO (2008): T H: ab a.

ATLAS COPCO (2009): D a c.

BARCLAY, Mca; DENTON, N (2005): Sc LNG c,

b ://.c.c/bca/c_a//LNJ09110534

36.

CHART ENERGY & CHEMICAL, INC. (2008): LNG c, b

://.ca.c


83/152

73

CHART ENERGY & CHEMICAL, INC. (2009): Ba a a ca.

CHART ENERGY & CHEMICAL, INC. (2009): C b aa, a, a

aac.

CHART ENERGY & CHEMICAL, INC. (ca. 2009): A a a ca.

CHELLINI, Rb (2008): LabGI c LNG ca c,

b ://.bcac.c

CONOCO PHILLIPS (2009): O caca c, b

://c.cc.c

DBI; Ra (2009): Ecc BOG a FLNG aca,

b ://.bcac.c/c128E.

GENERAL ELECTRIC (2005): Ca a aa c, b

://.aa.c/b/_aa//_//c

//c_c.

GUPTA, Paba Ka; KUSH, P.K. TIWARI, A (2006): D a a

c b a ca cc aca, b

..c/ca/cc.

HATANAKA, N; YONEYAMA, Hac IRIE, Ta (ca. 2001): T BOG

ac ba "LNG Jaa", b

://..//c2003/WGC_/10410_1045203324_415_1.

IACS (2008): Ia IMCO c cc a

ca a b, b

://.ac../c/bc/Pbca/U_a/PDF/U

I_GC_164.


84/152

74

KWANG PIL, Ca a. RAUSAND, Ma a. VATN, J (2007): Rab

a ac LNG ca, b

..c/ca/.

MAN B&G (ca. 2010): LNG ca b ME a ac,

b ://.ab.c

MARKUSSEN, Da (2004): T ca a ba a a

ca, b ://b.c/

NORDON CRYOGENIE (ca. 2009): A ca, b

://.c.c/

PAZ, Na (ca. 2006): B a, c aa a, b

://a.aaa.c

PILLARELLA, Ma a. LIU, YNa a. PETROWSKI, J a. BOWER, Ra

(ca. 2007): T C3MR ac cc: a a a , ca

LNG , b ://.a.c

SNCHEZ BARRIOS, Rc (ca. 2008): B a, a ba c,

b ://a.aaa.c

SANDSTRM, Rb E. a. BRAY, Wa H. a. BOURGOYNE, Da A. (ca.

2006): N a ba a LNG ca,

b ://.../

SHIN, Y; PYO LEE, Y (2008): D a b aa a ac

c LNG ca, b ..c/ca/a.

SKJEGGEDAL, O GASTECH (2009): O a ca Ba

a cc a LNG aca, b

://.a.c/PcS/OGa/GaS/FLNG/

THE LINDE GROUP (2009): LNG c, b ://..c/


85/152

75

THE LINDE GROUP (2009): L a c a

ca.

THE LINDE GROUP (ca. 2009): A a a ca.

TIMMERHAUS, K.D.; RIZZUTO, Ca (ca. 2008): Cc a

c, b ://..c

://.aa./., Acac abca caba

ca a aca aa a.

://.aacca.c/b__a_c/a., cc

c b.

://.baabaa.c/bb/ca/.a, ac b a aa

acac BBG Vcaa.

://.

.c//a_c/a__a_ca/. ,

Iac b caba aca aa.

://.aa.c/, ac b a aa acac Saa

Sa.

://.

.c//a_c/a__a_ca/. ,

Iac b caba aca aa.


86/152


87/152

77

1

S a ca a abca b a, b a a ca c c, a ca

aa a ac c a , a a

ca a c, b ac a a .

L caba cacaa b a 22 000 USD.

O , c a aaca aa

ac a a, b a a c. E c

caba ab ca a abcac, cac c

c a aa b a a caa b

aa. C ccca a aa caa a a a a

caba, c c a bba c a aa 20 000 USD.

E ca a a a ca a ac aaa

ac bca SccDc [28] Aca ca a

caa aa c b aca a IGC.

La a cab aca aa a ca ac, a

a caba . E ac a a ac a ac

c cab ca a aa a ca

ca 1 400 /.

Tab ca c

caba aa a ca aa a ac caa

aa c, ca .

E a aba 1 c a a ac ca c

a a aa, ca a aca a a ba caa a

aac.


88/152

78

1: I

Inversin

Equipos Coste en dlares Coste en euros Redundancia Costes finales

Compresores BOG 350 000,00 $ 253.623,19 2 x100% 507.246,38

Intercambiador criognico 280 000,00 $ 202.898,55 1 x100% 202.898,55

Compander 850 000,00 $ 615.942,03 2 x100% 1.231.884,06

Tuberas e instrumentacin 660 000,00 $ 478 260,87 1 x100% 478 260,87

Intercambiadores 60 000,00 $ 43 478,25 1 x100% 43 478,25

Otros equipos 20 000,00 $ 14 492,75 1 x100% 14 492,75

Unidad de combustin 2 000 000,00 $ 1 449 275,36 1 x100% 1 449 275,36

Mano de obra Coste en dlares Coste en euros Costes finales

Construccin e instalacin 6 000 000,00 $ 4 347 826,09 4 347 826,09

Total de la inversin 8 275 362,31

Divisa 1,38 $ / mar-10


89/152

79

2

L caacc a aac a aa cacc b a , a c ca GNL a

cc a a cbb baa.

E aa a b c a, c c a

cc c a ac. S a aca a a

caac a a cbb caa, c a,

ca aa a ba

, a c c ac a a a

a.

La ac ac c b aa , 140000 caaca, c a ca a 19 () a a 9,7 / (1 =

0,5144 /).

L a a Eaa aa ca Na, Qaa Ta Tba, a a a cca 9 000 aca. S a

ca a aca a a GNL a cca

c Lba E, a aa ac GNL c a.

E ca a c, a aa c a, b

c a c 2008, a ca. E B a ca a

2010 caba a 35 EUR/MW a CNE. E ca a aaa, c H Hb caba cca ,

a 9,91 EUR/MW, a a .

E Eaa, a a a a c a ca aa a, 17,7

EUR/MW c a CNE

[26].


90/152

80

Paa a ac c a a a c

ca a a cc a MAN B&W, 150

USD/ aa , 22 % ca aa a, c, 183 USD/. Ea

ca a ac, aa a aa

c cbb c a caa a

cca.

S a a 1, a a caaca a aaa b c aa

a a ca 26 000 W.

F: MA B& 27

F 1: C 19, 20 21

A a ca a aa c a

3000 W. S ca a c a , a


91/152

81

ccca aba. Ua ba a

c 35 %, a a a 50 %. M

aa a aa a a c

45%.A cac aa a a cc a aba 2

aa a aba 3 aba 4 aa a cc a a

ac a aa b 140 000 aa a a a.

2: D

Rendimiento turbina de vapor 0,3

Rendimiento motor diesel 0,45

PCS (MJ/kg) Precio (EUR/MWh)

Gas Natural 50 17,7

Fuelleo 41 9,5

Gasleo 43 11,1

Recorrido completo

9 000 km

257 h

91% Porcentaje de tiempo en viaje

Viaje 233 h

Trayecto 116,678 h


92/152

82

3: C

Turbina de vapor sin plantade relicuado

Turbina de vapor con plantade relicuado

Motor diesel con plantade relicuado

Consumo de PotenciaMotorCargado 26 000,00 kW 26 000,00 kW 26 000,00 kW

86 666,67 kW 86 666,67 kW 57 777,78 kW

Lastrado 26 000,00 kW 26 000,00 kW 26 000,00 kW86 666,67 kW 86 666,67 kW 57 777,78 kW

Sistemas auxiliaresCargado 3 000,00 kW 3 000,00 kW 3 000,00 kW

6 666,67 kW 6 666,67 kW 6 666,67 kW

Lastrado 3 000,00 kW 3 000,00 kW 3 000,00 kW6 666,67 kW 6 666,67 kW 6 666,67 kW

Planta

Cargado - kW 2 606,60 kW 2 606,60 kW

Lastrado - kW 1 303,70 kW 1 303,70 kW

Total requeridoCargado 93 333,33 kW 95 939,93 kW 67 051,04 kW

336 000,00 MJ/h 345 383,76 MJ/h 241 383,76 MJ/h

Lastrado 93 333,33 kW 94 637,03 kW 65 748,14 kW336 000,00 MJ/h 340 693,32 MJ/h 236 693,32 MJ/h

Consumo de CombustibleBOG disponible

cargado 1,02 kg/s - kg/s - kg/s183 600,00 MJ/h - MJ/h - MJ/h

lastrado 0,41 kg/s - kg/s - kg/s73 800,00 MJ/h - MJ/h - MJ/h

Energa necesariacargado 152 400,00 MJ/h 345 383,76 MJ/h 241 383,76 MJ/hlastrado 262 200,00 MJ/h 340 693,32 MJ/h 236 693,32 MJ/h

Costes de operacinCoste de FO

cargado 404,25 /h 916,14 /h - /hlastrado 695,49 /h 903,7 /h - /h

Coste de GO

cargado 469,99 /h 1.065,14 /h 744,41 /hlastrado 808,6 /h 1 050,67 /h 729,94 /h

Prdida de GNLcargado 1,02 kg/s 0,12 kg/s 0,12 kg/slastrado 0,41 kg/s 0,05 kg/s 0,05 kg/s

Coste por prdidacargado 902,7 /h 106,2 /h 106,2 /hlastrado 362,85 /h 44,25 /h 44,25 /h


93/152

83

4: A

Turbina de vapor sin plantade relicuado

Turbina de vapor con plantade relicuado

Motor diesel con planta derelicuado

Costes totales con FuelleoCostes de operacin

cargado 1 306,95 /h 1 022,34 /h - /h

lastrado 1 058,34 /h 947,95 /h - /h

Coste total por viaje 275 977,06 229 889,29 -

Ahorro por viaje 46 087,76

Costes totales con Gasleo

Costes de operacin

cargado 1 372,69 /h 1 171,34 /h 850,61 /h

lastrado 1 171,45 /h 1 094,92 /h 774,19 /h

Coste total por viaje 296 845,70 264 422,57 189 578,76

Ahorro por viaje 32 423,13 107 266,93


94/152


95/152


96/152

86

FABICANE O G, OLNG

H,

C,

H H B

B

AO 2000 2004 2006 2008 2008 2009 2009

CONMO DEOENCIA (M)

3 4,875 5,8 6 4,9 6

O A A A A A C

() ()

C () (/)

1193,1 666,5 824,3 917,4 937,8 1013,1 1741,67

19,31% 14,55% 3,36% 7,03% 30,14% 14,82%

IEMA DEOLIN

M

M

M

M

ALIMENACIN O C

2 3 2 3 3 4

BOG (/ .) 3 6,25 6,8 7 6,8 6,8

LIEFACCIN ,

,

BE LNG J M F M M

C 135.000 3 228.000 3 216.000 3 265.000 3 265.000 3 210.000 3 210.000 3D 11.000

COMONENE N N N N N N E,

EIO BOG 2 C

1 C 2 C ALACOCO

2 C COA

3 C ALACOCO

2 C. LGI

LGI

O C

.

I

I

I

C

INECAMB.CIOGNICO

I .C

CHA INDIE

. NODONCOGENIE

I. .C LINDE

. NODONCOGENIE

. NODONCOGENIE

O LNG, LNG

B LNG B LNG I, . B LNG

B LNG B LNG

EIOEFIGEANE

3 C 1 .L

3 C 1, ALA COCO

3 C 1 ALA COCO

3 C 1 COA"/1996"

3 C 1 ALA COCO

3 C 1 ALA COCO

LGI

O I ,

I ,

I ,

I ,

I ,

I ,

I ,

OO GC GC GC GC GC

/

/

/

/

/

/

F 300 3/ 700 3/

45C ; 37C

32C

DIMENIONE L M I 7 20,5

3 0

7 20,5

30


97/152

87

EDNDANCIA 2105% ,1105% .1125%

2100% , 1 ,1 N2

2100% , 1 ,1 N2

1100% , 2100% BOG

275% BOG E, 275%

OBEACIONE B

.

,

.

L, G/L. M

N2 .

C 15% MI

E .

E .

5,2 M BOG 100C.

I , .

.

16% BOG

L ,

E .

I , .

.

E .


98/152


99/152


100/152

209 210 211 212

301 203 202 201

202 301 203 202

:

/

2 0.6425478 0.6425478 0.6425478 0.6425478

4 0 0 0 0

26 0 0 0 0

38 0 0 0 0

410 0 0 0 0

2 0 0 0 0

2 1 1 1 1

4 0 0 0 0

26 0 0 0 0

38 0 0 0 0

410 0 0 0 0

2 0 0 0 0

/

2 18 18 18 18

4 0 0 0 0

26 0 0 0 0

38 0 0 0 0

410 0 0 0 0

2 0 0 0 0

2 1 1 1 1

4 0 0 0 0

26 0 0 0 0 38 0 0 0 0

410 0 0 0 0

2 0 0 0 0

/ 0.6425478 0.6425478 0.6425478 0.6425478

/ 18 18 18 18

/ 0.1388544 0.4608406 0.4619621 0.8271984

125 166.5124 166.5109 87.34464

57 12 12 12

1 0 .9 68 88 65 0 .9 71 38 12 1

0 0 .0 31 11 35 0 .0 28 61 87 0

0 0 0 0

/ 4366.493 5700.349 5690.232 3270.523

/ 155.8711 203.4859 203.1248 116.7482

2805.68 3662.747 3656.246 2101.468

/ 53863.84 51656.49 51561.6 34317.32

/ 1922.783 1843.987 1840.599 1225.029

/ 4.627495 1.394295 1.39091 0.7767759

/ 129.6322 39.05905 38.96424 21.7602

28.01348 28.01348 28.01348 28.01348

60 / 0.0344134 0.0344134 0.0344134 0.0344134


101/152

N207

N212

N208

N201

N210

BOG04

N211

N205N206 N203N204

N202

N209

BOG03

LNG01

BOG05

H2O05

H2008

H2O04

H2O07

H2O03

H2O06

H2O09

E201

E203

C303 C302

C301

T301

C102

E303E302

E301

M301

E202

BOG01

BOG06

BOG07

LNG02

C101

BOG02

B201

LNG03

1

W 2W

3

W 4

W

5

W

6

W

8

W


102/152


103/152

BOG01

N207

N201

BOG02 BOG03

N205

N206

N203

N204

N202

N209

H2O05H2008

H2O04

H2O07

H2O03

H2O06

H2O09

E201

C303 C302

C301

T201

C101

E303E302

E301

S

M301

N210

V201

BOG04

S302

BOG05

BOG06

1

W

2W3

W

4W

5W


104/152


105/152


106/152

BOG05

BOG06

N207

N212

N208

N201

N210

BOG08

N211

BOG09

N205

N206N203

N204 N202

N209

BOG07

BOG11

BOG10

H2O05H2008

H2O04

H2O07

H2O03

H2O06

H2O01

H2O09

C101

E201

E203

C303 C302

C301

T301

C102

S201

E303E302

E301

S301

M301

E202

P301

H2O02

S302

E101

BOG13

BOG12

M101

BOG02

BOG01

BOG03

1

W

2

W

3

W

4

W

5

W

6

W

7

W


107/152


108/152


109/152

BOG01

N207

N215

N201

N209

BOG05

BOG06

N205N206 N203

N204N202

N208

BOG04

BOG08

BOG07

H2O05

H2008H2O04

H2O07

H2O03

H2O06

H2O09

C101

C303C302

C301

T301C102

S201

E303 E302 E301

M301

E202

E101

M201

S202

N214

N210N213

BOG02 BOG03

N211

N212

E304

E201

Cryostar Ecorel

B1

1

B2


110/152


111/152


112/152

216

201

202

:

/

2 1.070913

4 0

26 0

38 0

410 0

2 0

2 1

4 0

26 0

38 0

410 0

2 0

/

2 30

4 0

26 0

38 0

410 0

2 0

2 1

4 0

26 0 38 0

410 0

2 0

/ 1.070913

/ 30

/ 3.148984

25.58625

7

1

0

0

/ 1472.904

/ 52.57841

1577.352

/ 21483.08

/ 766.8836

/ 0.3400821

/ 9.526882

28.01348

60 / 0.0573557


113/152


114/152


115/152


116/152


117/152


118/152


119/152

BOG09

BOG11

BOG10

H2O01

H2O02

C303

C302

S201

E301

E202

B1

B2

C331 C332

S311

PRO02

BOG08

S331

ETH09

PRO06

ETH07

PRO05

PRO01

ETH01B

ETH02

ETH01

ETH05

BOG06

BOG05

BOG02

BOG01

PRO03

B8

1

B9

PRO02B

B10

ETH03

Critical point:Methane: -82.1 C, 46.4 barEthylene: 9.9C, 50 bar.Propylene: 91.77 C, 46.19bar

B12

ETH08

PRO04B

B14

7

B15

ME-GI

E203

BOG07

ETH10

PRO04A

ETH01A

2

B4

B3

3

4

W

5

W

6W

8W

9W


120/152


121/152


122/152

207 208 209 210 211 212

201 202 301 203 202 201

303 201 202 301 203 202

:

/

01 0 0 0 0 0 0

01 0.4212258 0.4212258 0.4212258 0.4212258 0.4212258 0.4212258

01 0 0 0 0 0 0

01 0 0 0 0 0 0

0 0 0 0 0 0

01 0 0 0 0 0 0

01 1 1 1 1 1 1

01 0 0 0 0 0 0

01 0 0 0 0 0 0

0 0 0 0 0 0

/

01 0 0 0 0 0 0

01 11.8 11.8 11.8 11.8 11.8 11.8

01 0 0 0 0 0 0

01 0 0 0 0 0 0

0 0 0 0 0 0

01 0 0 0 0 0 0

01 1 1 1 1 1 1

01 0 0 0 0 0 0

01 0 0 0 0 0 0

0 0 0 0 0 0

. . . . . .

/ 11.8 11.8 11.8 11.8 11.8 11.8

/ 0.1893772 0.1203459 0.0970299 0.2964281 0.4260583 0.5656833

35.06961 79 118 163.1176 121.0823 79.32384

57 5 6.5 56 13 1 2.5 12 1 1 1 1 1 1

0 0 0 0 0 0

0 0 0 0 0 0

/ 293.3148 3027.647 4162.757 5475.907 4252.469 3037.073

/ 10.47049 108.0782 148.5984 195.474 151.8008 108.4147

123.5517 1275.323 1753.461 2306.593 1791.25 1279.293

/ 32538.29 45920.34 52372.98 50231.72 40488.67 33087.25

/ 1161.522 1639.223 1869.564 1793.127 1445.328 1181.119

/ 2.224269 3.500127 4.341192 1.421005 0.9886576 0.7446318

/ 62.30952 98.05074 121.6119 39.8073 27.69574 20.85973

28.01348 28.01348 28.01348 28.01348 28.01348 28.01348

60 / 0.0225599 0.0225599 0.0225599 0.0225599 0.0225599 0.0225599


123/152


124/152


125/152

Results Summary

Exchangers in parallel 3

Total length mm 1920.84

Exchanger width mm 342.10

Depth (Stack Height) mm 372.20

Effective length mm 1674.47

Effective width mm 319.10

Distributor length at end A mm 123.18

Distributor length at end B mm 123.18

Orientation vertical

Streams 3

Layers per exchanger 44

Heat Transfer Area m 751.13

Exchanger metal Aluminium

Weight empty kg 932.3

full of water kg 1327.0

operating kg 957.0Side bar width mm 11.50

Parting sheet thickness mm 1.50

File: PlatefinHX


126/152

Specified Duty

Stream name n210 bog04 n207

Stream number 1 2 3

Heat Load kW 2791.6 -113.3 -2228.8

Inlet temperature C -163.10 -100.60 35.10Outlet temperature C 28.20 -160.00 -118.00

Inlet pressure bar (abs) 12.500 4.000 56.500

Pressure change bar -1.56190 -0.44398 -1.07610

Mass flowrate kg/h 50400.0 3686.4 50400.0

Inlet vapour mass fraction 1.0000 1.0000 1.0000

Outlet vapour mass fraction 1.0000 1.0000 1.0000

Fouling resistance m K/W 0.000 0.000 0.000

File: PlatefinHX


127/152

Stream 1 cold Stream 2 hot Stream 3 hot Wall

Distance from End A (mm)

200 400 600 800 1000 1200 1400 1600 1800

Temperature(C)

-160

-140

-120

-100

-80

-60

-40

-20

0

20

40

Creator: Plot Date: 27/08/2010 Time: 0:39:13


128/152

Stream 1 cold Stream 2 hot Stream 3 hot

Distance from End A (mm)

200 400 600 800 1000 1200 1400 1600 1800

TemperatureDifference(C)

-20

-15

-10

-5

0

5

10

15

20

25

Creator: Plot Date: 27/08/2010 Time: 0:39:33


129/152

Stream Geometry


Stream number 1 2 3

Number of layers 23 4 17

Type cold hot hot

Flow direction up down down

Surface area m 450.35 17.28 283.50

Length - dead zone mm 11.50 1201.74 11.50

Length - end A distributor mm 111.68 189.87 111.68

Length - main fin mm 1674.47 406.05 1359.80

Length - end B distributor mm 111.68 111.68 83.62

Length - dead zone mm 11.50 11.50 354.23

Inlet distributor type End Diagonal End

Outlet distributor type End End Indirect

Inlet header side Left Left Left

Outlet header side Right Right Right

Header diameter - inlet mm 117.87 189.87 137.86Header diameter - outlet mm 142.56 138.06 83.62

Nozzle diameter - inlet mm 102.26 52.48 102.26

Nozzle diameter - outlet mm 128.20 41.14 62.68

No. of nozzles/inlet header 3 3 3

No. of nozzles/outlet header 3 3 3

Other stream in same layers

Redistributed in extra layers no no yes

Main fin number 1 2 3

Main fin type Serrated Serrated Serrated

Main fin height mm 7.10 6.40 6.40

Main fin frequency /m 787 787 787

Main fin thickness mm 0.31 0.31 0.41

Length of (first) main fin mm 1674.47 406.05 1078.83

Second main fin number 3

Length second main fin mm 280.98

File: PlatefinHX


130/152

Distributor Geometry


Stream number 1 2 3

Inlet distributor type End Diagonal End

Outlet distributor type End End Indirect

Inlet header side Left Left Left

Outlet header side Right Right Right

Inlet distrib dimension a mm 111.68 189.87 111.68

Inlet distrib dimension b mm 117.87 137.86

Outlet distrib dimension a mm 111.68 111.68 83.62

Outlet distrib dimension b mm 142.56 138.06 159.55

Distrib fin no. (inlet pad 1) 4 5 6

Distributor fin type Perforated Perforated Plain

Distributor fin height mm 7.10 6.40 6.40

Distributor fin frequency /m 472 472 590

Distributor fin thickness mm 0.61 0.61 0.61

Distrib fin no. (inlet pad 2) 4 5 6Distrib fin no. (outlet pad 1) 4 5 6

Distrib fin no. (outlet pad 2) 4 5 6

File: PlatefinHX


131/152

end A

o t e:

EffectiveLengt

h=

1674mm

1921

mm

Width = 342 mm Depth = 372 mm

1

1

2

2

3

3

3


132/152

end A

o t e:

EffectiveLengt

h=

1674mm

1921

mm


1

1

2

2

3

3

3

1

1

fin 1


133/152

end A

o t e:

EffectiveLengt

h=

1674mm

1921

mm


1

1

2

2

3

3

32

2

fin 2


134/152

end A

o t e:

EffectiveLengt

h=

1674mm

1921

mm


1

1

2

2

3

3

3

3

3

3 redist.

fin 3

fin 3


135/152

Fin Geometry

Fin 1 Fin 2 Fin 3 Fin 4 Fin 5 Fin 6

Fin Number from Databank

Fin Type Serrated Serrated Serrated Perforated Perforated Plain

Fin Height mm 7.10 6.40 6.40 7.10 6.40 6.40

Fin Thickness mm 0.305 0.305 0.406 0.610 0.610 0.610

Fin Frequency fins/m 787 787 787 472 472 590

Fin Porosity 0.050 0.050

Serration Length mm 3.00 3.00 3.00

Subchannel Aspect Ratio 7.04 6.31 6.93 4.30 3.84 5.34

Blockage Fraction 0.273 0.276 0.363 0.349 0.356 0.421

Subchannel Hydraulic Diameter mm 1.691 1.667 1.511 2.448 2.394 1.827

Flow Area mm2/m 5164.0 4632.0 4078.8 4621.4 4122.9 3706.2

Primary Perimeter mm/m 1519.9 1519.9 1361.0 1424.2 1424.2 1280.2

Secondary Perimeter mm/m 10695.3 9593.5 9434.6 5820.2 5192.5 6832.2

Used in Streams 1 2 3 1 2 3

File: PlatefinHX


136/152

0

562.48380

R - refinery service

Flat Metal Jacket Fibe

ASME Code Sec VIII Div 1

-

Flat Metal Jacket Fibe

Single segmentalCarbon Steel-

Exp.

-

mm373 5400 BEM 1 1

48.9 m 1 48.9 m

nitrogen seawater

14 16kg/s

14 14kg/s 0 0

0 0kg/s 16 16

kg/s 0

109.4 35.1C 25.1 42.3

C

50.65 62.16kg/m

mPa s

28.01 28.01

kJ/(kg K)

W/(m K)

kJ/kg

57.5 3bar

10.75 0.55m/s

0.7 0.63942bar 0.4 0.03406

0 0m K/W

kW1080.3 C29.97

737.2 774.6 W/(m K)774.6

bar 5

210 140C

1 1

3.18 3.18mm

203.2 - 127 -

203.2 - 101.6 -

- -

mm

2137.4 2678.4 kg843.4

4045 1530 kg/(m s)1461

38.94mmmm

154 23.8119.05 1.65 5400mm mm mm

Plain Carbon Steel 30

mm406.4

Carbon Steel

Carbon Steel

- None

-

-

-

Carbon Steel

Hor

H

Avg

373.08

0 0

56.86058 2.96594

68

993.95 977.2

0.0213 0.0182 0.9111 0.6432

1.043 1.04 3.857 3.977

0.0313 0.0262 0.6064 0.6286

T1

S1

S2

T2

0

#/m

Nominal

Size/rating

Ao based

Vapor/Liquid

--

Code

Remarks

TEMA class

Intermediate

BundleFilled with waterWeight/Shell

Code requirements

Floating head

Tube SideGaskets - Shell side

Bundle exitBundle entrance

TypeExpansion joint

Tube-tubesheet jointBypass seal

TypeU-bendSupports-tube

Impingement protection

Tubesheet-floating

Channel cover

Floating head cover

Tubesheet-stationary

Channel or bonnet

Out

In

Surf/shell (eff.)Shells/unitSurf/unit(eff.)

seriesparallelConnected inTypeSize

OD

Sketch

1

2

3

4

5

6

7

PERFORMANCE OF ONE UNIT8Fluid allocation9

Fluid name10

Fluid quantity, Total11

Vapor (In/Out)12

Liquid13

Noncondensable14

Temperature (In/Out)

15

Dew / Bubble point

16

17

18

19

20

2122

23

24

25

26

27

28

Heat exchanged29

Transfer rate, Service30

CONSTRUCTION OF ONE SHELL31

Design/Test pressure

32

Design temperature

33

Number passes per shell

34

Corrosion allowance

35

Connections

36

37

38

Tube No.

39

Tks-40

41

Length

42

Pitch

43

Tube type

44

Material

45

Shell

46

ID

47

OD

48

Shell Side

49

Tube Side

50

Shell cover

51

Tube pattern

52

Baffle-crossing

53

Type

54

Cut(%d)

55

Spacing: c/c

56

Baffle-long

57

Seal type

58

Inlet

RhoV2-Inlet nozzle

Shell Side Tube Side

Fouling resist. (min)

Pressure drop, allow./calc.

Velocity

Pressure

Latent heat

Thermal con

planta de relicuefaccion en buque metanero

Documents