12. Ｃｕｒｒｅｎｔ status of tigar prototype plant in indonesia2

7/25/2019 12. Status of TIGAR Prototype Plant in Indonesia2

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Current Status of Twin IHI Gasifier

(TIGAR

®

) Prototype Plant inIndonesia

~ IHI Gasification technoloy~

PT! IHI Gasification Indonesia

IHI Corporation

C"##"$%I%& tek &IRA '*



Net Sales : JPY 1,456 bil.

(USD 12,120 mil)

Foune ： 1!5"

#o$%s : ! &$an' **i'es : 1+(Jaan) ,15(-e$seas) mlo/ees : 2!,5""

e Fi$st Steamsi &uilt b/ JaaneseP$i-ate oman/ 3suun ma$u.

Co+pany Profile (IHI Corporation)

2

6n*o$mation is on 'onsoliat basis an is 'o$$ 't as o* 7a$'( 2015

Sales b/ business se8ment(on 'onsoliate basis)

o/$i8t 9 2015 o$o$ation ;ll <i8ts <ese$-e.

=>?@ABC ; 29%

EG ; 30%

HIK / LMK ; 28%

OQ / R ; 13%

-e$seas **i'e

Tlobal Subsiia$/oman/

Tlobal Neto$%



Industrial Syste+s(Steel Manufacturing Furnaces, Heat/Surface Treatment

Eui!ment, "#gistics S$stems, Material Hanling Eui!ment, etc&'

Social Infrastructure and "ffshore ,acilities

(rige, Trans!#rtati#n S$stem, Securit$, etc&'

IHI -usiness Areas

3

General.Purpose &achinery()#m!ress#r, Se!arat#r, Tur*# c+arger, etc&'

Resources/ 0nery and 0n1iron+ent

(#iler, as Tur*ine/as Engine, "- Terminal, .r#cess .lant, -uclear Eui!ment, etc&'

er#, Engines

an S!ace

eel#!ment

es#urces,

Energ$ an

Enir#nment

S#cial nfrastructure

an

4ffs+#re Facilities

nustrial S$stems

an

eneral5.ur!#se

Mac+iner$

Aero 0nines and Space

(6et Engine, #c7et'

)#!$rig+t 201 H )#r!#rati#n ll ig+ts esere&


http://slidepdf.com/reader/full/12-status-of-tigar-prototype-plant-in-indonesia2 4/28:

nreacte

c+ar is*urne

<it+ air

Hig+

tem!erature

*e materialsare circulate

Circulation

Steam gasificati#n

Co+2ustor

Gasifier

,uel

Stea+Air

(heat e+ission)

・

At+ospheric

pressure

・

#ow

te+perature

! Characteristics of TIGAR

(heat a2sorption)


・ )#m!#nents #f T are *ase #n mature Fluii=e e tec+n#l#g$

・ T+e l#< grae material (lignite, *i#mass' can *e gasifie,

an a!!lie t# c+emical ra< material, fuel

Applica2le ,uel

Coal (linite)

-io+ass

Application

CT#

3&0

&ethanol

,uel cell

4H5

S4G

Che+ical

feedstoc6

Auto fuel

Shift

Synthesis

Hydroen

&ethaneRefor+in

Synas

(C"/H')

GT/ G0 ,uel 3irect

reduction

iron +a6in

Synas

H2

1%

)4

18%

)4219%

)H:

9%

4t+er H)

3%

Synas

co+ponent

・ Hydroen

rich as



Co+2ustor

Cyclone

Gasifier

Heat

Reco1ery

Area

(HRA)

-a ,ilter

07haust Pipe

(HRA)

Cyclone

Synas

Treat+entProcess

TIGAR Process

"perationIHI8s C,- e7perience

・ Stea+ ,low Rate ～ 5 ton9 hr (&a7! *ton9day as #inite feed rate)

・ Since ::'

・ 3eli1ery Record ;apan/ China/

Thailand

"peration philosophy of TIGAR is si+ilar to C,- 0asy fa+iliari<ation 2y operator

TIGAR has 2een de1eloped 2ased on C,- as +ature technoloy/ so TIGAR has sa+e

features such as ood fuel fle7i2ility and en1iron+ental adaptation!

,urnace Cyclone

07ternalHeat

07chaner

Heat

Reco1ery

Area

(HRA)

-a ,ilter

Stac6

C,- process

Si+ilarity

Si+ilarity 2etween C,- and TIGAR

&aintenance Con1entional e=uip+ent can 2e adopted ,a+iliar +aintenance 6now.how

'! ,eature of TIGAR




>

C,- structure TIGAR structure

Cyclone

,urnace

HRA

Hopper

0>A

PSH

SSH

0C"

GAH

0H0

Heiht

**+

Co+2ustor

Gasifier

Cyclone

HRA

Cyclone

Heiht

**+

Actual C,- -oiler

( tons9day)

Co++ercial Plant

( tons9day)

?ey co+ponents of TIGAR and e=uip+ent such as coal feeder and fans are si+ilar to C,-!

In addition/ si<e of the co++ercial plant of TIGAR is within IHI8s e7perienced C,-!

Si+ilarity of ?ey Co+ponents 2etween C,- and TIGAR

'! ,eature of TIGAR




?

.alm @aste

@##

( i # m

a s s i s a 1

a i l a * l

e, t # #

TIGAR

0asy utili<ation of #inite and

-io+ass

2ecause of operation under

at+ospheric pressure

Applyin si+ple feedin syste+

to asifier 2y ra1ity!

(4ow %sin little a+ount of seal

4itroen)

4o special preparation @

"nly rouh crushed (-ul6) @

・ .article si=e A 10mm uner

・ T#tal m#isture A B 3～ : %C

"ignite

Cs receie *ase

is acce!ta*le

'! ,eature of TIGAR

,uel 1ariety

and si+ple fuel supply syste+




8

① "#<er ).ED an sim!le 4!erati#n Maintenance

5 "#<er !ressure an l#<er tem!erature in #!erating c#niti#n

② Sim!le Fuel !re!arati#n 5 )#arse si=e an +ig+er m#isture are acce!ta*le

③ -# -2 c#ntaminati#n in S$n5gas, -# S f#r gasificati#n,

*ecause #f Steam gasificati#n

IHI

.TIGAR. 0ntrained 2ed &o1in 2ed

Gasifier type ,luidi<ed 2ed

Pressure At+ospheric 5&Pa 5&Pa .5&Pa

Te+perature B./℃ /℃ /℃ /'℃

Gasification aent Stea+ "7yen "7yen "7yen

,uel particle si<e D++ D!++ D!++ ~*++

,uel confiuration -ul6/ powder Powder Slurry -ul6

Residue 3ry Ash Sla Sla 3ry Ash

'! ,eature of TIGAR




9

Et9dFo6oha+a/ ;APA4 Co++ercial plant i+ae

TIGARunits (reser1e)

Coal feed 5 t9d

( Su2stantially 4H5

t9d)

4

～

9 2010 2011 2012 2013 2014 2015 2016 2017

-asic Test ETP3 Pilot Plant

*TP3 Prototype Plant0PC

3e+onstrationTest

Co++ercial

Plant

at present

;apanese Go1ern+ent (&0TIJ) Support

J&inistry of 0cono+y/ Trade and Industry

*t9dF?uKan/ I43"40SIA


History

5! 3e1elop+ent of TIGAR



)#!$rig+t 201 H )#r!#rati#n ll ig+ts esere& 10

T esign met+# +as *een c#nstructe *$ seeral funamental e!eriments

an simulati#ns, an c#nfirme at .il#t .lant& sing t+is met+#, 0t/em#nstrati#n !lant <as esigne&

Gasification 2eha1ior Et9d pilot plant F o6oha+a

Prediction of

asification efficiency

5! 3e1elop+ent of TIGAR

3esin +ethod of asifier

Prediction of coal residence ti+e in the asifier

Taret fuel

3esin

Condition

G)a!acit$GTem!erature

GS/)G)#m*usti#n ir H H H



11

＜

Plant site＞

＜ *t9d 53 2ird8s 1iew＞

! *t9d 3e+onstration at Indonesia

Purpose

＜ *t9d plant spec＞

①)+ec7 t+e maintenance ura*ilit$ in l#ng

#!erati#n （ T#tal :,000 +r #!erati#n） usingn#nesia lignite&

②)#nfirmati#n #f T !erf#rmance an

relia*ilit$, an reflect in c#mmercial !lant

engineering&

③em#nstrati#n #f T gasificati#n

tec+n#l#g$ f#r future clients&

)#al fee rate

0 t/ （ as receie,

:3% m#isture）

S$ngas #ut!ut 1,800 m3-/+5r$

Steamgenerati#n

:& t/+ (2&0M.a,

13eg&)'

Site area 100m I 80m

;a6arta

IHI Cileon factory

PT Pupu6 ?uKan(A2out L*6+ fro+ ;a6arta)

;a1a/ I43"40SIA

0asy access

for site 1isit

0asy access

for +aintenance




12

"rani<ation chart

METMinistr$ #f Ec#n#m$,

Trae an nustr$

MEMMinistr$ #f Energ$ an

Mineral es#urces

Ministr$ #f

nustr$

Ministr$ #f

state5#<ne

enter!rises

EM genc$ #f esearc+ an

eel#!ment #f Energ$ an

Mineral es#urce

.T& .u!u7

n#nesia

(.H)'

te7M.T& .u!u7

JuKang

Cooperation

Go1ern+ent Tal6

H )#r!#rati#n

.T& H asificati#n

n#nesia

Support





)#!$rig+t 201 H )#r!#rati#n ll ig+ts esere&13

History

Signing )erem#n$, 13 Fe*ruar$ 2013 First asificati#n, 1? 6anuar$ 201

naugulati#n

)erem#n$,

2> Fe*ruar$ 201




1:

Site "1er1iew





1

&aterial

Handlin

TIGAR

Stea+ f#r gasificati#nAir f#r c#m*usti#n

Maste water

treat+ent

HRA

HRA

-a ,ilter

07haust Pipe

Incinerator

Gas purification

(low pressure)

Gas purification

(hih pressure)

9

59

%tility Syste+

"' Supply

Syste+

4' Supply

Syste+

#PG Syste+ Instru+entation

Air Syste+

Coolin Mater

Syste+ A+ine Supply

Syste+

0+erency Generator

Stea+ 3ru+

Process flow

"' supply

Tar Crac6er





1>

Maste Mater area

Gasifier structure area

Gas Purification area

TIGAR Control Center

?I?C

Gate

? I ? C

& a i n R

o a d

?uKan

Plant

TIGAR Site

#ayout

Coal yard

Coal handlin

syste+

#PG area

&achinery

house

%tility area

+

B+





1?

Maste Mater area

Gasifier structure and Coal crusher area

Gas Purification area

Control Center


Plant photo


Coal yard



18

"#aing at c#al Kett$:000 t#n c#al #n 230 ft arge

nl#aing at !#rt (near 6a7arta'

3esin Coal N0ast ?ali+antan coalO 56cal96 GAR at 5 +oisture

,ro+ 0ast ?ali+antan to ;awaTruc7 trans!#rts c#al fr#m

st#c7$ar near !#rt

t# t+e T site&T site +ae 10 a$s

st#c7$ar (00t#n'



Coal deli1ery

9



19

Plan

（ East Jalimantan

c#al, Kustment）

（ .J-炭、他炭種）

（他炭種、バイオマス）

Test schedule

（ East Jalimantan

c#al, n#t+er c#al, ）

（ n#t+er c#al,

i#mass）

Ealuati#n, Maintenance




（ East Jalimantan c#al,

.erf#rmance test）



*t9d 3 t ti t I d i



20

"peration Result

➤ T#tal ?00+r gasificati#n #!erati#n➤ @it+#ut r$ing, r#ug+l$ crus+e lignite

<ere acce!te

07a+ple of operation

0ast ?ali+antan Coal

TM (ar' :2 %

s+ (a*' 8 %

LM (a*' 38 %

F) (a*' 3? %

T#tal Sul!+ur (a*' 0 %

r#ss )al#rific Lalue(ar'

3380 7cal/7g



crus+ B 10mm

*t9d 3 t ti t I d i



21)#!$rig+t 201 H )#r!#rati#n ll ig+ts esere&

"peration Result


➤ @it+ n#nesian #!erat#rs <e succeee t# ensure t+e sta*le #!erati#n

➤ 4!timi=ati#n #f #!erati#n are still neee

Co+position of Gasifier

outlet synas

Seal -2 f#r )#al feeing

line are etecte&

J

J

* &ar6eta2ility of linite asification



*! &ar6eta2ility of linite asification

. Mhy IndonesiaQ

4atural GasCoal

Policy of Indonesia enery supply

07port

Indonesia Coal Resources 4atural as %tili<ation in Indonesia

@E), Sure$ #f Energ$ es#urces 2010 T+e 1st 6.-5-4-ES E-E F4M, 2013

T+e 1st 6.-5-4-ES E-E F4M, 2013

22

I+portant source of forein e7chane

ac=uisition 2y #4G e7port 0nery security

0nery situation in Indonesia


* &ar6eta2ility of linite asification



23

4atural Gas Refor+er

A++onia

Process

%rea Process

Gasifier

TIGAR#inite

Chane @

4H5 +anufacturin capacity of Pupu6 Indonesia holdins (PIHC) Group

Pusri

130 t/?90 t/

1200 t/

1200 t/

?uKan

11>0 t/

1000 t/

Petro6i+ia Gresi6

130 t/

?alti+

1800 t/

1800 t/

1000 t/

1000 t/

Is6andar &uda1100 t/

1200 t/

*! &ar6eta2ility of linite asification

. Indonesian ,ertili<er Industry


E Conclusion



E! Conclusion

)#!$rig+t 201 H )#r!#rati#n ll ig+ts esere& 2:

G TIGAR is 2ased on C,- technoloy/ and stea+

asification! It has the feature of easy "&/ fuelfle7i2ility (#inite/ -io+ass)/ H' rich synas!

G ,ro+ the *t9d 3e+onstration operation in Indonesia/ we

are ettin data for co++ercial plant! And we will pro1e

and appeal a2o1e TIGAR8s +erit throuh hr

de+onstration operation!

G Me would li6e to contri2ute for effecti1e use of

resources 2y TIGAR technoloy!



Thank you for your attention !

Sa+pai 2erte+u 2eso6

,S Results . Co+parison of 4G and TIGAR Process .



)#!$rig+t 2013 H )#r!#rati#n ll ig+ts esere& 2>

mm#nia

.r#cess

rea

.r#cess

asifier

T"ignite

-atural

asef#rmer

T .r#cess

mm#nia

.r#cess

rea

.r#cess

- .r#cess

)#st c#m!aris#n #f *#t+ cases

p

18 Ma$ 2011

Taret site ,ertili<er plant

Capacity Synas supply 2y TIGAR for t9d A++onia production

Plant condition Considered as newly construction for 2oth process

,S Results on t9d A++onia Production



)#!$rig+t 2013 H )#r!#rati#n ll ig+ts esere& 2?

S esu ts o t9d o a oduct o

Bssum!ti#n #f calculati#nG T+e nitial c#st inclues gasifier, gas treatment, <aste <ater treatment, electric an

c#ntr#l eui!ment&

G S$ngas c#st is annual c#st(S/$ear' / annual !r#ucti#n #f -H3(t#n/$ear'&G S$ngas c#st inclues !r#cess feest#c7(lignite c#al', maintenance, utilit$, la*#r,

e!reciati#n(20$ears', interest&

Lignite cost --- 30USD/t ,

NG rice --- 0USD/""#TU ＞

)#al(:0%TM'

12S/MMT

10S/MMT

8S/MMT

1:S/MMT

- !rice

S $ n g a

s c # s t N M M ; S 0 / t 5 - H 3

O4!erati#nal c#st

merit #f T

5E&&%S3

n n u a l c # s t N M M ; S 0 / $ O

NT T;<Vi8nite 'ost WUSDXｔ」

・ TIGAR process has the "& cost +erit of 5E&&%S39year co+pared with 4G process!

・

TIGAR has the +erit at linite cost which is 5%S39t or less/ if 4G price is%S39&&-T%!

0&0

:0&0

80&0

120&0

1>0&0

.r#cess feest#c7

tilit$

"a*#r

Maintenance

nterest

e!reciati#n

0 20 :0 >0 800

0

100

10

200

20

,S Results on t9d A++onia Production



)#!$rig+t 2013 H )#r!#rati#n ll ig+ts esere& 28

0 20 40 60 800

100

200

300

400

500

600

700

Bssum!ti#n #f calculati#nG T+e nitial c#st inclues gasifier, gas treatment, <aste <ater treatment, electric an

c#ntr#l eui!ment&

G S$ngas c#st is annual c#st(S/$ear' / annual !r#ucti#n #f -H3(t#n/$ear'&G S$ngas c#st inclues !r#cess feest#c7(lignite c#al', maintenance, utilit$, la*#r,

e!reciati#n(20$ears', interest&

G Lignite cost --- 30USD/t , NG rice --- $USD/""#TU )#al(:0%TM'

12S/MMT

10S/MMT

8S/MMT

1:S/MMT

- !rice

0.0

20.0

40.0

60.0

80.0

100.0

S $ n g a s c # s t N M M ; S 0 / t 5 - H 3 O

4!erati#nal c#st

merit #f T

5E&&%S3

4 E M

c # s t N M M ; S 0 / $ O

NG TIGAR

-P8S/MMT, "igniteP30S/t

.r#cess feest#c7

tilit$

"a*#r

Maintenance

Lignite cost [!"#ｔ」

・ TIGAR process has the "& cost +erit of 5E&&%S39year co+pared with 4G process!

・ TIGAR has the +erit at linite cost which is 5%S39t or less/ if 4G price is B%S39&&-T%!

12. Ｃｕｒｒｅｎｔ status of tigar prototype plant in indonesia2

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