The Korean Case Study of CCS Pipeline Transport Cost with CO2CRC/UNSW Model

(1)

Vol. 49, No. 4G O2012PG pp. 537-544

෹சॷߢࠜୡ૳෉$$4൞ଲඹޭ଴৤৉ଭ֝ٛण૳ਏॺ

׌஺ฅ

The Korean Case Study of CCS Pipeline Transport Cost with CO2CRC/UNSW Model

Kim, Ji-Whan

Abstract : The world makes efforts to reduce carbon dioxide gas and Korea also. Korea gives a lot of attention to storing underground in the field, as one way to reduce CO2 in the atmosphere, and has promoted actively.

In order to promote the CCS (Carbon Capture and Storage) projects, Korea tries to develope the related technologies, draw the cost-efficient way of linkage between the sources and the storage sites, build the profit structure to invest in the projects and establish the legislation and maintenance system. In this regard, this study is to present the estimation results of pipeline transport cost for several cases of the linkage between the sources and the storage candidates. The results of those case study based on CO2CRC/UNSW model show pipeline cost of 4.9-12US$ per CO2 avoided (US$/t) of US$.

Key words : Carbon capture and storage, Transport cost, Cost estimation, Sources and storage site

څ أ ՃćəН΁ۋČॢĶً֨CO2۹Çںڦ३ɰتॢȤͳںşڐۋČەəʚ, ݓܼ۹ۤқآقʪψڹ

ě֮ںÍČটь০߸ݕॠČەəʚ, CCS(Carbon Capture and Storage)ۆԐغজεڦ३Դəěʹşցۆঝ҃, Ҽڌ߯ՙজεڦॢ۹ۤՙٮѕ߻ڙۆٍćѓ؋, ࣊ۙۦڙυʹ̚əԐغজεڦॢą܃ۺϭ࠶ɦݏঝ҃, υݓφڷͿԐغজεڦॢѪ/܃ʪ܁Ҽۚغۋज़څॠɰ. ۋÀڏʚٍ҆ĵقԴəѕ߻ڙę۹ۤ঳҃ݓۆٍć ѓ؋ęսբäνق˰δCCSԐغۆսբҼڌں߸܁ॠٕɰ. ĶǴѕ߻ڙę۹ۤՙ঳҃ݓٍćۆąڍ३Ԝ

ࣷۋ॒͆ۍսբںۻ܃Ϳ70-250 km ܁ʪۆսբäνεÀ܁ॠČ, ԐغşÂڹ20-40țںÀ܁ॠٕɰ. ۋÏڹ

À܁ںۻ܃ͿCO2CRC/UNSWۆԸॱԐͻقŖäॠيқԵॢĀęԐغşÂęսբäνق˰͆CO2 ۹Ç

ɳڦ(ࢻ)ɾ4.9US$قԴ12US$ūݓǣࢍǮɰ.

ܳڅر ۋԓজ࢏ՙपݚф۹ۤ, սբҼڌ, Ҽڌ߸܁, ѕ߻ڙ, ۹ۤՙ

2011ț12ښ22ێۿս, 2012ț5ښ10ێ֮ԐٰΒ 2012ț8ښ23ێóۦঝ܁

1) ॢĶݓݗݓڙٍĵڙۙڙą܃ٍࣳĵڙ

*Corresponding Author(ťݓঞ) E-mail; [email protected]

Address; Korea Institute of Geoscience and Mineral Resources, Gwahang-no 124, Yuseong-gu, Daejeon 305-350, Korea

Դ΁

IEA(International Energy Agency)ə 2008țʪ ҃Č ԴقԴ٣֬À֟قۆॢş঳Ѻজٮ߯ŖজԵٍΒՙҼ

͟ÂۆěćεČͲॣ˺, 2050țūݓ2005țCO2ѕ

߻͟ۆ50%εÇ߹ॠيآॢɰəۆþں܃֨॰ɰ. ۋ ə2005țʪѕ߻͟սܵقԴ48֯زࢻۆCO2 ۹Çۋ

څĵʽɰəìۋɰ. ̚ॢ2050țūݓЀशॢCO2 ۹Ç

ںɵՁॠşڦ३قȃݓমڱݒݕ, ֪ۦԦقȃݓԐڌ, CCSق ÁÁۆ ًॣں ҙيॠČ ەɰ.¹⁾

ॢĶۆąڍ3ÀݓÇ߹ćনںČͲॠČەɰ. ۋə

2009țॢĶ܁ҙÀ2020ț۹ÇЀशɵՁ֨ǣν١ε3 ÀݓͿ܃؋ॢìۍʚ, ÁÁڹ21, 27, 30%ۆÇ߹ںǣ

ࢍǶɰ. ۋəÁÁ2005țѕ߻͟594іχࢻقҼ३8%

ݒÀʽԜࢗεɵՁॠəąڍ, ʴێॠóڮݓॠəąڍ, 4% Ç߹ॠəąڍεǣࢍǶɰ. 21% Ç߹֨ǣν١ə

ɳşۺڷͿҼڌں࣊ۓ३ۤşۺڷͿCO2 ѕ߻ںÇՙ

֨ࢅəČমڱ܃ुںԦԓॠəѓѪۋɰ. 27% Ç߹֨

ǣν١ə21% Ç߹֨ǣν١ۆѓѪقॠۋҵν˚ۙ

ʴ޲εۋڌॠäǣbio-fuelںۋڌॠəѓѪęÏڹʂ ߕՁۦজۆমęεۋڌॠəѓѪۋɰ. 30% Ç߹֨ǣ

1) IEA(2008) ޷ܓ.

şց҃Č

(2)

538 ťݓঞ

ν١ə27% Ç߹֨ǣν١قCCSεۺŕۺڷͿʪۓ ॠə ìۋɰ²⁾.

CCS şցÒьںߤݕॠşڦ३ȥԟՁۤڦڙধধۆ قԴCCS ߪĜĶÀćনںьशॠٕɰ³⁾. ۋćনقə

2015țūݓCO2۹ۤݓεԸ܁ॠČ, 2017țںЀशͿ

Ԝڌজॠي1 іχࢻőϿۆܛ०CCS ॒Ϳ܄࣡ε޳ս

ॢɰəǴڌںप॥ॠČەɰ. ۋćনʂͿʽɰϸ2030 țق3.2 іχࢻۆCO2۹ÇںɵՁॠóʽɰ. ۋٮÏ ڹ܁޾ۺȦۆεѕąڷͿĶǴCCSə٣֬À֟۹Ç ق ܼڅॢ ًॣں ॣ ìڷͿ şʂʽɰ.

CO2ۆѕ߻ڙڹɰتॢʚ, Ŕܼपݚۋڌۋॢѕ߻

ڙęҼڌমڱۺۍսբѓѪںࣀ३ۺۼॢ۹ۤՙق

CO2ε üν֨ࢅə ìۋ ०νۺۋɰ. ڍνǣ͆ۆ ąڍ, ইۦ۹ۤՙ܁҃εҼ΅३CCS Ԑغěʹ܁҃εঝ҃

३Àəę܁قەرÀɠॢ۹ۤՙսǣ۹ۤɠͳսܵ

ˣںɳ܁ॣսػəԜডۋɰ. χێÀɠॢ۹ۤՙÀڮ ێॢìڷͿࣺɳʼʌ͆ʪ܁޾֨ॱۆě۾قԴəҼڌ মڱՁںêࢹॠəìۋԐغ֨ॱقज़սۺۋдͿɳć ۺڷͿ, ÀɠॢѩڦǴقԴ͆ʪҼڌ߸܁ںݓ՚ۺڷͿ

֨ʪॣज़څÀەɰ.⁴⁾ ইۦपݚقěॢ܁҃ǣڍνǣ

͆ۆ۹ۤՙيæ܁҃À߿қॠݓ؍ڼںČͲॠϸ܃

ॢۺۋǣυսբҼڌۆ߸܁ںڍԸۺڷͿ֨ʪॣսە ɰ⁵⁾.˰͆Դ҆ČقԴəҼڌ߸܁ۆߒɳćͿԸॱԐͻ εࣀ३CCS ԐغقԴڅĵʾìڷͿşʂʼəսբҼ ڌں ߸܁३ ҃Čۙॢɰ.

սբҼڌڹCCS ॒Ϳ܄࣡ۻߕۆҼڌߕćقԴࢀҼ

ܼں޲ݓॢɰČ҇սəػɰ. McKinsey & Company (2008)ق˰βϸʂߕͿߣşԜڌজɳćۆ॒Ϳ܄࣡ق ԴսբҼڌڹۻߕҼڌۆأ11%ε޲ݓॣìڷͿ҃

Čەəʚ, ۋəڮͥۆथŒۺۍيæںČͲॢìڷͿ

ڍνيæęəɰՙ޲ۋÀەںսەɰ. ࣢০ČÄڮ

À֟ۻںيͦ҃ڮॢĶÀقҼ३ڍνǣ͆ə۹ۤՙٮ

ѕ߻ڙۆٍćÀڌۋॠݓ؍ںսʪەڷ϶, ۋąڍԜ ʂۺڷͿսբäνÀţرݓČ, սբҼڌۋݒÀॠóʼ

2) 2009ț8ښ4ێьशʽȥԟՁۤڦڙধ҃ʪۙΒ“ĶÀ٣

֬Àܼ֟şÇ߹ЀशԺ܁ںڦॢ3Àݓ֨ǣν١܃֨”ۆ

३ɾԐ२ں څأॠٕɰ.

3) 2010ț7ښ܃8 ޲ȥԟՁۤڦڙধ҃ČʂধقԴ“ĶÀCCS ܛ०߸ݕćন”ۋьशʼؽڷ϶, ԜՃǴڌڹȥԟՁۤڦڙ ধ҃ʪۙΒ“ȥԟՁۤ, ֨ۤę॥ƍ঒ড়ॢɰ”(2010ț7ښ

12ێ)ق ǣࢍǣ ەɰ.

4) Ji-Whan Kim and Yong-Chan Park (2011) “A Case Study of CCS Cost Estimation : ICCSEM applied to Korea”, CO2CRC Research Symposium 2011 ьशۙΒ ޷ܓ.

5) чڌ޴ٽ(2011) “CCS ą܃ՁқԵϿʝ”, ܃1ধKorea CCS Conference ьशۙΒ ޷ܓ.

дͿ ۻߕ ҼڌĵܓÀ ɵ͆ݗ սʪ ەɰ.

ۋ঳ۆȦۆقԴəĶǴCO2ѕ߻фܳڅѕ߻ڙই ডęۍۿқݓقʂ३Â͜০ԺϼॠČԸॱԐͻεࣀ ३ սբҼڌں ߸܁ॠşͿ ॢɰ.

ĶǴ$$4Ԑغيæ

ܳڅѕ߻ڙڦ࠘ٮ۹ۤՙ঳҃ݓۆڦ࠘фŔäν

ˣۋCCS Ԑغۆş҆ۺۍيæڅՙ͆ॣսەəʚ,

ॢĶۆ CCS Ԑغ يæڹ ܞɰČ ॣ սəػɰ.

Ϥ۹٣֬À֟ܛ०܁҃ՅࢢÀ܃ėॠə٣֬À֟ࣀć ق˰͆ڍνǣ͆ۆ٣֬À֟ѕ߻Òڅεԕट҃ϸ, 2009 țۆąڍقȃݓҙЛقԴ516.0 іχࢻۆ٣֬À֟(CO2

eq.)Àѕ߻ʼؽəʚ, ۋəۻߕѕ߻͟ۆ83.9%قɵॠ ə͟ۋɰ. ۋܼьۻںप॥ॢۻঞ(conversion)ۋق ȃݓҙЛ⁶⁾ۆ44.3%, ԓغҙЛۋ27.3%ε޲ݓॢɰ. ܳ څѕ߻ڙڹьۻ, ܃ߏ, Եڮজॡę֨ϯ࣡ԓغۋɰ.

Ե࢏ьۻۆąڍ5ÒьۻԐÀەڷ϶ۋ˞قԴ2009 țق191.8 іχࢻۋѕ߻ʼؽɰ. ɰڼܳڅѕ߻ڙڹ

POSCOٮÏڹ܃ߏغߕۋ϶, 68.4 іχࢻۋ2009țق

ѕ߻ʼؽɰ. Եڮজॡۆąڍ43.9 іχࢻۋѕ߻ʼؽɰ.⁷⁾

ॢठ, ۹ۤՙ঳҃ݓقě३Դəݓݗ܁҃À߿қ০

ঝ҃ʼؽɰČ҇սəػڷǣݓ՚ۺڷͿঝ҃قȤͳॠ Čەəʚ, ķԓ, ܃ܳ, ڐιқݓٮÏڹ३تࣅۺқݓ قʂ३ÀɠՁںَر˃Čەɰ. ࣢০ڐιқݓۆą ڍ, ۺ०ॢ۹ۤĵܓÀɰսەںìڷͿ߸܁ʼČەə ʚ, 2004țÀ֟ԦԓۋۋΘرݕʴ३-1ۆČ͒-Vεप

॥ॢ˃ƍ200 m ۋԜۆԐؒࠗۋەəìڷͿ؎Ͳ܋

ەɰ⁸⁾.

Fig. 1ڹܳڅѕ߻ڙęŔÒ͜ۺѕ߻͟ںश֨ॢŔ ρۋɰ. ьۻՙəԴ३؋ݓًقݚܼʼرەəʚ, ʂʪ

֨ݓًقۻͳںėśॠşڦॢìۋ϶, ǫҙ३؋ݓً

ۆ ąڍə ҙԓق ۻͳںėśॠş ڦॢ ìۋɰ.

ڐιқݓÀūۋقەəܳڅѕ߻ڙڹ܃ߏՙۍPOSCO

6) ۹࢏ՙȥԟՁۤş҆Ѫڹ܃45ܓقԴ܁ҙͿॠيŚ٣֬

À֟ܛ०܁҃ěνߕćεĵ߹ॠʪ΀ॠČەəʚ, ܃2२ق Դəۋۆڙটॢڏٖںڦ३قȃݓԓغė܁Ȭغदş НԓρˣڷͿĵқॠيҙЛѻ܁҃фࣀćεۚՁф܃

ėॠʪ΀ ॠٕڷ϶ ʴѪ ֨ॱͺ ܃36ܓ ܃4२ڹ ʴқΪق

˰δҙЛѻěۤşěںݓ܁ॠČەɰ. ȥԦՁۤڦڙধə

ҙЛѻ٣֬À֟ѕ߻͟ࣀćεۚՁ॥قەرقȃݓҙЛ ںIPCC Àۋ˚ق˰͆ۻঞ, ԓغ, սբ, À܁Ԝغ, ėėş

ࢍͿ ĵқॠي ėशॠČ ەɰ.

7) ٣֬À֟ܛ०܁҃Յࢢ(http://www.gir.go.kr)À܃ėॠəۙ

Βε ۦĵՁॠٕɰ.

8) чڌ޴ ٽ(2009) p. 583 ޷ܓ.

(3)

Source : Huh et al. (2011) p. 4885.

Fig. 1. Major Sources and Possible Storage Sites.

ۋ϶, ьۻՙۆąڍə150-200 km ܁ʪ̆ر܋ەəʚ, گԜۋǣ३Ԝওڹگ३ԜսբۋÀɠॠɰ. گԜۆą ڍࣷۋ॒͆ۍսբͿεæԺॠəę܁قԴԐڮݓۆϔ ۓфے޲ҼڌۋьԦॠóʼəʚ, ڍνǣ͆ۆݓÀս

ܵںԦÁॠϸۺݓ؍ڹҼڌۋ߸ÀۺڷͿՙڅʼر

३ԜսբۆąڍقҼ३ҝνॣÀɠՁۋȭںìۋɰ.

ॢठĶǴѕ߻ڙęٽĶ ۹ۤՙε ČͲॠəѓ؋ʪ

ەڷǣ, սբäνÀϔڍţرݗӼχ؉ɦ͆ĶÀÂঊ ۆˣ܁࠘ۺۍҼڌʪԓۓॠيآ॥ںČͲॠϸɳş ۺڷͿÀɠՁںݕɳॣʂ؋ڷͿəĎ͈ॢ۾ۋەɰ.

঒ܳǣйĶۆąڍѕ߻ڙęϥݓ؍ڹĖقęäԵ ڮÀ֟εԦԓॢ۹ۤՙ঳҃ݓÀەرսբäνÀݥ Č, şܕۆԵڮÀ֟ԦԓԺҼεটڌॣսەرҼڌ ࠑϸقڮνॢԐͻÀψڹʚ, ѕ߻ڙę۹ۤՙ঳҃ݓ ÀԜʂۺڷͿϥČটڌॣսەəşܕۆԺҼÀػə

ڍνǣ͆ۆ يæڹ ڮνॠɰČ ҇ սə ػɰ.

঒ܳԐͻεۺڌॢĶǴսբҼ֨ԓ

ي͠ĶÀÀCCS Ԑغقě֮ںÍČٍĵεݕॱॠ äǣࣷێͦսܵڷͿԐغںݕॱॠČەڷ϶, ĶÀυ ɰ, ԐغυɰÁÁɰتॢҼڌ߸܁ں֨ʪॠČەɰ. CCS ą܃ՁқԵںÀۤটь০ݕॱॠČەəԐͻͿə, ߯ ŖūݓۆԐغݕॱۆ܁ʪǣٍĵфԐغজটʴ܁ʪ Ϳ҇˺, ঒ܳٮйĶۆԐͻε˞սەںìڷͿࣺɳ ʽɰ. ࣢০঒ܳOtway ॒Ϳ܄࣡ə঒ܳ߯ߣۆCCS ֬

ݒ॒Ϳ܄࣡Ϳ2005țҙࢢ2010ț6ښūݓ1ɳćԐغ ۋՁėۺڷͿݕॱʼؽڷ϶, ۋ঳5țÂ2ɳćԐغق

ʂॢ঒ܳ܁ҙۆ֧ۍںন˛ॠيݕॱܼقەɰ. ॳ঳

ڍνǣ͆قԴ߸ݕॣCCS Ԑغۆ֨ॱ޳١εܶۋČज़ څ४֮şցںঝ҃ॠşڦ३঒ܳ١࣡ڟۋԐغۆą ॹں টڌॠə ìۋц͋ݔॠɰ⁹⁾.

ۋق҆ČقԴəйĶę঒ܳۆԐͻεÂ͜০ՙÒॠ ČҼڌ߸܁ۆĵܓεԜʂۺڷͿϼঝ০܃֨ॠČەə

঒ܳۆԐͻق˰͆ڍνǣ͆ۆѕ߻ڙę۹ۤՙÀٍć ʽ սբҼڌں ߸܁३҃şͿ ॢɰ.

йĶۆսբҼ߸܁Ԑͻ

йĶۆąڍəMIT(Massachusetts Institute of Technology), CMU(Carnegie Melon University) ˣʂॡ, ŔνČTVA (Tennessee Valley Authority) ˣݓѓ܁ҙşěقԴě

֮ںÍČٍĵεݕॱॠČەɰ. EPA(Environmental Protection Agency)ۆąڍCCS ۹ۤҼڌ߸܁ۆÀۋ

˚ε܃֨ॠČەڷ϶, MIT, CMU, TVAۆąڍEPA Àۋ˚ٮəѻʪͿҼڌ߸܁قȤͳॠČەČ, ܁҃ėڮ

ф Ԝ঒ঊͳ ٍĵÀ টьॠɰ.

Carnegie Mellon UniversityۆCCS ą܃ՁथÀٍĵ əࣷۋ॒͆ۍսբę֮ҙّʂսࠗق۹ۤॠəìںÀ

܁ॠيٍĵεݕॱॠČەɰ. ۋ˞ٍĵəCO2 ࣷۋ॒

͆ۍսբę۹ۤՙ۹ۤقەرԴࣷۋ॒͆ۍࣷ͆йࢢ ۆѺজق˰͆, ŔνČ۹ۤՙ࣢Ձࣷ͆йࢢۆѺজق

9) ॴʂş, чڌ޴(2009)قԴ ۍڌॠٕɰ.

(4)

540 ťݓঞ

FACTORS - CO2 Inlet

- Temperature - Pipeline Length - Elevation Change - CO2 Inlet Pressure

- Capital Charge Rate - CO2 Outlet Pressure - Material Roughness - Number of Pumps

- Pump Pressure Ratio - Pump Efficiency - Capacity Factor - Energy Cost



TRANSPORT MODEL - CO2 Density

- CO2 Viscosity - P Per Unit Length¹¹⁾ - Reynolds Number

- Friction Factor - Pump Size

- Pumping Power Required



ESTIMATED COSTS - Pipe Diameter

- Total Capital Cost - Total O & M Cost¹²⁾

- Total Annual Cost - Total Cost Per Tonne

Fig. 2. Transport Cost Estimation Model of CMU.

˰͆ěʹҼڌۋٖॳںыóʿںъٖॠيࣷ͆йࢢ ۆԸ܁ںߕćজॠČ̚ॢࣷ͆йࢢѺজق˰͆ضυ ǣлÇॠó ҼڌۋѺজॠəÀق Ҽܼں ˃Č ەɰ.

CMUۆϿ঍ڹࣷۋ॒͆ۍۆţۋ, CO2 ݗ͟ڮʴ(mass flow)ۆԺ܁, şࢍą܃Ͽս(Č܁Ҽڌ, ڏٖфڮݓě νҼڌˣ) ˣęÏڹيæقŖäॠيÒьʼؽɰ. սբ Ҽڌ߸܁Ͽ঍ۆąڍMIT(Massachusetts Institute of Technology)ٮ DOE(Department of Energy)À Ըॱٍ

ĵॢϿ঍ںŖÂڷͿÒьʼؽəʚ, ࣷۋ॒͆ۍսբ֨

ԺۆԸ܁قٖॳںܳəڅۍ˞ںČͲॠيսբϿʝں

ĵՁॠČۋق˰͆Ҽڌںʪ߻ॠəĵܓͿʼرەɰ (Fig. 2¹⁰⁾ ޷ܓ).

սբҼڌ Ͽ঍ۆ Ը܁قə Àؓऒ॒(booster pump)˞

ÂÁࣷۋ॒͆ۍѻͿݔąۆԸ܁ۋԸॱʼرآॠəʚ, ۋÉڹڮʴCO2ۆًॡۺقȃݓј֟͢(mechanical energy balance)قşߣॠيԓ߻ॠٕɰ. قȃݓј֟͢

ə߯ʂؓ߹ʽڮߕۋ϶ࣷۋ॒͆ۍڮʴߕͿԴߣےć Ԝࢗۆ CO2Ϳ ɳտজ֨ࡈ ԓ߻ॠٕɰ.

Àؓऒ॒ۤ(booster pumping station)ڹڙäν, ԓۋ

10) Fig. 2ə2005ț‘4th Annual Conference on Carbon Capture and Sequestration’(DOE/NETL)قԴьशʽSean T. McCoy and Edward S. Rubinۆ “Models of CO2 Transport and Storage Costs and Their Importance in CCS Cost Estimates”

ق ս΀ʽ Ǵڌں ۦĵՁॢ ìۋɰ.

11) Pə ؓͳѺজε ۆйॢɰ.

12) total operating and managing costε ۆйॢɰ.

ǣسʍݓًںäߝࣷۋ॒͆ۍںࣀ३CO2εѕբॣ

սەəőϿيآॢɰ. Àؓऒ॒ۆԸ࢘ڹࣷۋ॒͆ۍ ۆҼڌ, ߸ÀۺۍÀؓऒ॒ۆज़څՁقٖॳںܳóʽ ɰ. Àؓऒ॒ۆԸ࢘ڹࣷۋ॒͆ۍݔąۆԸ࢘ęڮԐ ॠóقȃݓј֟͢εČͲॠيԸ࢘ॠ϶ۋԸ࢘قʂ ३Àؓऒ॒ۆőüɳڦͿ࠘ঞॠيҼڌ߯ՙজőϿε

Ը࢘ॠəę܁ںäߝĀ܁ॣսەɰ. ۋ˺, Àؓऒ॒

Ӽχ؉ɦ͆Àؓऒ॒ۤۆæԺфŔҙݓԸ܁ۆҼڌ ʪ߯ՙজԸ࢘ںॣսەɰ. ĀĶÀؓऒ॒ۆԺ࠘ф

Àؓऒ॒ۤæԺęࣷۋ॒͆ۍݔąۆԸ࢘ڹCO2ۆݗ

͟ڮʴέ(mass flow rate)ۆĀ܁قŖäॠيʪ߻ʽɰ Č҇սەɰ. يşقěʹČ܁ҼڌęÀѺҼڌںČͲ ॠي Ҽڌ߸܁ق ۺڌॢɰ.

CMUۆٍĵقԴəCO2ࣷۋ॒͆ۍČ܁Ҽڌ(capital cost)ۆąڍйٍѓقȃݓěνڦڙধ(FERC; US Federal Energy Regulatory Commission)قս΀ʽߎٍÀ֟ࣷ

ۋ॒͆ۍۆČ܁Ҽڌࣀćεڙڌॠيۋڌॠٕɰ. ॢठ

ڏٖҼڌ(operating cost)ڹCO2 ࣷۋ॒͆ۍۚغۋݕ ॱʼČەəPermian BasinقԴۺڌʽҼڌѺսεŖ äͿ ߸܁ॠٕɰ.

঒ܳۆսբҼ߸܁Ԑͻ¹³⁾

ٍ҆ĵقԴسśॠČۺڌॣ঒ܳԐͻəCO2CRC

13) Òѻ ŖäÀ سśʼݓ ؍ڹ À܁˞ڹ Bukhteeva et al.

(2009)ق ܃֨ʽ ì˞ں ڙڌॢ ìۋɰ.

(5)

Compressor Pipeline Compressor type

Location

Power Source type Power Source Technology Efficiency of Compressor Override Flowrate Sparing Ratio

Minimum No. of Train CPEX, OPEX, EPC

Length, Location

Relative Elevation of Segment Steel Grade, Water Depth Override Pipeline Diameter Override Flowrate

Linepipe Density, Design Pressure Corrosion Allowance

Max/Min Pipeline Pressure Topography

CPEX, OPEX, EPC

 

Platform EPC CAPEX Abandonment COST Total/Annual OPEX Total EPC CAPEX

Total/Annual Fixed/Variable OPEX Abandonment COST

Total/Annual OPEX Total EPC CAPEX Fig. 3. Transport Cost Estimation Model of CO2CRC/UNSW.

(Cooperative Research Center for Greenhouse Gas Tech- nologies)ٮUNSW(the University of New South Wales) ÀܳʪॠيݕॱॠČەəٍĵۋɰ. ۋə঒ܳۆي͠

ٍĵşě, ʂॡ, şغ, ėėҙЛ˞ۋ ޷يॠČ ەڷ϶,

঒ܳۋٽĶÀۆٍĵݕ˞ęʂşغ˞ʪψڹě֮ں

҃ۋČەɰ. Wandoan, Otway ˣ֬ݒԐغںݕॱॠ Čەرę܁قԴصرݕąॹę֬ݒԐ२ںࢹʂͿٍ

ĵĀęε܃֨ॠČەşقψڹşʂεыČەɰ. ࣢০

঒ܳOtway ԐغڹCO2 ۹ۤęěʹʽϿ˜қآ, ݌, ė܁, ٍĵ, ő܃, İگ, ঵ʹ, ঊͳ, ࠶Яɦ࣯ˣںप॥

ॠيܛ०ۺۍݓ֩ںঝ҃ॠəìںЀशͿݕॱʼČ

ەČ, ۋقҙ०ॠó঒ܳCO2CRC ܳěॠقйĶ, ࠪ ǣɰ, ɑݗ͔˚ˣՃć ܳڅĶ CCSěʹ ٍĵşěф

ʂॡęBHP Billiton, Chevron, Schlumberger ˣՃć

ܳڅěʹşغۋėʴ޷يॠČەɰ¹⁴⁾. ۋٮÏڹيæ قԴ֬܃۹ۤۋݕॱʼČەرCCS Ԑغěʹۙ˞ۆ

ܳڅě֮ʂԜۋ϶, ؉ڐ͠ɰتॢ޷يܳߕ˞ۆٍĵ Ձę˞ۋȦۆфۺڌʼČەرՃćٍĵՁęۆܛ० ߕًॣں ॠČ ەɰČ ҇ սەɰ.

঒ܳ CO2CRCٮ UNSWÀ Òьॢ ҼڌϿ঍ڹ ێъ জεЀۺڷͿĵ߹ʼؽڷ϶, ˰͆ԴथŒۺۍԐ२˞ں

ܼ֮ڷͿҼڌĵܓε ঍ՁॠČ ߸܁࠘ε ʪ߻ॢɰ.

Ҽڌ߸܁قČͲʼə२ЀڹFig. 3¹⁵⁾ق܃֨ʽцٮ

14) ťচş(2012) “३ٽCO2 ۹ۤࣷێ॒ͦͿ܄࣡ٮڍνق ۆ֨Ԑ۾”, ܃2ধKorea CCS Conference ьशۙΒ޷ܓ.

15) Fig. 3ڹAllison et al.(2006)ۋ܃֨ॢԐ२ں۹ۙÀۦĵ Ձॢ ìۋɰ.

ÏۋՃҙۺۍԐ२˞ںČͲॠيۻߕҼڌ߸܁ں֨ʪ ॠəʚ, ۋəؘقسśॢйĶCMUۆԐͻٮڮԐॢ

ĵܓε ҃ۋČ ەɰ.

঒ܳԐͻۆCCS ԐغۻߕقʂॢҼڌ߸܁ѓѪڷͿ əNPV(Net Present Value method)εۺڌॢɰ. ܳۓş Âڹߪ20țںş҆ڷͿÀ܁ॠ϶, ۻߕԐغşÂقě ćػۋ2țÂۆԺćфæԺę1țÂۆदşۚغۋप

॥ʼرەɰ. ইۦÀ࠘εԓ߻ॠşڦ३ज़څॢॣۍڱ ڹ7%εۺڌॢɰ.¹⁶⁾ ҼڌĵܓəæԺфۤҼԺ࠘Ҽ ڌęÁܛॱ܁ۼ޲ݕॱقՙڅʼəҼڌۍCAPEX(real capital costs), æԺওڹԺ࠘ʽۙ҆ۆێԜۺڮݓě νҼڌۍOPEX(real operating costs), ԐغܛΒق˰͆Č

܁ԦԓڅՙεदşॠəʚقՙڅʼəҼڌۍABEX(real abandonment costs)Ϳĵқॢɰ. ۋ˺, OPEXٮABEX ə३ɾҙқۆCAPEXεČͲ३߸܁ॢɰ. CO2 ѕ߻

ڙۍьۻՙۆąڍ500MWśڷͿÀ܁ॠ϶CCS ͔॔

࣡æԺڹ2țܼߒ३ق40%, ۋˠ३ق60%Àݕॱʼ əìڷͿॢɰ. CAPEXقəCAPEXۆأ9.1%ق३ ɾʼəٚҼҼ(contingency)εप॥֨ࢅ϶, ۍæҼ, ՙϿ

ुҼ, ćأфۍॴÀڮݓҼəæԺҼۆ4%ͿÀ܁ॢ

ɰ. ۋ˺, ۍæҼقəݔۿڏۻŖͿۙ, Çʫۍͳ, ۍͳě νقՙڅʼəҼڌۋϿ˃प॥ʼرݔۿڏۻŖͿۙۍ

16) ۋə঒ܳقԴۙڙÒьԐغقۺڌॠəێъۺۍॣۍڱ ͿԴ঒ܳԵڮÀ֟ʂşغ֬ݗʂҙۋۙڱۆ߯Ŗ߸ۋق

ŖäॢÉۋɰ. ڍνۆąڍʴێॢ२ЀۆÉںʪ߻ॣս

ػČ, ɳտ০֬ݗʂşغʂ߻ۋۙڱںۺڌॠşقəۙڙ Òьşغۆ࣢ՁʪъٖॠݓЇॠдͿٍ҆ĵۆĶǴ֨ԓ قʪ ঒ܳԐͻۆ ॣۍڱں ۺڌॠٕɰ.

(6)

542 ťݓঞ

Table 1. Four Cases for Korean CCS Pipeline Transport Project

CASE 1 CASE 2 CASE 3 CASE 4

70 km 100 km 250 km 200 km

- ڐιқݓٮPOSCO/Եڮজ ॡɳݓ

- ڐιқݓٮ ֪ьۻՙ

- ܃ܳқݓٮǫҙ३؋ьۻՙ - ڐιқݓٮǫҙ३؋ьۻՙ - ڐιқݓٮ ġت(Ԙߎप) - ķԓқݓٮԴ३؋ьۻɳݓ

- CASE 3ۆʂԜقʂ३گ ३Ԝ ѿॱ

- ĶǴঞąقԴ ߯ۺԸ࢘

- ڐιқݓٮԵڮজॡɳݓə

50 km, POSCOə70 km սܵ

- ֪ьۻՙεæԺॢɰϸۋ

70 km սܵقæԺॢɰČ

À܁

- ǫҙ३؋ݓًق3 GW ś

Ե࢏ьۻՙÀॠʴ, Ԙߎप ق ەڼ

- ۋ äνÀ 100 km սܵ

- ڐιқݓٮҼİॠϸۋݓً

قəɳ3Òۆdrilling wells Àەڷǣߪ10,000 line-km ۆ2D ф3D seismic dataÀ

ەڼ

- ڐιқݓۆ ߯ۺ ۹ۤҙݓ ٮġتۆ֪ьۻՙওڹǫ ҙ३؋ ьۻՙ˞ęۆ äν À ʂ͜ 200-300 km - ̚ॢķԓқݓٮԴ३؋ь

ۻɳݓۆäνəأ200-250 km

- ķԓқݓə dataÀ ߿қݓ

Ї॥

- ڐιқݓٮ ǫҙ३؋ ьۻ ՙ: ڐԓݓًں äߝ گԜ

150 km սբ঳३Ԝ50 km սբ

- ࣷۋ॒͆ۍ æԺę܁ق ज़ څॢҙݓϔۓфے޲Ҽڌ ڹ ঒ܳ Ԑͻق ˰ζ

æҼۆ1.56ѕͿۺڌॢɰ.¹⁷⁾ ࣷۋ॒͆ۍսբںۻ܃ॠ

϶ࣷۋ॒͆ۍҼڌڹCO2 ܳۓۋ110bar ؓͳڷͿۋ Θرݕɰə ìں À܁ॠي ԓ߻ॢɰ. दşҼڌڹ ߯ߣ

æԺҼٮproject ěνҼڌۆ25%ۍìڷͿÀ܁ॢɰ.¹⁸⁾

঒ܳԐͻəێъজॣսەəҼڌ߸܁Ͽʝںĵ߹ॠ əʚقێ܁Ҽܼں˃Čەر֬܃ԜغۺԐغ֨ॱ

֬ۺۋййॢCCS қآقʂ३ҼڌڅۍęҼڌÂۆ

थŒۺěćεۺڌॢѓѪڷͿҼڌ߸܁ĵܓε܃֨ॠ Čەرڍνǣ͆ۆąڍٮÏۋ܁҃ÀҙܔॢʂԜق

ʂॢ CCS Ԑغ Ҽڌ߸܁ق ڿڌॠş ڌۋॠɰ.

ĶǴѕ߻ڙф۹ۤՙٍćսբҼ߸܁

ࣷۋ॒͆ۍսբҼεࣷ؊ॠşقə؉ݔ܁҃À߿қ ॠݓ؍ɰ. ࣷۋ॒͆ۍۆ঍ࢗǣڦ࠘ˣقʂ३ԴʪĀ

܁ॣսەəսܵۆ܁҃Àঝ҃ʽԜࢗÀ؉ɦǣ, Ò͜

ۺۍɳڦҼڌںࣷ؊ॠəìڹ܁޾ۺۆԐĀ܁ۆşߣ ŖäͿԴज़սۺۍۙΒۋɰ. ˰͆ԴɰڼۆशTable 1 ęÏڹ4ÀݓԜডقʂ३঒ܳۆԐͻٮÏڹيæق

ەɰəÀ܁ॠقսբäνق˰δɳڦҼڌں֨ԓॠ şͿ ॢɰ.

սբҼڌ߸܁ڹCO2CRC/UNSWۆϿ঍ںۋڌॠٕ

ڷ϶ڦ4ÒCASE¹⁹⁾(70, 100, 250, 200 km)قʂ३3 ÒܳۓşÂ-20, 30, 40ț-ںۺڌॠٕɰ. ۋ˺Ըॱ3

17) ۋə঒ܳۙڙÒьԐغߕۆҼڌĵܓ֬ԐͿʪ߻ॢÉڷ Ϳ ؎Ͳ܋ ەɰ.

18) ҆ԐͻقԴÀ܁ʽÉ˞ڹۙڙÒьşغۆąॹ࠙قŖä ॠي ʪ߻ʽ ìۋɰ.

19) чڌ޴ٽ(2009)ٮDae-Gee Huh et al.(2010)ق܃؋ʽٍ

ć Ͽ঍ں ŖäͿ ॠٕɰ.

Ò CASEə ѕ߻ڙۋ ३؋ق ڦ࠘ॠдͿ ३۹ق Ͽ˜

ࣷۋ॒͆ۍۋ Ժ࠘ʼə ìں À܁ॠٕɰ. Ūۋə ३۹

140 mε ێĜ ۺڌॠٕɰ. ѕ߻ڙ ьۻՙə 500 MW śԵ࢏ьۻՙεԜ܁ॠٕڷ϶ٍÂ3,378іχࢻںѕ

߻ॠə ìڷͿ À܁ॠٕɰ²⁰⁾. ʴێॢ ѕ߻À܁ق սբ ͿÀگԜф३ԜڷͿܓՁʽąڍقʂ३Դʪ޷Čۺ ڷͿ߸܁ں֨ॱॠٕɰ. ۋəCASE 4ق܃֨ॠٕəʚ, ǫҙ३؋ьۻՙεѕ߻ڙڷͿ, ڐιқݓε۹ۤՙͿԸ

܁ॢąڍͿԴ, ǫҙ३؋ьۻՙقԴڐԓݓًūݓəگ Ԝࣷۋ॒͆ۍڷͿ, ڐԓݓًقԴ۹ۤՙūݓə३Ԝࣷ

ۋ॒͆ۍڷͿ սբॠə ìں Ԝ܁ॢ ìۋɰ.

Ժ܁ʽÀ܁ۋ±10% ١޲εÍəɰəۻ܃ॠقĵÂ ڷͿʪ߻ʽĀęεTable 2 фFig. 4ق܃֨॰ɰ. CO2

ɳڦɾսբҼəܳۓşÂۋţս΀, սբäνÀÀūڐ ս΀Çՙॠٕɰ. սբäνÀ70 kmقԴ100 km, 250 kmͿݒÀ॥ق˰͆20țşÂقʂ३أ6.6%, 47.4%

ݒÀॠəìڷͿǣࢍǮڷ϶, گԜę३Ԝںѿॱॢą ڍقʂ३Դəأ57.9% ܁ʪݒÀॠəìڷͿǣࢍǮ ɰ. şÂۋ30ț, 40țڷͿݒÀ॥ق˰͆CO2սբɳ ڦɾҼڌڹأ14.9%, 24.1% ܁ʪǰ؉ܐɰ. گԜę३ ԜսբѿॱڷͿÀ܁ʽսբͿεۺڌॢąڍəԐغ

ԺćæԺфÇʫęۼ޲ۺěνҼڌˣۆԜ֧ڷͿҼ ڌۋ ݒÀॠə Āęε ٕ҃ɰ.

ɰδ Ըॱٍĵ˞ę Ҽİॠϸ, ঒ܳ ۋٽۆ Ԑͻٮə

ɰՙ߸܁ѓѪق޲ۋÀەşʪॠݓχ, CO2۹Çɳڦ ɾ߸܁Āęۆ޲ۋÀьԦॠəܳڅڙۍڹսբäν

20) ঒ܳԐͻÀԜ܁ॢ500 MWśԵ࢏ьۻՙۆѕ߻͟ںڙ ڌॠٕɰ.

(7)

Table 2. Estimation Results

Pipeline Route 70 km 100 km 250 km 200 km

Injection Period (yrs) 20 30 40 20 30 40 20 30 40 20 30 40

Transport CAPEX (US$MM)

122.8 122.8 122.8 135.1 135.1 135.1 191.3 191.3 191.3 207.8 207.8 207.8 100.5 100.5 100.5 110.5 110.5 110.5 156.5 156.5 156.5 170.0 170.0 170.0 Transport OPEX

(US$MM)

24.7 28.7 30.8 25.5 29.8 32.0 30.8 35.1 37.7 31.3 36.6 39.3 24.7 28.6 30.8 25.4 29.8 32.0 30.7 35.0 37.6 31.2 36.5 39.2 Transport ABEX

(US$MM)

7.5 3.7 1.9 7.9 4.0 2.1 11.8 5.7 2.9 12.1 6.1 3.2 6.0 3.0 1.5 6.5 3.3 1.7 9.7 4.7 2.4 10.0 5.0 2.6 Transport cost of CO2

avoided (US$/t)

7.6 6.4 6.0 8.1 6.9 6.5 11.2 9.5 8.9 12.0 10.3 9.5 6.2 5.2 4.9 6.6 5.7 5.3 9.2 7.8 7.3 9.8 8.4 7.8

Fig. 4. Effects of distance between source and sink and injection period on transport.

фսբيæęѕ߻͟ۆ޲ۋۋɰ. ۋəܳڅԸॱٍĵ ÀگԜČÄڮÀ֟ۻں۹ۤ঳҃ݓͿÀ܁ॠي۹ۤ

঳҃ݓٮѕ߻ڙÂäνεݥóԺ܁ॠČ, ۹ۤ঳҃ݓ ͿÀ܁ॢČÄڮÀ֟ۻقǫ؉ەəբڮѕěˣսբ

֨֟ࢰںۦটڌॣÀɠՁںۍ܁ॠČ߸܁ॠٕڼںϊ

ॢɰ. Ӽχ؉ɦ͆ѕ߻͟ۆÀ܁ʪڙۍڷͿۚڌॠş ʪॠəʚѕ߻ڙۆőϿεԜʂۺڷͿࡾóÀ܁ॠČ

ʴşÂपݚʽ CO2ۆ սբ͟ں ɚͲ À܁ॢ ąڍ˞ۋ

ەɰ. ۋͩóսբ͟ۆÀ܁ۋɰδąڍəܳͿսբۤ

࠘ۆॠǣۍؓ߹ş(compressor)ۆɠͳںȭóۍ܁ॢ

ąڍͿɳڦ֨ÂɾսॱɠͳۋʌܞڹìڷͿÀ܁ॢ

ìۋɰ. McCoy and Rubin(2005)əսբäνε30 km սܵڷͿÀ܁ॠČѕ߻ڙۍŖۆČÄڮ·À֟ۻں ۹ۤ

ՙͿ Ԝ܁ॠٕڷ϶, şܕۆ սբěʹ څՙε ۦটڌॣ

սەڼںۻ܃Ϳ߸܁ॠيɳڦսբ͟ɾҼڌں3US$

ۋǴͿʪ߻ॠٕČ, McCoy and Rubin(2008)ڹѕ߻ڙ ں800 MWśԵ࢏ьۻںÀ܁ॠي200 km սբäν

ۆąڍقʪڮԐॢۻ܃ॠق5US$ йχۆɳڦսբ͟

ɾ Ҽڌں ʪ߻ॠٕɰ.

Ā΁

҆ČəĶǴCCS ԐغۆսբҼڌ֨ԓقЀۺں˃ؽ ɰ. ۋ֨ԓڹěʹ܁҃À߿қ০ঝۍʼݓ؍ڹيæق Դ, ॢĶۆيæقҙ०ॠə२Ѐ˞ںϸн০ČͲॠي

߸܁ॠş҃ɰə, Ըॱ߸܁ԐͻÀԐڌॢѓѪںۺڌ ॠيĶǴܳڅѕ߻ڙęܳڅ۹ۤՙ঳҃ݓÂۆٍć ق˰δսբҼڌں߸܁ॠəìںЀۺڷͿॠٕɰ. Դ

˃قԴəইۦĶǴٽͿݕॱʼČەəCO2 ۹Çćন قʂ३Â͜ॠóՙÒॠٕČ, ۋرܳڅCO2ьԦф

ѕ߻ڙۆőϿٮݓًقʂ३ÒĜۺڷͿԕट҃ؕڷ϶

ۋεۻ܃ͿĶǴCCS Ԑغۋ֨ॱʾąڍۆCO2 ۹Ç

ɳڦɾ սբҼڌق ě३ ߸܁ॠٕɰ. ĶǴ Ҽڌ߸܁ق

ؘԴ, CCS Ҽڌ֨ԓۆԸॱԐͻεÒĜۺڷͿ܃֨ॠٕ

ڷ϶঒ܳۆCO2CRC/UNSWÀÒьॢԸॱԐͻεŖ äͿĶǴѕ߻ڙ-۹ۤ঳҃ݓÂܓ०˞قʂ३ࣷۋ॒

͆ۍսբҼڌں߸܁ॠٕɰ. սբѓѪڹ३Ԝںܼ֮ڷ ͿॠČ, گԜф३Ԝںѿॱॠəąڍقʂ३ԴʪČͲ ॠٕڷ϶, ÁÁقʂ३CAPEX, OPEX, ABEXεʪ߻

ॠČۋεࢹʂͿܛ०ۺۍथŒɳڦɾҼڌںʪ߻ॠ

ٕɰ. ߸܁Āęə ܳۓşÂ 20țں şܵڷͿ սբäν ق˰͆CO2 ۹Çɳڦ(t)ɾ4.9 US$ - 12.0 US$ ūݓ

ǣࢍǮɰ.

҆ĀęəێъজʽϿ঍ںĵ߹ॠČۙÒьʽԸॱٍ

ĵԐͻεࢹʂͿĶǴيæقԴÀɠॢäν, սբф۹

ۤՙ঳҃ݓܓæںʪۓॠي߸܁ں֨ʪॢìۋɰ. ɰ δԸॱٍĵقԴǣࢍǦ߸܁ęɳտ০ĀęεҼİॠş

҃ɰČÄڮ·À֟ۻۋǣ şܕڮ·À֟ÒьԦԓ֨Ժۋ

(8)

544 ťݓঞ

׌஺ฅ

1999ț ąڙʂॡİ ą܃ॡę ॡԐ 2002ț ČͲʂॡİ ą܃ॡę ԵԐ

ইۦ ॢĶݓݗۙڙٍĵڙ ٍĵۻ֬͜ ۙڙą܃ࣳ ٍĵڙ (E-mail; [email protected])

ػəيæقԴۆ߸܁ۋдͿ, ۻߕCCS Ԑغݕॱقە رڍνيæقԴսբڷͿۍ३ԓۓʼرآॣҼڌۋ

رɗ܁ʪۍݓε߸܁ॠəʚقşيॠČۙॢɰ. ؉ڐ

͠ইۦCCSԐغں߸ݕॠČەəԜডقԴҼڌқԵ ڹ०νۺ܁޾ۆԐĀ܁ںڦ३Դʪݕॱʼرآॠ϶, ʌڎعнॢҼڌқԵقͿǣ؉Àşڦॢɳߣε܃ė॥

ق ҆ ٍĵۆۆۆÀ ەɰČ ॣ ìۋɰ.

ԐԐ

ٍ҆ĵəݓ֩ą܃ҙقԴ֨ॱॢ“঒ܳ١࣡ڟۋࣷ

ێ॒ͦͿ܄࣡޷يεࣀॢݓܼ۹ۤ֬ݒşъĵ߹”ę

܃ۆ ݓڙڷͿ սॱʼؽڷ϶, ҆ ٍĵۆ ֮Ԑę܁قԴ

ψڹܓسęæԺۺۍҼࣺںࣀ३ȦЛۆݗۺॳԜق

ψڹʪړں֪ܳیϼۆ֮Ԑڦڙ˞ƍŪڹÇԐε˚

ςɦɰ.

޷ČЛॶ

׌ก׆, 2012, “ැ૤CO2ୠୋ൞ଵߍඹߦ୫ൈ૕૴ࠤ઩

ଭਏॷ୥,”୪2ฎKorea CCS Conference, Korea CCS Conference ୺஻଍଀ฎ, ୪சޭࠬۗරޭୀ෹ഖ, ୪ச, 3

ଁ 16ଵ.

ڌআনୋ଍଀ฎ, 2009, “֝ԧ૊ਓԧਆண׆Ԯౠࡧඝড ୨ଡ଍෉3ԧ஺ਏيࠤૈ୪ਏ,” ڌআনୋ଍଀ฎܑ࣪

ୀ߹, 2009ڂ 8ଁ 4ଵ.

ڌআনୋ଍଀ฎ, 2010, “ڌআনୋ, ਏୋր෌״෹ใ෉ۗ,”

ڌআনୋ଍଀ฎ ܑ࣪ୀ߹, 2010ڂ 7ଁ 12ଵ.

ࢮ૳ఛ, ෛ۩׆, ׌஺ฅ, 2011, “CCS լ୪নंজࡦ܄,”୪ 1ฎKorea CCS Conference, Korea CCS Conference ୺஻

଍଀ฎ, ୪ச ޭࠬۗරޭୀ෹ഖ, ୪ச, 4ଁ 13-15ଵ.

ࢮ૳ఛ, ෛ۩׆, କܛֽ, จপ෹, ଲๅ઴, ڋଡ, 2009, “֝ٛ

CO2 ஺ணୠୋॷડฃࢺੲՑഠ,” ஺ா෈ฎ஺, ୪45֫

5෹, pp. 579-587.

૊ਓԧਆஂ෍୨࣪বഉ૊ਓԧਆധծ, 2011. 12. 3, http://

www.gir.go.kr.

ෛ۩׆, ࢮ૳ఛ, 2009, “෹சૈൈଆଲଲॺฃ೶ী஺ணୠ

ୋ ॷડ෮จ”, ஺ா෈ฎ஺, ୪45֫ 5෹, pp. 517-525.

Allinson G, Neal P, Ho M, Wiley D and McKee G, 2006, CCS Economics Methodology and Assumption, CO2CRC, pp. 8-30.

Bukhteeva, O., Neal, P. and Allinson, G., 2009, “Optimisation economics for CO2 capture and storage in Central Queens- land (Australia)”, Energy Procedia, Vol. 1, pp. 3969-3976.

Dae-Gee Huh, Yong-Chan Park, Dong-Geun Yoo and Se-Ho Hwang, 2011, “CO2 Geological storage potential in Korea,”

Energy Procedia, pp. 4881-4888.

IEA, 2008, “Energy technology perspectives 2008: scenarios

& strategies to 2050,” OECD/IEA.

Ji-Whan Kim and Yong-Chan Park, 2011, “A case study of CCS Cost estimation : ICCSEM applied to Korea,”

CO2CRC Research Symposium 2011, CO2CRC, Adelaide Australia, November 29-December 1.

McCoy S., Rubin E., 2005, “Models of CO2 transport and storage costs and their importance in CCS cost estimates,” Fourth Annual Conference on Carbon Capture and Sequestration, U.S. Department of Energy/National Energy Technology Laboratory, May 2-5.

McCoy and Rubin, 2008, “An engineering economic model of pipeline transport of CO2 with application to carbon capture and storage,” International Journal of Greenhouse Gas Control, Vol. 2 No. 2, pp. 219-229.

McKinsey & Company, 2008, “Carbon capture & storage:

assessing the economics,” McKinsey & Company, http://

www.mckinsey.com/clientservice/ccsi/.