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  • 2016-09-29

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    CBE4016 CBE4016

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    1. Introduction

    l Refining Industry (, Chapter 2)

    l Petrochemical Industry (, Chapter 3)

    (Petroleum Industry)

    CBE4016

    1. Introductionl Refining Industry (, ):

    v Refinery products : gasoline, , , , grease, asphalt, , , ,

    v Process (straight-run distillation) (conversion): cracking, reforming and others (purification) (formulation) others: alkylation, dehydration, isomerization,

    polymerization, hydrotreating, coking, etc.

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    1. Introductionl Petrochemical industry

    ,

    v , , () , , , , , ,

    () , , ()

    v Process Manufacture of base chemicals by naphtha cracking Conversion into main product groups Processing of finished products

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    5

    1 2 3 4 5

    2011

    2012

    2013

    M$

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    1. Introduction

    1)

    : hydrocarbon (H: 10~14%, C:79~88%)*

    Oxygen compounds (0~3%):

    in naphthenic acid, alkyl acid, phenolic acidNitrogen (0.1~0.7%): found in naphthenic acid,

    in the form of basic compounds (alkyl quinoline)Sulfur (0.1~5%): present in crude oil or produced during refining; free S, H-S-H, organic compounds

    foul smell, , , Trace amount (ppm) of metal-organic compounds

    1.

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    Organosulfur Compounds

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    1. Introduction

    2)

    ) Hydrocarbon (HC) series:

    CnH2n+2, CnH2n, CnH2n-2, CnH2n-4, CnH2n-6, CnH2n-8, CnH2n-10, CnH2n-14, CnH2n-20, etc.

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    Structural Formulae of HC Series (C6)

    H C C

    H

    H

    H

    H

    C C

    H

    H

    C C

    H

    H

    H

    H

    H

    H

    H

    H C C

    H

    H

    H

    H

    C C

    H

    H

    C C

    H

    H

    H

    H

    H

    H

    H HH

    H

    H

    H

    H H

    H

    H

    H

    H

    H

    H

    H

    H

    H

    H

    C C

    H

    H

    H

    C C

    H

    H

    C C

    H

    H

    H H

    H

    H C C

    H

    H

    H

    H

    C C

    H

    H

    C

    H

    H

    H

    H

    CH

    H

    HH C

    H

    H

    C C

    H

    H

    C

    H

    H

    H

    CH

    H

    H

    CH H

    H

    (a) Normal Hexane, C6H14 (b) Normal Hexene, C6H12

    (c) Cyclohexane, C6H14 (d) Benzene, C6H6

    (e) Hexadiene-1, 5, C6H10

    (d) 2 Methylpenthane, C6H14 (f) 2-2 Dimethylbutane, C6H14

    Isomeric IsoparaffinCompounds

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    1. Introduction) Hydrocarbon (HC) series:

    Paraffin series (CnH2n+2) physical state b.p: normal > iso- > neo-

    Olefin series (CnH2n) direct reaction with Cl, Br, HCl, H2SO4 recovered by H2SO4 (dissolution) low bp olefin: not present in crude oil by thermal

    cracking

    Naphthenic series (CnH2n) ring or cyclic compounds aromatic olefin

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    1. Introduction Aromatic series (CnH2n-6) or benzene series (Bz)

    : susceptible to oxidation organic acid (high b.p) ENPLA

    Diolefin series (CnH2n-2) : extremely active polymerize, combine with unsaturated compounds

    higher MW

    Cyclic series (CnH2n-2, (CnH2n-4 ) Not well known

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    1. Introduction) Sulfur compounds - Structural formulae

    H S HH S R

    H S CH3H S C6H5

    R S RH3C S CH3C4H9 S C4H9

    S S RRS S CH3H3C

    S

    CH2

    CH2 n

    R O

    S

    OR O

    O

    R

    S

    OH O

    O

    R S R

    O

    R S

    O

    O

    R

    C

    S

    C

    C C

    HH

    H H

    Hydrogen sulfideMercaptans:

    Methyl

    Benzyl

    Sulfides:Methyl

    n-Butyl

    Cyclic sulfide:

    Alkyl sulfide

    Sulfonic acid

    Sulfoxides

    Sulfones

    Thiophene

    Disulfides:Methyl

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    1. Introductionv Problems:

    Corrosion of metals by H-S-H, free S, some of lowest bp sulfides, disulfides, mercaptans

    Pollution: rxn with O2 SO2 acid rain

    Obnoxious odor: with low b.p or gaseous sulfur compounds such as H-S-H, SO2 in flue gas, mercaptanup to 6 carbon atoms, sulfides up to 8 carbon atoms, methyl disulfides

    Poor explosion characteristics of gasoline fuel

    removed by sweetening treatment or alkalies

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    1. Introduction

    1) /: (~ ) (low bp sat. HC, aromatics) (N-, S-compounds, HC)

    (vs. high bp HC)

    2) : 0.65 ~ 0.95 (refers to 60 oF = 15 oC)aromatics > naphthene > paraffinl specific gravity ()

    l API gravity ()

    l characterization factor

    2.

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    1. Introduction3) ()

    - its resistance to internal flow or indication of oilness in the lubrication / :

    l relative viscosity (): numerically equal to viscosity in cp

    l kinematic viscosity, l fluidity: reciprocal of viscosity

    l viscosity index (VI): Pennsylvania crude oil (H): VI = 100 Gulf coast crude oil (L): VI = 0

    the higher, the better 100VI --

    =HLUL

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    1. Introduction

    4) (specific heat, cal/g oC): 0.3 ~ 0.5 @ 25 oC (0.3 ~ 0.5) H

    5) (heat of vaporization/mole- or g-basis) 70 ~90 cal/g (less than H2O, alcohol) HC () g

    u , Q (calorific value): 9,500~12,000 kcal/kg (> coal)( g )

    v TOE: ton of oil equivalent, 1 107kcal

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    1

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    kcal MJ

    kg 10,750 45.0 1.075 8,000 33.5 0.800

    8,800 36.8 0.880B-C 9,900 41.4 0.990 kg 12,050 50.4 1.205 kg 11.850 49.6 1.185

    (LNG) kg 13,000 54.5 1.300(LNG) Nm3 10,550 44.2 1.055(LPG) Nm3 15,000 62.8 1.500

    kg 4,650 19.5 0.456 kg 6,550 27.4 0.655

    () kg 6,200 26.0 0.620

    kWh 2,150 9.0 0.215 kg 4,500 18.8 0.450

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    One pound of hydrogen holds 52,000 Btu, three times the energy of a pound of gasoline

    CBE4016

    Transition to Hydrogen Economy

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    1. Introduction

    6) Cloud point & Pour point- useful in estimation of relative amount of wax cloud point (): solid point: 5

    (heat to 115 oF and then cooled to 90 oF, DT = 5 oF) pour point (): cold filter plugging point:

    v flow improver: poly(isobutene), poly(methacrylic ester), poly(alkyl styrene)

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    1. Introduction7)

    8) Smoke point: (in mm)

    9) (distillate) eg. 10%

    95% boiling point (LPG)

    * (distillate, cut, fraction)

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    1. Introduction

    1) l 1870. () Ohio Standard Oil

    (10 )l 1882. :

    Standard Petroleum Trust ( )l 1885. Benz: /Ford:

    l 1890. : Royal Dutch Petroleum ()l 1898. Diesel engine l 1907. Shell Royal Dutch Shell l 1903. Wright: Application of gasoline engine to air plane

    *

    3.

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    1. Introduction

    l 1908. DArcy (): Anglo Persian Petroleum ( ) British Petroleum (BP)

    l 1909. Standard Oil: * l 1911. Anti-Trust law ( ):

    Standard Petroleum Trust 34 NJ Standard Exxon Indiana Mobil Ohio Sohio Atlantic, Continental, etc.

    l 1913. / l 1914~1918. 1

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    1. Introduction

    l 1920. San Remo ( ) (Turkey )

    l 1928. (Anglo Persian, Royal Dutch Shell, NJ Standard) Major

    Major: (50s ~ 1973)(, , , )

    7 Sisters: Exxon, Mobil, Texaco, GulfChevron, Shell, BP

    8 Sisters: + CFP Independent /OPEC

    (1960 )

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    1. Introduction

    l 1960. 9 OPEC (S.A, Kuwait, Iran, Iraq, Venezuela) 11 (97)

    l 1973. 1st oil shock ( 4 ), OPEC (, , ) Major ( )

    (2.5 11.25 $/9)l 1979. 2nd oil shock ( ) (12.95 32 $/10)l 1980 - l 1990. Gulf war (17 41 $/3)l 1992. 17 $/bbl

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    1. Introduction

    l 2004. l 2005. 3rd oil shock ? (28 32 >60 $)

    OPEC (, 8/30: 80 $ ?)

    l 2008. 3 ~ 100 $ (WTI) : Another Oil Shock ?l 2008. 10 ~ 70 $l 2009. 9 ~ 70 $/bbll 2001. 9. 11 100$ l 2012. 9 ~ 91 (WTI) ~ 108 (Brent) $/bbl

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    3.0

    ,

    (: 110$ (7) 85$ (14) 76$ ??)

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    3.0

    (IEA: - 22%)

    -

    (: 9240 bpd; 20 bpd )

    - , /

    - 70 (IEA)

    , -

    - , , , ()

    - OPEC

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    3rd

    4th

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    2015

    40$

    2015 8 16

    49$

    08-14

    42.5$

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    (500 bbl/d to 850 bbl/d: 70% )

    OPEC

    ()

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    41.87$ (817) 6 ( 2009.03) " 30 : 15 ,

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    ,

    : - 90% , ()

    - :

    ( 10% 0.02%P)

    - ( 20%) : - - () :

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    I

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    II

    ,

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    ,

    ,

    10 ~ 20$ ??

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    3. :

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    70()

    80()

    80 ~90

    ()

    90

    ( )

    00 ~()

    ()

    ()

    ()

    M&A

    Capa()

    155/(1)

    505/(2)

    4,330/(8)

    5,700/(7)

    8,500/(15)/(6)

    GDP()

    2.9(28.0%)

    1.4(12.0%)

    1.3(10.0%)

    1.0(3.0%)

    IT,BT,NT

    /('86)

    ( )

    ) -

    ( )

    ()

    *Restructuring, M&A*/

    Mega competition

    */ * *

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    07/13

    B/D

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    2013

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    (103 bbl)

    (103 bbl)

    1986 219,667 209,729 17,477 575 4.3 790 72.7

    1990 308,368 307,281 25,607 842 3.6 840 100.2

    1994 573,714 560,866 46,739 1,537 3.1 1,700 90.4

    1995 624,945 631,078 52,590 1,729 12.5 1,818 95.1

    1996 721,927 720,846 60,071 1,970 13.9 2,438 80.8

    1997 873,415 871,974 72,665 2,389 21.3 2,438 98.0

    2000 893,943 890,304 74,192 2,433 1.7 2,438 99.8

    2001 859,367 860,115 71,676 2,356 -3.1 2,438 96.7

    2002 790,992 786,805 65,567 2,156 -8.5 2,438 88.4

    2003 804,809 782,951 65,246 2,145 -0.5 2,438 88.0

    2004 825,790 826,551 68,879 2,258 5.3 2,438 92.6

    2005 843,203 852,439 71,037 2,335 3.4 2,735 85.4

    2006 888,794 878,395 73,200 2,407 3.0 2,808 85.7

    2008 864,872 865,663 72,139 2,365 -2.1 2,875 82.3

    2010 872,415 872,247 72,687 2,390 4.0 2,935 81.4

    2011 927,044 924,441 77,037 2,533 6.0 3,039 83.3

    2012 947,292 945,162 78,764 2,582 2.0 2,949 87.6

    2013 915,075 906,674 75,556 2,484 -3.8 2,949 84.2

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    2(2008 1~12)

    2008 370 $

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    2015

    (7 ~ 9 : 75$ )

    1$

    (9 : 7,279$)

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    (Jan. 2015)

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    GDP

    2.22%

    1.59%

    1.46%

    1.31%

    0.66%

    ?

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    1. Introduction

    2) l 1960s (3)

    / ( ) (Major )

    1962. (, ) + Gulf ( ) 35,000 bpd (1964) 810,000 bpd (2003, SK)

    1965. () + Shell 50,000 bpd () (, 92) (93) 310,000 bpd (02)

    1966. (, ) + Caltex LG 60,000 bpd (1969) 600,000 bpd (GS-Caltex)

    1967. (1966)

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    1. Introduction

    2) ()l 1970s (3~4 )

    Major ( ) /

    1972. (, ) + Indep. Union Oil 50,000 bpd

    Oil bank (99) (275,000 bpd)

    1972.10 1973. 1979.02

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    1. Introduction

    2) ()l 1980s *

    , (83~86) 1980. () + NIOC:

    60,000 bbl 443,000 bbl (S-Oil)

    l 1981.9 (1990s)l 1980s 3

    /* (, )

    l 1989 () 60,000 bpd

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    1. Introduction

    *

    * : / /

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    1. Introduction

    2) ()l 1990s , 1990~91. (90.08)

    - NCC, PE/PP 1992~93.

    - downsizing, reengineering 1992. () 60,000 bbl

    - hydrocracking (7 $) 1993. : 1993.12 (3.14 *) 1994~95 : 1994. : Oil Bank (02)

    (310,000 bbl)

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    1. Introduction

    2) () 1990s . ,

    :

    ,

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    1. Introduction

    l2000s 100$ 2001 (9.11), 2002 (: 31.5 35)

    : - > 60%,- ,

    : - / ,

    , () &

    2009 ~70$ 2010 BP: Gulf oil spill (~ 80$)

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    SK()

    LG-Caltex( Group)

    ( Group)

    S-Oil()

    Oil Bank()

    1962.10 1967.05 1968.09 1976.01 1965

    1964.04 1969.06 1971.06 1980.05 1965.03

    () (1989)

    (BPDS)

    2000 35 60 50 60 50

    2003 810 600 275 443 310

    2008 1.115 770 275 580 390

    ()

    GULF

    1980

    Caltex

    -

    Union Oil

    1983

    ARAMCO

    Shell

    1977

    39.1 28.7 10.4 12.5 5.8

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    SK()

    LG-Caltex( Group)

    ( Group)

    S-Oil()

    Oil Bank()

    1962.10 1967.05 1968.09 1976.01 1965

    1964.04 1969.06 1971.06 1980.05 1965.03

    () (1989)

    (BPDS)

    2000 35 60 50 60 50

    2003 810 600 275 443 310

    2008 1.115 770 0 580 390

    ()

    GULF

    1980

    Caltex

    -

    Union Oil

    1983

    ARAMCO

    Shell

    1977

    39.1 27.0 0 20.3 13.7

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    SK LG-Caltex S-Oil

    1969 115 60 0 5 0 1801970 115 100 0 5 0 2201971 115 100 50 5 0 2701972 175 160 60 5 0 4001974 215 160 60 5 0 4401977 215 160 60 5 0 4401978 280 230 60 10 0 5801979 280 230 60 10 0 5801980 280 230 60 10 60 6401981 280 380 60 10 60 7901988 280 380 60 10 60 7901989 280 380 60 60 60 8401990 280 380 60 60 60 8401991 375 380 60 60 160 1,0351992 585 380 275 110 325 1,6751993 585 380 275 110 325 1,6751994 610 380 275 110 325 1,7001995 610 380 275 110 443 1,8181996 810 600 275 310 443 2,4381997 810 600 275 310 443 2,4381998 810 600 275 310 443 2,4381999 810 600 275 310 443 2,4382000 810 600 275 310 443 2,4382003 810 600 275 310 443 2,4382004 840 650 275 390 580 2,7352005 840 650 275 390 580 2,7352006 840 687 275 390 580 2,7722007 840 727 275 390 580 2,8122008 1,115 770 0 390 580 2,855

    ( : BPSD)

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    4

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    1. Introduction

    1) + (< 50 years) (uncertainty): / (volatility)

    4.

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    CBE4016

    : 1.2 bbl CBE4016

    OPEC (2014)

    2,634

    ~ 3,300

    tb/d = 103 b/d

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    non-OPEC liquids supply

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    Medium-term liquids supply outlook

    MB/D

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    World Oil Demand and Supply

    91.6

    MB/D

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    Crude Oil Prices

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    2015.08.14

    : 49: 49 WTI: 42.5

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    World supply of primary energy

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    World supply of primary energy by fuel type

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    Technically recoverable shale gas

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    1 MTOE

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    2) Major (~1973)

    l ///

    OPEC (1973 ~ 1980)l l Independent l OPEC l 1, 2 oil shock ,

    OPEC: Organization of Petroleum Exporting Countries60.09 SA, , , , : UAE, , , , ,

    (11, 96.6 )( 12, 14 )

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    (spot market) l l l 1980

    (Non-OPEC OPEC )

    Paper : 1990 l 90.8 ( ) 41$/bbl l l (future), (forward) option l

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    ()

    Trader

    Major term

    Spot term

    Spot

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    (spot market): ~ 40%l ( )

    l 2 OPEC (, , )

    l OPEC

    l *

    l (Physical Market):

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    (term-contract market)l l ,

    l, , l :

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    : , , ,

    :

    (, , , , , )

    ( )

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    WTI spot 50 5

    Brent spot 40 10

    (Oman+Dubai)/2

    Arabian Light

    l WTI: API 39.6, 0.24(% weight); light sweet crude, 70 bpd

    l Brent: API 38.3, 0.37(% weight); light sour crude, 75 bpd

    l Dubai: API 31.0, 2.04(% weight); 20 bpd

    CBE4016

    * Paper : (hedging/speculation )

    (future market)l l / l (NYMEX, IPE, SIMEX)

    XG.Oheating oil

    gasoline

    CBE4016

    (forward market)

    l l

    l / l l :

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    Option l () l (, holder), (, writer)l (premium)l l call or put option

    CBE4016

    :

    l

    l l

    :l , , l

    : WTI, Brent, Dubai

    CBE4016

    CBE4016

    1. Introduction

    1)

    l C LPG, LNG, l

    , (NON-OPEC: / )

    2) l l l

    4.

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    1. Introduction

    1) + paper market (30~40%) , spot (30~40%)

    2) / () or NG gashol Fuel cell, solar cell green energy

    3) // : = 75 : 25 ()

    5.

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    4) () 1970 4 20 Africa, ,

    CBE4016