07 heavy oil - simon

28
U g e l s t a d L a b o r a t o r y 1 Fundamental Chemistry of Heavy Crude Oils Sébastien SIMON, Johan SJÖBLOM Ugelstad Laboratory, NTNU, Trondheim, Norway Tekna, Stavanger , September 25 th 2013

Upload: alexander

Post on 06-Nov-2015

19 views

Category:

Documents


4 download

DESCRIPTION

HEavy oil

TRANSCRIPT

  • U g e l s t a d L a b o r a t o r y

    1

    Fundamental Chemistry of Heavy Crude Oils

    Sbastien SIMON, Johan SJBLOM

    Ugelstad Laboratory, NTNU, Trondheim, Norway

    Tekna, Stavanger , September 25th 2013

  • U g e l s t a d L a b o r a t o r y

    2

    Goal

    Briefly describe evolution of composition of crude oils from light to heavy

    Do we have more flow assurance problems with heavy crude oil? Asphaltene precipitation

    Oil/water separation

    Calcium naphthenate deposits

  • U g e l s t a d L a b o r a t o r y

    3

    Bulk Properties are Ruled by API

    Co-variance of important bulk properties

    Hannisdal et al.,

    2007

  • U g e l s t a d L a b o r a t o r y

    4

    Composition: SARA Separation based on polarity and solubility of crude oil components Separation in 4 fractions

    Increasing polarity

    Crude oil

    Saturates Aromatics Resins Asphaltenes

    Heavy

    crude

    A S R A

  • U g e l s t a d L a b o r a t o r y

    5

    Asphaltenes Most polar molecules of crude oil Soluble in toluene, insoluble in n-alkanes

    Strongly aromatics

    Contains heteroatoms and metals

    Average M750 g.mol-1

    Self-associate in model systems and oils

    Murgich,

    2003

    The continental model The archipelago model

  • U g e l s t a d L a b o r a t o r y

    6

    Asphaltene model compounds

    Nordgrd and

    Sjblom, 2008

    Modulable

    head group

    Molecular

    weight 700

    g.mol-1

    Polyaromatic core +

    protruding alkane chains

    Model molecules having similar functionalities of asphaltenes Obtaining a better understanding of emulsion formation, fouling and deposition

  • U g e l s t a d L a b o r a t o r y

    7

    Difference Resins/Asphaltenes

    Primary difference: solubility in n-alkane Resins less aromatics

    Contain most of acids and bases

    Do not (or little) self-associate in model systems and oils

    Important to keep asphaltenes dissolved in oil

    Pfeiffer,

    1940

    Aphaltene

    Resin

    Preponderantly aromatic

    Mixed aromatic- naphthenic nature

    Mixed naphthenic-aliphatic nature

    Aliphatic

  • U g e l s t a d L a b o r a t o r y

    8

    Evolution SARA with API More and more polar molecules Ex. for Athabasca crude oil

    Koots and Speight,

    1975

  • U g e l s t a d L a b o r a t o r y

    9

    Asphaltene Precipitation

    Can lead to deposition and fouling

    The asphaltene precipitation can happen: During the depressurization of crude oil

    If the composition of crude oil changes or another component is mixed with

    crude oil

    Ex: Asphaltene Precipitation due to mixing with condensate from gas

    compressor station

    Courtesy of Hans

    Oschmann,

    Champion Tech./

    NTNU

  • U g e l s t a d L a b o r a t o r y

    10

    Precipitation Risk vs API % asphaltenes increases with API Are precipitation risks higher for heavy crude oils?

    Reply with the de Boer plot

    From the de Boer plot, less risk with heavy crude oil

    More problem with light crudes already noticed by de Boer et al.

    Yonebayashi et al.

    2013

  • U g e l s t a d L a b o r a t o r y

    11

    Precipitation Risk vs API Diagram proposed by Stankiewicz et al. (2002) Consistent with the peptization model by Pfeiffer et al. (1940)

    Plot predict problem when the peptizing fraction content is low

    No indication for more problems with heavy crude oils (low saturate content)

    Yonebayashi et al.

    2013

  • U g e l s t a d L a b o r a t o r y

    12

    New JIP at Ugelstad Laboratory Precipitation/deposition/fouling of asphaltenes Goal: Create knowledge and understanding needed for a reliable assessments of precipitation/deposition/fouling risks during oil production and transport

    Starting early 2014

    Contact: Prof. Johan Sjblom

  • U g e l s t a d L a b o r a t o r y

    13

    Amount quantified by TAN (Total Acid Number) measurements

    Naphthenic acids CnH2n-ZO2 with z specifies a homologous series

    Mostly part of resin fraction Some example of mono-acids

    Acids Present in Crude Oils

  • U g e l s t a d L a b o r a t o r y

    14

    Heavy and extra heavy oils are acidic Main mechanism: Biodegradation increases the density (lower API) and synthesizes NA

    TAN vs API

    Katz and Robison,

    2006

  • U g e l s t a d L a b o r a t o r y

    15

    Metabolization of paraffins first

    Mechanism Biodegradation

    Wenger et al.,

    2002

  • U g e l s t a d L a b o r a t o r y

    16

    Biodegradation increases the TAN via NA formation

    Evolution of NA with Biodegradation

    Meredith et al.

    2000

  • U g e l s t a d L a b o r a t o r y

    17

    Biodegradation increases complexity of NA composition Gas chromatogram of acid fraction

    Evolution of NA with Biodegradation

    Meredith et al.

    2000

    Retention time

    Undegraded oil

    (n-alkyl visible)

    degraded oil +

    degraded oil ++

  • U g e l s t a d L a b o r a t o r y

    18

    A Special Type of Naphthenic Acid: Arn

    4 acid groups

    C80, M=1230 g.mol-1

    Responsible for the formation of calcium naphthenate deposit

    Low concentration compared with Monoacids but big importance!

    Methods developed by Ugelstad Laboratory to determine Arn content in deposits and crude

    oils (ppm level)

    Discovered by Statoil and ConocoPhillips in 2004

    Lutnaes et al. 2006

  • U g e l s t a d L a b o r a t o r y

    19

    Trends with API List of fields where Arn has been detected in crude oil

    Arn presents in very different oils, consistent with suspected archaea origin

    Deposition seems to happen with very different crudes

    Need more data to be more conclusive (sampling data, produced water data)

    Field TAN

    (mgKOH/g) API

    Fields

    deposit Ref

    Tchibelli 0.66 36.5 No Brocart et al., 2007

    Acacia 0.36 36 ? Brocart et al., 2007

    Usan 3 0.58 35 ? Brocart et al., 2007

    Offshore Nigerian field B 0.2 34 Yes Igwebueze et al., 2013

    Ofon 0.4 34 No Brocart et al., 2007

    Girassol 0.38 30.5 No Brocart et al., 2007

    Blake 0.11 30 Yes Melvin et al., 2008

    Offshore Nigerian field A 0.5-0.8 29 Yes Igwebueze et al., 2013

    Heidrun 2.7 26 Yes Vindstad et al., 2002

    Gimboa 0.65 25.3 Yes Junior et al., 2013

    Afia 1 25 Yes Brocart et al., 2007

    Kuito 2.15 20 Yes Brocart et al., 2007

  • U g e l s t a d L a b o r a t o r y

    20

    Bases Present in Crude Oil

    Derivatives of pyridine and its benzologs (cores)

    1Aksenov V.S. et al. Chemistry of Heterocyclic Compounds, 1979, 15, 119-135

    N N N

    N

    Pyridine

    pKa=5.25

    Quinoline

    pKa=4.90

    3,4-benzoquinoline 7,8-benzoquinoline

    No or very little amines

    Amount of base quantified by TBN (Total Base Number) measurement

  • U g e l s t a d L a b o r a t o r y

    21

    Seems to be a loose correlation between density and TBN Generally higher TBN value for heavy crude oil

    Evolution of TBN with Density

    Data from

    Simon et al., 2010

    Eftekhardadkhah et

    al., 2013

    d at 50 C g.cm-3

    0,75 0,80 0,85 0,90 0,95 1,00

    TB

    N m

    g.g

    -1

    0

    1

    2

    3

    4

    5

    6

  • U g e l s t a d L a b o r a t o r y

    22

    Oil/Water Separation JIP program at Ugelstad Laboratory to determine parameters

    responsible for emulsion stability

    30 crude oils

    Composition

    Bulk and Interfacial Properties

    Stability determined by the Ecrit method

    Correlations

  • U g e l s t a d L a b o r a t o r y

    23

    Multivariate Data Analysis Co-variance of several properties/composition parameters (slide 3)

    Stability of emulsions can be well-fitted with viscosity alone Comparison experimental and semi-theoretical destabilization time

    Silset et al.

    2010

    More research to find effect of other properties/composition parameters

  • U g e l s t a d L a b o r a t o r y

    24

    Conclusion

    Complexity of chemistry increases with oil density

    Do we have more flow assurance problems with heavy crude oil? Oil/water separation: Yes

    Asphaltene precipitation: No

    Calcium naphthenate deposition: Need more data to be conclusive

  • U g e l s t a d L a b o r a t o r y

    25

    Acknowledgments to our Sponsors (Emulsion and Naphthenate Programs)

  • U g e l s t a d L a b o r a t o r y

    26

    Back Slides

  • U g e l s t a d L a b o r a t o r y

    27

    Classification of crude oil with density

    Density linked to API gravity

    o

    o

    141.5API= -131.5

    Sp.gr@15 C

  • U g e l s t a d L a b o r a t o r y

    28

    Crude Oil Matrix Tested at Ugelstad Lab

    Hemmingsen et al. 2005