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Copyright © Yokogawa Electric Corporation 31 October 2011 - 1 - Mass & Energy Balancing at LNG Receiving Terminals LNG Metrology Workshop Glasgow, 31 October 2011 Martin te Lintelo

Mass & Energy Balancing at LNG Receiving Terminals · 2015-04-14 · Exaquantum Batch @ LNG Receiving Terminals Automatic status -based batch-based collection of information for the

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Page 1: Mass & Energy Balancing at LNG Receiving Terminals · 2015-04-14 · Exaquantum Batch @ LNG Receiving Terminals Automatic status -based batch-based collection of information for the

Copyright © Yokogawa Electric Corporation 31 October 2011 - 1 -

Mass & Energy Balancing at LNG Receiving Terminals LNG Metrology Workshop Glasgow, 31 October 2011 Martin te Lintelo

Page 2: Mass & Energy Balancing at LNG Receiving Terminals · 2015-04-14 · Exaquantum Batch @ LNG Receiving Terminals Automatic status -based batch-based collection of information for the

Copyright © Yokogawa Electric Corporation 31 October 2011 - 2 -

Outline

Mass & energy balancing at LNG receiving terminals – What? – Why? – How?

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Mass & Energy Balancing What?

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Mass & Energy Balancing – Application Areas

Custody transfer handling

Inventory monitoring – Shipper/owner level – Tank composition tracking (overall and/or per tank)

Energy consumption & losses – Shrinkage – Electrical power

Instrumentation error identification

Send-out Wobbe control

Environmental monitoring

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Energy Consumption & Losses

Gas – Vaporizers (Open Rack vs. SCV or IFV) – Flare – Leaks or repairs

Electrical power – Pumps – Compressors – Nitrogen production – Etc.

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LNG Terminal Process – Simplified Main Flows

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Mass and Energy Balancing –Subjects to be Considered

Main and minor flows (include or not) Measurements available Measurement accuracies Assumptions on composition Operating Modes of LNG Receiving Terminals (no loading!) – Unloading with send-out – Unloading without send-out – Send-out without unloading – Neither unloading or sending out

# Units (simultaneously) used for operations – E.g. 2 tanks for unloading, 2 tanks for send-out, and re-

circulation between tanks

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Mass & Energy Balancing Why?

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Interest in Mass & Energy Balancing (1)

Both on liquefaction and receiving / regasification side

Changing LNG business – Spot – Cargo trades – Open contracts

Multi-user terminals – Dedicated with TPA – Merchant

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Interest in Mass & Energy Balancing (2)

Potentially interested parties – Shippers (buyers) / terminal users – Suppliers (sellers) – Terminal operators – Society represented by authorities (regulatory compliance)

Depending on contract type – Incoterms

Contractual arrangements – Terminal Access Code – Individual throughput agreements

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Interest in Mass & Energy Balancing (3)

Net energy amount available to shipper =

Delivered energy amount (carrier unload)

– Shrinkage (in terminal)

± Inventory corrections (by operator)

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Mass & Energy Balancing How?

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Measurement @ LNG Terminals

Location of measurements Quality/accuracy – Importance of accuracy based on time line of the purpose

(daily, weekly, monthly, annual). Level measurement most accurate over long period of time

– Relative error introduced by measurement errors of different devices (e.g. LNG vs gas)

– Variance in accuracy depending on the state of the terminal at the beginning and end of the (un)loading job (e.g. related to temperature influences on strapping tables)

Redundancy of measurements – Option to use ship readings and integrate these data in a

reconciled mass balance Timing of (un)loading measurements – Accuracy in starts/stops of (un)loading phases

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How Mass & Energy Balancing

Manual

Dedicated IT solution for unloading cross-check (Japan)

Spreadsheet

High level in commercial IT system

Detailed in PIMS/MES system

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High Level in Commercial IT System

Prevailing method ?! Backed by contracts & agreed procedures – Terminal Access Codes – Individual contracts

Unloaded energy amount calculations (simple) Built-in high-level reconciliation methods Manual interventions – Inventory / book stock changes – Shrinkage figure updates

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Detailed in PIMS/MES System

Unloading monitoring – Composition OK? i.e. cargo acceptable? – Instrumentation OK? i.e. challenge capability for surveyor

report – Tracking of carrier unloading stages incl. interrupts (can also

allow comparison of (un)loading occasions and/or aggregation of (un)loading occasions)

– Determine unloaded amount based on terminal operational status (challenge surveyor report)

Energy consumption monitoring Loss monitoring Flare monitoring Environmental monitoring

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LNG Terminal Automation Solution

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LNG PIMS - Functional Distribution

PIMS – Time series histories and alarm and event log

Interpretation and presentation of the history data in terms of non-continuous periods (batches)

Interpretation of the history data in terms of material properties, mass and energy flows, reconciliation

The LNG Terminal

(passage of start/end times)

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Data Historian / PIMS (Exaquantum)

Data collection of (tag-based) time series data and Alarm & Event (A&E) data – Process data from PCS – Manual entries – Data from other systems

Aggregations of time series data Calculations Graphical display of data, trends, etc. Reporting Export capability (e.g. Excel)

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Exaquantum Batch @ LNG Receiving Terminals

Automatic status-based batch-based collection of information for the LNG unloading process rather than retrospective batch analysis

The different stages in the unloading process are tracked allowing even complicated (e.g. interrupted) unloading sequences to be handled

Collected information can be made available to other applications e.g. to reconcile ship unloading records

Comparison of different carrier unloads based on different properties (carrier, size, volume, etc.)

Use of previous carrier data (metering error?)

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Exaquantum/mPower

The mPower Plant Model-based applications provide self-configuring management level reports based on data from history systems like PIMS, LIMS, logbooks, etc.

mPower models the physical plant with a software object structure that understands the key concepts of material location, plant connectivity and containment

When this plant model is linked to the lower level data sources, it is simple to define any physical or time boundaries and then request reports based on them

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mPower: Plant Model Features

Definition of Plant Objects – Sites, Plants, Units, Tanks, Streams

Definition of Data Sources – Within mPower and to legacy software applications

Physical Mapping of Plant Layout – Units and interconnections to Nodes and Streams

Data Conversion to Information – Calculation and validation

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Example Terminal Model

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Relevant mPower Functions

Mass and Energy Balancing to detect problems quickly when mass balancing shows an inconsistency – Leaks – Unauthorized removal of material – Instrumentation faults or failure

Data Reconciliation to improve the quality of the process data used by mPower – Reports on instrumentation inaccuracies – Able to determine missing measurements to

reduce the need for instrumentation

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mPower: Possible LNG Terminal Functions

1. Collecting measurement information 2. Calculating mass and energy balances 3. Investigating faulty measurements 4. Reconciling redundant measurements

discrepancies 5. Reconciling ship unloading records 6. Investigating excessive losses 7. Reporting end of period reconciliation

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Data Reconciliation

Purpose – Online error check and warning/alarm (e.g.

instrumentation failures) – Unloaded amount – Daily/Weekly/Monthly stock balance

Automatic vs. manual Pre-defined vs user-definable (on the fly) General reconciliation meanings

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Reconciliation: Two Meanings

1. Adjustment of flows and inventories to values different from the raw measured values so as to achieve a balance (if acceptable)

2. Analysis of the flows and inventories so as to identify “lost” material

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Reconciliation illustrations (1a)

1. Adjusting values to achieve a balance

10

+2

7

10 <> 2 + 7

Raw

9.8

+1.9

7.9

9.8 = 1.9 + 7.9

Adjusted

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Reconciliation illustrations (1b)

1. Adjusting values to achieve a balance

20

63

63 <> 20 + 40

Raw

40

62.3

62.3 = 20.8 + 41.5

Adjusted

20.8

41.5

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Reconciliation illustrations (2)

2. Calculating loss

10

+2

7

10 <> 2 + 7

Raw

10

+2

7

10 = 2 + 7 + 1

Adjusted

1

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Conclusion

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Conclusion

Mass and energy balancing at LNG receiving terminals is getting more attention The technology to do detailed, automated mass and energy balancing is available It makes more detailed and frequent mass & energy balances possible

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Thank you for your attention