WO2012163715A2 - Système de collecte de gaz depuis un champ de gaz comprenant un compresseur haute-pression à efficacité élevée - Google Patents

Système de collecte de gaz depuis un champ de gaz comprenant un compresseur haute-pression à efficacité élevée Download PDF

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Publication number
WO2012163715A2
WO2012163715A2 PCT/EP2012/059386 EP2012059386W WO2012163715A2 WO 2012163715 A2 WO2012163715 A2 WO 2012163715A2 EP 2012059386 W EP2012059386 W EP 2012059386W WO 2012163715 A2 WO2012163715 A2 WO 2012163715A2
Authority
WO
WIPO (PCT)
Prior art keywords
gas
mass flow
input
pressure compressor
low pressure
Prior art date
Application number
PCT/EP2012/059386
Other languages
English (en)
Other versions
WO2012163715A3 (fr
Inventor
Bob OKHUIJSEN
Arthur KAUFFELD
Bernd Wacker
Original Assignee
Siemens Aktiengesellschaft
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Siemens Aktiengesellschaft filed Critical Siemens Aktiengesellschaft
Priority to US14/123,215 priority Critical patent/US20140178208A1/en
Priority to EP12725663.4A priority patent/EP2691656A2/fr
Priority to CA2837615A priority patent/CA2837615C/fr
Priority to AU2012264989A priority patent/AU2012264989B9/en
Publication of WO2012163715A2 publication Critical patent/WO2012163715A2/fr
Publication of WO2012163715A3 publication Critical patent/WO2012163715A3/fr

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02—Surge control
    • F04D27/0207—Surge control by bleeding, bypassing or recycling fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D15/00—Control, e.g. regulation, of pumps, pumping installations or systems
    • F04D15/0005—Control, e.g. regulation, of pumps, pumping installations or systems by using valves
    • F04D15/0011—Control, e.g. regulation, of pumps, pumping installations or systems by using valves by-pass valves
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D15/00—Control, e.g. regulation, of pumps, pumping installations or systems
    • F04D15/0005—Control, e.g. regulation, of pumps, pumping installations or systems by using valves
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D25/00—Pumping installations or systems
    • F04D25/16—Combinations of two or more pumps ; Producing two or more separate gas flows
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02—Surge control
    • F04D27/0207—Surge control by bleeding, bypassing or recycling fluids
    • F04D27/0215—Arrangements therefor, e.g. bleed or by-pass valves

Definitions

  • the present invention relates to a system for gathering gas from a gas field and to a method for controlling a gas mass flow of a system for gathering gas from a gas field.
  • gas is gathered from conventional gas field types and unconventional gas field types exist.
  • the stored gas comprises an initially high pressure such that further compression by external compressors is not needed in the beginning.
  • a high pressure central compressor for example of a centrifugal type compressor
  • low pressure wellhead compressors are implemented and connected to the respective wellheads of the gas field.
  • the high pressure central compressor and the low pressure wellhead compressor are adapted for sucking the gas out of the gas field and generating a high pressure gas flow for subsequent gas export systems, such as pipelines or gas gen ⁇ erators .
  • the gas pressure inside the gas field decreases in a short time interval, such that central high pressure compressors and low pressure wellhead compres- sors are needed from the beginning of the gathering of the gas from the gas field.
  • the low pressure wellhead compressors and the high pressure central compressor are designed as separate and independent subsystems.
  • the low pressure wellhead compressors and the high pressure wellhead compressor often form independent and separated units.
  • the high pressure central compressor is optimised for a small range of inlet pressures and inlet mass flow values.
  • the low pressure wellhead compressors are optimised for individual ranges of respective inlet pressures and mass flows.
  • each low pressure wellhead compressor produces an output pressure and an output mass flow of gas without considering the small range of inlet pressures and mass flow of gas at which the high pressure central compressor works efficiently.
  • a variation of the gas pressure in the gas field does not affect the efficiency of the low pressure wellhead compressors dramatically, whereas the effi ⁇ ciency of the subsequent high pressure central compressor is affected dramatically during pressure changes.
  • the gathering of the gas is inefficient, if the inlet gas pressures and inlet mass flow of the high pressure central com ⁇ pressor, the high pressure central compressor is not working under its efficient working point for which the high pressure central compressor is designed for.
  • a sys ⁇ tem for gathering a gas from a gas field comprises a high pressure compressor which comprises a gas input and a gas output.
  • the gas input is coupleable to the gas field for receiving the gas gathered from the gas field with a first gas pressure.
  • the gas output is coupleable to a gas export system for providing the gas with a second pressure to the second gas export system.
  • the second gas pressure is higher than the first gas pressure.
  • the system comprises a measuring unit which is coupled to the gas input, wherein the measuring unit measures an input mass flow value which is indicative of an input mass flow at the gas input. Furthermore, the system comprises a mass flow control unit, wherein the mass flow control unit is coupled to the measuring for receiving the measured input mass flow value. The mass flow control unit is coupled to the gas input for controlling the input mass flow such that the measured input mass flow value corresponds to a set point input mass flow value.
  • a method for controlling a gas mass flow of a system for gathering gas from a gas field is presented.
  • an input mass flow at a gas input of a high pressure compressor is measured.
  • the gas input receives the gas gathered from the gas field with a first gas pressure
  • the high pressure compressor comprises a gas output for pro ⁇ viding gas with a second pressure to a gas export system.
  • the second gas pressure is higher than the first gas pressure.
  • An input mass flow value which is indicative of an input mass flow at the gas input is measured by a measuring unit which is coupled to the gas input.
  • the measured input mass flow value is received by a mass flow control unit.
  • the input mass flow is controlled by the mass flow control unit which is coupled to the gas input.
  • the mass flow control unit controls the input mass flow such that the input mass flow value at the gas input corresponds to a set point input mass flow value .
  • the high pressure compressor is installed between the gas field and the gas export system.
  • the high pressure compressor is adapted for receiving the gas from the gas field with a first pressure, e.g. approximately 10 to 14 bars, and adapted to compress the gas up to a second gas pressure of approximately 60 to 90 bars which are needed by the gas export system.
  • the high pressure central compressor may be e.g. of a centrifugal type compressor and is most suitable for the gas gathering in order to generate the high gas pressure for the subseguent gas export system.
  • the high pressure compressor comprises a small efficient range regarding the inputted mass flow and input pressure in which the high pressure compressor works efficient. Hence, changes in inlet conditions, such as in the mass flow and in the inlet gas pressure, a high impact on the operation efficiency is caused.
  • the gas export system comprises for example a pipeline system for transporting the gas to a desired destination.
  • the export gas system may comprise a gas power plant for generating electricity or further gas treatment systems.
  • the measuring unit is coupled to the gas input of the high pressure compressor and is adapted for measuring a variety of parameters which are indicative of the input mass flow of the gas at the gas input of the high pressure compressor. In par- ticular, the measuring unit measures the input mass flow value ([kg/s]) . Additionally, the measuring unit may measure the first gas pressure of the gas at the gas input and the second gas pressure at the gas output. Moreover, the measur- ing unit is also adapted for measuring the output mass flow at the gas output of the high pressure compressor. Addition ⁇ ally, the measuring unit may measure the composition of the gas as well as the temperature of the gas at the gas input and the gas output of the high pressure compressor.
  • the measured values are provided to the mass flow control unit.
  • the mass flow control unit compares the measured values, i.e. the input mass flow value, with a given set point input mass flow value. If there is a difference between the input mass flow value and the set point input mass flow value, the mass flow control unit controls the input mass flow value such that the input mass flow value corresponds to the set point input mass flow value.
  • the set point input mass flow value defines the mass flow at the gas input of the high pressure compressor, by which the high pressure compressor is working at its working point and thus is working with the highest efficiency.
  • the working point is dependent on the pressure relation between the first gas pressure at the gas input and the second gas pressure at the gas output, the mass flow of the gas through the high pressure compressor (i.e. the mass flow at the gas input) and the rotational speed of the high pressure compressor.
  • the mass flow control unit is adapted for reducing the deviation of the measured input mass flow value from the given set point input mass flow value.
  • the mass flow control unit may control various subsystems for influencing the input mass flow of the gas at the gas input.
  • the mass flow control unit may control upstream installed low pressure com- pressors, delivery valves or a mass flow in a return flow tubing and/or a mass flow of a bypass tubing which will be explained in more detail below.
  • a predeter ⁇ mined and desired input mass flow at the gas input of the high pressure compressor is adjustable by the mass flow control unit such that the high pressure compressor is working approximately at its working point.
  • the efficiency of the high pressure compressor and hence the gathering of gas from a gas field is more efficient.
  • the system comprises a first low pressure compressor which is connectable to a first wellhead arrangement of the gas field for receiving the gas from the first wellhead arrangement.
  • the first low pressure compressor is connected to the gas input for providing the gas to the gas input with a first mass flow.
  • the system comprises a second low pressure compres- sor which is connectable to a second wellhead arrangement of the gas field for receiving the gas from the second wellhead arrangement.
  • the second low pressure compressor is connected to the gas input for providing the gas to the gas input with the second mass flow.
  • the mass flow control unit is connected to a) the first low pressure compressor for controlling the first low pressure compressor and b) the second low pressure compressor for controlling the second low pressure compressor such that the first mass flow and the second mass flow are controllable for controlling the input mass flow at the gas input.
  • Each wellhead arrangement is connected to a borehole through which gas of the gas field is gathered.
  • a gas field may com ⁇ prise a plurality of boreholes, wherein to each borehole a respective wellhead arrangement is attached for gathering gas.
  • Each wellhead arrangement is connected to a respective low pressure compressor. For example, if a wellhead arrange ⁇ ment delivers gas with approximately 1 to 4 bars to the low pressure compressor, the low pressure compressor increases the pressure up to approximately 5 to 20 bars.
  • the measuring unit is adapted for measuring each mass flow and pressure at a respective gas input of a respec- tive low pressure compressor and at a gas output of a respective low pressure compressor. These measured data are sent to the mass flow control unit.
  • the mass flow control unit re ⁇ ceives also the information of the input mass flow at the gas input of the high pressure compressor. If more or less mass flow is needed at the gas input of the high pressure compressor, the mass flow control unit controls the respective low pressure compressors, i.e. the first low pressure compressor and the second low pressure compressor. In particular, the mass flow control unit receives the infor ⁇ mation of the working points of the respective low pressure compressors.
  • each low pressure compressor is controlled under consideration of its respective working points such that each low pressure compressors is operated more efficiently. Hence, the overall efficiency of the system is increased.
  • the system comprises a first delivery valve which is connectable to a first wellhead arrangement of the gas field for receiving the gas from the first wellhead ar- rangement, wherein the first delivery valve is connected to the gas input for providing the gas to the gas input with a further first mass flow.
  • the system further comprises a second delivery valve which is connectable to a second wellhead arrangement of the gas field for receiving the gas from the second wellhead arrangement, wherein the second delivery valve is connected to the gas input for providing the gas to the gas input with a further second mass flow.
  • the mass flow control unit is connected to a) the first de- livery valve for controlling the first delivery valve and b) the second delivery valve for controlling the second delivery valve such that the further first mass flow and the further second mass flow are controllable for controlling the input mass flow at the gas input.
  • the first and second delivery valves may be installed between the respective first and second wellhead arrangement and the respective first and second low pressure compressors.
  • the first and second delivery valves may be in- stalled behind, i.e. downstream, of the respectively first and second low pressure compressors.
  • the further first mass flow and the further second mass flow of the gas gathered from a respective borehole is adjustable and con ⁇ trollable individually, such that a desired input mass flow of the gas at the gas input of the high pressure compressor is adjustable.
  • gas may be gathered without using low pressure compressors.
  • the delivery valves are installed downstream of the wellhead arrangement in order to control mass flow from the respective wellhead arrangement to the gas input of the high pressure compressor.
  • the system com- prises a return flow tubing which is connected to the gas output for bleeding off a part of the gas from the gas output and which is connected to the gas input for injecting the part of the gas in the gas input.
  • the mass flow control unit is coupled to the return flow tubing for controlling the bleeding off of the part of the gas from the gas output and for controlling the injecting of the part of the gas in the gas input such that the input mass flow at the gas input is controllable . For example, if the measured input mass flow value is below the set point input mass flow value, a part of the gas may be bled off from the gas output and injected at the gas input, so that the input mass flow is increased at the gas input.
  • a control valve may be installed which is controllable by the mass flow control unit.
  • the mass flow control unit may act as a supervisory system and controls the anti-surge system.
  • the mass flow control unit may act as a supervisory system and controls the anti-surge system.
  • the system further comprises a bypass tubing which is connected to the gas input for bleeding off a further part of the gas from the gas input.
  • the mass flow control unit is coupled to the bypass tubing for controlling the bleeding off of the further part of the gas from the gas input such that the input mass flow at the gas input is controllable.
  • the bypass tubing may bleed off the gas from the gas input e.g. to the environment or to a further use, for example into a gas generator. Hence, by bleeding off the gas from the gas input, the input mass flow is reduced till the desired set point input mass flow value is adjusted.
  • the high pressure compressor of a gas gathering system is controlled and operated more efficiently.
  • predetermined set point input values, in particular set point input mass flow values, of the gas at the gas input of the high pressure compressor are determined, so that already at the design phase the high pressure com- pressor may be optimised for predetermined operating ranges in order to run more efficiently at the given set point input mass flow values.
  • the high pressure compressor may be designed with a certain number of stator rings, cool ⁇ ing systems, etc., so that already at the design phase of the high pressure compressor an optimised high pressure compressor is constructable .
  • optimised inlet conditions for the high pressure compressor are generated in particular by adapting and controlling the low pressure compressors.
  • the low pressure compressors dependent on the de ⁇ sired input values of the high pressure compressor, an interconnected efficient and effective gathering system is achieved .
  • the Figure shows schematically a gas gathering system accord ⁇ ing to an exemplary embodiment of the present invention.
  • the Figure shows a system for gathering a gas from a gas field 170.
  • the system comprises a high pressure compressor 100 which comprises a gas input 101 and a gas output 102.
  • the gas input 101 is coupleable to the gas field 170 for receiving the gas gathered from the gas field 170 with a first gas pressure pi.
  • the gas output 102 is coupleable to a gas export system 130 for providing the gas with the second gas pressure p2 to the gas export system 130.
  • the second gas pressure p2 is higher than the first gas pressure pi.
  • a measuring unit 110 is coupled to the gas input 101, wherein the measuring unit 110 measures, for example by sensor ele ⁇ ments 111, an input mass flow value (e.g. in [kg/s]) which is indicative of an input mass flow mi at the gas input 101.
  • the system comprises a mass flow control unit 120, wherein the mass flow control unit 120 is coupled to the measuring unit 110 for receiving the measured input mass flow value and the gas input 101 for controlling the in ⁇ put mass flow mi such that the measured input mass flow value corresponds to a set point input mass flow value.
  • the measuring unit 110 may measure additionally further mass flow affecting parameters, such as the first pressure pi and the temperature at the gas input 101 and/or the second pres- sure p2, the output mass flow mi and/or the temperature at the gas output 102.
  • the mass flow control unit 120 may calculate on the basis of the inputted data values, such as the input mass flow mi , the first pressure pi, the second pressure p2, the output mass flow mi, the respective gas temperature at the gas input 101 and the gas output 102, a set point input mass flow value (e.g. [kg/s]) at which the high pressure compres- sor 100 is operated approximately at its working point. More ⁇ over, the mass flow control unit 120 may be connected to the high pressure compressor 100 for controlling for example the speed of rotation of the high pressure compressor 100. In the figure the tubing which transports the gas between the system devices are shown by the solid lines, whereas the data lines, for transmitting measuring data and control data are shown with the dotted lines.
  • a respective low pressure compressor 141-144 is installed.
  • Each low pressure compressor 141-144 may increase the pressure from ap ⁇ proximately 1 to 4 bars to approximately 5 to 20 bars.
  • the mass flow control unit 120 is adapted for controlling the respec- tive low pressure compressors 141-144 individually, so that each low pressure compressor 141-144 may deliver a predetermined input mass flow mi of gas to the gas input 101.
  • the mass flow control unit 120 is adapted for example for controlling the rotational speed of each low pressure compressor 141-144, for example.
  • low pressure compressors 141-144 In the exemplary embodiment shown in the figure four low pressure compressors 141-144, four wellhead arrangements 151- 154 and four delivery valves 161-164 are shown. In other ex- emplary embodiments, more or less of low pressure compressors 141-144, wellhead arrangements 151-154 and delivery valves 161-164 may be installed.
  • a gathering group may be formed by one low pressure compres ⁇ sor 141-144, one wellhead arrangement 151-154 and one deliv ⁇ ery valve 161-164. Each gathering group is coupled to a respective borehole. All gathering groups deliver gas to a com- mon collecting manifold to which the high pressure compressor 100 is coupled.
  • a gas field may comprise a plurality of boreholes, wherein to each borehole a respective gathering group is coupled.
  • the system may comprise a further high pressure compressor 100, wherein first gathering groups are connected the one high pressure compressor 100 and second gathering groups are connected to the further high pressure compressor.
  • the high pressure compressor 100 is adapted for increasing the received gas at the gas input 101 from approximately 10 to 14 bars to approximately 60 to 90 bars at the gas outlet 102.
  • a high gas pressure is provided which is needed e.g. for the further processing of the gas.
  • the system comprises a re ⁇ turn flow tubing 103 to which a bleeder valve 104 is con ⁇ nected.
  • the bleeder valve 104 is controlled by the mass flow control unit 120. If the measured input mass flow mi is lower than the set point input mass flow, the mass flow con ⁇ trol unit 120 controls the bleeder valve 104 such that a part of the gas is bled off from the gas outlet 102 and injected into the gas input 101, such that the input mass flow value is increased until it corresponds to the set point input mass flow value.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Control Of Positive-Displacement Pumps (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Pipeline Systems (AREA)

Abstract

La présente invention se rapporte à un système destiné à collecter un gaz depuis un champ de gaz (170). Le système comprend un compresseur haute-pression (100) qui comprend une entrée de gaz (101) et une sortie de gaz (102). L'entrée de gaz (101) peut être accouplée au champ de gaz (170) pour recevoir le gaz collecté depuis le champ de gaz (170) à une première pression de gaz et la sortie de gaz (102) peut être accouplée à un système d'exportation de gaz (130) pour distribuer à ce dernier le gaz à une seconde pression de gaz. La seconde pression de gaz est supérieure à la première pression de gaz. Le système comprend en outre une unité de mesure (110, 111) accouplée à l'entrée de gaz (101), l'unité de mesure (110, 111) mesurant une valeur de débit massique d'entrée qui indique un débit massique d'entrée à l'entrée de gaz (101). Le système comprend en outre une unité de commande (120) de débit massique, l'unité de commande (120) de débit massique étant accouplée à l'unité de mesure (110, 111) pour recevoir la valeur de débit massique mesurée et à l'entrée de gaz (101) pour commander le débit massique d'entrée de sorte que la valeur de débit massique d'entrée mesurée corresponde à une valeur de débit massique d'entrée de point de consigne.
PCT/EP2012/059386 2011-05-30 2012-05-21 Système de collecte de gaz depuis un champ de gaz comprenant un compresseur haute-pression à efficacité élevée WO2012163715A2 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US14/123,215 US20140178208A1 (en) 2011-05-30 2012-05-21 System for gathering gas from a gas field comprising a high efficient high pressure compressor
EP12725663.4A EP2691656A2 (fr) 2011-05-30 2012-05-21 Système de collecte de gaz depuis un champ de gaz comprenant un compresseur haute-pression à efficacité élevée
CA2837615A CA2837615C (fr) 2011-05-30 2012-05-21 Systeme de collecte de gaz depuis un champ de gaz comprenant un compresseur haute-pression a efficacite elevee
AU2012264989A AU2012264989B9 (en) 2011-05-30 2012-05-21 System for gathering gas from a gas field comprising a high efficient high pressure compressor

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP11168122A EP2530329A1 (fr) 2011-05-30 2011-05-30 Système de collecte de gaz d'un champ de gaz comprenant un compresseur haute pression
EP11168122.7 2011-05-30

Publications (2)

Publication Number Publication Date
WO2012163715A2 true WO2012163715A2 (fr) 2012-12-06
WO2012163715A3 WO2012163715A3 (fr) 2013-05-10

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PCT/EP2012/059386 WO2012163715A2 (fr) 2011-05-30 2012-05-21 Système de collecte de gaz depuis un champ de gaz comprenant un compresseur haute-pression à efficacité élevée

Country Status (5)

Country Link
US (1) US20140178208A1 (fr)
EP (2) EP2530329A1 (fr)
AU (1) AU2012264989B9 (fr)
CA (1) CA2837615C (fr)
WO (1) WO2012163715A2 (fr)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018055105A1 (fr) * 2016-09-26 2018-03-29 Siemens Aktiengesellschaft Actionnement d'un compresseur de tête de puits

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Publication number Priority date Publication date Assignee Title
US5347467A (en) * 1992-06-22 1994-09-13 Compressor Controls Corporation Load sharing method and apparatus for controlling a main gas parameter of a compressor station with multiple dynamic compressors
DE19860639A1 (de) * 1998-12-29 2000-07-06 Man Turbomasch Ag Ghh Borsig Verfahren zum Betreiben eines Kompressors mit nachgeschaltetem Verbraucher, und nach dem Verfahren arbeitende Anlage
EP2331825B1 (fr) * 2008-10-07 2017-06-21 Shell Internationale Research Maatschappij B.V. Procédé de commande d'un compresseur et appareil correspondant
US8155764B2 (en) * 2009-02-27 2012-04-10 Honeywell International Inc. Multivariable model predictive control for coalbed gas production
US20110210555A1 (en) * 2010-02-26 2011-09-01 Xia Jian Y Gas turbine driven electric power system with constant output through a full range of ambient conditions

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Also Published As

Publication number Publication date
CA2837615C (fr) 2019-12-17
EP2691656A2 (fr) 2014-02-05
EP2530329A1 (fr) 2012-12-05
CA2837615A1 (fr) 2012-12-06
WO2012163715A3 (fr) 2013-05-10
AU2012264989B2 (en) 2017-01-12
AU2012264989B9 (en) 2017-05-25
US20140178208A1 (en) 2014-06-26
AU2012264989A1 (en) 2013-11-14

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