CA2837615A1 - System for gathering gas from a gas field comprising a high efficient high pressure compressor - Google Patents
System for gathering gas from a gas field comprising a high efficient high pressure compressor Download PDFInfo
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- CA2837615A1 CA2837615A1 CA2837615A CA2837615A CA2837615A1 CA 2837615 A1 CA2837615 A1 CA 2837615A1 CA 2837615 A CA2837615 A CA 2837615A CA 2837615 A CA2837615 A CA 2837615A CA 2837615 A1 CA2837615 A1 CA 2837615A1
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- 230000001276 controlling effect Effects 0.000 claims description 38
- 238000012384 transportation and delivery Methods 0.000 claims description 24
- 230000000740 bleeding effect Effects 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 9
- 208000036366 Sensation of pressure Diseases 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 230000001419 dependent effect Effects 0.000 description 3
- 239000003245 coal Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 208000034423 Delivery Diseases 0.000 description 1
- 229910052729 chemical element Inorganic materials 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000003455 independent Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
Classifications
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- 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
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- 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
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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
A system includes a high pressure compressor having a gas input and a gas output. The gas input is coupleable to a gas field for receiving a gathered gas with a first gas pressure, and the gas output is coupleable to a gas export system for providing the gas with a second gas pressure, which is higher than the first gas pressure, to the gas export system. The system also includes a measuring unit coupled to the gas input. The measuring unit measures an input mass flow value indicative of an input mass flow at the gas input. The system also includes a mass flow control unit that is coupled to the measuring unit for receiving the measured input mass flow value and 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.
Description
DESCRIPTION
System for gathering gas from a gas field comprising a high efficient high pressure compressor Field of invention 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.
Art Background In the technical field of gas gathering, gas is gathered from conventional gas field types and unconventional gas field types exist.
In conventional gas fields the stored gas comprises an ini-tially high pressure such that further compression by exter-nal compressors is not needed in the beginning. After years of so-called free-flow production a high pressure central compressor, for example of a centrifugal type compressor, is installed for another couple of years. In the end of the gas field lifetime, low pressure wellhead compressors are imple-mented and connected to the respective wellheads of the gas field. The high pressure central compressor and the low pres-sure 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.
In unconventional gas fields, such as tight gas, shell gas or coal bed methane gas fields, the gas pressure inside the gas field decreases in a short time interval, such that central high pressure compressors and low pressure wellhead compres-
System for gathering gas from a gas field comprising a high efficient high pressure compressor Field of invention 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.
Art Background In the technical field of gas gathering, gas is gathered from conventional gas field types and unconventional gas field types exist.
In conventional gas fields the stored gas comprises an ini-tially high pressure such that further compression by exter-nal compressors is not needed in the beginning. After years of so-called free-flow production a high pressure central compressor, for example of a centrifugal type compressor, is installed for another couple of years. In the end of the gas field lifetime, low pressure wellhead compressors are imple-mented and connected to the respective wellheads of the gas field. The high pressure central compressor and the low pres-sure 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.
In unconventional gas fields, such as tight gas, shell gas or coal bed methane gas fields, the gas pressure inside the gas field decreases in a short time interval, such that central high pressure compressors and low pressure wellhead compres-
2 sors are needed from the beginning of the gathering of the gas from the gas field.
Up to now, the low pressure wellhead compressors and the high pressure central compressor are designed as separate and in-dependent subsystems. The low pressure wellhead compressors and the high pressure wellhead compressor often form inde-pendent and separated units. The high pressure central com-pressor 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 pres-sures and mass flows. Hence, each low pressure wellhead com-pressor 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 com-pressor works efficiently. A variation of the gas pressure in the gas field does not affect the efficiency of the low pres-sure wellhead compressors dramatically, whereas the effi-ciency of the subsequent high pressure central compressor is affected dramatically during pressure changes. Hence, the gathering of the gas is inefficient, if the inlet gas pres-sures 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.
Summary of the Invention It may be an objective of the present invention to provide an efficient gas gathering system for gathering gas from a gas field.
This objective is solved by a system for gathering a gas from a gas field and by a method for controlling a gas mass flow of a system for gathering gas from a gas field according to the independent claims.
Up to now, the low pressure wellhead compressors and the high pressure central compressor are designed as separate and in-dependent subsystems. The low pressure wellhead compressors and the high pressure wellhead compressor often form inde-pendent and separated units. The high pressure central com-pressor 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 pres-sures and mass flows. Hence, each low pressure wellhead com-pressor 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 com-pressor works efficiently. A variation of the gas pressure in the gas field does not affect the efficiency of the low pres-sure wellhead compressors dramatically, whereas the effi-ciency of the subsequent high pressure central compressor is affected dramatically during pressure changes. Hence, the gathering of the gas is inefficient, if the inlet gas pres-sures 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.
Summary of the Invention It may be an objective of the present invention to provide an efficient gas gathering system for gathering gas from a gas field.
This objective is solved by a system for gathering a gas from a gas field and by a method for controlling a gas mass flow of a system for gathering gas from a gas field according to the independent claims.
3 According to a first aspect of the present invention, a sys-tem for gathering a gas from a gas field is presented. The system 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. Furthermore, 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 con-trol 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.
According to a further aspect of the present invention, a method for controlling a gas mass flow of a system for gath-ering gas from a gas field is presented. According to the method an input mass flow at a gas input of a high pressure compressor is measured. The gas input receives the gas gath-ered from the gas field with a first gas pressure, wherein 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.
According to a further aspect of the present invention, a method for controlling a gas mass flow of a system for gath-ering gas from a gas field is presented. According to the method an input mass flow at a gas input of a high pressure compressor is measured. The gas input receives the gas gath-ered from the gas field with a first gas pressure, wherein 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.
4 By the above-described system and by the above-described method for controlling a gas mass flow, (natural) gas may be gathered from a conventional gas field or from an unconven-tional gas field, in which tight gas, shell gas or coal bed methane gas is gathered.
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 approxi-mately 60 to 90 bars which are needed by the gas export sys-tem.
The high pressure central compressor may be e.g. of a cen-trifugal type compressor and is most suitable for the gas gathering in order to generate the high gas pressure for the subsequent 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. Moreover, the export gas system may comprise a gas power plant for gen-erating 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-
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 approxi-mately 60 to 90 bars which are needed by the gas export sys-tem.
The high pressure central compressor may be e.g. of a cen-trifugal type compressor and is most suitable for the gas gathering in order to generate the high gas pressure for the subsequent 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. Moreover, the export gas system may comprise a gas power plant for gen-erating 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-
5 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 5 and the gas output of the high pressure compressor.
The measured values, in particular the measured input mass flow value, 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.
Hence, under given first pressures and second pressures, a set point input mass flow value is given for running the high pressure compressor at its working point and hence at its best efficiency. It has been shown, that a deviation of the input mass flow value causes a severe effect on the effi-ciency of the high pressure compressor. In particular, if the measured input mass flow value differs dramatically to the set point input mass flow value, in particular at given first and second gas pressures, compressor surge may occur.
The mass flow control unit is adapted for reducing the devia-tion of the measured input mass flow value from the given set
The measured values, in particular the measured input mass flow value, 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.
Hence, under given first pressures and second pressures, a set point input mass flow value is given for running the high pressure compressor at its working point and hence at its best efficiency. It has been shown, that a deviation of the input mass flow value causes a severe effect on the effi-ciency of the high pressure compressor. In particular, if the measured input mass flow value differs dramatically to the set point input mass flow value, in particular at given first and second gas pressures, compressor surge may occur.
The mass flow control unit is adapted for reducing the devia-tion of the measured input mass flow value from the given set
6 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. For example, 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.
Hence, by the present invention, even when the gathered mass flow of gas from a gas field varies dramatically, a predeter-mined and desired input mass flow at the gas input of the high pressure compressor is adjustable by the mass flow con-trol unit such that the high pressure compressor is working approximately at its working point. Hence, the efficiency of the high pressure compressor and hence the gathering of gas from a gas field is more efficient.
According to a further exemplary embodiment, the system com-prises a first low pressure compressor which is connectable to a first wellhead arrangement of the gas field for receiv-ing 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.
Moreover, 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 con-trolling 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.
Hence, by the present invention, even when the gathered mass flow of gas from a gas field varies dramatically, a predeter-mined and desired input mass flow at the gas input of the high pressure compressor is adjustable by the mass flow con-trol unit such that the high pressure compressor is working approximately at its working point. Hence, the efficiency of the high pressure compressor and hence the gathering of gas from a gas field is more efficient.
According to a further exemplary embodiment, the system com-prises a first low pressure compressor which is connectable to a first wellhead arrangement of the gas field for receiv-ing 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.
Moreover, 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 con-trolling 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.
7 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. By increasing the pressure, a sucking effect is achieved, such that the gas is sucked out of the respective borehole, so that also the respective mass flow through the low pressure compressor is increased.
For the low pressure wellhead compressors, screw-type or re-ciprocating compressors may be used. These kind of compres-sors are relative insensitive to changes in inlet conditions.
They have a large operating range and can easily handle a wide range of inlet pressure variations and inlet mass flows variations under which an effective operation is still possi-ble.
For example, 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 respec-tive 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 compres-sor, 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. Hence, for adjusting the desired input mass flow of the high pressure compressor, each low pressure compressor
For the low pressure wellhead compressors, screw-type or re-ciprocating compressors may be used. These kind of compres-sors are relative insensitive to changes in inlet conditions.
They have a large operating range and can easily handle a wide range of inlet pressure variations and inlet mass flows variations under which an effective operation is still possi-ble.
For example, 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 respec-tive 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 compres-sor, 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. Hence, for adjusting the desired input mass flow of the high pressure compressor, each low pressure compressor
8 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.
Additionally or alternatively, according to a further exem-plary embodiment, 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 sec-ond 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. Alter-natively, the first and second delivery valves may be in-stalled behind, i.e. downstream, of the respectively first and second low pressure compressors.
By controlling the respective delivery valves, 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.
Additionally or alternatively, according to a further exem-plary embodiment, 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 sec-ond 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. Alter-natively, the first and second delivery valves may be in-stalled behind, i.e. downstream, of the respectively first and second low pressure compressors.
By controlling the respective delivery valves, 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.
9 In gas gathering systems, in particular in conventional gas gathering systems, gas may be gathered without using low pressure compressors. In this case only 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.
According to a further exemplary embodiment, 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. In the return flow tubing a control valve may be installed which is controllable by the mass flow control unit.
By using the return flow tubing, an anti-surge system is es-tablished. The mass flow control unit may act as a supervi-sory system and controls the anti-surge system. By control-ling the input gas parameters, in particular the input mass flow of the gas, and by influencing the upstream located sys-tems, such as the low pressure (wellhead) compressors, the anti-surge system for the high pressure compressor is safer and more efficient.
According to a further exemplary embodiment, the system fur-ther 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.
For example, if the input mass flow is higher than the set point input mass flow value, 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
According to a further exemplary embodiment, 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. In the return flow tubing a control valve may be installed which is controllable by the mass flow control unit.
By using the return flow tubing, an anti-surge system is es-tablished. The mass flow control unit may act as a supervi-sory system and controls the anti-surge system. By control-ling the input gas parameters, in particular the input mass flow of the gas, and by influencing the upstream located sys-tems, such as the low pressure (wellhead) compressors, the anti-surge system for the high pressure compressor is safer and more efficient.
According to a further exemplary embodiment, the system fur-ther 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.
For example, if the input mass flow is higher than the set point input mass flow value, 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
10 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.
By the present invention, the high pressure compressor of a gas gathering system is controlled and operated more effi-ciently. In particular, 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. For example, 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 compres-sor is constructable.
By the present invention, optimised inlet conditions for the high pressure compressor are generated in particular by adapting and controlling the low pressure compressors. By controlling the low pressure compressors dependent on the de-sired input values of the high pressure compressor, an inter-connected efficient and effective gathering system is achieved.
It has to be noted that embodiments of the invention have been described with reference to different subject matters.
In particular, some embodiments have been described with ref-
By the present invention, the high pressure compressor of a gas gathering system is controlled and operated more effi-ciently. In particular, 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. For example, 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 compres-sor is constructable.
By the present invention, optimised inlet conditions for the high pressure compressor are generated in particular by adapting and controlling the low pressure compressors. By controlling the low pressure compressors dependent on the de-sired input values of the high pressure compressor, an inter-connected efficient and effective gathering system is achieved.
It has to be noted that embodiments of the invention have been described with reference to different subject matters.
In particular, some embodiments have been described with ref-
11 erence to apparatus type claims whereas other embodiments have been described with reference to method type claims.
However, a person skilled in the art will gather from the above and the following description that, unless other noti-fied, in addition to any combination of features belonging to one type of subject matter also any combination between fea-tures relating to different subject matters, in particular between features of the apparatus type claims and features of the method type claims is considered as to he disclosed with this application.
Brief Description of the Drawing The aspects defined above and further aspects of the present invention are apparent from the examples of embodiment to be described hereinafter and are explained with reference to the examples of embodiment. The invention will be described in more detail hereinafter with reference to examples of embodi-ment but to which the invention is not limited.
The Figure shows schematically a gas gathering system accord-ing to an exemplary embodiment of the present invention.
Detailed Description The illustration in the drawing is schematical. It is noted that in the figure, similar or identical elements are pro-vided with the same reference signs.
The Figure shows a system for gathering a gas from a gas field 170. The system comprises a high pressure compres-sor 100 which comprises a gas input 101 and a gas output 102.
The gas input 101 is coupleable to the gas field 170 for re-ceiving the gas gathered from the gas field 170 with a first gas pressure pl. The gas output 102 is coupleable to a gas
However, a person skilled in the art will gather from the above and the following description that, unless other noti-fied, in addition to any combination of features belonging to one type of subject matter also any combination between fea-tures relating to different subject matters, in particular between features of the apparatus type claims and features of the method type claims is considered as to he disclosed with this application.
Brief Description of the Drawing The aspects defined above and further aspects of the present invention are apparent from the examples of embodiment to be described hereinafter and are explained with reference to the examples of embodiment. The invention will be described in more detail hereinafter with reference to examples of embodi-ment but to which the invention is not limited.
The Figure shows schematically a gas gathering system accord-ing to an exemplary embodiment of the present invention.
Detailed Description The illustration in the drawing is schematical. It is noted that in the figure, similar or identical elements are pro-vided with the same reference signs.
The Figure shows a system for gathering a gas from a gas field 170. The system comprises a high pressure compres-sor 100 which comprises a gas input 101 and a gas output 102.
The gas input 101 is coupleable to the gas field 170 for re-ceiving the gas gathered from the gas field 170 with a first gas pressure pl. The gas output 102 is coupleable to a gas
12 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 pl.
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.
Furthermore, 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 pl and the temperature at the gas input 101 and/or the second pres-.
sure p2, the output mass flow m2 and/or the temperature at the gas output 102.
All measured data are provided to the mass flow control unit 120. The mass flow control unit 120 may calculate on the basis of the inputted data values, such as the input mass flow ml, the first pressure p1, the second pressure p2, the output mass flow m2, 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
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.
Furthermore, 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 pl and the temperature at the gas input 101 and/or the second pres-.
sure p2, the output mass flow m2 and/or the temperature at the gas output 102.
All measured data are provided to the mass flow control unit 120. The mass flow control unit 120 may calculate on the basis of the inputted data values, such as the input mass flow ml, the first pressure p1, the second pressure p2, the output mass flow m2, 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
13 lines, for transmitting measuring data and control data are shown with the dotted lines.
Besides the high pressure compressor 100, in the figure fur-ther components of the system for gathering gas are shown.
Generally, from the gas field 170 gas is gathered through a plurality of boreholes. At each borehole, a respective well-head arrangement 151-154 is attached. Downstream of each wellhead arrangement 151-154, a respective delivery valve 161-164 is coupled. Hence, by controlling the delivery valves 161-164, a respective mass flow from a respective wellhead arrangement 151-154 to the gas input 101 is controllable.
In order to increase the amount of gathered gas from the gas field, in all or in some tubes between the gas input 101 and a respective first wellhead arrangement 151-154, a respective low pressure compressor 141-144 is installed. Each low pres-sure compressor 141-144 may increase the pressure from ap-proximately 1 to 4 bars to approximately 5 to 20 bars.
By controlling the low pressure compressor 141-144 the mass flow of gas which is delivered by a respective wellhead ar-rangement 151 to the gas input 101 is adjustable. 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 predeter-mined input mass flow ati of gas to the gas input 101. The mass flow control unit 120 is adapted for example for con-trolling the rotational speed of each low pressure compressor 141-144, for example.
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.
Besides the high pressure compressor 100, in the figure fur-ther components of the system for gathering gas are shown.
Generally, from the gas field 170 gas is gathered through a plurality of boreholes. At each borehole, a respective well-head arrangement 151-154 is attached. Downstream of each wellhead arrangement 151-154, a respective delivery valve 161-164 is coupled. Hence, by controlling the delivery valves 161-164, a respective mass flow from a respective wellhead arrangement 151-154 to the gas input 101 is controllable.
In order to increase the amount of gathered gas from the gas field, in all or in some tubes between the gas input 101 and a respective first wellhead arrangement 151-154, a respective low pressure compressor 141-144 is installed. Each low pres-sure compressor 141-144 may increase the pressure from ap-proximately 1 to 4 bars to approximately 5 to 20 bars.
By controlling the low pressure compressor 141-144 the mass flow of gas which is delivered by a respective wellhead ar-rangement 151 to the gas input 101 is adjustable. 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 predeter-mined input mass flow ati of gas to the gas input 101. The mass flow control unit 120 is adapted for example for con-trolling the rotational speed of each low pressure compressor 141-144, for example.
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.
14 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 re-spective borehole. All gathering groups deliver gas to a corn-mon collecting manifold to which the high pressure compressor 100 is coupled. In particular, a gas field may comprise a plurality of boreholes, wherein to each borehole a respective gathering group is coupled.
Furthermore, 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 out-let 102. Hence, for the gas export system 130, a high gas pressure is provided which is needed e.g. for the further processing of the gas.
Moreover, as shown in the figure, 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.
It should be noted that the term "comprising" does not ex-clude other elements or steps and "a" or "an" does not ex-clude a plurality. Also elements described in association with different embodiments may be combined. It should also be noted that reference signs in the claims should not be con-strued as limiting the scope of the claims.
Furthermore, 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 out-let 102. Hence, for the gas export system 130, a high gas pressure is provided which is needed e.g. for the further processing of the gas.
Moreover, as shown in the figure, 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.
It should be noted that the term "comprising" does not ex-clude other elements or steps and "a" or "an" does not ex-clude a plurality. Also elements described in association with different embodiments may be combined. It should also be noted that reference signs in the claims should not be con-strued as limiting the scope of the claims.
Claims (5)
1. System for gathering a gas from a gas field (170), the system comprising a high pressure compressor (100) which comprises a gas input (101) and a gas output (102), wherein 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, wherein the gas output (102) is coupleable to a gas export system (130) for providing the gas with a second gas pressure to the gas export system (130), and wherein the second gas pressure is higher than the first gas pressure, a measuring unit (110, 111) coupled to the gas input (101), wherein the measuring unit (110, 111) measures an in-put mass flow value which is indicative of an input mass flow at the gas input (101), a first low pressure compressor (141) which is connect-able to a first wellhead arrangement (151) of the gas field (170) for receiving the gas from the first wellhead arrange-ment (151), wherein the first low pressure compressor (141) is con-nected to the gas input (101) for providing the gas to the gas input (101) with a first mass flow, and a second low pressure compressor (142) which is connect-able to a second wellhead arrangement (152) of the gas field (170) for receiving the gas from the second wellhead arrange-ment (152), wherein the second low pressure compressor (142) is con-nected to the gas input (101) for providing the gas to the gas input (101) with a second mass flow, and a mass flow control unit (120), wherein the mass flow control unit (120) is coupled to the measuring unit (110, 111) for receiving the measured in-put mass flow value, and wherein the mass flow control unit (120) is further con-nected to a) the first low pressure compressor (141) for control-ling the first low pressure compressor (141) and b) the second low pressure compressor (142) for control-ling the second low pressure compressor (142) such that the first mass flow and the second mass flow are controllable for controlling the input mass flow at the gas input (101) such that the measured input mass flow value corresponds to a set point input mass flow value.
2. System according to claim 1, further comprising a first delivery valve (161) which is connectable to a first wellhead arrangement (151) of the gas field (170) for receiving the gas from the first wellhead arrangement (151), wherein the first delivery valve (161) is connected to the gas input (101) for providing the gas to the gas input (101) with a further first mass flow, and a second delivery valve (162) which is connectable to a second wellhead arrangement (152) of the gas field (170) for receiving the gas from the second wellhead arrangement (152), wherein the second delivery valve (162) is connected to the gas input (101) for providing the gas to the gas input (101) with a further second mass flow, wherein the mass flow control unit (120) is connected to a) the first delivery valve (161) for controlling the first delivery valve (161) and h) the second delivery valve (162) for controlling the further second mass flow 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 (101).
3. System according to claim 1 or 2, further comprising a return flow tubing (103) which is connected to the gas output (102) for bleeding off a part of the gas from the gas output (102) and which is connected to the gas input (101) for injecting the part of the gas in the gas input (101), wherein the mass flow control unit (120) is coupled to the return flow tubing (103) for controlling the bleeding off of the part of the gas from the gas output (102) and for con-trolling the injecting of the part of the gas in the gas in-put (101) such that the input mass flow at the gas input (101) is controllable.
4. System according to one of the claims 1 to 3, further comprising a bypass tubing which is connected to the gas input (101) for bleeding off a further part of the gas from the gas input (101), wherein the mass flow control unit (120) is coupled to the bypass tubing for controlling the bleeding off of the further part of the gas from the gas input (101) such that the input mass flow at the gas input (101) is controllable.
5. Method for controlling a gas mass flow of a system for gathering gas from a gas field (170), the method comprising measuring an input mass flow at a gas input (101) of a high pressure compressor (100), wherein the gas input (101) receives the gas gathered from the gas field (170) with a first gas pressure, wherein the high pressure compressor (100) comprises a gas output (102) for providing gas with a second gas pressure to a gas export system (130), wherein the second gas pressure is higher than the first gas pressure, measuring an input mass flow value which is indicative of an input mass flow at the gas input (101) by a measuring unit (110, 111) which is coupled to the gas input (101), receiving the measured input mass flow value by a mass flow control unit (120), wherein a first low pressure compressor (141) is con-nectable to a first wellhead arrangement (151) of the gas field (170) for receiving the gas from the first wellhead ar-rangement (151), wherein the first low pressure compressor (141) is con-nected to the gas input (101) for providing the gas to the gas input (101) with a first mass flow, and wherein a second low pressure compressor (142) is con-nectable to a second wellhead arrangement (152) of the gas field (170) for receiving the gas from the second wellhead arrangement (152), wherein the second low pressure compressor (142) is con-nected to the gas input (101) for providing the gas to the gas input (101) with a second mass flow, and and controlling the input mass flow by the mass flow control unit (120) which is coupled to the gas input (101), wherein the mass flow control unit (120) is coupled to the measuring unit (110, 111) for receiving the measured in-put mass flow value, and wherein the mass flow control unit (120) is further con-nected to a) the first low pressure compressor (141) for control-ling the first low pressure compressor (141) and b) the second low pressure compressor (142) for control-ling the second low pressure compressor (142) such that the first mass flow and the second mass flow are controllable for controlling the input mass flow at the gas input (101) such that the measured input mass flow value corresponds to a set point input mass flow value.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP11168122A EP2530329A1 (en) | 2011-05-30 | 2011-05-30 | System for gathering gas from a gas field comprising a high pressure compressor |
| EP11168122.7 | 2011-05-30 | ||
| PCT/EP2012/059386 WO2012163715A2 (en) | 2011-05-30 | 2012-05-21 | System for gathering gas from a gas field comprising a high efficient high pressure compressor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2837615A1 true CA2837615A1 (en) | 2012-12-06 |
| CA2837615C CA2837615C (en) | 2019-12-17 |
Family
ID=46208456
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2837615A Expired - Fee Related CA2837615C (en) | 2011-05-30 | 2012-05-21 | System for gathering gas from a gas field comprising a high efficient high pressure compressor |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20140178208A1 (en) |
| EP (2) | EP2530329A1 (en) |
| AU (1) | AU2012264989B9 (en) |
| CA (1) | CA2837615C (en) |
| WO (1) | WO2012163715A2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20190249525A1 (en) * | 2016-09-26 | 2019-08-15 | Siemens Aktiengesellschaft | Operation of a wellhead compressor |
Family Cites Families (5)
| 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 (en) * | 1998-12-29 | 2000-07-06 | Man Turbomasch Ag Ghh Borsig | Method for operating a compressor with a downstream consumer, and system operating according to the method |
| WO2010040734A1 (en) * | 2008-10-07 | 2010-04-15 | Shell Internationale Research Maatschappij B.V. | Method of controlling a compressor and apparatus therefor |
| 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 |
-
2011
- 2011-05-30 EP EP11168122A patent/EP2530329A1/en not_active Ceased
-
2012
- 2012-05-21 EP EP12725663.4A patent/EP2691656A2/en not_active Withdrawn
- 2012-05-21 CA CA2837615A patent/CA2837615C/en not_active Expired - Fee Related
- 2012-05-21 WO PCT/EP2012/059386 patent/WO2012163715A2/en active Application Filing
- 2012-05-21 US US14/123,215 patent/US20140178208A1/en not_active Abandoned
- 2012-05-21 AU AU2012264989A patent/AU2012264989B9/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| US20140178208A1 (en) | 2014-06-26 |
| WO2012163715A2 (en) | 2012-12-06 |
| AU2012264989B9 (en) | 2017-05-25 |
| AU2012264989B2 (en) | 2017-01-12 |
| WO2012163715A3 (en) | 2013-05-10 |
| AU2012264989A1 (en) | 2013-11-14 |
| EP2691656A2 (en) | 2014-02-05 |
| CA2837615C (en) | 2019-12-17 |
| EP2530329A1 (en) | 2012-12-05 |
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