WO2013087740A2 - System and method for producing a liquefied hydrocarbon stream and method of operating a compressor - Google Patents
System and method for producing a liquefied hydrocarbon stream and method of operating a compressor Download PDFInfo
- Publication number
- WO2013087740A2 WO2013087740A2 PCT/EP2012/075314 EP2012075314W WO2013087740A2 WO 2013087740 A2 WO2013087740 A2 WO 2013087740A2 EP 2012075314 W EP2012075314 W EP 2012075314W WO 2013087740 A2 WO2013087740 A2 WO 2013087740A2
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- WO
- WIPO (PCT)
- Prior art keywords
- power supply
- compressor
- supply network
- refrigerant
- guide vanes
- Prior art date
Links
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 62
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 62
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 57
- 238000000034 method Methods 0.000 title claims abstract description 50
- 238000004519 manufacturing process Methods 0.000 title description 6
- 239000003507 refrigerant Substances 0.000 claims abstract description 106
- 239000012530 fluid Substances 0.000 claims abstract description 35
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 40
- 230000008569 process Effects 0.000 claims description 22
- 239000003949 liquefied natural gas Substances 0.000 claims description 16
- 239000003345 natural gas Substances 0.000 claims description 14
- 238000012544 monitoring process Methods 0.000 claims description 4
- 238000010248 power generation Methods 0.000 description 12
- 230000007246 mechanism Effects 0.000 description 8
- 239000007789 gas Substances 0.000 description 6
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical class CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 235000013844 butane Nutrition 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- -1 H20 Chemical class 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical class CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical class [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0022—Hydrocarbons, e.g. natural gas
-
- 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
- F04D27/002—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids by varying geometry within the pumps, e.g. by adjusting vanes
-
- 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
- F04D27/0246—Surge control by varying geometry within the pumps, e.g. by adjusting vanes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
- F25J1/0281—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc. characterised by the type of prime driver, e.g. hot gas expander
- F25J1/0284—Electrical motor as the prime mechanical driver
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
- F25J1/0298—Safety aspects and control of the refrigerant compression system, e.g. anti-surge control
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2280/00—Control of the process or apparatus
- F25J2280/20—Control for stopping, deriming or defrosting after an emergency shut-down of the installation or for back up system
Abstract
At least part of a fluid is compressed in a compressor driven by an electric motor. The compressor has variable inlet guide vanes of which an angle can be adjusted. The electric motor is powered using a power supply network, and a signal representative of a condition of the power supply network is monitored. From the signal, it is automatically determined whether additional load shedding is needed, by comparing the signal to a predetermined criterion. The variable inlet guide vanes angle is automatically adjusted when the criterion is satisfied and additional load shedding is needed. This automatically reduces the loading of the compressor. The compressor and the method of operating it may be employed as part of a system for producing a liquefied hydrocarbon stream and/or in the course of producing a liquefied hydrocarbon stream, in which case the compressor can be a refrigerant compressor and the fluid a refrigerant fluid.
Description
- -
SYSTEM AND METHOD FOR PRODUCING A LIQUEFIED HYDROCARBON STREAM AND METHOD OF OPERATING A COMPRESSOR
In a first aspect, the present invention relates to a method of producing a liquefied hydrocarbon stream. In a second aspect, the present invention relates to a system for producing a liquefied hydrocarbon stream. In a further aspect, the present invention relates to a method of operating a compressor.
A common liquefied hydrocarbon stream in the industry is liquefied natural gas (LNG) , which may be obtained by liquefying a natural gas stream. It is desirable to liquefy natural gas for a number of reasons. As an example, natural gas can be stored, and transported over long distances, more readily in the form of LNG than in gaseous form, because as LNG it occupies a smaller volume and does not need to be stored at a high pressure.
US pre-grant patent application publication No.
2010/0257895 describes an all electric LNG plant wherein LNG is produced, in which compressors in the form of refrigerant compressors are employed to refrigerate the natural gas. The refrigerant compressors are driven by electric motors. A power plant supplies the electrical power for these motors. The power plant contains a plurality of power generation units, each based on an electric generator driven by a gas or steam turbine.
If, for some reason, the available electrical power suddenly goes down, or is partially interrupted, the LNG production process will fail and it can take at least a number of hours before the refrigerant compressor ( s ) have started up again and before the LNG production process has regained it stability of operation.
- -
This risk can be reduced by installing an overcapacity of power generation (based on the so-called N+l principle) in the form of stand-by power generation units, or by operating a plurality of power generation units at less than full capacity (sometimes referred to as maintaining "spinning reserve") . These solutions have in common that failure of one generation unit can be afforded because, compared to the N power generation units minimally required to deliver the total power demand of the LNG plant, an additional power generation unit is provided in accordance with the N+l principle.
US 2010/0257895 further proposes that in the event of the failure of a power generation unit in the power plant, the (rotational) speed of the compressor drive will preferably be lowered if a previously determined overall positive load reserve is smaller than the power which was being supplied by the power generation unit before its failure. According to the quadratic load characteristic curve of a turbine compressor, the power drawn from the electric motors reduces as the cube of the rotational speed. Only if the actual energy demand of the LNG plant is not covered even taking into account the reduction in the compressor drive speed, it is expedient to switch off at least one predetermined electrical consumer in the gas liquefaction plant.
One drawback of the load shedding solution proposed in US 2010/0257895 is that the response time for load shedding to take effect is limited by the total
rotational inertia of rotating parts of the motors, compressors and drive shafts. Another drawback is that the solution of US 2010/0257895 requires the
compressor ( s ) to be driven by variable-speed motors.
- -
In a first aspect, the present invention provides a method of producing a liquefied hydrocarbon stream, comprising :
- circulating a refrigerant fluid through a refrigerant circuit, comprising compressing at least part of the refrigerant fluid in a refrigerant compressor driven by an electric motor wherein the refrigerant compressor comprises variable inlet guide vanes of which an angle compared to a reference position can be adjusted;
- removing heat from an initially vaporous hydrocarbon stream thereby condensing at least part of the initially vaporous hydrocarbon stream to form the liquefied
hydrocarbon stream, said removing of heat comprising heat exchanging at least said part of the initially vaporous hydrocarbon stream against at least part of the
refrigerant fluid circulating through the refrigerant circuit ;
- powering the electric motor using a power supply network ;
- monitoring a signal representative of a condition of the power supply network;
- automatically determining from the signal whether additional load shedding is needed by comparing the signal to a predetermined criterion;
- automatically adjusting the variable inlet guide vanes angle thereby reducing the loading of the refrigerant compressor when the criterion is satisfied and additional load shedding is needed.
In a further aspect, the invention provides a system for producing a liquefied hydrocarbon stream, comprising:
- a refrigerant circuit arranged to circulate a
refrigerant fluid, comprising a refrigerant compressor for compressing at least part of the refrigerant fluid
- - and an electric motor engaged to the refrigerant
compressor to drive the refrigerant compressor wherein the refrigerant compressor comprises variable inlet guide vanes having an adjustable angle compared to a reference position;
- a heat exchanger train comprising at least one heat exchanger, said heat exchanger train arranged to remove heat from an initially vaporous hydrocarbon stream thereby condensing at least part of the initially
vaporous hydrocarbon stream to form the liquefied
hydrocarbon stream, said least one heat exchanger
arranged to accommodate at least said part of the
initially vaporous hydrocarbon stream and at least part of the refrigerant fluid circulating through the
refrigerant circuit in a mutual heat exchanging
relationship;
- a power supply network connected to the electric motor for powering the electric motor;
- a load shedding controller arranged to monitor a signal representative of a condition of the power supply
network, to automatically determine from the signal whether additional load shedding is needed by comparing the signal to a predetermined criterion, and, when the criterion is satisfied and additional load shedding is needed, to adjust the variable inlet guide vanes angle to a position wherein the refrigerant compressor is unloaded relative to the loading in a previous condition whereby the variable inlet guide vanes angle was in a previous position when the criterion was not satisfied.
In still another aspect, the invention provides a method of operating a compressor, comprising:
- compressing at least part of a fluid in a compressor driven by an electric motor, wherein the compressor
- - comprises variable inlet guide vanes of which an angle can be adjusted;
- powering the electric motor using a power supply network ;
- monitoring a signal representative of a condition of the power supply network;
- automatically determining from the signal if additional load shedding is needed by comparing the signal to a predetermined criterion;
- automatically adjusting the variable inlet guide vanes angle thereby reducing the loading of the compressor when additional load shedding is needed.
The present invention will now be further illustrated by way of example, and with reference to the accompanying non-limiting drawings, in which:
Figure 1 schematically shows a system for producing a liquefied hydrocarbon stream; and
Figure 2 schematically shows an illustrative non- limiting example of an embodiment of variable inlet guide vanes in a centrifugal compressor.
For the purpose of this description, a single
reference number will be assigned to a line as well as a stream carried in that line. The same reference numbers refer to similar components, streams or lines.
The present disclosure describes methods and systems for producing a liquefied hydrocarbon stream. In the course of producing the liquefied hydrocarbon stream, a compressor is employed which is driven by an electric motor. At least part of a fluid is compressed in the compressor. The compressor has variable inlet guide vanes of which an angle can be adjusted. The electric motor is powered using a power supply network, and a signal representative of a condition of the power supply
- - network is monitored. From the signal, it is
automatically determined whether additional load shedding is needed, by comparing the signal to a predetermined criterion. The variable inlet guide vanes angle are automatically adjusted when the criterion is satisfied and additional load shedding is needed, thereby
automatically reducing the loading of the compressor.
By adjusting the variable inlet guide vanes angle, the power demand can be reduced without relying on reducing the motor speed. Therefore, the presently proposed method of load shedding can be employed
irrespective of whether a variable speed electric drive is used or a fixed speed electric drive.
Moreover, the inertia of the rotating mass such as rotating parts of the motor, the compressor and the drive shaft, does not influence the response time of a load shedding action. Inlet guide vanes have much less inertia than the rotating parts of the motor/compressor system, and therefore it is envisaged that the response time associated with adjusting the variable inlet guide vanes can be much lower.
For instance, the compressor is unloaded by adjusting the variable inlet guide vanes angle when the monitored signal indicates that the available power drops below a predetermined value. The condition of the power supply network represented by the signal may thus represent power available on the power supply network relative to power being consumed, whereby the predetermined criterion is satisfied when the available power, according to the monitored signal, drops below a predetermined value.
This way the power supply network can be protected by quickly unloading the compressor thereby imposing a quick
- - relief of the power being demanded from the power supply network .
If the predetermined criterion is not satisfied, no additional load shedding is needed.
In one group of embodiments the signal representative of the condition of the power supply network is
representative of a network frequency at which the power supply network operates. The need for additional load shedding can be inferred from such a signal if the network frequency deviates from a pre-determined nominal network frequency. Typically, if the actual network frequency is lower than the nominal network frequency load shedding may be needed in order to reduce the power demand on the network which helps to bring the actual network frequency back to the nominal network frequency.
Automatically determining from the signal whether
additional load shedding is needed may comprise comparing the actual network frequency to a pre-determined nominal network frequency. The predetermined criterion to determine whether additional load shedding is needed may include the nominal network frequence and the criterion is satisfied when the actual network frequence drops below the predetermined nominal network frequency.
In preferred embodiments, the compressor is provided in the form of a refrigerant compressor, whereby the fluid is a refrigerant fluid, such as may be employed in a system and/or process for producing a liquefied
hydrocarbon stream. Suitably, the compressor is driven only by the electric motor.
The proposed load shedding method can also be used to prevent overloading that could result from an increase in ambient temperature. This may be useful particularly if the compressor is provided in the form of a refrigerant
- - compressor employed for compressing at least part of a refrigerant fluid, as may be done in the course of operating a process of producing as liquefied hydrocarbon stream. An increase in ambient temperature generally increases the power demand for liquefying the hydrocarbon stream. In addition, if the power supply network is powered via one or more gas turbines, the available power will reduce as a result of the increase in ambient temperature .
The proposed load shedding method can be used in connection with compressors relying on so-called "island- mode" power generation, where the power supply network is powered by a dedicated power plant, as well as those powered by imported power such as imported power from a domestic grid or from an industrial grid to which other consumers of power are connected as well.
Provided that the compressor comprises variable inlet guide vanes of which an angle can be adjusted,
implementation of the proposed load shedding method does not require significant adaptations of equipment.
Implementation may be achieved by changing the existing control system which is typically already in place for controlling the inlet guide vane settings, or by adding a dedicated control system.
Figure 1 illustrates the method of operating the compressor in the context of a method and system for producing a liquefied hydrocarbon stream. However, the teachings provided herein below regarding the operation of the compressor are not necessarily restricted to, or limited to, embodiments wherein the compressor is a refrigerant compressor and/or wherein the fluid is a refrigerant fluid.
- -
The system illustrated in Figure 1 employs at least one refrigerant circuit, including a first refrigerant circuit 100 arranged to circulate a refrigerant fluid 110. Each of the at least one refrigerant circuits comprises a compressor in the form of a refrigerant compressor 120, for compressing at least part of the refrigerant fluid 110 being circulated in the refrigerant circuit 100. Each refrigerant compressor is engaged with an electric motor 130, typically via a mechanical drive shaft 125 extending between the respective
refrigerant compressor 120 and the electric motor 130 to drive the rotor of the respective refrigerant compressor 120 into rotation.
The electric motor 130 is connected to a power supply network 400, for powering the electric motor 130. The power supply network comprises a power source, typically in the form of a power plant 410 and a distribution network 420 connected to the power source. The power plant can be of the "island-mode" type, which is a dedicated power plant for powering the hydrocarbon liquefaction facility, or it can be an external power source from which power is imported into the facility. The distribution network 420 may be connected to a power busbar 430, arranged to feed power to the at least one electric motor 130 via a power feed line 140.
In the embodiment of figure 1, the at least one refrigerant circuit comprises an optional second
refrigerant circuit 200 as well, to circulate a second refrigerant fluid 210. It comprises a second refrigerant compressor 220; a second electric motor 230; a second power feed line 240; and a second mechanical drive shaft 125 all similarly interrelated as described above with reference to the first refrigerant circuit 100.
- -
The system depicted in Figure 1 further comprises a heat exchanger train 300. The heat exchanger train 300 is very schematically shown, as many different types of such heat exchanger trains are known in the art . The heat exchanger train 300 is arranged to remove heat from an initially vaporous hydrocarbon stream 10, thereby
condensing at least part of the initially vaporous hydrocarbon stream 10 to form a liquefied hydrocarbon stream 90. The heat exchanger train typically comprises at least one heat exchanger that is arranged to
accommodate at least said part of the initially vaporous hydrocarbon stream 10 in a mutual heat exchanging
relationship with at least part of the refrigerant fluid 110 circulating through the refrigerant circuit 100.
The compressor ( s ) may be of any type that is provided with variable inlet guide vanes, including axial
compressors (for example the AN 200 axial compressor manufactured by General Electric) and centrifugal
compressors .
Inlet guide vanes are often installed on commercially available refrigerant compressors to increase efficiency and to extend the operating envelope. Inlet guide vanes are typically installed on the first compression stage, but for instance in case of integrally geared
compressors, with multiple compressor stages, inlet guide vanes can also be installed on one or more subsequent stages such as the second stage.
Inlet guide vanes are typically provided in the form of radially positioned aerofoils in the vapour flow of the compressor. Suitably the inlet guide vanes are positioned inside the suction duct. Generally and under normal operating conditions such inlet guide vanes serve to guide the refrigerant vapour into the subsequent
- - compression stage at the most efficient direction onto the vanes or impellers of the subsequent compression stage .
Variable inlet guide vanes, such as may be employed in the context of the present invention, are normally rotatable about their mounting axes. Under normal operating conditions, different refrigerant entry speeds can be accommodated by rotating the variable inlet guide vanes into different positions. Rotation may be imparted on the variable inlet guide vanes by a vane adjustment mechanism coupled to an actuator.
The invention is expressly not limited to any
particular type of inlet guidvane geometry and or vane adjustment mechanism. There are various suitable ways for acting on the vanes, including rotating ring
concepts, lever concepts, hydraulic pistons concepts, all acting on the variable inlet guide vanes. Examples of variable inlet guide vanes and possible mechanisms for adjusting their angle are shown in for instance US patent application publication 2010/0172745 and US patent
7,520,716. In these examples the vapour flows generally inwardly towards the rotating axis of the compressor. US patent application publication 2010/0329898 shows an example wherein the vapour generally flows axially, in the direction along the rotating axis. US patent
application publications 2010/0172745 and 2010/0329898, and US patent 7,520,716 are incorporated in the present disclosure by reference.
An embodiment of variable inlet guide vanes of a centrifugal compressor, derived from US patent
application publication 2010/0172745, is shown in Figure 2 as an illustrative non-limiting example. It comprises a vane adjustment mechanism employing a rotating ring 13
- - provided with a plurality of elongated slots 31, and inlet guide vanes 11 positioned around a circumference of the rotating ring 13. The inlet guide vanes 11 are pivotably attached to a base plate (not shown, in the interest of clarity) , such that each one of the inlet guide vanes 11 can pivot around a shaft 45. The inlet guide vanes 11 are each coupled to an end of one of a plurality of lever arms 43 by the shaft 45. Each lever arm 43 is provided with an outwardly protruding pin 35 in a direction perpendicular to a plane of rotation of the lever arms 43 around their shafts 45. Each pin 35 is configured to be positioned within one of the elongated slots 31. As rotating ring 13 rotates relative to the base plate, each inlet guide vane 11 is rotated by the same amount.
Still referring to Figure 2, the vane adjustment mechanism also includes a rack and pinion drive mechanism 21 configured to drive one of the plurality of inlet guide vanes 11, thereby creating a drive vane 47. The rack and pinion drive mechanism includes a pinion 53 coupled to an elongated shaft 55 of the drive vane 47, which replaces the shaft 45, and a rack 57. The rack 57 includes a plurality of teeth 59 that is configured to engage with a plurality of teeth 61 on the pinion 53, thereby operationally coupling the rack 57 to the pinion
53. An end of the rack 57 is coupled to a drive shaft 23, which may be actuated by for instance hydraulic cylinder (not shown) .
The drive shaft 23 is arranged to impart a linear motion 24 to the rack 57, which is converted to
rotational motion 25 in the pinion 53 thereby rotating drive vane 47 relative to the base plate. Drive vane 47 transfers torque to the rotating ring 13 due to the
- - positioning of each pin 35 on each lever arm 43 within the associate elongated slot 31 of the rotating ring 13 with which the pin 35 interacts. The torque is thereby transmitted to the remaining inlet guide vanes 11, as shown in Figure 2, whereby the respective inlet guide vanes 11 are caused to synchronously change their angular position by the same amount. This way the variable inlet guide vanes angle a compared to a reference
position 16 can be adjusted. In Figure 2, the radial position is taken to be the reference position 16 as an example, but any suitable reference position can be selected .
Referring again to Figure 1, the system is further provided with a load shedding controller C. The load shedding controller C is arranged to monitor a signal that is representative of the available power on the power supply network relative to the power being
consumed, and to adjust the variable inlet guide vanes angle when the available power, as monitored, drops below a predetermined value. In such a case, the variable inlet guide vanes angle is adjusted to a position wherein the refrigerant compressor is unloaded relative to the loading in a previous condition whereby the variable inlet guide vanes angle was in a previous position. To this end, the controller C may interact with the actuator of the compressor 120.
A suitable signal to monitor is the network
frequency. When an AC power supply network is in stable operation it operates at a (pre-determined) nominal frequency. The network frequency, which may be defined as the frequency of the overall system associated with the power network (including the active electric
generators and all the running loads that consume power) ,
- - generally depends directly on the amount of power that the generators can deliver to the system compared to the power being demanded for consumption. Gradual or sudden downward changes in generation capacity result in
frequency decline. The network frequency is thus a good indicator for the need of load shedding, which is
particularly suitable in combination with island mode power generation. Preferably, the controller C interacts with the actuator of the compressor 120 so as to halt the drop in network frequency.
Particularly when operating on imported power, the signal may suitably be an external signal, generated by the power provider or one of the power providers
providing power to the network, to request load shedding.
Thus, the variable inlet guide vanes angle are preferably adjusted whereby the refrigerant compressor is unloaded by a portion of the original load that is equal to or greater than the power generation deficiency.
Herewith the balance between power generation and the power demand will be restored where after the power network can continue its stable operation.
The system may further comprise a process controller PC for controlling the production of the liquefied hydrocarbon stream 90. It may advantageously be arranged to maintain the variable inlet guide vanes at an
optimized target angle, to optimize one or both of efficiency and operating envelope of the refrigerant compressor 120 when the available power as monitored is at or above the predetermined value.
The load shedding controller C can be a separate dedicated controller unit or it can be integrated with another controller, for instance one that is arranged to control also other aspects of the system, or it can be a
- - hybrid controller whereby selected parts of the load shedding controller C are provided as a separate
controller and other parts are provided integrated with the other controller. In one example, the other
controller can be the process controller PC.
The system described above may be operated as
follows .
The refrigerant fluid 110 is circulated through the refrigerant circuit 100. In the course of this
circulating, at least part of the refrigerant fluid 100 is compressed in the refrigerant compressor 120 to form a compressed refrigerant. The refrigerant compressor 120 is driven by the electric motor 130, which typically imparts a rotational motion to the mechanical drive shaft 125 about its longitudinal axis. The electric motor 130 is powered using power from the power supply network 400.
The compressed refrigerant is passed to the heat exchanger train 300, where it is typically allowed to expand to a lower pressure and evaporate by receiving heat from at least an initially vaporous hydrocarbon stream 10. In many cases, but this is not a requirement for every type of heat exchanger train 300, the
compressed refrigerant is condensed and preferably sub- cooled before it is allowed to expand to said lower pressure. The evaporated refrigerant is led back from the heat exchanger train 300 to the refrigerant compressor 120, to be recompressed . This completes one cycle in the refrigerant circuit 100. Simultaneously during the cycle, heat is removed from the initially vaporous hydrocarbon stream 10 by at least part of the evaporating refrigerant, by heat exchanging at least said part of the initially vaporous hydrocarbon stream 10 against said at least part of the refrigerant fluid circulating through
- - the refrigerant circuit 100. Ultimately at least part of the initially vaporous hydrocarbon stream 10 is condensed as a result of removing heat from it by the refrigerant fluid 120 and optional second and further refrigerant fluids, to form the liquefied hydrocarbon stream 90.
Under normal stable operation, the variable inlet guide vanes are set manually by the operator or automated by the process controller PC and/or a compressor anti surge controller. The variable inlet guide vanes are set at a selected angle, for instance to achieve a desired operating window.
The available power on the power supply network 400 is monitored, and the variable inlet guide vanes can be maintained at the selected angle or moved to another selected angle as desired as long as the available power as monitored is at or above a predetermined value. In preferred embodiments of operation, the variable inlet guide vanes are maintained at an optimized target angle to optimize one or both of efficiency and operating envelope of the refrigerant compressor as long as the available power as monitored is at or above the
predetermined value.
However, when the available power as monitored drops below the predetermined value, the load shedding
controller reacts by adjusting the variable inlet guide vanes angle, thereby unloading the refrigerant compressor 120. This can be done by quickly changing the angle to a position different from the selected angle. If the selected angle was at the optimized target angle, which would be the case in preferred embodiments of operation, the unloading of the refrigerant compressor 120 is achieved by deliberately changing the variable inlet guide vanes angle away from the optimized target angle.
- -
Normally, the load demand by the refrigerant
compressor is reduced by closing the variable inlet guide vanes which in accordance with convention in the art corresponds to moving the position of the variable inlet guide vanes to increasingly negative angles, whereby 0° corresponds to the optimized target angle.
The heat exchanger train 300 in the present
specification has been depicted very schematically. It can represent any suitable hydrocarbon liquefaction process, in particular any natural gas liquefaction process producing liquefied natural gas, and the
invention is not limited by the specific choice of heat exchanger train. Examples of suitable heat exchanger trains are derivable from single refrigerant cycle processes (usually single mixed refrigerant - SMR - processes, such as PRICO described in the paper "LNG Production on floating platforms" by K R Johnsen and P Christiansen, presented at Gastech 1998 (Dubai), but also possible is a single component refrigerant such as for instance the BHP-cLNG process also described in the afore-mentioned paper by Johnsen and Christiansen) ;
double refrigerant cycle processes (for instance the much applied Propane-Mixed-Refrigerant process, often
abbreviated C3MR, such as described in for instance US Patent 4,404,008, or for instance double mixed
refrigerant - DMR - processes of which an example is described in US Patent 6,658,891, or for instance two- cycle processes wherein each refrigerant cycle contains a single component refrigerant); and processes based on three or more compressor trains for three or more
refrigeration cycles (an example is described in US Patent 7, 114,351) .
- -
Other examples of suitable heat exchanger trains are described in: US Patent 5,832,745 (Shell SMR) ; US Patent 6,295,833; US Patent 5,657,643 (both are variants of Black and Veatch SMR); US Pat. 6,370,910 (Shell DMR) . Another suitable example of DMR is the so-called Axens
LIQUEFIN process, such as described in for instance the paper entitled "LIQUEFIN: AN INNOVATIVE PROCESS TO REDUCE LNG COSTS" by P-Y Martin et al, presented at the 22nd World Gas Conference in Tokyo, Japan (2003) . Other suitable three-cycle heat exchanger trains include for example US Pat. 6,962,060; WO 2008/020044; US Pat.
7,127,914; DE3521060A1; US Pat. 5,669,234 (commercially known as optimized cascade process); US Pat. 6,253,574 (commercially known as mixed fluid cascade process); US Pat. 6,308,531; US application publication 2008/0141711;
Mark J. Roberts et al "Large capacity single train AP- X(TM) Hybrid LNG Process", Gastech 2002, Doha, Qatar (13- 16 October 2002) . These suggestions are provided to demonstrate wide applicability of the invention, and are not intended to be an exclusive and/or exhaustive list of possibilities. Not all examples listed above employ electric motors as refrigerant compressor drivers. It will be clear that any drivers other than electric motors can be replaced for an electric motor to be suitable for application in the context of the present invention .
The initially vaporous hydrocarbon stream 10 to be refrigerated, and ultimately preferably liquefied, may be derived from any suitable gas stream to be refrigerated and optionally liquefied. An often used example is a natural gas stream, obtained from natural gas or
petroleum reservoirs or coal beds. As an alternative the initially vaporous hydrocarbon stream 10 may also be
- - obtained from another source, including as an example a synthetic source such as a Fischer-Tropsch process.
When the initially vaporous hydrocarbon stream 10 is a natural gas stream, it is usually comprised
substantially of methane. Preferably the gaseous
hydrocarbon stream 10 comprises at least 50 mol% methane, more preferably at least 80 mol% methane.
Depending on the source, natural gas may contain varying amounts of hydrocarbons heavier than methane such as in particular ethane, propane and the butanes, and possibly lesser amounts of pentanes and aromatic
hydrocarbons. The composition varies depending upon the type and location of the gas.
Conventionally, the hydrocarbons heavier than methane are removed as far as needed to produce a liquefied hydrocarbon product stream in accordance with a desired specification. Hydrocarbons heavier than butanes (C4) are removed as far as efficiently possible from the natural gas prior to any significant cooling for several reasons, such as having different freezing or liquefaction
temperatures that may cause them to block parts of a methane liquefaction plant.
The natural gas may also contain non-hydrocarbons such as H20, N2, CO2, Hg, H2S and other sulphur compounds, and the like. Thus, if desired, the initially vaporous hydrocarbon stream 10 comprising the natural gas may be (pre- ) treated before or during being refrigerated. This (pre- ) treatment may comprise reduction and/or removal of undesired components such as CO2 and H2S or other steps such as early cooling, pre-pressurizing or the like. As these steps are well known to the person skilled in the art, their mechanisms are not further discussed here.
- -
In preferred embodiments disclosed herein, the initially vaporous hydrocarbon stream 10 comprises natural gas, whereby the liquefied hydrocarbon stream 90 is a liquefied natural gas stream.
The compressor, such as the refrigerant compressor, used herein may be exclusively driven by the electric motor, meaning the electric motor is the only driver driving the compressor.
The person skilled in the art will understand that the present invention can be advantageously applied in combination with other load shedding techniques and/or power plant designs, in particular including one or more of the elements as described in US pre-grant patent application publication No. 2010/0257895; US Patent
7,114,351; Gastech 2005 paper "All Electric Driven
Refrigeration Compressors in LNG Plants Offer Advantages" by Fritz Kleiner and Steve Kaufmann. For instance, in case the presently proposed system and method for
producing a liquefied hydrocarbon stream comprises two or more refrigerant compressors in parallel operation (each compressing a portion of the total amount of refrigerant flow) one or more of the compressors can be tripped while keeping the remainder in operation. This may be
particularly considered if an extreme adjusting of the inlet guide vanes is required and/or operation under significant reduced load is anticipated for a prolonged period of time.
The person skilled in the art will understand that the present invention can be carried out in many various ways without departing from the scope of the appended claims .
Claims
1. A method of producing a liquefied hydrocarbon stream, comprising :
- circulating a refrigerant fluid through a refrigerant circuit, comprising compressing at least part of the refrigerant fluid in a refrigerant compressor driven by an electric motor wherein the refrigerant compressor comprises variable inlet guide vanes of which an angle compared to a reference position can be adjusted;
- removing heat from an initially vaporous hydrocarbon stream thereby condensing at least part of the initially vaporous hydrocarbon stream to form the liquefied
hydrocarbon stream, said removing of heat comprising heat exchanging at least said part of the initially vaporous hydrocarbon stream against at least part of the
refrigerant fluid circulating through the refrigerant circuit ;
- powering the electric motor using a power supply network ;
- monitoring a signal representative of a condition of the power supply network;
- automatically determining from the signal whether additional load shedding is needed by comparing the signal to a predetermined criterion;
- automatically adjusting the variable inlet guide vanes angle thereby reducing the loading of the refrigerant compressor when the criterion is satisfied and additional load shedding is needed.
2. The method of claim 1, further comprising maintaining the variable inlet guide vanes at an optimized target angle to optimize one or both of efficiency and operating envelope of the refrigerant compressor when the criterion is not satisfied.
3. The method of claim 2, wherein said adjusting the variable inlet guide vanes angle comprises deliberately changing the variable inlet guide vanes angle away from the optimized target angle.
4. The method of any one of the preceding claims, wherein said condition of the power supply network represents power available on the power supply network relative to power being consumed, and wherein the
predetermined criterion is satisfied when the available power, according to the monitored signal, drops below a predetermined value.
5. The method of any one of the preceding claims, wherein the power supply network operates at a network frequency and wherein the signal representative of the condition of the power supply network represents the network frequency at which the power supply network operates .
6. The method of any one of the preceding claims, wherein the initially vaporous hydrocarbon stream
comprises natural gas and wherein the liquefied
hydrocarbon stream is a liquefied natural gas stream.
7. System for producing a liquefied hydrocarbon stream, comprising:
- a refrigerant circuit arranged to circulate a
refrigerant fluid, comprising a refrigerant compressor for compressing at least part of the refrigerant fluid and an electric motor engaged to the refrigerant
compressor to drive the refrigerant compressor wherein the refrigerant compressor comprises variable inlet guide vanes having an adjustable angle compared to a reference position; - a heat exchanger train comprising at least one heat exchanger, said heat exchanger train arranged to remove heat from an initially vaporous hydrocarbon stream thereby condensing at least part of the initially
vaporous hydrocarbon stream to form the liquefied
hydrocarbon stream, said least one heat exchanger
arranged to accommodate at least said part of the
initially vaporous hydrocarbon stream and at least part of the refrigerant fluid circulating through the
refrigerant circuit in a mutual heat exchanging
relationship;
- a power supply network connected to the electric motor for powering the electric motor;
- a load shedding controller arranged to monitor a signal representative of a condition of the power supply
network, to automatically determine from the signal whether additional load shedding is needed by comparing the signal to a predetermined criterion, and, when the criterion is satisfied and additional load shedding is needed, to adjust the variable inlet guide vanes angle to a position wherein the refrigerant compressor is unloaded relative to the loading in a previous condition whereby the variable inlet guide vanes angle was in a previous position when the criterion was not satisfied.
8. The system of claim 7, further comprising a process controller arranged to maintain the variable inlet guide vanes at an optimized target angle to optimize one or both of efficiency and operating envelope of the
refrigerant compressor when the criterion is not
satisfied.
9. The system of claim 7 or 8, wherein said condition of the power supply network represents power available on the power supply network relative to power being consumed, and wherein the predetermined criterion is satisfied when the available power, according to the monitored signal, drops below a predetermined value.
10. The system of any one of claims 7 to 9, wherein the power supply network operates at a network frequency and wherein the signal representative of the condition of the power supply network represents the network frequency at which the power supply network operates and wherein the predetermined criterion is satisfied when the network frequency drops below a pre-determined nominal network frequency .
11. Method of operating a compressor, comprising:
- compressing at least part of a fluid in a compressor driven by an electric motor, wherein the compressor comprises variable inlet guide vanes of which an angle can be adjusted;
- powering the electric motor using a power supply network ;
- monitoring a signal representative of a condition of the power supply network;
- automatically determining from the signal if additional load shedding is needed by comparing the signal to a predetermined criterion;
- automatically adjusting the variable inlet guide vanes angle thereby reducing the loading of the compressor when the criterion is satisfied and additional load shedding is needed.
12. The method of claim 10, further comprising
maintaining the variable inlet guide vanes at an
optimized target angle to optimize one or both of
efficiency and operating envelope of the compressor when the criterion is not satisfied.
13. The method of claim 12, wherein said adjusting of the variable inlet guide vanes angle comprises deliberately changing the variable inlet guide vanes angle away from the optimized target angle.
14. The method of any one of claims 11 to 13, wherein said condition of the power supply network represents power available on the power supply network relative to power being consumed, and wherein the predetermined criterion is satisfied when the available power,
according to the monitored signal, drops below a
predetermined value.
15. The method of any one of claims 11 to 14, wherein the power supply network operates at a network frequency and wherein the signal representative of the condition of the power supply network represents the network frequency at which the power supply network operates and wherein the predetermined criterion is satisfied when the network frequency drops below a pre-determined nominal network frequency .
16. The method of any one of claims 11 to 15, wherein the compressor is a refrigerant compressor, whereby the fluid is a refrigerant fluid.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201280061508.1A CN104350345A (en) | 2011-12-15 | 2012-12-13 | System and method for producing liquefied hydrocarbon stream and method of operating compressor |
| CA2859147A CA2859147C (en) | 2011-12-15 | 2012-12-13 | System and method for producing a liquefied hydrocarbon stream and method of operating a compressor |
| RU2014128901A RU2621591C2 (en) | 2011-12-15 | 2012-12-13 | System and method for producing liquefied hydrocarbons flow and method of compressor operation |
| AU2012324009A AU2012324009B2 (en) | 2011-12-15 | 2012-12-13 | System and method for producing a liquefied hydrocarbon stream and method of operating a compressor |
| KR1020147018666A KR20140112496A (en) | 2011-12-15 | 2012-12-13 | System and method for producing a liquefied hydrocarbon stream and method of operating a compressor |
| AP2014007627A AP2014007627A0 (en) | 2011-12-15 | 2012-12-13 | System and method for producing a liquefied hydrocarbon stream and method of operating a compressor |
| US14/365,171 US20140311183A1 (en) | 2011-12-15 | 2012-12-13 | System and method for producing a liquefied hydrocarbon stream and method of operating a compressor |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP11193688.6 | 2011-12-15 | ||
| EP11193688.6A EP2604960A1 (en) | 2011-12-15 | 2011-12-15 | Method of operating a compressor and system and method for producing a liquefied hydrocarbon stream |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2013087740A2 true WO2013087740A2 (en) | 2013-06-20 |
| WO2013087740A3 WO2013087740A3 (en) | 2015-09-11 |
Family
ID=47358181
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2012/075314 WO2013087740A2 (en) | 2011-12-15 | 2012-12-13 | System and method for producing a liquefied hydrocarbon stream and method of operating a compressor |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US20140311183A1 (en) |
| EP (1) | EP2604960A1 (en) |
| KR (1) | KR20140112496A (en) |
| CN (1) | CN104350345A (en) |
| AP (1) | AP2014007627A0 (en) |
| AU (1) | AU2012324009B2 (en) |
| CA (1) | CA2859147C (en) |
| RU (1) | RU2621591C2 (en) |
| WO (1) | WO2013087740A2 (en) |
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|---|---|---|---|---|
| ITFI20130076A1 (en) * | 2013-04-04 | 2014-10-05 | Nuovo Pignone Srl | "INTEGRALLY-GEARED COMPRESSORS FOR PRECOOLING IN LNG APPLICATIONS" |
| CN106015064B (en) * | 2016-06-06 | 2019-04-26 | 贵州赤天化股份有限公司 | The operating method of motor-driven compressor substitution steam driven compressor |
| IT201600109378A1 (en) * | 2016-10-28 | 2018-04-28 | Nuovo Pignone Tecnologie Srl | Natural gas liquefaction system including a turbocharger with integrated multiplier |
| IT201800000620A1 (en) * | 2018-01-08 | 2019-07-08 | Nuovo Pignone Tecnologie Srl | AMMONIA PRODUCTION PLANT |
| US10935312B2 (en) | 2018-08-02 | 2021-03-02 | Air Products And Chemicals, Inc. | Balancing power in split mixed refrigerant liquefaction system |
| FR3099818B1 (en) * | 2019-08-05 | 2022-11-04 | Air Liquide | Refrigeration device and installation and method for cooling and/or liquefaction |
| WO2021170525A1 (en) | 2020-02-25 | 2021-09-02 | Shell Internationale Research Maatschappij B.V. | Method and system for production optimization |
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Also Published As
| Publication number | Publication date |
|---|---|
| CA2859147A1 (en) | 2013-06-20 |
| WO2013087740A3 (en) | 2015-09-11 |
| AU2012324009B2 (en) | 2015-08-06 |
| CA2859147C (en) | 2020-04-28 |
| KR20140112496A (en) | 2014-09-23 |
| EP2604960A1 (en) | 2013-06-19 |
| CN104350345A (en) | 2015-02-11 |
| US20140311183A1 (en) | 2014-10-23 |
| AU2012324009A1 (en) | 2013-07-04 |
| AP2014007627A0 (en) | 2014-05-31 |
| RU2014128901A (en) | 2016-02-10 |
| RU2621591C2 (en) | 2017-06-06 |
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