Pump system
The pump system with interconnected pump modules and a centralized flow control mechanism simplifies the configuration and ensures stable operation by reducing complexity and fluid management issues.
Patent Information
- Authority / Receiving Office
- JP · JP
- Patent Type
- Applications
- Current Assignee / Owner
- KAWASAKI JUKOGYO KK
- Filing Date
- 2024-10-29
- Publication Date
- 2026-05-15
AI Technical Summary
Connecting multiple pumps in series results in a complex configuration.
A pump system with multiple pump modules connected in series, each comprising a suction pipe, discharge pipe, and a bypass pipe, with a minimum flow pipe and flow sensor in the downstream module, and a control device to maintain a minimum flow.
Simplifies the configuration of the pump system and ensures stable operation by minimizing fluid backflow and overheating, allowing for efficient startup and shutdown sequences.
Smart Images

Figure 2026078750000001_ABST
Abstract
Description
Technical Field
[0001] The present disclosure relates to a pump system including a plurality of pumps.
Background Art
[0002] Conventionally, a pump configured to rotate an impeller housed in a sealed pump casing to apply centrifugal force to a liquid sucked into the pump casing and discharge it is known. Patent Document 1 discloses this type of pump.
[0003] The pot-type centrifugal pump disclosed in Patent Document 1 includes an impeller and an electric motor for driving the impeller housed in a pot. The pump sucks LNG from a suction port provided on the side of the pot and discharges it from a discharge port provided on the upper part of the pot. A suction line for sending the LNG stored in the LNG tank to the pump is connected to the suction port. A high-pressure gas supply line, that is, a discharge line for sending the LNG to a high-pressure gas demand destination is connected to the discharge port. A flow meter, a vaporizer, and an on-off valve are provided in the high-pressure gas supply line. Also, a minimum flow line is connected to the high-pressure gas supply line downstream of the flow meter and upstream of the vaporizer. Even when LNG is not supplied to the high-pressure gas demand destination, the pump continues to be driven, and a minimum amount of LNG is returned to the LNG tank through the minimum flow line. A vent line for discharging the vaporized gas inside the pot is connected to a vent port provided on the upper part of the pot.
Prior Art Documents
Patent Documents
[0004]
Patent Document 1
Summary of the Invention
Problems to be Solved by the Invention
[0005] When gradually increasing the pressure of a fluid, it might be possible to connect multiple pumps in series. However, connecting multiple pumps results in a complex configuration.
[0006] This disclosure is made in view of the above circumstances, and its purpose is to simplify the configuration of a pump system comprising multiple pumps connected in series. [Means for solving the problem]
[0007] To solve the above problems, a pump system according to one aspect of this disclosure is: Equipped with multiple pump modules connected in series, Each of the plurality of pump modules includes a pump, a suction pipe connected to the suction port of the pump, a discharge pipe connected to the discharge port of the pump, and a bypass pipe having a bypass valve, through which fluid flows from the suction pipe to the discharge pipe, bypassing the pump. The pump module located furthest downstream among the plurality of pump modules further has a minimum flow pipe connected to the portion of the discharge pipe downstream of the connection point of the bypass pipe. [Effects of the Invention]
[0008] According to this disclosure, the configuration of a pump system comprising multiple pumps connected in series can be simplified. [Brief explanation of the drawing]
[0009] [Figure 1] Figure 1 is a block diagram showing a schematic configuration of a pump system according to one embodiment of the present disclosure. [Figure 2] Figure 2 shows a schematic configuration of the pump system according to a modified example. [Modes for carrying out the invention]
[0010] Next, embodiments of the present disclosure will be described with reference to the drawings. Figure 1 is a block diagram showing a schematic configuration of a pump system 1 according to one embodiment of the present disclosure. The pump system 1 according to this embodiment is installed, for example, in a line that supplies low-temperature liquefied gas from a liquefied gas source 11 to a high-pressure gas demanding device 12, and pressurizes the liquefied gas and sends it to the high-pressure gas receiving side. Examples of liquefied gas sources include liquefied gas storage tanks. Examples of high-pressure gas demanding devices 12 include turbines and internal combustion engines. The pump system 1 may be installed in a line that supplies liquefied gas to a tank or demand site instead of the high-pressure gas demanding device 12.
[0011] As shown in Figure 1, a pump system 1 according to one embodiment of the present disclosure comprises a plurality of pump modules 2 connected in series. The pump system 1 shown in Figure 1 comprises three stages of pump modules 2, but the number of pump modules 2 is not limited to this embodiment and may be two or more.
[0012] 《Configuration of Pump Module 2》 The configurations of multiple pump modules 2 are substantially the same, and the configuration of one of these pump modules 2 will be described in detail below. Pump module 2 comprises a suction pipe 3 connected to the suction port 22 of pump 21, a discharge pipe 4 connected to the discharge port 23 of pump 21, and a bypass pipe 5 that bypasses pump 21 and connects the suction pipe 3 and the discharge pipe 4. Note that while pump module 2 represents a functionally grouped part, it does not need to be assembled as a single unit.
[0013] Pump 21 is a centrifugal pump. The structure of pump 21 is not particularly limited. For example, pump 21 comprises a container 26 and a pump body 27 housed in the container 26. The pump body 27 comprises, for example, a casing, an impeller housed in the casing, and a motor that rotates the impeller and shaft. The container 26 of pump 21 surrounds the pump body 27 and has the function of maintaining the liquid level. The container 26 is provided with a suction port 22, a discharge port 23, and a vent port 24. Pump 21 pressurizes the fluid drawn in from the suction port 22 and discharges it from the discharge port 23.
[0014] The suction pipe 3 is connected to the suction port 22 of the container 26, and the fluid drawn in by the pump 21 flows through it. The suction pipe 3 is connected to the liquefied gas source 11, or to the discharge pipe 4 of the pump 21 located upstream. The suction pipe 3 is provided with a suction valve 31. The suction valve 31 opens and closes the flow path of the suction pipe 3, or adjusts the flow rate of the fluid flowing through the suction pipe 3.
[0015] The discharge pipe 4 is connected to the discharge port 23 of the container 26, and the fluid discharged from the pump 21 flows through it. The suction pipe 3 is connected to the suction pipe 3 of the high-pressure gas demand equipment 12, or to the pump 21 located downstream. A check valve 41 is provided in the discharge pipe 4. The check valve 41 prevents the backflow of fluid from the discharge pipe 4 to the pump 21. However, when the pump 21 is stopped, the check valve 41 allows a small flow rate of liquid backflow from the discharge pipe 4 to the pump 21. For example, the valve body of the check valve 41 has a hole, through which the backflow of fluid is permitted.
[0016] The bypass pipe 5 connects the suction pipe 3 and the discharge pipe 4 fluidly, bypassing the pump 21. The fluid flowing through the bypass pipe 5 flows from the suction pipe 3 to the discharge pipe 4 without passing through the pump 21. The bypass pipe 5 is equipped with a bypass valve 51. The bypass valve 51 opens and closes the flow path of the bypass pipe 5, or adjusts the flow rate of the fluid flowing through the bypass pipe 5.
[0017] A vent pipe 6 is connected to the vent port 24 of the pump 21. Gas, mainly containing vaporized liquefied gas, accumulates at the top of the container 26. The gas inside the container 26 is discharged to the outside through the vent pipe 6. A vent valve 61 is provided on the vent pipe 6. The container 26 is equipped with a liquid level sensor 25 that detects the liquid level of the liquefied gas inside the container 26. In the container 26, the liquid level is controlled within a predetermined range by the gas inside the casing. Specifically, when the liquid level detected by the liquid level sensor 25 falls below a predetermined range, the vent valve 61 is opened until the liquid level recovers to the predetermined range, the gas inside the container 26 is discharged, and liquid flows into the container 26. Through this level control, the liquid level in the container 26 is maintained within a predetermined range.
[0018] In the pump system 1 according to this embodiment, a first pump module 2A, a second pump module 2B, and a third pump module 2C are connected in series. Specifically, the suction pipe 3 of the first pump module 2A is connected to a liquefied gas source 11, the discharge pipe 4 of the first pump module 2A is connected to the suction pipe 3 of the second pump module 2B, the discharge pipe 4 of pump module 2 is connected to the suction pipe 3 of the third pump module 2C, and the discharge pipe 4 of the third pump module 2C is connected to a high-pressure gas demanding device 12.
[0019] Furthermore, the pump system 1 has the upstream end of the minimum flow pipe 15 connected to the downstream portion of the pump module 2 located furthest downstream, i.e., the third pump module 2C in this embodiment. The minimum flow pipe 15 may be connected to the portion of the discharge pipe 4 of the third pump module 2C downstream from the connection to the bypass pipe 5, or it may be connected to the piping connecting the discharge pipe 4 of the third pump module 2C to the high-pressure gas demand equipment 12. The downstream end of the minimum flow pipe 15 may be connected to the liquefied gas source 11, or it may be connected to the liquefied gas demand destination.
[0020] The minimum flow pipe 15 is provided with a minimum flow valve 16 that is controlled by the control device 7. The minimum flow valve 16 is a flow rate adjustment valve. Further, the pump system 1 is provided with a flow sensor 17 that detects the total flow rate of the fluid flowing through the pump system 1. In the pump system 1 according to the present embodiment, in the discharge pipe 4 of the third pump module 2C, the flow sensor 17 is disposed downstream of the connection portion with the bypass pipe 5 and upstream of the connection portion of the minimum flow pipe 15. The control device 7 adjusts the opening degree of the minimum flow valve 16 so that the flow rate of the liquefied gas in the minimum flow pipe 15 can ensure the minimum flow. When the pump system 1 is in operation, the control device 7 adjusts the opening degree of the minimum flow valve 16 so that when the flow rate of the liquefied gas detected by the flow sensor 17 becomes less than a predetermined minimum flow, the liquefied gas detected by the flow sensor 17 in the minimum flow pipe 15 flows with a liquefied gas sufficient to ensure the minimum flow. The minimum flow is the minimum flow rate at which the pump 21 can operate stably and continuously without causing overheating, noise, vibration, etc. When the performances of the plurality of pumps 21 included in the pump system 1 are different, the largest value among the minimum flows of the plurality of pumps 21 is adopted as the minimum flow.
[0021] The minimum flow pipe 15 may be provided with a bypass pipe 18. Both ends of the bypass pipe 18 are connected to the minimum flow pipe 15, and the liquefied gas flowing into the minimum flow pipe 15 bypasses the minimum flow valve 16 through the bypass pipe 18 and flows downstream of the minimum flow valve 16. The minimum flow pipe 15 is provided with an orifice 19 that restricts the flow rate of the liquefied gas passing through the bypass pipe 18. During the operation of the pump system 1, liquefied gas at the minimum flow always flows through the bypass pipe 18. Further, instead of the bypass pipe 18, the minimum opening degree of the minimum flow valve 16 may be restricted so that it does not fully close, and fluid may be allowed to flow through the minimum flow pipe 15.
[0022] 《Operation Method of Pump System 1》 Here, the operation method of the pump system 1 with the above configuration will be described. In the operating pump system 1, all the pumps 21 continue to operate regardless of the high or low pressure of the liquefied gas supplied from the liquefied gas source 11 to the high-pressure gas-consuming equipment 12. The pressure of the liquefied gas supplied to the high-pressure gas-consuming equipment 12 may be adjusted by the number of pump modules 2 in use and the number of pump modules 2 that are stopped from use.
[0023] In the pump system 1 during shutdown, all the pump modules 2A, 2B, and 2C are in a standby state where the bypass valve 51 is open, the suction valve 31 is closed, and the pump 21 is stopped.
[0024] In the pump system 1 during shutdown, when the temperature of the pump 21 and its surroundings rises, the discharge of the pump 21 is obstructed by the gas pressure of the vaporized gas generated in the pipes around the pump 21, and there is a risk that the pump 21 will stop without being able to ensure a minimum flow at pump startup. Also, in order to quickly start the pump 21, it is useful to cool the pump 21 and the pipes around it in the pump system 1 during shutdown. Therefore, in the pump system 1 during shutdown, by level control of the pump 21, a small amount of liquefied gas flows from the discharge pipe 4 into the pump 21, and a small amount of liquefied gas flows through the pump 21 and the discharge pipe 4, and the pump 21 and the discharge pipe 4 are cooled by the liquefied gas. Also, in the pump system 1 during shutdown, a small amount of liquefied gas flows through the minimum flow pipe 15 via the relief pipe 18, and the minimum flow pipe 15 is cooled.
[0025] When starting the pump system 1 from a stopped state, the starting operations are performed sequentially from the upstream pump modules 2A, 2B, and 2C. The starting operation of the pump system 1 includes a series of operations performed in the following order: closing the bypass valve 51, opening the suction valve 31, and starting the pump 21. Specifically, the starting operation is performed first in the first pump module 2A, during which time the fluid in the standby second pump module 2B and the third pump module 2C flows through the bypass pipe 5, avoiding the pump 21. This prevents the fluid from flowing into the pump 21 and causing the pump 21 to start up in the standby second pump module 2B and the third pump module 2C. Consequently, the occurrence of malfunctions in the pump 21 is suppressed. After the starting operation of the first pump module 2A is completed, the starting operation of the second pump module 2B is performed while the third pump module 2C remains in standby mode. After the starting operation of the second pump module 2B is completed, the starting operation of the third pump module 2C is performed last.
[0026] In the above configuration, the pump modules 2A, 2B, and 2C are started in order from the upstream modules. However, the pump modules 2A, 2B, and 2C may be started in order from the downstream modules. Alternatively, all pump modules 2A, 2B, and 2C may be started simultaneously. However, even if operation commands are issued to all pump modules 2A, 2B, and 2C simultaneously, it is difficult for all of them to operate synchronously due to individual differences, etc. Therefore, it is preferable to start the pump modules 2A, 2B, and 2C in order from either the upstream or downstream modules.
[0027] When pump system 1 is started, in each pump module 2A, 2B, and 2C, the liquefied gas flowing into the suction pipe 3 flows into the pump 21 from the suction port 22, is pressurized, and then discharged from the discharge port 23 into the discharge pipe 4, and flows through the discharge pipe 4 to the downstream pump module 2 or piping. If there is a pump module 2 that is not in use, the pump module 2 that is not in use is put into a standby state and fluid flows through the bypass pipe 5.
[0028] When stopping the pump system 1 while it is in operation, the stopping operations are performed sequentially from the downstream pump modules 2A, 2B, and 2C. The stopping operation of the pump system 1 includes a series of operations performed in the following order: stopping the pump 21, closing the suction valve 31, and opening the bypass valve 51. Specifically, first, the stopping operation is performed on the third pump module 2C while the first pump module 2A and the second pump module 2B are still in operation. After the stopping operation of the third pump module 2C is completed, the stopping operation is then performed on the second pump module 2B while the first pump module 2A is still in operation. After the stopping operation of the second pump module 2B is completed, finally, the stopping operation of the first pump module 2A is performed. By performing the stopping operations sequentially from the downstream pump modules 2A, 2B, and 2C in this manner, the fluid flows to the bypass pipe 5, avoiding the stopped pump 21, thereby preventing fluid from flowing into the stopped pump 21 and causing malfunctions in the pump 21.
[0029] In the above configuration, the pump modules 2A, 2B, and 2C are stopped in order from the downstream. However, the pump modules 2A, 2B, and 2C may be stopped in order from the upstream. Alternatively, all pump modules 2A, 2B, and 2C may be stopped simultaneously. However, even if operation commands are issued to all pump modules 2A, 2B, and 2C simultaneously, it is difficult for all of them to operate synchronously due to individual differences, etc. Therefore, it is preferable to stop the pump modules 2A, 2B, and 2C in order from the upstream or downstream.
[0030] [Variation] Next, a modified example of the above embodiment will be described. Figure 2 is a block diagram showing the schematic configuration of the pump system 1 according to the modified example. In this description of the modified example, the same or similar components as in the above embodiment are denoted by the same reference numerals in the drawings, and their descriptions are omitted.
[0031] As shown in Figure 2, the modified pump system 1 comprises multiple pump modules 2 connected in series to form a single pump row 201, 202, and multiple pump rows 201, 202 connected in parallel. The configuration of the pump rows 201, 202 is substantially the same as that of the previously described embodiment, and a detailed explanation is omitted.
[0032] In the modified pump system 1, the suction pipes 3 of the uppermost pump modules 2 of pump trains 201 and 202 are connected to each other, and the discharge pipes 4 of the lowermost pump modules 2 of pump trains 201 and 202 are connected to each other.
[0033] Thus, by providing multiple pump rows 201, 202, the pump system 1 can increase or decrease the flow rate of liquefied gas delivered by the pump system 1.
[0034] [Summary] The pump system 1 relating to item 1 of this disclosure is It is equipped with multiple pump modules 2 connected in series, Each of the multiple pump modules 2 includes a pump 21, a suction pipe 3 connected to the suction port 22 of the pump 21, a discharge pipe 4 connected to the discharge port 23 of the pump 21, and a bypass pipe 5 that bypasses the pump 21 and connects the suction pipe 3 and the discharge pipe 4. The pump module 2 located furthest downstream of the multiple pump modules 2 further includes a minimum flow pipe 15 connected to the portion of the discharge pipe 4 downstream of the connection point of the bypass pipe 5.
[0035] Conventionally, each pump module is equipped with numerous pipes, such as suction pipes, discharge pipes, and minimum flow pipes, resulting in a very complex piping configuration when multiple pump modules are connected in series. In contrast, in the pump system 1 according to this disclosure, the minimum flow pipe 15 is provided only in the downstream pump module 2 of the multiple pump modules 2 connected in series. Therefore, the configuration can be simplified compared to a pump system 1 equipped with multiple pumps 21 connected in series, where each pump module 2 is equipped with a minimum flow pipe 15. Since pump systems that pressurize fluids with low liquid density, such as liquefied hydrogen, require multi-stage pumps, the pump system 1 according to this disclosure is particularly useful as a pump system 1 for pressurizing fluids with low liquid density.
[0036] The pump system 1 relating to the second item of this disclosure is a pump system 1 relating to the first item in which the pump module 2 located furthest downstream of the plurality of pump modules 2 includes a flow sensor 17 located downstream of the connection of the bypass pipe 5 of the discharge pipe 4 and upstream of the connection of the minimum flow pipe 15.
[0037] In the pump system 1 with the above configuration, the flow sensor 17 is provided only in the pump module 2 located furthest downstream among the multiple pump modules 2 connected in series. Therefore, the configuration can be simplified compared to a pump system 1 with multiple pumps 21 connected in series, where the flow sensor 17 is provided in each pump module 2.
[0038] The pump system 1 relating to the third item of this disclosure is the pump system 1 relating to the second item, wherein the minimum flow pipe 15 has a minimum flow valve 16 that opens when the fluid flow rate detected by the flow sensor 17 falls below a predetermined minimum flow rate.
[0039] In the pump system 1 with the above configuration, the minimum flow pipe 15 and minimum flow valve 16 are provided only in the downstream pump module 2 among the multiple pump modules 2 connected in series. Therefore, compared to the case where each pump module 2 is provided with a minimum flow pipe 15 in multiple directly connected pump modules 2, the number of minimum flow valves 16 can be reduced, and the configuration can be simplified.
[0040] The pump system 1 according to the fourth item of this disclosure is the pump system 1 according to the third item, and includes a control device 7 that operates a minimum flow valve 16 so that the flow in the minimum flow pipe 15 maintains a predetermined minimum flow based on the flow rate detected by the flow sensor 17.
[0041] In the pump system 1 with the above configuration, the minimum flow pipe 15 and minimum flow valve 16 are provided only in the downstream pump module 2 among the multiple pump modules 2 connected in series. This simplifies the configuration compared to the case where each pump module 2 is equipped with a control device 7.
[0042] The pump system 1 relating to item 5 of this disclosure is the pump system 1 relating to item 3 or 4, wherein the minimum flow pipe 15 has a relief pipe 18 through which the fluid flows, avoiding the minimum flow valve 16.
[0043] As a result, in the pump system 1 with the above configuration, the minimum flow pipe 15 and relief pipe 18 are provided only in the downstream pump module 2 among the multiple pump modules 2 connected in series, thus simplifying the configuration compared to the case where each pump module 2 is equipped with a relief pipe 18.
[0044] The pump system 1 relating to item 6 of this disclosure is a pump system 1 relating to any of items 1 to 5, wherein a plurality of pump modules 2 connected in series are made into a single pump row 201, 202, and a plurality of pump rows 201, 201 connected in parallel are provided.
[0045] In the pump system 1 with the above configuration, the flow rate of liquefied gas can be increased by increasing the number of pump rows 201 and 202.
[0046] The functions realized by the control device 7 described herein may be implemented in a circuit or processing circuitry, including a general-purpose processor, an application-specific processor, an integrated circuit, an ASIC (Application Specific Integrated Circuit), a CPU (Central Processing Unit), conventional circuits, and / or a combination thereof, programmed to realize the described functions. A processor, including transistors and other circuits, is considered a circuit or processing circuitry. A processor may be a programmed processor that executes a program stored in memory. In this specification, a circuit, unit, or means is hardware programmed to realize or execute the described functions. Such hardware may be any hardware disclosed herein, or any hardware known to be programmed to realize or execute the described functions. If such hardware is a processor that is considered a type of circuit, then the circuit, means, or unit is a combination of hardware and software used to constitute such hardware and / or processor.
[0047] The embodiments described above are presented for illustrative and explanatory purposes only and are not intended to limit the disclosure to the forms disclosed herein. For example, in the detailed description above, various features of the disclosure are grouped into one embodiment for the purpose of streamlining the disclosure, but some of the features may be combined. Also, some of the features included in the disclosure may be combined into alternative embodiments, configurations, or aspects other than those discussed above. [Explanation of Symbols]
[0048] 1: Pump System 2: Pump module 3: Suction pipe 4:Discharge pipe 5: Bypass pipe 7: Control device 15: Minimum flow tube 16: Minimum flow valve 17: Flow sensor 18: Relief pipe 21: Pump 22: Inlet 23:Discharge port 51: Bypass valve 201,202: Pump row
Claims
1. Equipped with multiple pump modules connected in series, Each of the plurality of pump modules includes a pump, a suction pipe connected to the suction port of the pump, a discharge pipe connected to the discharge port of the pump, and a bypass pipe that bypasses the pump and connects the suction pipe and the discharge pipe. The pump module located furthest downstream of the aforementioned plurality of pump modules further includes a minimum flow pipe connected to the portion of the discharge pipe downstream of the connection point of the bypass pipe. Pump system.
2. The pump module located furthest downstream of the aforementioned plurality of pump modules includes a flow sensor located downstream of the connection point of the bypass pipe in the discharge pipe and upstream of the connection point of the minimum flow pipe. The pump system according to claim 1.
3. The minimum flow pipe has a minimum flow valve that opens when the fluid flow rate detected by the flow sensor falls below a predetermined minimum flow rate. The pump system according to claim 2.
4. The system includes a control device that operates the minimum flow valve so that the flow in the minimum flow pipe maintains a predetermined minimum flow based on the flow rate detected by the flow sensor. The pump system according to claim 3.
5. The minimum flow pipe has a relief pipe through which fluid flows, avoiding the minimum flow valve. The pump system according to claim 3 or 4.
6. Multiple pump modules connected in series form a single pump row, and multiple such pump rows are connected in parallel. The pump system according to claim 1.