Compressor feed system

Abstract

To provide a liquid supply system for a compressor that can readily convert liquid that is jetted from a compressor into a fine droplet.SOLUTION: A liquid supply system 100 adjusts temperature of liquid 50 to be jetted to a compressor 1 to saturation temperature Tf or higher accommodating to internal pressure of the compressor 1 and then jets liquid 50 to the compressor 1.SELECTED DRAWING: Figure 3

Description

[Technical Field]

[0001] The present invention relates to a liquid feed system for a compressor. [Background technology]

[0002] A screw compressor is a compressor that compresses gases such as steam or air. A screw compressor is a device that generates compressed gas by meshing a pair of screw rotors, a male rotor and a female rotor, each formed in a screw shape. To improve the gas compression efficiency, the screw compressor is provided with a liquid supply system that injects liquid into a compression chamber in a casing that houses the male rotor and the female rotor.

[0003] The injected liquid plays a role in cooling the compressed gas through heat exchange. Furthermore, the injected liquid plays a role in sealing the gap between the male rotor and the female rotor, and the gap between the male rotor or the female rotor and the casing, thereby reducing gas leakage from these gaps. When the injected liquid evaporates in the compression chamber, as in the case of water, the liquid can cool the compressed gas not only through heat exchange but also through the latent heat of evaporation. In this case, for efficient heat exchange and evaporation, the liquid needs to be injected so that it breaks into fine droplets in the compression chamber.

[0004] Prior art liquid supply systems are disclosed in, for example, Patent Document 1 and Patent Document 2. Patent Document 1 discloses a liquid supply mechanism that generates a swirling flow of liquid inside the liquid supply mechanism and injects the liquid into a compressor. The liquid supply mechanism disclosed in Patent Document 1 breaks the liquid into fine droplets by the action of centrifugal force generated by the swirling flow.

[0005] Patent Document 2 discloses a liquid supply mechanism in which two jet nozzles are arranged facing each other and liquid jetted from the two jet nozzles is caused to collide. The liquid supply mechanism disclosed in Patent Document 2 attempts to break the liquid into fine droplets by forming a liquid film from the colliding liquid, the tip of which breaks off and forms fine droplets. [Prior art documents] [Patent documents]

[0006] [Patent Document 1] U.S. Patent Publication No. 2019 / 093659 [Patent Document 2] International Publication No. 2019 / 239703 Summary of the Invention [Problem to be solved by the invention]

[0007] However, the liquid supply mechanisms disclosed in Patent Documents 1 and 2 both have complex structures, and it is difficult to easily turn the liquid into fine droplets in the narrow space inside the compressor, that is, the compression chamber.

[0008] The present invention has been made in view of the above, and aims to provide a liquid supply system for a compressor that can easily turn the liquid to be injected into the compressor into fine droplets. [Means for solving the problem]

[0009] In order to solve the above problem, the compressor liquid supply system of the present invention is a compressor liquid supply system that injects liquid into the inside of a compressor that compresses gas, and is characterized in that the temperature of the liquid injected into the compressor is adjusted to a temperature higher than a saturation temperature corresponding to the internal pressure of the compressor, and the liquid is injected into the compressor. [Effects of the Invention]

[0010] According to the present invention, it is possible to provide a liquid supply system for a compressor that can easily turn the liquid to be injected into the compressor into fine droplets. Problems, configurations, and effects other than those described above will become apparent from the following description of the embodiments. [Brief explanation of the drawings]

[0011] [Figure 1]FIG. 2 is a diagram showing the configuration of a compressor. [Figure 2] 2 is a cross-sectional view of the compressor taken along line AA in FIG. 1. [Figure 3] FIG. 1 is a diagram showing the configuration of a liquid supply system according to a first embodiment. [Figure 4] 10A and 10B are diagrams illustrating the injection form of the liquid when the saturated vapor pressure corresponding to the temperature of the liquid injected into the compressor is lower than the pressure in the compression chamber. [Figure 5] 10A and 10B are diagrams illustrating the injection form of the liquid when the saturated vapor pressure corresponding to the temperature of the liquid injected into the compressor is higher than the pressure in the compression chamber. [Figure 6] FIG. 2 is a diagram showing the saturated vapor pressure curve of the liquid injected into the compressor. [Figure 7] 4 is a flowchart relating to temperature control of the liquid injected into the compressor. [Figure 8] FIG. 10 is a diagram showing the configuration of a liquid supply system according to a second embodiment. [Figure 9] FIG. 10 is a diagram showing the configuration of a liquid supply system according to a third embodiment. DETAILED DESCRIPTION OF THE INVENTION

[0012] Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that components with the same reference numerals in each embodiment have the same functions in each embodiment unless otherwise specified, and description thereof will be omitted.

[0013] [Embodiment 1] A liquid supply system 100 according to a first embodiment will be described with reference to FIGS.

[0014] The liquid supply system 100 is a system that supplies the liquid 50 to the inside of the compressor 1 by injecting the liquid 50, such as water, into the interior (e.g., compression chamber 13) of the compressor 1 that compresses a gas such as air or water vapor. In this embodiment, the compressor 1 will be described using a screw compressor as shown in FIG. 1 as an example, but the compressor 1 may be another type of compressor. In this embodiment, the gas compressed by the compressor 1 will be described using water vapor as an example, but the gas compressed by the compressor 1 may be a gas other than water vapor. In this embodiment, the liquid 50 injected into the compressor 1 will be described using water as an example, but the liquid 50 injected into the compressor 1 may be a liquid other than water. That is, in this embodiment, the liquid 50 injected into the compressor 1 is a substance of the same type (components) as the gas compressed by the compressor 1.

[0015] Fig. 1 is a diagram showing the configuration of a compressor 1. Fig. 2 is a cross-sectional view of the compressor 1 taken along line AA shown in Fig. 1.

[0016] The compressor 1 includes a screw rotor 2 and a casing 5 that houses the screw rotor 2. The screw rotor 2 has a male rotor 3 and a female rotor 4, each with twisted teeth (lobes) that rotate in mesh with each other. In this embodiment, the screw rotor 2 is a collective term for the male rotor 3 and the female rotor 4. The suction side end of the male rotor 3 is connected via a rotor shaft to a motor 20, which is a rotational drive source. The male rotor 3, driven to rotate by the motor 20, drives the female rotor 4 to rotate.

[0017] The compressor 1 includes a suction side bearing 6 and a discharge side bearing 7 for rotatably supporting the male rotor 3 and the female rotor 4, respectively, and a shaft sealing component 8 such as an oil seal or a mechanical seal. In this embodiment, the "suction side" refers to the gas suction side in the axial direction of the screw rotor 2, and the "discharge side" refers to the gas discharge side in the axial direction of the screw rotor 2.

[0018] The inner surface of the casing 5 is formed with a cylindrical male side bore 9 that covers the male rotor 3, and a cylindrical female side bore 10 that covers the female rotor 4. A gap of several tens to several hundreds of micrometers is formed between the male side bore 9 and the male rotor 3, and between the female side bore 10 and the female rotor 4. There are two intersection lines between the male side bore 9 and the female side bore 10: one on the low-pressure side and one on the high-pressure side. The intersection line on the low-pressure side is defined as a suction side cusp 11. The intersection line on the high-pressure side is defined as a compression side cusp 12.

[0019] The space defined by each tooth groove of the male rotor 3 and the female rotor 4 and the male side bore 9 and female side bore 10 surrounding them is the compression chamber 13. The compression chamber 13 repeatedly expands and contracts due to the rotation of the male rotor 3 and the female rotor 4. As a result, the gas to be compressed is sucked into the compression chamber 13 through the suction port 14 communicating with the compression chamber 13, compressed to a predetermined pressure in the compression chamber 13, and then discharged to the outside of the compressor 1 through the discharge port 15 communicating with the compression chamber 13.

[0020] The compressor 1 also has a liquid supply hole 16 for supplying liquid 50 to the compression chamber 13, a liquid supply hole 17 for supplying liquid 50 to the suction side bearing 6 and the shaft seal component 8, and a liquid supply hole 18 for supplying liquid 50 to the discharge side bearing 7.

[0021] Fig. 3 is a diagram showing the configuration of the liquid supply system 100 of embodiment 1. In Fig. 3, the flow path for supplying the liquid 50 from the liquid supply hole 17 or the liquid supply hole 18 to the suction side bearing 6, the discharge side bearing 7, or the shaft seal component 8 is not shown.

[0022] The liquid supply system 100 injects liquid 50 (water) into the compression chamber 13 of the compressor 1, which compresses gas (water vapor). The liquid 50 injected into the compression chamber 13 cools the compressed gas present in the compression chamber 13 through heat exchange with the compressed gas. Furthermore, the liquid 50 injected into the compression chamber 13 evaporates in the compression chamber 13, cooling the compressed gas by the latent heat of evaporation. The liquid 50 injected into the compression chamber 13 also seals the gap between the male rotor 3 and female rotor 4, and the gap between the male rotor 3 or female rotor 4 and the casing 5, thereby reducing gas leakage from these gaps.

[0023] The liquid supply system 100 includes a steam generator 101, a gas side flow path 102, a liquid side flow path 103, a pump 104, a discharge side flow path 105, a gas-liquid separator 106, a transport flow path 107, a relief flow path 108, a first flow path 109, a second flow path 110, a mixer 111, a third flow path 112, a temperature measuring device 113, and a flow rate adjustment valve 114. The liquid supply system 100 may also include a control device (not shown) that controls the overall operation of these components.

[0024] The steam generator 101 is a device that generates gas (water vapor) to be compressed. The gas-side flow path 102 is a pipe that connects the gas chamber of the steam generator 101 with the suction port 14 of the compressor 1. The gas-side flow path 102 supplies the gas generated by the steam generator 101 to the compressor 1. The gas supplied to the compressor 1 is compressed in the compression chamber 13 by the rotation of the screw rotor 2, and is discharged from the discharge port 15 of the compressor 1 as compressed gas.

[0025] The liquid-side flow path 103 is a pipe that connects the liquid chamber of the steam generator 101 with the suction port of the pump 104. The liquid-side flow path 103 supplies the liquid 50 stored in the liquid chamber of the steam generator 101 as a gas generation source in the steam generator 101 to the pump 104. The pump 104 pressurizes the liquid 50 supplied from the liquid chamber of the steam generator 101. In other words, the pump 104 pressurizes the liquid 50 before it is injected into the compressor 1.

[0026] The discharge-side flow path 105 is a pipe that connects the discharge port 15 of the compressor 1 and the gas-liquid separator 106. The discharge-side flow path 105 supplies the compressed gas discharged from the compressor 1 to the gas-liquid separator 106. Note that a portion of the liquid 50 injected into the compression chamber 13 does not completely evaporate and remains as liquid, and is discharged from the compression chamber 13 to the discharge-side flow path 105 via the discharge port 15. The discharge-side flow path 105 supplies the liquid 50 discharged from the compressor 1 to the gas-liquid separator 106.

[0027] The gas-liquid separator 106 is a device that separates the compressed gas and liquid 50 supplied from the discharge-side flow path 105. The transport flow path 107 is a pipe that connects the gas chamber of the gas-liquid separator 106 with a transport target of the compressed gas. The transport flow path 107 transports the compressed gas separated by the gas-liquid separator 106 to the transport target. The relief flow path 108 is a pipe that connects the liquid chamber of the gas-liquid separator 106 with the liquid chamber of the steam generator 101. The relief flow path 108 releases the liquid 50 that has accumulated in the liquid chamber of the gas-liquid separator 106 by more than a predetermined amount to the liquid chamber of the steam generator 101.

[0028] The first flow path 109 is a pipe that connects the discharge port of the pump 104 and the mixer 111. The first flow path 109 supplies the liquid 50 pressurized by the pump 104 to the mixer 111. In other words, the first flow path 109 is a flow path through which the liquid 50 pressurized by the pump 104 flows before being injected into the compressor 1.

[0029] The second flow path 110 is a pipe that connects the liquid chamber of the gas-liquid separator 106 with the mixer 111. The second flow path 110 supplies the liquid 50 separated by the gas-liquid separator 106 to the mixer 111. That is, the second flow path 110 is a flow path through which the liquid 50 flows after being injected into the compressor 1 and then discharged from the compressor 1. The liquid 50 that flows after being injected into the compressor 1 and then discharged from the compressor 1 is the liquid 50 that has exchanged heat with the compressed gas. Therefore, the liquid 50 flowing through the second flow path 110 has a higher temperature than the liquid 50 flowing through the first flow path 109.

[0030] The mixer 111 is a device that mixes the liquid 50 flowing through the first flow path 109 and the liquid 50 flowing through the second flow path 110. As described above, the liquid 50 flowing through the second flow path 110 has a higher temperature than the liquid 50 flowing through the first flow path 109. Therefore, the temperature of the liquid 50 mixed in the mixer 111 becomes an intermediate temperature between the temperature of the liquid 50 flowing through the first flow path 109 and the temperature of the liquid 50 flowing through the second flow path 110.

[0031] The third flow path 112 is a pipe that connects the mixer 111 and the liquid supply hole 16 of the compressor 1. The third flow path 112 supplies the liquid 50 mixed by the mixer 111 to the liquid supply hole 16 of the compressor 1. The liquid 50 mixed by the mixer 111 is the liquid 50 that has been pressurized by the pump 104, and is therefore sprayed when it passes from the third flow path 112 through the liquid supply hole 16 and flows into the compression chamber 13. That is, the third flow path 112 sprays the liquid 50 mixed by the mixer 111 into the compressor 1.

[0032] The temperature measuring device 113 is a device that measures the temperature of the liquid 50 flowing through the third flow path 112. That is, the temperature measuring device 113 measures the temperature of the liquid 50 injected into the compressor 1. The flow rate adjustment valve 114 is a valve that adjusts the flow rate of the liquid 50 flowing through the first flow path 109 or the second flow path 110. In this embodiment, the flow rate adjustment valve 114 is provided in the second flow path 110, and adjusts the flow rate of the liquid 50 flowing through the second flow path 110.

[0033] When the flow rate adjustment valve 114 increases the flow rate of the liquid 50 flowing through the second flow path 110, the flow rate of the high-temperature liquid 50 increases, and the temperature of the liquid 50 mixed in the mixer 111 rises. As a result, the temperature of the liquid 50 flowing through the third flow path 112 measured by the temperature measuring device 113 rises. When the flow rate adjustment valve 114 decreases the flow rate of the liquid 50 flowing through the second flow path 110, the flow rate of the high-temperature liquid 50 decreases, and the temperature of the liquid 50 mixed in the mixer 111 falls. As a result, the temperature of the liquid 50 flowing through the third flow path 112 measured by the temperature measuring device 113 falls. The same applies when the flow rate adjustment valve 114 adjusts the flow rate of the liquid 50 flowing through the first flow path 109.

[0034] The flow rate control valve 114 adjusts the flow rate of the liquid 50 flowing through the first flow path 109 or the second flow path 110, so that the liquid supply system 100 can adjust the temperature of the liquid 50 measured by the temperature measuring device 113, i.e., the temperature of the liquid 50 injected into the compressor 1. The temperature of the liquid 50 injected into the compressor 1 affects the injection pattern of the liquid 50.

[0035] Fig. 4 is a diagram illustrating the injection mode of liquid 50 when the saturated vapor pressure corresponding to the temperature of liquid 50 injected into compressor 1 is lower than the pressure of compression chamber 13. Fig. 5 is a diagram illustrating the injection mode of liquid 50 when the saturated vapor pressure corresponding to the temperature of liquid 50 injected into compressor 1 is higher than the pressure of compression chamber 13. Figs. 4 and 5 are enlarged views of the vicinity of liquid supply hole 16 in Fig. 2.

[0036] When the saturated vapor pressure corresponding to the temperature of the liquid 50 injected into the compressor 1 is lower than the pressure in the compression chamber 13, the liquid 50 does not boil in the compression chamber 13. In this case, as shown in FIG. 4 , the liquid 50 flies through the compression chamber 13 in the form of a liquid column 51 and collides with the wall surfaces of the male rotor 3 and the female rotor 4. The colliding liquid column 51 forms a liquid film 52 on the wall surface. Part of the liquid column 51 forms droplets 53, which scatter and fly through the compression chamber 13.

[0037] On the other hand, when the saturated vapor pressure corresponding to the temperature of the liquid 50 injected into the compressor 1 is higher than the pressure in the compression chamber 13, the liquid 50 boils in the compression chamber 13. In this case, as shown in FIG. 5, the liquid 50 flies through the compression chamber 13 in the form of a liquid column 51. As the liquid column 51 boils, bubbles 54 are generated within the liquid column 51. The volume of the liquid column 51 expands due to the generation of the bubbles 54, causing the liquid column 51 to break up earlier than in the case shown in FIG. 4, forming droplets 53. This phenomenon is called flash boiling. Due to this phenomenon, the length of the liquid column 51 in the injection direction is shorter in the case shown in FIG. 5 than in the case shown in FIG. 4, and the amount of the liquid column 51 that collides with the wall surfaces of the male rotor 3 and the female rotor 4 is reduced. As a result, the amount of the liquid film 52 decreases and the amount of the droplets 53 increases. In addition, due to this phenomenon, the energy of boiling contributes to reducing the particle size of the droplets 53. Therefore, the droplets 53 are smaller in the case shown in FIG. 5 than in the case shown in FIG. 4. As the amount of droplets 53 increases and the particle size of droplets 53 becomes finer, the phase change of liquid 50 in compression chamber 13 is further promoted, so that liquid 50 can evaporate in a shorter time (evaporation rate is improved). For this reason, it is desirable that the temperature of liquid 50 injected into compressor 1 be a temperature at which flash boiling can occur in compression chamber 13.

[0038] FIG. 6 is a diagram showing the saturation vapor pressure curve of the liquid 50 injected into the compressor 1.

[0039] In order to cause a flash boiling phenomenon in the compression chamber 13, the saturation vapor pressure of the injected liquid 50 needs to be equal to or higher than the pressure in the compression chamber 13. That is, the temperature of the injected liquid 50 needs to be equal to or higher than the saturation temperature Tf corresponding to the pressure in the compression chamber 13.

[0040] On the other hand, if the temperature of the injected liquid 50 is too high, boiling starts before the liquid 50 reaches the liquid supply hole 16, and the vapor of the liquid 50 fills the third flow path 112. As a result, a problem occurs in that a sufficient amount of the liquid 50 cannot be injected into the compression chamber 13. In order not to cause this problem, the saturation vapor pressure of the injected liquid 50 needs to be lower than the pressure of the liquid 50 when it is injected into the compressor 1 (hereinafter also referred to as the "injection pressure of the liquid 50"). That is, the temperature of the injected liquid 50 needs to be lower than the saturation temperature Ti corresponding to the injection pressure.

[0041] Therefore, in order to appropriately cause a flash boiling phenomenon in the compression chamber 13, the temperature of the injected liquid 50 needs to be equal to or higher than the saturation temperature Tf corresponding to the pressure in the compression chamber 13 and lower than the saturation temperature Ti corresponding to the injection pressure. Thus, the liquid supply system 100 sets the target temperature range of the temperature T of the injected liquid 50 to the range of Tf ≦ T < Ti so that a flash boiling phenomenon appropriately occurs in the compression chamber 13, and controls the temperature of the liquid 50.

[0042] FIG. 7 is a flowchart regarding the temperature control of the liquid 50 injected into the compressor 1.

[0043] In step S1, the liquid supply system 100 measures the temperature T of the injected liquid 50 using the temperature measuring device 113.

[0044] In step S2, the liquid supply system 100 predicts the pressure inside the compressor 1 (compression chamber 13). As a method for predicting this pressure, a method using the following Equation 1 can be considered, assuming that the gas compression process is an adiabatic compression process.

[0045]

number

[0046] In Equation 1, p is the pressure of the compression chamber 13, p1 is the pressure of the gas sucked from the suction port 14, v is the volume of the compression chamber 13 at the injection position of the liquid 50, v1 is the volume of the first stage of the compression chamber 13, and n is the polytropic index. The polytropic index n may be adjusted between 1 and γ, where γ is the specific heat ratio of the gas. Note that the liquid supply system 100 may measure the pressure of the compression chamber 13 using a pressure sensor, rather than predicting the pressure of the compression chamber 13.

[0047] Furthermore, in step S2, the liquid supply system 100 predicts the spray pressure of the liquid 50. The liquid supply system 100 can regard the discharge pressure of the pump 104 as the spray pressure of the liquid 50. The discharge pressure of the pump 104 can be calculated from the total head and suction pressure of the pump 104. Note that the liquid supply system 100 may measure the spray pressure of the liquid 50 using a pressure sensor provided in a flow path downstream of the pump 104 (for example, the first flow path 109 or the third flow path 112) instead of calculating the discharge pressure of the pump 104.

[0048] In step S3, the liquid supply system 100 calculates the saturation temperature Tf corresponding to the pressure in the compression chamber 13. The saturation temperature Tf may be calculated by interpolation from a preset table, or may be calculated using an approximate formula such as that shown below. When the liquid 50 is water, the Tetens formula shown in the following Equation 2 is known as an approximate formula for the saturated vapor pressure.

[0049]

number

[0050] In Equation 2, E(t) is the saturation vapor pressure (hPa), and t is the temperature (°C). Rearranging Equation 2 with respect to t gives the following Equation 3. When the liquid 50 is water, the saturation temperature Tf can be calculated using Equation 3.

[0051]

Number

[0052] In step S4, the liquid supply system 100 calculates the saturation temperature Ti corresponding to the injection pressure of the liquid 50. Similar to the saturation temperature Tf, the saturation temperature Ti may be calculated by interpolation from a preset table, or may be calculated using an approximation formula as shown in the above Equations 2 and 3. Then, the liquid supply system 100 sets the target temperature range of the temperature T of the injected liquid 50 to Tf ≤ T < Ti.

[0053] In step S5, the liquid supply system 100 determines whether the temperature T of the liquid 50 measured in step S1 falls within the target temperature range set in step S4. That is, the liquid supply system 100 determines whether Tf ≤ T < Ti is satisfied. If Tf ≤ T < Ti is satisfied, the liquid supply system 100 ends the temperature control of the liquid 50 shown in FIG. 7. If Tf ≤ T < Ti is not satisfied, the liquid supply system 100 proceeds to step S6.

[0054] In step S6, the liquid supply system 100 determines whether the temperature T of the liquid 50 measured in step S1 is lower than the saturation temperature Tf set in step S4. That is, the liquid supply system 100 determines whether T < Tf is satisfied. If T < Tf is satisfied, the liquid supply system 100 proceeds to step S7 to increase the temperature T of the injected liquid 50. If T < Tf is not satisfied, the liquid supply system 100 proceeds to step S8 to decrease the temperature T of the injected liquid 50.

[0055] In step S7, the liquid supply system 100 adjusts the flow rate control valve 114 so that the flow rate of the high-temperature liquid 50 flowing through the second flow path 110 increases. As a result, the temperature T of the injected liquid 50 rises. Thereafter, the liquid supply system 100 terminates the temperature control of the liquid 50 shown in FIG. 7.

[0056] In step S8, the liquid supply system 100 adjusts the flow rate control valve 114 so that the flow rate of the high-temperature liquid 50 flowing through the second flow path 110 decreases. As a result, the temperature T of the injected liquid 50 drops. Thereafter, the liquid supply system 100 terminates the temperature control of the liquid 50 shown in FIG. 7.

[0057] By performing the temperature control of the liquid 50 shown in FIG. 7 at regular intervals, the liquid supply system 100 can keep the temperature T of the injected liquid 50 within the target temperature range Tf ≦ T < Ti that can appropriately cause a flash boiling phenomenon in the compression chamber 13.

[0058] As described above, the liquid supply system 100 of Embodiment 1 is a liquid supply system that injects the liquid 50 into the interior (compression chamber 13) of the compressor 1 that compresses gas. The liquid supply system 100 adjusts the temperature of the liquid 50 injected into the compressor 1 to a temperature equal to or higher than the saturation temperature Tf corresponding to the pressure in the compression chamber 13, and then injects the liquid 50 into the compressor 1.

[0059] Thereby, the liquid supply system 100 of Embodiment 1 can cause a flash boiling phenomenon of the liquid 50 inside the compressor 1 (compression chamber 13). The liquid supply system 100 can atomize and evaporate the liquid 50 in a short time without generating a swirling flow of the liquid 50 or causing the liquids injected from the two injection nozzles to collide. Therefore, according to Embodiment 1, it is possible to provide the liquid supply system 100 of the compressor 1 that can easily achieve atomization of the liquid 50 injected into the compressor 1.

[0060] Furthermore, the liquid supply system 100 of embodiment 1 adjusts the temperature of the liquid 50 injected into the compressor 1 to a temperature lower than the saturation temperature Ti corresponding to the pressure of the liquid 50 when injected into the compression chamber 13, and then injects the liquid 50 into the compressor 1.

[0061] As a result, the liquid supply system 100 of the first embodiment can prevent the liquid 50 from starting to boil before being injected into the compressor 1. The liquid supply system 100 can appropriately cause the flash boiling phenomenon of the liquid 50 inside the compressor 1. Therefore, according to the first embodiment, it is possible to provide the liquid supply system 100 for the compressor 1 that can easily and appropriately turn the liquid 50 to be injected into the compressor 1 into fine droplets.

[0062] Furthermore, the liquid supply system 100 of the first embodiment includes a pump 104 that pressurizes the liquid 50, a first flow path 109 through which the liquid 50 pressurized by the pump 104 flows, and a second flow path 110 through which the liquid 50 discharged from the compressor 1 and having a higher temperature than the liquid 50 flowing through the first flow path 109 flows. The liquid supply system 100 also includes a mixer 111 that mixes the liquid 50 flowing through the first flow path 109 with the liquid 50 flowing through the second flow path 110, and a third flow path 112 that injects the liquid 50 mixed by the mixer 111 into the compressor 1. The liquid supply system 100 also includes a flow rate adjustment valve 114 that adjusts the flow rate of the liquid 50 flowing through the first flow path 109 or the second flow path 110 to adjust the temperature of the liquid 50 flowing through the third flow path 112.

[0063] As a result, the liquid supply system 100 of embodiment 1 has a relatively simple configuration, yet is able to adjust the temperature of the liquid 50 injected into the compressor 1 so as to cause the flash boiling phenomenon in the narrow space inside the compressor 1. In addition, the liquid supply system 100 can adjust the temperature of the liquid 50 injected into the compressor 1 by utilizing the high-temperature liquid 50 discharged from the compressor 1, so that no special heating means is required and a simple flow path configuration can be achieved. Therefore, according to embodiment 1, it is possible to provide a liquid supply system 100 for a compressor 1 that can more easily turn the liquid 50 injected into the compressor 1 into fine droplets.

[0064] Furthermore, in the liquid supply system 100 of embodiment 1, the flow rate control valve 114 adjusts the flow rate of the liquid 50 so that the temperature of the liquid 50 flowing through the third flow path 112 is equal to or higher than the saturation temperature Tf corresponding to the internal pressure of the compressor 1.

[0065] As a result, the liquid supply system 100 of the first embodiment has a relatively simple configuration, but is able to generate a flash boiling phenomenon in the narrow space inside the compressor 1 and turn the liquid 50 into fine droplets in a short time and evaporate them. Therefore, according to the first embodiment, it is possible to provide the liquid supply system 100 for the compressor 1 that can easily and reliably turn the liquid 50 to be injected into the compressor 1 into fine droplets.

[0066] Furthermore, in the liquid supply system 100 of embodiment 1, the flow control valve 114 adjusts the flow rate of the liquid 50 so that the temperature of the liquid 50 flowing through the third flow path 112 is lower than the saturation temperature Ti corresponding to the pressure (injection pressure) of the liquid 50 when injected into the compressor 1.

[0067] As a result, the liquid supply system 100 of the first embodiment can prevent the liquid 50 from starting to boil before being injected into the compressor 1, and prevent the vapor of the liquid 50 from filling the third flow path 112. The liquid supply system 100 can inject a sufficient amount of liquid 50 into the compressor 1, and can appropriately cause the flash boiling phenomenon of the liquid 50 inside the compressor 1. Therefore, according to the first embodiment, it is possible to provide a liquid supply system 100 for a compressor 1 that can easily and appropriately turn the liquid 50 to be injected into the compressor 1 into fine droplets.

[0068] Furthermore, in the liquid supply system 100 of the first embodiment, the liquid 50 (for example, water) injected into the compressor 1 is a substance of the same type (components) as the gas (for example, water vapor) compressed by the compressor 1.

[0069] That is, in the liquid supply system 100, when the liquid 50 injected into the compressor 1 evaporates inside the compressor 1, it becomes the same substance as the compressed gas of the compressor 1, and therefore the density (vapor density) of the compressed gas can be improved. As a result, even when the suction pressure of the compressor 1 is low, the liquid supply system 100 can improve the discharge pressure of the compressor 1 by evaporating the liquid 50 injected into the compressor 1 inside the compressor 1, and can suppress a decrease in the output of the compressor 1. Therefore, according to the first embodiment, not only can the liquid 50 injected into the compressor 1 be easily turned into fine droplets, but also high output and stable output of the compressor 1 can be achieved despite a simple configuration.

[0070] 7 is an example of temperature control of the injected liquid 50, and the order of the steps may be reversed as necessary. Furthermore, it is not necessary for all of the steps shown in FIG. 7 to be performed all the time while the compressor 1 is in operation. For example, when the flow rate of the liquid 50 supplied to the gas-liquid separator 106 is low and the flow rate of the liquid 50 flowing through the second flow path 110 is low, the flow rate control valve 114 may be closed until the flow rate of the liquid 50 flowing through the second flow path 110 is sufficiently increased, and only the liquid 50 flowing through the first flow path 109 may be supplied to the mixer 111.

[0071] [Embodiment 2] A liquid supply system 100 of the second embodiment will be described with reference to Fig. 8. In the liquid supply system 100 of the second embodiment, the description of the same configuration and operation as in the first embodiment will be omitted.

[0072] 8 is a diagram showing the configuration of a liquid supply system 100 according to the second embodiment. FIG. 8 is a diagram corresponding to FIG.

[0073] The liquid supply system 100 of the second embodiment is configured by adding a distributor 115 and a fourth flow path 116 to the liquid supply system 100 of the first embodiment. The distributor 115 is provided on the first flow path 109. The distributor 115 divides the liquid 50 flowing through the first flow path 109 into liquid 50 flowing toward the mixer 111 and liquid 50 flowing toward the compressor 1. The fourth flow path 116 is a pipe that connects the distributor 115 to the liquid supply hole 19 of the compressor 1. The fourth flow path 116 supplies the liquid 50 divided by the distributor 115 to the compressor 1. In other words, the fourth flow path 116 is a flow path that supplies the liquid 50 flowing through the first flow path 109 to the compressor 1, bypassing the mixer 111.

[0074] As a result, the liquid supply system 100 of embodiment 2 can supply the liquid 50 for sealing the gaps between the male rotor 3 and the female rotor 4 and the gaps between the male rotor 3 or the female rotor 4 and the casing 5 to the compressor 1 via a flow path separate from the liquid 50 for cooling the compressed gas. Therefore, the liquid supply system 100 of embodiment 2 can more easily ensure the amount of liquid 50 required to seal these gaps than embodiment 1. Therefore, the liquid supply system 100 of embodiment 2 can not only easily turn the liquid 50 to be injected into the compressor 1 into fine droplets, but can also stabilize the output of the compressor 1 despite its simple configuration.

[0075] [Embodiment 3] A liquid supply system 100 according to the third embodiment will be described with reference to Fig. 9. In the liquid supply system 100 according to the third embodiment, the description of the same configuration and operation as those according to the first embodiment will be omitted.

[0076] 9 is a diagram showing the configuration of a liquid supply system 100 according to the third embodiment. FIG. 9 is a diagram corresponding to FIG.

[0077] The liquid supply system 100 of the third embodiment is different from the liquid supply system 100 of the first embodiment in that it additionally includes a heater 117. The heater 117 is provided on the third flow path 112 between the mixer 111 and the temperature measuring device 113. The heater 117 heats the liquid 50 flowing through the third flow path 112. At this time, the heater 117 heats the liquid 50 so that the temperature of the liquid 50 flowing through the third flow path 112 becomes equal to or higher than a saturation temperature Tf corresponding to the internal pressure of the compressor 1.

[0078] As a result, the liquid supply system 100 of embodiment 3 can raise the temperature of the liquid 50 flowing through the third flow path 112 to the saturation temperature Tf or higher even when the amount of high-temperature liquid 50 stored in the liquid chamber of the gas-liquid separator 106 is insufficient and the temperature of the liquid 50 flowing through the third flow path 112 does not rise even when the flow rate adjustment valve 114 is fully opened. Therefore, the liquid supply system 100 of embodiment 3 can reliably cause the flash boiling phenomenon of the liquid 50 inside the compressor 1 even in the early stage of operation of the compressor 1. Therefore, according to embodiment 3, it is possible to easily and reliably break down the liquid 50 to be injected into the compressor 1 into fine droplets.

[0079] Note that, when an electric heater or the like is used as the heater 117, the amount of energy consumed by the compressor 1 and the liquid supply system 100 as a whole increases. If the heater 117 can heat the liquid 50 by utilizing the exhaust heat of an external heat source, this is preferable because the amount of energy consumed by the compressor 1 and the liquid supply system 100 as a whole can be reduced.

[0080] [others] The present invention is not limited to the above-described embodiments and includes various modifications. For example, the above-described embodiments have been described in detail to clearly explain the present invention, and the present invention is not necessarily limited to those including all of the described configurations. Furthermore, it is possible to replace part of the configuration of one embodiment with the configuration of another embodiment, or to add the configuration of another embodiment to the configuration of one embodiment. Furthermore, it is possible to add, delete, or replace part of the configuration of each embodiment with other configurations.

[0081] Furthermore, the above-described configurations, functions, processing units, processing means, etc. may be partially or entirely realized by hardware, for example, by designing them as integrated circuits. The above-described configurations, functions, etc. may also be realized by software, in which a processor interprets and executes a program that realizes each function. Information such as the program, tape, and file that realizes each function can be stored in a memory, a recording device such as a hard disk or solid state drive (SSD), or a recording medium such as an IC card, SD card, or DVD.

[0082] In addition, the control lines and information lines shown are those that are considered necessary for the explanation, and do not necessarily show all the control lines and information lines in the product. In reality, it can be assumed that almost all components are interconnected. [Explanation of symbols]

[0083] 1...compressor, 50...liquid, 100...liquid supply system, 104...pump, 109...first flow path, 110...second flow path, 111...mixer, 112...third flow path, 113...temperature measuring device, 114...flow rate control valve, 115...distributor, 116...fourth flow path, 117...heater

Claims

1. A liquid supply system for a compressor that injects liquid into the inside of a compressor that compresses gas, adjusting a temperature of the liquid to be injected into the compressor to a temperature equal to or higher than a saturation temperature corresponding to the internal pressure of the compressor, and injecting the liquid into the compressor; The liquid supply system includes: a pump for pressurizing the liquid; a first flow path through which the liquid pressurized by the pump flows; a second flow path through which the liquid discharged from the compressor and having a temperature higher than that of the liquid flowing through the first flow path flows; a mixer that mixes the liquid flowing through the first flow path and the liquid flowing through the second flow path; a third flow path that injects the liquid mixed by the mixer into the compressor; a flow rate regulating valve that adjusts the flow rate of the liquid flowing through the first flow path or the second flow path to adjust the temperature of the liquid flowing through the third flow path. A liquid supply system for a compressor.

2. The temperature of the liquid to be injected into the compressor is adjusted to a temperature lower than a saturation temperature corresponding to the pressure of the liquid when injected into the compressor, and the liquid is injected into the compressor.

2. The compressor liquid supply system according to claim 1.

3. The flow rate adjustment valve adjusts the flow rate so that the temperature of the liquid flowing through the third flow path is equal to or higher than the saturation temperature corresponding to the pressure inside the compressor.

2. The compressor liquid supply system according to claim 1.

4. The flow rate adjustment valve adjusts the flow rate so that the temperature of the liquid flowing through the third flow path is lower than a saturation temperature corresponding to a pressure of the liquid when injected into the compressor.

4. A liquid supply system for a compressor according to claim 3.

5. The liquid injected into the compressor is of the same type as the gas compressed by the compressor.

2. The compressor liquid supply system according to claim 1.

6. a fourth flow path that supplies the liquid flowing through the first flow path to the compressor, bypassing the mixer; 2. The compressor liquid supply system according to claim 1.

7. further comprising a heater that heats the liquid flowing through the third flow path; The heater heats the liquid flowing through the third flow path so that the temperature of the liquid is equal to or higher than the saturation temperature corresponding to the pressure inside the compressor.

2. The compressor liquid supply system according to claim 1.

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