Scrubber Equipment

Abstract

To prevent clogging of a flow path by removing a scale that is an inorganic salt compound such as silica in a scrubber device.SOLUTION: There is provided a scrubber device including: a reaction tower in which an internal space is formed; a liquid spray unit configured to spray a liquid in the internal space; a gas inlet port configured to introduce a gas to the reaction tower; a liquid outlet port configured to discharge, from the reaction tower, drainage generated by treatment of taking, into the liquid, a substance in the gas; a gas deriving unit configured to derive the treated gas from the reaction tower; and a heating unit provided in at least a part of a portion close to the liquid outlet port with the gas inlet port as a reference in the reaction tower, and a portion of a liquid outlet tube connected in the downstream of the liquid outlet port, and configured to heat the drainage.SELECTED DRAWING: Figure 2

Description

[Technical field]

[0001] The present invention relates to a scrubber unit. [Background technology]

[0002] Conventionally, scrubber devices that use cyclone separation technology to remove suspended solids from geothermal water are known (e.g., Patent Documents 1 and 2). Also, a scrubber device that connects a dry scrubber and a wet scrubber is known (e.g., Patent Document 3). Also, a technology is known for removing precipitates of inorganic salt compounds, such as calcium, magnesium, or silica, contained in water in a ship scrubber device (e.g., Patent Document 4). Patent Document 1: Japanese Patent Application Laid-Open No. 11-239702 Patent Document 2: Japanese Utility Model Application Publication No. 3-83615 Patent Document 3: International Publication WO2005 / 039723 Patent Document 4: International Publication WO2014 / 118819 Summary of the Invention [Problem to be solved by the invention]

[0003] In gas treatment equipment, it is desirable to remove deposits of inorganic salt compounds such as silica to prevent clogging of flow paths. [Means for solving the problem]

[0004] In a first aspect of the present invention, a scrubber apparatus is provided. The scrubber apparatus may include a reaction tower. An internal space may be formed in the reaction tower. The scrubber apparatus may include a liquid spray section for spraying a liquid in the internal space. The scrubber apparatus may include a gas inlet for introducing a gas into the reaction tower. The scrubber apparatus may include a liquid outlet for discharging, from the reaction tower, a waste liquid generated by a process in which the liquid takes in a substance in the gas. The scrubber apparatus may include a gas outlet section for discharging the treated gas from the reaction tower. The scrubber apparatus may include a heating section. The heating section may be provided in at least a part of a portion of the reaction tower that is close to the liquid outlet and a portion of a liquid outlet pipe that is connected downstream of the liquid outlet, based on the gas inlet. The heating section may heat the waste liquid.

[0005] The heating section may heat the effluent to 80°C or higher.

[0006] The scrubber may be a scrubber for geothermal power generation. The gas inlet may introduce steam used for geothermal power generation as gas into the reaction tower. The gas outlet may supply treated steam to the power generation device.

[0007] Based on the composition of impurities in the gas or effluent, the heating section may vary the heating temperature of the effluent.

[0008] Based on the concentration of silica in the gas or effluent, the heating section may vary the heating temperature of the effluent.

[0009] The scrubber device may further comprise a chemical introduction section for adding a chemical to the effluent.

[0010] The agent may make the effluent more acidic.

[0011] The drug may adjust the pH of the effluent to 5.5 or less.

[0012] Based on the composition of impurities in the gas or effluent, the drug introduction section may adjust the pH of the effluent.

[0013] Based on the concentration of silica in the gas or effluent, the drug introduction section may adjust the pH of the effluent.

[0014] The heating unit may continuously heat the effluent during operation of the geothermal power generation. The chemical agent introduction unit may temporarily cause the effluent to contain a chemical agent when the composition of impurities or the concentration of silica in the gas or the effluent satisfies a predetermined condition.

[0015] The scrubber may include a diluent supplying unit. The diluent supplying unit may be connected to at least a part of a portion of the reaction tower close to the liquid outlet based on the gas inlet and a portion of the liquid outlet pipe connected downstream of the liquid outlet. The diluent supplying unit may supply a diluent for diluting the effluent.

[0016] The diluent supply unit may adjust the amount of diluent supplied based on the amount of water in an injection well for returning steam used in geothermal power generation to an underground geothermal reservoir.

[0017] The diluent supply unit may adjust the amount of diluent supplied based on the amount of steam and hot water pumped from the geothermal reservoir in the production well.

[0018] The scrubber unit may include a pressure booster unit that may boost the pressure of the liquid to be sprayed to a pressure higher than the internal pressure of the reaction tower.

[0019] The scrubber unit may include a dry cyclone scrubber section having a tube with a swirling space formed therein, in which the suspension swirls, upstream of the gas inlet.

[0020] The scrubber unit may include a plurality of dry cyclone scrubber units having different pipe diameters. The scrubber unit may include a switching unit. The switching unit may select a dry cyclone scrubber unit that supplies gas to the gas inlet from among the plurality of dry cyclone scrubber units.

[0021] The scrubber may be a marine scrubber. The gas inlet may introduce exhaust gas from an internal combustion engine of the marine vessel as a gas into the reaction tower. The gas outlet may exhaust the treated exhaust gas into the atmosphere. [Brief description of the drawings]

[0022] [Figure 1] FIG. 1 is a diagram showing an example of a geothermal power generation system to which a scrubber unit according to an embodiment of the present invention is applied. [Diagram 2] FIG. 2 is a diagram showing an example of a wet cyclone scrubber section in the scrubber device of the first embodiment. [Diagram 3] FIG. 4 is a diagram showing another example of the wet cyclone scrubber section in the first embodiment. [Figure 4] FIG. 11 is a diagram showing an example of a wet cyclone scrubber section in a second embodiment. [Diagram 5] FIG. 11 is a diagram showing another example of the wet cyclone scrubber section in the second embodiment. [Figure 6] FIG. 11 is a diagram showing another example of the wet cyclone scrubber section in the second embodiment. [Figure 7] FIG. 13 is a diagram showing an example of a wet cyclone scrubber section in a third embodiment. [Figure 8] FIG. 13 is a diagram showing another example of the wet cyclone scrubber section in the third embodiment. [Figure 9] FIG. 2 is a diagram showing an example of a dry cyclone scrubber section. [Figure 10] FIG. 1 is a diagram showing another example of a scrubber device; [Figure 11] FIG. 1 is a diagram showing an example of a ship system to which a marine scrubber apparatus according to an embodiment of the present invention is applied. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0023] The present invention will be described below through embodiments of the invention, but the following embodiments do not limit the scope of the invention according to the claims. Furthermore, not all of the combinations of features described in the embodiments are necessarily essential to the solution of the invention.

[0024] FIG. 1 is a diagram showing an example of a geothermal power generation system 1000 according to an embodiment of the present invention. The geothermal power generation system 1000 includes a scrubber unit 2, a gas outlet unit 300, a power generation unit 400, and a gas recovery unit 500. In FIG. 1, the scrubber unit 2 is a scrubber unit for geothermal power generation. The scrubber unit 2 processes gas. In this example, the gas is steam 30. Processing gas means removing harmful substances contained in the gas. In this example, the scrubber unit 2 processes steam 30 used for geothermal power generation and supplies the steam 30 to the power generation unit 400 through the gas outlet unit 300. The gas outlet unit 300 may be a pipe for supplying the treated steam 30 to the power generation unit 400. The steam 30 may include mist. The scrubber unit 2 supplies the purified steam 30 to the power generation unit 400 by incorporating impurities in the steam 30 into the liquid 40. The waste liquid 46 generated by the process in which the liquid 40 takes in substances in the gas is discharged from the liquid outlet 19 in the reaction tower of the wet cyclone scrubber section 100 through the liquid discharge pipe 20 to the outside of the reaction tower. The scrubber device 2 prevents impurities from precipitating in the waste liquid 46 and clogging the flow path of the waste liquid 46. The means for preventing the precipitating of impurities will be described later.

[0025] The power generation device 400 includes a turbine 410 and a generator 420. In this example, the generator 420 generates power by rotating the turbine 410 using the steam 30. The gas recovery section 500 recovers the steam 30. The gas recovery section 500 may be provided downstream of the turbine 410 in the traveling direction of the steam 30. In this example, the gas recovery section 500 includes a recovery tank 510, a cooling tower 520, and a pump 530. The steam 30 used in the power generation device 400 returns to the liquid 540 in the recovery tank 510. The recovery tank 510 functions as a condenser. The liquid 540 is further cooled in the cooling tower 520. The cooled liquid 540 is returned to the recovery tank 510 by the pump 530. The liquid 540 returned to the recovery tank 510 is used to cool the steam 30. The gas recovery section 500 may recover condensed water 430 from the vicinity of the turbine 410. The liquid 540 from the recovery tank 510 may be introduced into a reinjection well 1200, which is a well that returns the used liquid 540 to the underground geothermal reservoir.

[0026] The steam 30 is obtained from a production well 1100. The steam 30 may be pumped together with hot water 31. The production well 1100 is a well that pumps the steam 30 and hot water 31 from an underground geothermal reservoir. The steam 30 from the production well 1100 may contain fine dust particles such as soil, silica, and sulfides as impurities. The scrubber unit 2 removes the impurities in the steam 30. This can prevent breakdowns in the power generation equipment.

[0027] The scrubber unit 2 has a wet cyclone scrubber section 100. The scrubber unit 2 may further have a dry cyclone scrubber section 200. In this example, the steam 30 and hot water 31 obtained in the production well 1100 are introduced into the dry cyclone scrubber section 200. In this example, the dry cyclone scrubber section 200 performs gas-liquid separation of the steam 30 and the hot water 31. The dry cyclone scrubber section 200 also removes relatively large suspended matter from the fine dust in the steam 30. In one example, the suspended matter includes silica. However, unlike this example, the scrubber unit 2 may not include the dry cyclone scrubber section 200. In that case, a gas-liquid separator may be provided instead of the dry cyclone scrubber section 200.

[0028] The wet cyclone scrubber section 100 treats the steam 30 with the liquid 40. In this example, the wet cyclone scrubber section 100 treats the steam 30 as a gas discharged from the dry cyclone scrubber section 200. The liquid 40 is introduced into the wet cyclone scrubber section 100. In one example, the liquid 40 may be water, or water containing a solvent. As the liquid 40, a liquid 540 obtained by condensing the steam 30 in the recovery tank 510 of the gas recovery section 500 may be used. However, the liquid 40 is not limited to this case, and may be water separately procured from outside.

[0029] The liquid 40 may be pressurized by the pressure booster 550 so that the pressure is higher than the internal pressure of the reaction tower of the wet cyclone scrubber section 100. The pressurized liquid 40 is sprayed in the wet cyclone scrubber section 100. The liquid 40 takes in impurities contained in the steam 30. Taking in impurities may mean at least one of chemically dissolving, chemically reacting, and physically absorbing. The impurities are removed from the steam 30 by taking in the impurities into the liquid 40. The steam 30 thus treated is led out of the wet cyclone scrubber section 100 and sent to the turbine 410 of the power generation device.

[0030] The waste liquid 46 generated by the liquid 40 taking in the substances in the gas is discharged from the liquid outlet 19 in the reaction tower of the wet cyclone scrubber section 100 through the liquid outlet pipe 20 to the outside of the reaction tower. The waste liquid 46 means the liquid after being used in the process of taking in the substances in the gas. In one example, the waste liquid 46 contains fine dust such as sand, silica, and sulfides as impurities. In this example, the hot water 31 obtained by gas-liquid separation by the dry cyclone scrubber section 200 may also be discharged as the waste liquid 46 through the gas-liquid separation pipe 21. The waste liquid 46 may be introduced into the reinjection well 1200. The scrubber device 2 of this embodiment prevents impurities such as silica from precipitating and clogging the flow path in the liquid outlet 19 or the liquid outlet pipe 20 in the reaction tower of the wet cyclone scrubber section 100. The precipitates such as silica are called "scale". The structure of the wet cyclone scrubber section 100 for removing scale will be described later.

[0031] According to the scrubber apparatus 2 shown in Fig. 1, the steam 30 may proceed from the dry cyclone scrubber section 200 to the wet cyclone scrubber section 100 in that order. That is, the steam 30 is processed in the dry cyclone scrubber section 200 and then the wet cyclone scrubber section 100. After removing relatively large suspended solids in the dry cyclone scrubber section 200, the fine suspended solids are removed in the wet cyclone scrubber section 100. This makes it possible to suppress a decrease in pressure loss of the steam 30 with a simple structure. Also, it is possible to prevent the fine suspended solids from passing through.

[0032] 2 is a diagram showing an example of a wet cyclone scrubber section 100 in the scrubber unit 2. The wet cyclone scrubber section 100 includes a reaction tower 10. The reaction tower 10 includes a gas treatment section 18, which is an internal space. The scrubber unit 2 may include a gas inlet pipe 32 and a liquid outlet pipe 20. In this example, steam 30 is introduced into the reaction tower 10 from a dry cyclone scrubber section 200.

[0033] The reaction tower 10 has a gas inlet 11 for introducing a gas to be treated. The gas inlet 11 introduces steam 30 used for geothermal power generation as a gas into the reaction tower 10. The reaction tower 10 has a gas outlet 17 for discharging the treated gas from the reaction tower 10. The gas outlet 17 is connected to a gas outlet section 300 for discharging the treated gas from the reaction tower 10. In this example, the gas outlet section 300 supplies the treated steam 30 to a power generation device 400. The reaction tower 10 is supplied with a liquid 40 for treating the steam 30. The liquid 40 supplied to the reaction tower 10 treats the steam 30 inside the reaction tower 10. After treating the steam 30, the liquid 40 becomes a waste liquid 46.

[0034] The reaction tower 10 of this example has a side wall 15, a bottom surface 16, a gas treatment section 18, and a liquid outlet 19. The reaction tower 10 of this example is cylindrical. In this example, the gas outlet 17 is disposed at a position facing the bottom surface 16 in a direction parallel to the central axis of the cylindrical reaction tower 10. In this example, the side wall 15 and the bottom surface 16 are the inner surface and the bottom surface 16 of the cylindrical reaction tower 10, respectively. The gas inlet 11 may be provided in the side wall 15. In this example, the steam 30 is introduced into the gas treatment section 18 after passing through the gas inlet 11 from the gas inlet pipe 32.

[0035] The gas treatment section 18 is an internal space surrounded by the side wall 15, the bottom surface 16, and the gas outlet 17. The gas treatment section 18 contacts the side wall 15, the bottom surface 16, and the gas outlet 17. The gas treatment section 18 treats the steam 30 inside the reaction tower 10. The bottom surface 16 is the surface onto which the waste liquid falls. The waste liquid 46 passes through the liquid outlet 19 and is then discharged via the liquid outlet pipe 20. The liquid outlet 19 discharges the waste liquid generated by the process in which the liquid takes in the gas, i.e., the material in the steam 30, from the reaction tower 10.

[0036] The sidewall 15 and bottom surface 16 are formed of a material that is resistant to the steam 30, as well as the liquid 40 and the drainage liquid 46. The material may be a combination of an iron material such as SS400 or S-TEN (registered trademark) with at least one of a coating and a paint, a copper alloy such as Nevar brass, an aluminum alloy such as aluminum brass, a nickel alloy such as cupronickel, or a stainless steel such as Hastelloy (registered trademark), SUS316L, SUS329J4L, or SUS312.

[0037] In this specification, technical matters may be described using orthogonal coordinate axes of the X-axis, Y-axis, and Z-axis. In this specification, a plane parallel to the bottom surface 16 of the reaction tower 10 is defined as the XY plane, and a direction from the bottom surface 16 toward the gas exhaust port 17 (a direction perpendicular to the bottom surface 16) is defined as the Z axis. In this specification, a predetermined direction in the XY plane is defined as the X-axis direction, and a direction perpendicular to the X-axis in the XY plane is defined as the Y-axis direction.

[0038] The Z-axis direction may be parallel to the direction of gravity. When the Z-axis direction is parallel to the direction of gravity, the XY plane may be a horizontal plane. The Z-axis direction may be parallel to the horizontal direction. When the Z-axis direction is parallel to the horizontal direction, the XY plane may be parallel to the direction of gravity.

[0039] In this specification, a side view refers to a view of the gas treatment device from a direction perpendicular to the Z axis (a predetermined direction in the XY plane). In this specification, a side view refers to a view from the side.

[0040] In the wet cyclone scrubber section 100, the steam 30 introduced into the reaction tower 10 advances in a direction from the gas inlet 11 to the gas outlet 17 (in the Z-axis direction in this example) while swirling inside the reaction tower 10. In this example, the steam 30 swirls within the XY plane when viewed in the direction from the gas outlet 17 to the bottom surface 16.

[0041] The reaction tower 10 has a liquid spraying section 90. The liquid spraying section 90 is provided between the gas inlet 11 and the gas outlet 17. The liquid spraying section 90 may be a part of the region between the gas inlet 11 and the gas outlet 17 in the traveling direction of the steam 30 (Z-axis direction). The liquid spraying section 90 may be the entire region of the reaction tower 10 when the reaction tower 10 is viewed in the direction from the gas outlet 17 to the bottom surface 16 (XY plane). The liquid spraying section 90 sprays the liquid 40 in the internal space of the reaction tower 10.

[0042] The reaction tower 10 may have one or more trunk pipes 12 to which the liquid 40 is supplied, and one or more branch pipes 13. The reaction tower 10 may have one or more ejection parts 14 that eject the liquid 40. In this example, the ejection parts 14 are connected to the branch pipes 13, and the branch pipes 13 are connected to the trunk pipe 12.

[0043] In this example, at least a part of the trunk pipe 12, the branch pipe 13 and the jetting part 14 are provided in the liquid spraying part 90. In the figure, the range of the liquid spraying part 90 inside the reaction tower 10 is indicated by a double arrow. The liquid spraying part 90 may spray the liquid 40 in a range from the jetting part 14 arranged closest to the gas inlet 11 to the jetting part 14 arranged closest to the gas outlet 17 in a direction parallel to the Z axis. The liquid spraying part 90 may spray the liquid 40 in a range surrounded by the side wall 15 in the XY plane.

[0044] In this example, the steam 30 travels inside the reaction tower 10 from the gas inlet 11 to the gas outlet 17 while swirling in a predetermined direction (swirling direction) in the liquid spraying section 90. The traveling direction of the steam 30 from the gas inlet 11 to the gas outlet 17 inside the reaction tower 10 is defined as a traveling direction E1. In this example, the traveling direction E1 of the steam 30 is parallel to the Z axis. That is, in this example, the steam 30 travels in the traveling direction E1 in a side view of the reaction tower 10, and swirls in a swirling direction F as viewed from the traveling direction E1.

[0045] In this example, the wet cyclone scrubber section 100 includes a swirl section 80. The swirl section 80 has an inlet end 102 into which the steam 30 is introduced, and an outlet end 104 from which the steam 30 is discharged. The steam 30 advances inside the swirl section 80 in a direction from the inlet end 102 to the outlet end 104. The traveling direction of the steam 30 from the inlet end 102 to the outlet end 104 is parallel to the Z axis. That is, in this example, the steam 30 advances in a traveling direction E1 in a side view of the swirl section 80, and swirls in a predetermined swirl direction as viewed from the traveling direction E1.

[0046] In this example, the cylindrical reaction tower 10 may be placed so that the central axis of the reaction tower 10 is parallel to the vertical direction, or may be placed so that the central axis is parallel to the horizontal direction. When the reaction tower 10 is placed so that the central axis is parallel to the vertical direction, the traveling direction E1 of the steam 30 (direction parallel to the Z axis) is parallel to the vertical direction and is a direction from below to above in the vertical direction. When the reaction tower 10 is placed so that the central axis is parallel to the horizontal direction, the traveling direction E1 of the steam 30 (direction parallel to the Z axis) is parallel to the horizontal direction.

[0047] In this example, the swirling section 80 is provided downstream of the steam 30 in the traveling direction of the steam 30 (the Z-axis direction in this example). In this example, the swirling section 80 is provided between the liquid spraying section 90 and the gas exhaust port 17 in the Z-axis direction. The swirling section 80 increases the speed of the steam 30.

[0048] In this example, the gas inlet 11 is provided on the side surface at a position in the Z-axis direction closer to the bottom surface 16 than the gas outlet 17 in a side view. A portion of the reaction tower 10 close to the liquid outlet 19 with respect to the gas inlet 11 is referred to as a liquid outlet region 702.

[0049] The wet cyclone scrubber section 100 of this example includes a heating section 700. The heating section 700 is provided in at least a part of the liquid discharge area 702 and the part of the liquid discharge pipe 20 connected downstream from the liquid discharge port 19, and heats the waste liquid 46. The heating section 700 may include a first heating section that heats the liquid discharge area 702 of the reaction tower 10 and a second heating section that heats the part of the liquid discharge pipe 20. In this example, the heating section 700 may heat at least a part of the liquid discharge area 702 and the liquid discharge pipe 20 of the wet cyclone scrubber section 100 by geothermal water 713. The geothermal water 713 may be hot water 31 pumped from the production well 1100, or may be a liquid obtained by diluting the hot water 31 as necessary to adjust the temperature.

[0050] The heating section 700 includes a heating pipe 710 and a pump 720. The heating pipe 710 may include a first heating pipe 711 and a second heating pipe 712. The first heating pipe 711 is provided in the liquid discharge region 702 of the reaction tower 10 so as to cover the side wall 15 and the bottom surface 16 of the reaction tower 10 from the outside of the reaction tower 10. On the other hand, the second heating pipe 712 is provided so as to cover the side surface of the liquid discharge pipe 20 from the outside of the liquid discharge pipe 20. The first heating pipe 711 and the second heating pipe 712 may be in communication with each other. The heating section 700 may have at least one of the first heating pipe 711 and the second heating pipe 712. The pump 720 circulates the geothermal water 713 in the heating pipe 710. The heating section 700 may heat the waste liquid 46 to 70° C. or more, 80° C. or more, or 100° C. or more.

[0051] In this way, the heating unit 700 heats at least a part of the liquid discharge area 702 of the reaction tower 10 and the liquid discharge pipe 20, thereby preventing the precipitation of fine suspended matter in the waste liquid 46, i.e., silica, calcium, aluminum, magnesium, etc. As a result, it is possible to prevent the generation of "scale" and the clogging of the flow path of the waste liquid 46. In particular, when the waste liquid 46 is a silica solution, it is possible to reduce the generation of silica scale in which silica is precipitated.

[0052] The heating section 700 may include a measuring section 730 and a geothermal water temperature adjusting section 722. In one example, the measuring section 730 may measure the concentration or composition of impurities (suspended matter) in the steam 30, or may measure the concentration or composition of impurities (suspended matter) in the effluent 46. In one example, the measuring section 730 may measure the concentration of silica in the steam 30, or may measure the concentration of silica in the effluent 46. Note that the measurement of the concentration or composition in the measuring section 730 can utilize conventional technology, and therefore detailed description thereof will be omitted.

[0053] The geothermal water temperature adjusting unit 722 may change the temperature at which the effluent 46 is heated according to the measurement result by the measuring unit 730. The geothermal water temperature adjusting unit 722 may adjust the temperature of the geothermal water 713 by selecting the geothermal water 713 collected at a different collection position according to the measurement result by the measuring unit 730. The heating unit 700 may change the heating temperature of the effluent 46 based on the composition of impurities in the gas (steam 30) or the effluent. The heating unit 700 may also change the heating temperature of the effluent 46 based on the concentration of silica in the gas (steam 30) or the effluent 46. In one example, the higher the concentration of silica, the easier it is for silica to precipitate, so the heating temperature may be increased to suppress the precipitation of silica. Alternatively, when the precipitation temperature at which the precipitation of suspended solids begins is determined according to the composition, the heating temperature may be increased so that the effluent 46 is at or above the precipitation temperature. However, the heating unit 700 may be configured without the measurement unit 730 and the geothermal water temperature adjustment unit 722.

[0054] 2, impurities in the gas, i.e., steam 30 in this example, can be taken in and purified by the liquid 40, and the steam 30 can be led to the turbine 410 of the power generation device. The heating section 700 heats the effluent 46 by heating at least a part of the liquid discharge area 702 and the liquid discharge pipe 20 of the wet cyclone scrubber section 100. Therefore, it is possible to suppress the precipitation of silica due to a decrease in the temperature of the effluent 46.

[0055] In addition, since the heating temperature can be increased depending on the concentration of silica in the steam 30 or the concentration of silica in the wastewater, it is possible to effectively utilize the geothermal water 713. However, the heating unit 700 is not limited to one that uses geothermal water to heat the wastewater.

[0056] Fig. 3 is a diagram showing another example of the wet cyclone scrubber section 100 in the scrubber apparatus 2. The structure of the wet cyclone scrubber section 100 shown in the figure is similar to the structure of the wet cyclone scrubber section 100 of the scrubber apparatus 2 shown in Fig. 1 and Fig. 2, except for the configuration of the heating section 700. Therefore, repeated explanation will be omitted.

[0057] The heating section 700 shown in FIG. 3 is also provided in at least a part of the liquid discharge area 702 and the part of the liquid discharge pipe 20 connected downstream from the liquid discharge port 19, and heats the waste liquid 46. The heating section 700 in this example is provided in both the liquid discharge area 702 and the liquid discharge pipe 20 connected downstream from the liquid discharge port 19. The heating section 700 may include a first heating section that heats the liquid discharge area 702 of the reaction tower 10 and a second heating section that heats a part of the liquid discharge pipe 20. In this example, the heating section 700 includes a heater section 740 and a heater power supply 750. The heater section 740 heats at least a part of the liquid discharge area 702 and the liquid discharge pipe 20 of the wet cyclone scrubber section 100. The heater section 740 may be an electric heater or an infrared heater. In this example, the heater section 740 is an electric heater.

[0058] The heater section 740 may include a plurality of heaters. In one example, the heater section 740 may include a first heater section 741 and a second heater section 742. The first heater section 741 may be provided in the liquid discharge region 702 of the reaction tower 10 so as to cover the side wall 15 and the bottom surface 16 of the reaction tower 10 from the outside of the reaction tower 10. On the other hand, the second heater section 742 is provided so as to cover the side surface of the liquid discharge pipe 20 from the outside of the liquid discharge pipe 20. The first heater section 741 and the second heater section 742 may be connected in series or in parallel. Note that the heating section 700 may have at least one of the first heater section 741 and the second heater section 742. The heater power supply 750 supplies power to the heater section 740. In one example, the first heater section 741 and the second heater section 742 are electrical resistors, and Joule heat is generated when a current flows through them. In this example, the heating section 700 may heat the drainage liquid 46 to 70° C. or higher, 80° C. or higher, or 100° C. or higher.

[0059] In this way, the heating unit 700 heats at least a part of the liquid discharge area 702 of the reaction tower 10 and the liquid discharge pipe 20, thereby preventing the precipitation of minute suspended matter in the waste liquid 46, i.e., silica, calcium, aluminum, magnesium, etc., and preventing the generation of "scale" and the clogging of the flow path of the waste liquid 46. In particular, when the waste liquid is a silica solution, the precipitation of silica can be prevented.

[0060] The heating section 700 may include a measuring section 730 and a heater control section 752. The measuring section 730 is the same as that shown in FIG. 2, and the heater control section 752 may change the temperature at which the effluent 46 is heated according to the measurement result by the measuring section 730. The heater control section 752 may adjust the heating temperature by adjusting the power supplied from the heater power source 750 to the heater section 740 according to the measurement result by the measuring section 730. As a result, the heating section 700 may change the heating temperature of the effluent 46 based on the composition of impurities in the gas (water vapor 30) or the effluent. The heating section 700 may also change the heating temperature of the effluent 46 based on the concentration of silica in the gas (water vapor 30) or the effluent. The configuration shown in FIG. 3 can also suppress the precipitation of silica due to a decrease in the temperature of the effluent.

[0061] FIG. 4 is a diagram showing an example of the wet cyclone scrubber section 100 in the scrubber unit 2 of the second embodiment. The wet cyclone scrubber section 100 in the scrubber unit 2 of the present embodiment is provided with an agent introduction section 800 for causing the wastewater 46 to contain an agent 813. In addition, in FIG. 4, the heating section 700 is omitted. Except for these points, the structure of the wet cyclone scrubber section 100 is similar to the structure of the wet cyclone scrubber section 100 shown in FIG. 1 to FIG. 3. Therefore, repeated explanation will be omitted. Note that the wet cyclone scrubber section 100 may be provided with both the agent introduction section 800 and the heating section 700.

[0062] The drug introduction section 800 causes the drainage liquid 46 to contain a drug 813. The drug 813 may be a drug that adjusts the drainage liquid 46 to be acidic. In particular, the drug 813 may adjust the hydrogen ion exponent (pH) of the drainage liquid 46 to 5.5 or less. The drug 813 may contain various acids such as HCl that are used to adjust the hydrogen ion exponent. In the example shown in FIG. 4, the drug introduction section 800 includes a drug introduction tube 810, a pump 820, a drug container 822, a drug amount adjustment section 824, and a measurement section 830.

[0063] In this example, the inner surface of the reaction tower 10 may be formed of a material resistant to the chemical 813. The chemical introduction pipe 810 may penetrate the side of the reaction tower 10. The chemical introduction pipe 810 introduces the chemical 813 into the reaction tower 10. The chemical 813 introduced into the reaction tower 10 through the chemical introduction pipe 810 is included in the waste liquid 46 stored on the bottom surface 16 in the reaction tower 10. As a result, the hydrogen ion exponent of the waste liquid 46 is adjusted. The adjusted waste liquid is introduced into the reinjection well 1200 through the liquid outlet 19 and the liquid discharge pipe 20. Note that the waste liquid 46 may be neutralized by a neutralizing agent before being introduced into the reinjection well 1200.

[0064] In this way, by adjusting the hydrogen ion potential of the waste liquid 46, it is possible to suppress the formation of "scale" due to precipitation of minute suspended solids in the waste liquid 46, i.e., silica, calcium, aluminum, magnesium, etc. As a result, it is possible to prevent the drainage flow path from being clogged with scale. In particular, when the waste liquid is a silica solution, it is possible to reduce the precipitation of silica.

[0065] The measuring unit 830 is the same as the measuring unit 730 in FIG. 2. Therefore, repeated description will be omitted. The drug amount adjusting unit 824 adjusts the hydrogen ion exponent (pH) of the effluent 46 according to the measurement result by the measuring unit 830. Specifically, the drug amount adjusting unit 824 adjusts the concentration or amount of the drug 813 to be mixed with the effluent 46. In one example, the drug 813 whose amount or concentration has been adjusted is temporarily stored in the drug container 822. The pump 820 injects the drug 813 in the drug container 822 into the reaction tower 10 through the drug introduction pipe 810. As a result, the drug introduction unit 800 may change the hydrogen ion exponent of the effluent 46 based on the composition of impurities in the gas (water vapor 30) or the effluent. The drug introduction unit 800 may also change the hydrogen ion exponent of the effluent 46 based on the concentration of silica in the gas (water vapor 30) or the effluent. However, the drug delivery section 800 does not necessarily have to include the measurement section 830 and the drug amount adjustment section 824 .

[0066] According to the wet cyclone scrubber section 100 shown in FIG. 4, impurities in the gas, i.e., in this example, the steam 30, can be taken in and purified by the liquid 40, and the steam 30 can be led to the turbine 410 of the power generation device 400. Then, the waste liquid 46 generated by the liquid 40 taking in the impurities is adjusted to be acidic by making the waste liquid 46 contain a chemical agent 813 in the wet cyclone scrubber section 100. In one example, the hydrogen ion exponent of the waste liquid 46 is adjusted to be 5.5 or less. As a result of the hydrogen ion exponent of the waste liquid 46 being 5.5 or less, it is possible to suppress the precipitation of silica. In addition, the hydrogen ion exponent can be adjusted to an appropriate value according to the concentration of silica in the steam 30 or the concentration of silica in the waste liquid 46. This can reduce as much as possible the corrosion of the piping through which the waste liquid 46 flows due to the chemical agent 813.

[0067] FIG. 5 is a diagram showing another example of the wet cyclone scrubber section 100 in the scrubber apparatus 2 of the second embodiment. In FIG. 5, the chemical introduction pipe 810 is connected to the trunk pipe 12 that introduces the liquid 40 into the reaction tower 10. As a result, the hydrogen ion index of the liquid 40 is adjusted upstream of where the liquid 40 is sprayed. As a result, the hydrogen ion index of the waste liquid 46 generated by the liquid 40 taking in impurities is also adjusted. The other configurations are the same as those of the wet cyclone scrubber section 100 in the scrubber apparatus of the second embodiment shown in FIG. 4. Therefore, detailed explanations will be omitted.

[0068] 6 is a diagram showing another example of the wet cyclone scrubber section 100 in the scrubber device 2 of the second embodiment. In FIG. 6, the chemical introduction pipe 810 is connected to the liquid discharge pipe 20 connected downstream from the liquid discharge port 19. This allows the hydrogen ion exponent of the wastewater 46 downstream from the connection between the chemical introduction pipe 810 and the liquid discharge pipe 20 to be adjusted. It is preferable that the chemical introduction pipe 810 is connected to the liquid discharge pipe 20 near the liquid discharge port 19. In one example, it is preferable that the chemical introduction pipe 810 is connected to the liquid discharge pipe 20 in a region within 1 m from the liquid discharge port 19.

[0069] The hydrogen ion exponent of the waste liquid 46 can also be adjusted by the configurations shown in Figs. 5 and 6. This makes it possible to suppress the formation of "scale" due to precipitation of minute suspended solids in the waste liquid 46, i.e., silica, calcium, aluminum, magnesium, etc. As a result, clogging of the flow path of the waste liquid by scale can be prevented. In particular, when the waste liquid is a silica solution, precipitation of silica can be reduced. Also, precipitated silica, etc. can be removed.

[0070] It is possible to use both the treatment by the heating unit 700 shown in Fig. 2 and Fig. 3 and the treatment by the chemical introduction unit 800 shown in Fig. 4 to Fig. 6. In this case, in one example, the heating unit 700 continuously heats the waste liquid 46 steadily during the operation of geothermal power generation, and the chemical introduction unit 800 may treat the waste liquid 46 to temporarily contain the chemical 813 when the composition of impurities or the concentration of silica in the gas (steam 30) or the waste liquid 46 meets a predetermined condition. This makes it possible to suppress the generation of scale by the heat treatment so as not to damage the inner surface of the liquid discharge pipe 20 and the reaction tower 10 through which the waste liquid 46 flows as much as possible, while the chemical treatment can be performed only when the composition of impurities or the concentration of silica is such that scale is generated even by the heat treatment.

[0071] FIG. 7 is a diagram showing an example of the wet cyclone scrubber section 100 in the scrubber apparatus 2 of the third embodiment. The wet cyclone scrubber section 100 in the scrubber apparatus 2 of the present embodiment includes a diluent supply section 900. In addition, in FIG. 7, the heating section 700 and the chemical introduction section 800 are omitted. Except for these points, the structure of the wet cyclone scrubber section 100 is similar to the structure of the wet cyclone scrubber section 100 shown in FIG. 1 to FIG. 6. Therefore, repeated explanation will be omitted. Note that the wet cyclone scrubber section 100 may include both the diluent supply section 900 and the heating section 700.

[0072] The diluent supply unit 900 shown in FIG. 7 supplies a diluent 913 for diluting the wastewater 46. The diluent supply unit 900 is provided in at least a part of the liquid discharge area 702 of the reaction tower 10 and a part of the liquid discharge pipe 20 connected downstream from the liquid discharge port 19. The diluent 913 may be, for example, water. The diluent supply unit 900 may collect river water or the like as the diluent 913. In the example shown in FIG. 7, the diluent supply unit 900 may include a diluent introduction pipe 910, a pump 920, an adjustment valve 922, a dilution amount control unit 924, and a well condition measurement unit 930.

[0073] The diluent introduction pipe 910 may penetrate the side surface of the reaction tower 10. The diluent introduction pipe 910 introduces the diluent 913 into the reaction tower 10. The diluent introduction pipe 910 is preferably provided in the liquid discharge area 702 of the reaction tower 10. If the diluent 913 is introduced into the reaction tower 10 on the gas exhaust port 17 side, there is a risk that the diluent 913 will take away heat from the steam 30. Therefore, it is advantageous to provide the diluent introduction pipe 910 in the liquid discharge area 702 of the reaction tower 10.

[0074] The diluent 913 introduced into the reaction tower 10 through the diluent introduction pipe 910 dilutes the waste liquid 46 stored on the bottom surface 16 in the reaction tower 10. As a result, the concentrations of impurities such as silica, calcium, aluminum, and magnesium in the waste liquid 46 can be reduced. Therefore, the precipitation of silica, calcium, aluminum, magnesium, and the like to form "scale" can be suppressed.

[0075] The well condition measurement unit 930 may measure the amount of liquid (amount of water) in the reinjection well 1200, which reconstitutes the steam 30 used for geothermal power generation into liquid and returns it to the underground geothermal reservoir. Alternatively or in addition to this, the well condition measurement unit 930 may measure the amount of steam 30 and hot water pumped up from the geothermal reservoir in the production well 1100.

[0076] The dilution amount control unit 924 adjusts the supply amount of the diluent 913 based on the measurement result of the well condition measurement unit 930. Specifically, the dilution amount control unit 924 may adjust the aperture of the adjustment valve 922. The adjustment valve 922 adjusts the supply amount of the diluent 913 according to the aperture. This allows the diluent supply unit 900 to adjust the supply amount of the diluent based on the amount of water in the reinjection well 1200. If the amount of water in the reinjection well 1200 is small, the diluent supply unit 900 may increase the supply amount of the diluent 913. This adjustment makes it possible to adjust the amount of liquid not to overflow from the reinjection well 1200.

[0077] The dilution liquid supply unit 900 may adjust the supply amount of the dilution liquid 913 based on the amount of the steam 30 and the hot water 31 pumped from the geothermal reservoir in the production well 1100. For example, the dilution amount control unit 924 calculates the amount of the steam 30 vaporized and discharged to the outside in the flow path between the production well 1100 and the reinjection well 1200 from information on the production well 1100 and the reinjection well 1200. Then, the dilution amount control unit 924 may supply the dilution liquid 913 in an amount corresponding to the amount of the steam 30 vaporized and discharged to the outside. This allows the wastewater 46 corresponding to the amount of the steam 30 and the hot water 31 pumped from the production well 1100 to be returned to the reinjection well 1200. However, the dilution liquid supply unit 900 does not necessarily have to have the well state measurement unit 930 and the dilution amount control unit 924.

[0078] FIG. 8 is a diagram showing another example of the wet cyclone scrubber unit 100 in the scrubber device of the third embodiment. In FIG. 8, the diluent introduction pipe 910 is connected to the liquid discharge pipe 20 connected downstream from the liquid discharge port 19. This makes it possible to lower the concentration of silica and the like in the drainage liquid 46 downstream of the connection between the diluent introduction pipe 910 and the liquid discharge pipe 20. It is desirable that the diluent introduction pipe 910 is connected to the liquid discharge pipe 20 near the liquid discharge port 19. For example, it is desirable that the diluent introduction pipe 910 is connected to the liquid discharge pipe 20 in a region within 1 m from the liquid discharge port 19. This makes it possible to suppress the precipitation of silica, calcium, aluminum, magnesium, and the like to form "scale".

[0079] The scrubber apparatus 2 may include a wet cyclone scrubber section 100 shown in FIGS. 1 to 8, and further, the scrubber apparatus 2 may include a dry cyclone scrubber section 200.

[0080] 1 to 8, a dry cyclone scrubber section 200 may be provided upstream of the gas inlet 11. In the dry cyclone scrubber section 200, a swirling space in which the suspension liquid swirls is formed therein.

[0081] FIG. 9 shows an example of a dry cyclone scrubber section 200. The dry cyclone scrubber section 200 has a tube body 201. The tube body 201 has a cylindrical section 202 and a conical section 204 that are connected to each other at their ends. The conical section 204 has a diameter that decreases in the Z-axis direction from one end to the other end. An inlet 206 is provided on the side of the cylindrical section 202. One end of the cylindrical section 202 is connected to one end of the conical section 204. The other end of the conical section 204 is a dust outlet 209. A partition plate 208 that separates the internal space of the dry cyclone scrubber section 200 from the outside world is provided on the other end of the cylindrical section 202. A gas outlet 207 that communicates between the internal space of the dry cyclone scrubber section 200 and the outside world is provided in the center of the partition plate 208.

[0082] The outer cylindrical diameter of the cylindrical portion 202 is Di. The height H of the cylindrical portion 202 is Di, and the height Hl of the conical portion 204 is 2Di. The height of the inlet 206 in the Z-axis direction is Di / 2. The width b of the inlet 206 in the Y-direction is Di / 5. The diameter d' of the gas outlet 207 is 2Di / 5. The diameter d of the dust outlet 209 is 4Di / 5. In this case, the viscosity of the gas is μ (kg / m s), the dust density is ρ (kg / m), the gas velocity at the inlet 206 is u (m / s), and the dust particle density is ρ p (kg / m) In this case, the limit minimum radius D of the particles that can be separated in the dry cyclone scrubber section 200 is pmin is (μb / {πu(ρ p For example, if Di = 0.8 m, the critical minimum radius Dpmin In other words, in one example, suspended solids (silica, etc.) of 7 μm or more can be removed by the dry cyclone scrubber unit 200. The smaller the outer cylinder diameter Di, the smaller the limit minimum radius D of the separable particles. pmin becomes smaller.

[0083] Fig. 10 shows another example of the scrubber unit 2. In the example shown in Fig. 10, the scrubber unit 2 includes a plurality of dry cyclone scrubber sections 200a and 200b having different tube diameters Di. Specifically, the diameter Di_a of the first dry cyclone scrubber section 200a is smaller than the diameter Di_b of the second dry cyclone scrubber section 200b. Therefore, the critical minimum radius D pmin is the critical minimum radius D of the second dry cyclone scrubber section 200a pmin In this embodiment, a switching unit 210 is provided for selecting the dry cyclone scrubber unit 200 that supplies gas to the gas inlet 11 of the wet cyclone scrubber unit 100 from among the multiple dry cyclone scrubber units 200a and 200b. The switching unit 210 is a switching valve in one example. The switching unit 210 can select an appropriate dry cyclone scrubber unit 200 depending on the size of fine particles contained in the gas.

[0084] Figures 1 to 10 have mainly been described using the scrubber unit 2 in a geothermal power generation system 1000 as an example, but the scrubber unit 2 described in Figures 1 to 10 can also be used as a scrubber unit for ships.

[0085] FIG. 11 is a diagram showing an example of a ship system 2000 to which a ship scrubber unit 2a according to one embodiment of the present invention is applied. In the ship scrubber unit 2a, exhaust gas 39 from an internal combustion engine 1300 is treated instead of steam 30 for geothermal power generation. The exhaust gas 39 treated in the wet cyclone scrubber unit 100 is exhausted into the atmosphere. In the case of the ship scrubber unit 2a, by using the scrubber unit 2a equipped with the heating unit 700, the chemical introduction unit 800, and the dilution liquid supply unit 900 as shown in FIG. 2 to FIG. 8, it is possible to suppress and remove "scale" caused by precipitation of silica, calcium, aluminum, magnesium, and the like in the ocean.

[0086] In particular, as shown in Fig. 11, the liquid discharge pipe 20 from the wet cyclone scrubber section 100 may be connected to at least a portion of the pipe body 201 near the dust outlet 209 based on the inlet 206 that takes in the exhaust gas from the internal combustion engine 1300 in the dry scrubber section 200, or the discharge pipe 22 connected downstream of the dust outlet 209. This allows the exhaust liquid 46 from the wet cyclone scrubber section 100 to wash away the exhaust gas dust in the dry scrubber section 200. In particular, it is desirable that the liquid discharge pipe 20 be connected to the pipe body 201 or the discharge pipe 22 of the dry scrubber section 200 near the dust outlet 209. In one example, it is desirable that the liquid discharge pipe 20 be connected to the pipe body 201 or the discharge pipe 22 in an area within 1 m of the dust outlet 209. In the embodiment shown in Figure 1, similarly to the case shown in Figure 11, the liquid discharge pipe 20 may be configured to be connected to a portion of the pipe body 201 of the dry scrubber section 200 or the gas-liquid separation pipe 21 near the dust discharge outlet 209.

[0087] Although the present invention has been described above using the embodiments, the technical scope of the present invention is not limited to the scope described in the above embodiments. It is clear to those skilled in the art that various modifications and improvements can be made to the above embodiments. It is clear from the description of the claims that such modifications and improvements can also be included in the technical scope of the present invention.

[0088] It should be noted that the order of execution of each process, such as operations, procedures, steps, and stages, in the devices, systems, programs, and methods shown in the claims, specifications, and drawings is not specifically stated as "before," "prior to," etc., and may be realized in any order unless the output of a previous process is used in a later process. Even if the operational flow in the claims, specifications, and drawings is explained using "first," "next," etc. for convenience, it does not mean that it is essential to perform the process in this order. [Explanation of symbols]

[0089] 2 scrubber unit, 10 reaction tower, 11 gas inlet, 12 main pipe, 13 branch pipe, 14 jet section, 15 side wall, 16 bottom surface, 17 gas outlet, 18 gas treatment section, 19 liquid outlet, 20 liquid outlet pipe, 21 gas-liquid separation pipe, 22 outlet pipe, 30 steam, 31 hot water, 32 gas inlet pipe, 39 exhaust gas, 40 liquid, 46 drainage liquid, 80 swirl section, 90 liquid spray section, 100 Wet cyclone scrubber section, 102, inlet end, 104, outlet end, 200, dry cyclone scrubber section, 201, tube body, 202, cylindrical section, 204, conical section, 206, inlet, 207, gas outlet, 208, partition plate, 209, dust outlet, 210, switching section, 300, gas outlet, 400, power generation device, 410, turbine, 420, generator, 430, condensate, 500, gas recovery section, 510, recovery tank, 52 0···Cooling tower, 530···Pump, 540···Liquid, 550···Pressure booster, 700···Heating section, 702···Liquid discharge area, 710···Heating pipe, 711···First heating pipe, 712···Second heating pipe, 713···Geothermal water, 720···Pump, 722···Geothermal water temperature adjustment section, 730···Measurement section, 740···Heater section, 741···First heater section, 742···Second heater section, 750···Heater power supply, 752···Heater control section, 800···Drug introduction section inlet, 810...chemical introduction pipe, 813...chemical, 820...pump, 822...chemical container, 824...chemical amount adjustment section, 830...measurement section, 900...diluent supply section, 910...diluent introduction pipe, 913...diluent, 920...pump, 922...regulating valve, 924...dilution amount control section, 930...well condition measurement section, 1000...geothermal power generation system, 1100...production well, 1200...injection well, 1300...internal combustion engine, 2000...ship system

Claims

1. A reaction tower having an internal space; A liquid spray unit that sprays liquid in the internal space; a gas inlet for introducing a gas into the reaction tower; a liquid outlet for discharging a waste liquid generated by a process in which the liquid takes in a substance in the gas to the outside of the reaction tower without circulating the waste liquid to the liquid spray section; a gas outlet section for outletting the treated gas from the reaction tower; a heating unit that is provided in at least a portion of a portion of the reaction tower that is close to the liquid discharge port with respect to the gas inlet and a portion of a liquid discharge pipe that is connected downstream of the liquid discharge port and that heats the discharged liquid. Scrubber equipment.

2. A scrubber apparatus for geothermal power generation, comprising: A reaction tower having an internal space; A liquid spray unit that sprays liquid in the internal space; a gas inlet for introducing a gas into the reaction tower; a liquid outlet for discharging waste liquid generated by the process of the liquid incorporating the substance in the gas from the reaction tower; a gas outlet section for outletting the treated gas from the reaction tower; a heating unit that is provided in at least a portion of a portion of the reaction tower that is close to the liquid discharge port with respect to the gas inlet and a portion of a liquid discharge pipe that is connected downstream of the liquid discharge port, and that heats the discharged liquid; The gas inlet introduces steam used for geothermal power generation as the gas into the reaction tower, The gas outlet supplies the treated steam to a power generation device. Scrubber equipment.

3. A reaction tower having an internal space; A liquid spray unit that sprays liquid in the internal space; a gas inlet for introducing a gas into the reaction tower; a liquid outlet for discharging waste liquid generated by the process of the liquid incorporating the substance in the gas from the reaction tower; a gas outlet section for outletting the treated gas from the reaction tower; a heating unit that is provided in at least a portion of a portion of the reaction tower that is close to the liquid discharge port with respect to the gas inlet and a portion of a liquid discharge pipe that is connected downstream of the liquid discharge port, and that heats the discharged liquid; a dry cyclone scrubber section that has a pipe upstream of the gas inlet, the pipe having a swirling space formed therein in which gas containing suspended solids swirls, and that supplies the gas from which at least a portion of the suspended solids has been removed to the gas inlet. Scrubber equipment.

4. A scrubber apparatus for geothermal power generation, comprising: A reaction tower having an internal space; A liquid spray unit that sprays liquid in the internal space; a gas inlet for introducing a gas into the reaction tower; a liquid outlet for discharging waste liquid generated by the process of the liquid incorporating the substance in the gas from the reaction tower; a gas outlet section for outletting the treated gas from the reaction tower; A drug introduction section for adding a drug to the drainage liquid, The gas inlet introduces steam used for geothermal power generation as the gas into the reaction tower, The gas outlet supplies the treated steam to a power generation device. Scrubber equipment.

5. A reaction tower having an internal space; A liquid spray unit that sprays liquid in the internal space; a gas inlet for introducing a gas into the reaction tower; a liquid outlet for discharging waste liquid generated by the process of the liquid incorporating the substance in the gas from the reaction tower; a gas outlet section for outletting the treated gas from the reaction tower; A drug introduction section for adding a drug to the drainage liquid, a dry cyclone scrubber section that has a pipe upstream of the gas inlet, the pipe having a swirling space formed therein in which gas containing suspended solids swirls, and that supplies the gas from which at least a portion of the suspended solids has been removed to the gas inlet. Scrubber equipment.

6. A scrubber apparatus for geothermal power generation, comprising: A reaction tower having an internal space; A liquid spray unit that sprays liquid in the internal space; a gas inlet for introducing a gas into the reaction tower; a liquid outlet for discharging waste liquid generated by the process of the liquid incorporating the substance in the gas from the reaction tower; a gas outlet section for outletting the treated gas from the reaction tower; a diluent supply unit that is connected to at least a portion of a portion of the reaction tower that is close to the liquid discharge port with respect to the gas inlet and a portion of a liquid discharge pipe that is connected downstream of the liquid discharge port, and that supplies a diluent for diluting the discharged liquid; The gas inlet introduces steam used for geothermal power generation as the gas into the reaction tower, The gas outlet supplies the treated steam to a power generation device. Scrubber equipment.

7. A reaction tower having an internal space; A liquid spray unit that sprays liquid in the internal space; a gas inlet for introducing a gas into the reaction tower; a liquid outlet for discharging waste liquid generated by the process of the liquid incorporating the substance in the gas from the reaction tower; a gas outlet section for outletting the treated gas from the reaction tower; a diluent supply unit that is connected to at least a portion of a portion of the reaction tower that is close to the liquid discharge port with respect to the gas inlet and a portion of a liquid discharge pipe that is connected downstream of the liquid discharge port, and that supplies a diluent for diluting the discharged liquid; a dry cyclone scrubber section that has a pipe upstream of the gas inlet, the pipe having a swirling space formed therein in which gas containing suspended solids swirls, and that supplies the gas from which at least a portion of the suspended solids has been removed to the gas inlet. Scrubber equipment.

8. The scrubber apparatus according to claim 1 , wherein the heating unit heats the effluent to 80° C. or higher.

9. The scrubber unit is a geothermal power generation scrubber unit, The gas inlet introduces steam used for geothermal power generation as the gas into the reaction tower, The scrubber unit according to any one of claims 1, 3, 5 and 7, wherein the gas outlet supplies the treated steam to a power generation unit.

10. The scrubber apparatus according to claim 1 , wherein the heating unit changes a heating temperature of the effluent based on a composition of impurities in the gas or the effluent.

11. The scrubber apparatus according to claim 1 , wherein the heating unit changes a heating temperature of the effluent based on a concentration of silica in the gas or the effluent.

12. A drug introduction section for adding a drug to the drainage liquid. A scrubber apparatus according to any one of claims 1 to 3, 6 and 7.

13. The scrubber apparatus according to claim 12, wherein the agent adjusts the effluent to be acidic.

14. The scrubber apparatus according to claim 12, wherein the agent adjusts the pH of the effluent to 5.5 or less.

15. The scrubber apparatus according to any one of claims 12 to 14, wherein the chemical introduction section adjusts a hydrogen ion concentration of the effluent based on a composition of impurities in the gas or the effluent.

16. The scrubber apparatus according to any one of claims 12 to 15, wherein the chemical introduction section adjusts a hydrogen ion potential of the effluent based on a concentration of silica in the gas or the effluent.

17. a diluent supply unit that is connected to at least a portion of a portion of the reaction tower that is close to the liquid discharge port with respect to the gas inlet and a portion of the liquid discharge pipe that is connected downstream of the liquid discharge port and that supplies a diluent for diluting the discharged liquid. The scrubber apparatus according to claim 2.

18. The scrubber apparatus according to claim 17, wherein the diluent supply unit adjusts the amount of the diluent supplied based on an amount of water in an injection well for returning the steam used for geothermal power generation to an underground geothermal reservoir.

19. The scrubber apparatus according to claim 17 , wherein the diluent supply unit adjusts the amount of the diluent supplied based on the amount of the steam and hot water pumped from the geothermal reservoir in the production well.

20. A pressure increasing device is provided for increasing the pressure of the liquid to be sprayed so that the pressure is higher than the internal pressure of the reaction tower. A scrubber apparatus according to any one of claims 1 to 19.

21. The scrubber apparatus according to any one of claims 1, 2, 4 and 6, further comprising a dry cyclone scrubber section having a pipe upstream of the gas inlet, the pipe having a swirling space formed therein in which gas containing suspended solids swirls, and configured to supply the gas from which at least a portion of the suspended solids has been removed to the gas inlet.

22. The system is equipped with multiple dry cyclone scrubber sections with different pipe diameters, The scrubber apparatus according to claim 21, further comprising a switching unit for selecting a dry cyclone scrubber unit which supplies gas to the gas inlet from among a plurality of dry cyclone scrubber units.

23. The scrubber unit is a marine scrubber unit, The gas inlet introduces exhaust gas from an internal combustion engine of a ship into the reaction tower as the gas, The scrubber apparatus according to claim 1 , wherein the gas outlet section exhausts the treated exhaust gas into the atmosphere.

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