Method for concentrating and recovering specific components in a fluid using renewable energy and renewable energy-based device for concentrating and recovering specific components in a fluid

Abstract

To provide a method for efficiently concentrating and recovering a specific component contained in a gas or liquid by utilizing renewable energy and multiple separation membranes, and a concentration and recovery device for a fluid component utilizing renewable energy that applies the method.SOLUTION: A specific component contained in a fluid is concentrated and recovered by utilizing renewable energy by discharging the specific component contained in the fluid after stepwise concentrating it through a plurality of separation membranes, by means of a multi-stage or multi-cylinder pump, or a plurality of pumps that are connected to be driven to a rotational shaft of a heat engine driven by a heat source of renewable energy, or a hydraulic engine or a wind engine driven by the energy of running water or wind and provided with the plurality of separation membranes at an intake port or on a supply pipe of the fluid containing the specific component to be separated and concentrated.SELECTED DRAWING: Figure 1

Description

[Technical Field]

[0001] The present invention relates to a method for concentrating and recovering specific components contained in a fluid, such as concentrating and recovering carbon dioxide contained in the atmosphere or combustion exhaust gas, or separating and concentrating and recovering carbon dioxide and methane from biogas, by utilizing renewable energy, without emitting carbon dioxide that is associated with the use of fossil fuels or electricity derived from fossil fuels, and to a renewable energy-based fluid component concentration and recovery device to which this method is applied. [Background technology]

[0002] While it is possible to generate electricity and utilize heat using renewable energy, there is a need for technology to effectively utilize unused renewable energy in places where it is difficult to supply electricity via power lines or thermal energy using heat pipes.In particular, there is a need for efficient carbon dioxide separation and capture technology that utilizes unused renewable energy as a measure to prevent global warming and to capture and reduce carbon dioxide that has accumulated in the atmosphere.

[0003] As technologies that can solve these problems, there are disclosed a method in which renewable energy sources that do not increase carbon dioxide, such as geothermal steam, hot spring heat, flowing river water, and heat from biomass combustion, are used to suck in and compress air, combustion exhaust gas, or biogas and supply it to a gas separation membrane, where the carbon dioxide gas contained in the air, combustion exhaust gas, or biogas is compressed, cooled, and recovered as liquefied carbon dioxide or dry ice (Patent Document 1), and a method in which a vacuum pump or suction blower driven by the energy of geothermal fluid or flowing water is provided in the flow path of carbon dioxide gas that permeates the gas separation membrane, and carbon dioxide is sucked and recovered from the air, combustion exhaust gas, or biogas (Patent Document 2). [Prior art documents] [Patent documents]

[0004] [Patent Document 1] Patent Publication No. 2023-10479 [Patent Document 2] Patent Publication No. 2023-36490 DISCLOSURE OF THE INVENTION [Problem to be solved by the invention]

[0005] As described above, the conventional technology disclosed in Patent Document 1 makes it possible to efficiently separate and capture carbon dioxide by utilizing renewable energy, and to recover the captured carbon dioxide as liquefied carbon dioxide or dry ice. However, these technologies have the following two problems.

[0006] First, all of the conventional technologies are equipped with only one carbon dioxide separation membrane or one stage, which means that the concentration of carbon dioxide that can be recovered through the separation membrane is low, or when separation and recovery at a higher concentration is performed, the amount of carbon dioxide separated and recovered decreases.

[0007] Separation membranes that separate and recover specific components contained in gases or liquids typically have two performance indicators: selectivity, which indicates the ability to recover a specific component with high purity, and permeability, which indicates the ability to recover a large amount of a specific component.In addition to the fact that these two performance indicators are in a contradictory relationship, it is difficult to achieve perfect performance for either performance indicator.

[0008] In other words, the more selective a membrane is selected, the lower the permeability and the smaller the amount of separated and recovered, but it is not possible to completely eliminate impurities in the separated and recovered fluid.On the other hand, the more permeable a membrane is selected, the greater the amount of separated and recovered, but the lower the selectivity, so the separated and recovered fluid will contain a large amount of impurities and the concentration of specific components in the separated and recovered fluid will be reduced.

[0009] In particular, in the technology disclosed in the prior art for separating and recovering carbon dioxide contained in air or combustion exhaust gas, nitrogen, the main component in air or combustion exhaust gas, is contained as an impurity in large amounts in the separated and recovered carbon dioxide gas, and in the technology for separating and recovering carbon dioxide from biogas, methane, the main component in biogas, is contained as an impurity in large amounts in the separated and recovered carbon dioxide gas. However, no method for removing these impurities or for suppressing the mixing of impurities has been disclosed, and therefore, when the separated and recovered carbon dioxide is used in commerce and industry, the quality of the gas is reduced, reducing its utility value. Furthermore, when the separated and recovered carbon dioxide is liquefied or converted into dry ice for transportation or underground storage, both nitrogen and methane have physical properties that make them more difficult to liquefy or solidify than carbon dioxide, which hinders the liquefaction or dry ice production process, posing the problem of reducing production efficiency and the quality of the product.

[0010] On the other hand, in order to minimize the influence of the above-mentioned impurities, conventional technologies that apply separation membranes with high selectivity and low permeability increase the purity of the separated and recovered carbon dioxide gas and make it easier to liquefy or turn it into dry ice, but there is a problem that the amount of separated and recovered decreases, limiting production volume.

[0011] Therefore, as a means to solve these problems, a method can be considered in which the concentration of a specific component in the separated and recovered fluid is gradually increased while maintaining the separated and recovered volume by passing the fluid through multiple separation membranes with low selectivity and high permeability in a layered manner, or a method in which a large amount of fluid containing a specific component is first separated and recovered using a separation membrane with low selectivity and high permeability, and then the fluid is passed through separation membranes with gradually changed properties in the second and subsequent stages so that the membranes have higher selectivity and lower permeability than the upstream separation membranes, thereby increasing the separated and recovered concentration while suppressing a decrease in the separated and recovered volume.However, the prior art does not disclose a concentration method using multiple separation membranes as described above, or a method of increasing the purity of the separated and recovered fluid while maintaining the separated and recovered volume by passing the fluid through a combination of separation membranes with different selectivities and permeabilities in multiple stages, and it has been impossible to realize such a method.

[0012] Furthermore, the renewable energy sources that drive gas separation and recovery in conventional technologies are limited to geothermal energy, heat from biomass combustion, or water flow, and no methods are disclosed for using solar heat or wind power as a driving source. As a result, the application of conventional technologies is limited to areas with abundant geothermal resources, biomass resources, and hydroelectric resources, and there is an issue that they cannot be applied to areas with abundant solar radiation or favorable wind conditions.

[0013] On the other hand, solar energy has the problem that it cannot generate electricity or collect heat at night, and the amount of electricity generated and heat collected is unstable depending on the season and weather. Wind energy has the problem that wind conditions change depending on the season and weather, so the driving force for separating and recovering specific components in a fluid fluctuates, and the energy required to compress and cool the separated and recovered components also fluctuates. However, if solar energy could be used in a way that uses solar heat, which has a higher energy conversion efficiency than photovoltaic power generation and can provide a stable energy supply continuously day and night by using heat storage materials and heat medium circulation, or if a method could be applied that is limited to areas where wind energy is constantly available, or if a method that operates only during seasons when a certain amount of wind energy is available is applicable, it would be possible to separate and recover carbon dioxide from outside air in a wide area, but these methods are not disclosed in the prior art. [Means for solving the problem]

[0014] The present invention has been made in consideration of the above-mentioned problems, and its purpose is to provide a method for concentrating and recovering specific components in a fluid using renewable energy, which uses renewable energy including geothermal energy, biomass combustion heat, solar heat, and wind power to concentrate and recover specific components contained in the fluid while maintaining the amount of separation and recovery, and a renewable energy-based device for concentrating and recovering specific components in a fluid to which the above-mentioned method is applied.

[0015] In order to solve the above problem, the invention described in claim 1 is: The system is characterized by comprising a heat engine that uses geothermal fluid, biomass combustion heat, or solar heat as its heat source, and a multi-stage or multi-cylinder pump that is connected to and driven by the rotating shaft of the heat engine directly or via a transmission, and that is equipped with multiple separation membranes on the fluid intake or fluid intake piping for separating specific components contained in the fluid, with the discharge outlet from the first stage or first cylinder connected to the intake of the second or subsequent stage or second or subsequent cylinder, thereby allowing the specific components contained in the fluid to be recovered while being concentrated via the multiple separation membranes.

[0016] The invention described in claim 2 is The system is characterized by comprising a hydraulic engine driven by a water flow as an energy source, and a multi-stage or multi-cylinder pump connected to the rotating shaft of the hydraulic engine directly or via a transmission and equipped with multiple separation membranes for separating specific components contained in the fluid, with the discharge outlet from the first stage or first cylinder connected to the intake port of the second stage or subsequent cylinder, thereby allowing the specific components contained in the fluid to be recovered while being concentrated via the multiple separation membranes.

[0017] The invention described in claim 3 is The system is characterized by comprising a wind engine driven by wind power as an energy source, and a multi-stage or multi-cylinder pump connected to the rotating shaft of the wind engine directly or via a transmission and equipped with multiple separation membranes for separating specific components contained in the fluid, with the discharge outlet from the first stage or first cylinder connected to the intake port of the second stage or second cylinder or later, thereby allowing the specific components contained in the fluid to be recovered while being concentrated via the multiple separation membranes.

[0018] The invention described in claim 4 is The system is characterized by comprising a heat engine that uses geothermal fluid, biomass combustion heat, or solar heat as its heat source, and a plurality of pumps connected to the rotating shaft of the heat engine directly or via a transmission, and equipped with separation membranes for separating specific components contained in the fluid on the fluid intake or fluid intake piping, with the pump discharge outlets connected to the intake ports of pumps in the second stage or later, thereby allowing the specific components contained in the fluid to be recovered while being concentrated through the plurality of separation membranes.

[0019] The invention described in claim 5 is The system is characterized by comprising a hydraulic engine driven by a water flow as an energy source, and a plurality of pumps connected to the rotating shaft of the hydraulic engine directly or via a transmission, and equipped with separation membranes for separating specific components contained in the fluid at the fluid intake or fluid intake piping, with the discharge outlets of the pumps connected to the intake ports of pumps in the second stage or later, thereby allowing the specific components contained in the fluid to be recovered while being concentrated via the plurality of separation membranes.

[0020] The invention described in claim 6 is The system is characterized by comprising a wind engine driven by wind power as an energy source, and a plurality of pumps connected to the rotating shaft of the wind engine directly or via a transmission, and equipped with separation membranes for separating specific components contained in the fluid at the fluid intake or fluid intake piping, with the discharge outlets of the pumps connected to the intake ports of pumps in the second stage or later, thereby allowing the specific components contained in the fluid to be recovered while being concentrated via the plurality of separation membranes.

[0021] The invention described in claim 7 is The present invention is characterized in that a plurality of separation membranes as described in claims 1 to 6 are provided so that the permeability of the separation membranes for separating and recovering specific components gradually decreases while the selectivity gradually increases from the fluid intake port and upstream side to the discharge port and downstream side where the specific components have been separated and concentrated from the fluid.

[0022] The invention described in claim 8 is The discharge port of the multi-stage or multi-cylinder pump described in claims 1 to 3 or the discharge port of the most downstream pump of the plurality of pumps described in claims 4 to 6 is further provided with a compressor connected directly or via a transmission to the rotating shaft described in claims 1 to 3 or claims 4 to 6, and compressing the specific component separated and concentrated from the fluid discharged from the discharge port, and the separated and concentrated specific component is pressurized or liquefied, thereby being recovered as a high-pressure gas or liquid.

[0023] The invention described in claim 9 is The heat engine according to claim 1 or claim 4 is a turbine or reciprocating steam engine that uses geothermal fluid, heat from biomass combustion, or solar heat as a heat source, or a turbine or reciprocating combustion engine that is driven by the combustion energy of biomass fuel.

[0024] The invention described in claim 10 is The pumps described in claims 1 to 6 are characterized in that they are either positive displacement pumps classified as reciprocating pumps or rotary pumps, or non-positive displacement turbo pumps classified as centrifugal pumps, mixed flow pumps or axial flow pumps.

[0025] The invention described in claim 11 is The compressor according to claim 8 is characterized in that it is either a positive displacement compressor classified as a reciprocating compressor, a swash plate compressor, a diaphragm compressor, a screw compressor, a scroll compressor, a rotary compressor, a rotary piston compressor or a sliding vane compressor, or a centrifugal or axial non-positive displacement turbo compressor.

[0026] The invention described in claim 12 is The present invention is characterized in that a heat exchanger is provided at the discharge port of the pump described in claims 1 to 6 or in the piping flow path of the discharge fluid, or at the discharge port of the compressed fluid from the compressor described in claim 8 or in the piping flow path of the compressed fluid, and the heat exchanger is supplied with one or more cold heat sources selected from the cold heat contained in river water, lake water, or seawater, and the cold heat contained in geothermal heat, groundwater heat, or snow and ice heat, or a radiator fan is provided to cool the specific components concentrated and recovered from the fluid using outside air to lower the temperature, or to recover them by condensing, liquefying, or solidifying.

[0027] The invention described in claim 13 is The pump of claim 1 or claim 4 is provided with a heat exchanger at its discharge port or in the piping flow path of the discharged fluid, and further includes an absorption chiller or adsorption chiller that is driven using as a heat source either hot water discharged from the steam-liquid separator for the geothermal fluid of claim 1 or claim 4, or the high-temperature heat contained in the steam, hot water, or heat medium obtained after driving the heat engine of claim 1 or claim 4, and the cold heat obtained from the chiller is supplied to the heat exchanger to cool the specific components concentrated and recovered from the fluid to lower their temperature, or to recover them by condensing, liquefying, or solidifying them.

[0028] The invention described in claim 14 is The present invention is characterized in that a heat exchanger is provided in the discharge port of the pump described in claim 2 or claim 5 or in the piping flow path of the discharged fluid, and cold heat obtained from the flowing water after driving the hydraulic engine described in claim 2 or claim 5 is supplied to the heat exchanger, thereby cooling the specific components concentrated and recovered from the fluid to lower their temperature, or recovering them by condensing, liquefying, or solidifying them.

[0029] The invention described in claim 15 is The pump according to claim 3 or claim 6 is provided with at least one of a radiator that radiates heat to outside air or an electrically driven heat pump refrigerator in the discharge port or in the piping flow path of the discharged fluid, and the specific components that have been concentrated and recovered from the fluid are recovered by lowering the temperature by radiating heat or blowing cold air, or by condensing, liquefying, or solidifying.

[0030] The invention described in claim 16 is The method for concentrating and recovering a fluid component according to claims 1 to 15 is characterized in that it further comprises a measuring device for measuring one or more of the temperature, pressure, flow rate, and concentration of the concentrated and recovered fluid or the fluid of the non-specific component generated during the concentration and recovery process, which is provided at the discharge port of the pump or compressor, in the piping flow path of the discharged fluid, or in the piping flow path for discharging the non-specific component that does not permeate the separation membrane, and one or more flow control valves in the intake port, discharge port, or piping flow path through which the concentrated and recovered fluid or the fluid of the non-specific component generated during the concentration and recovery process flows, and a control device for controlling one or more of the temperature, pressure, flow rate, and concentration of the fluid component to be concentrated and recovered by controlling the opening of the flow control valve based on the measurement value obtained from the measuring device.

[0031] The invention described in claim 17 is The system further comprises a steam turbine generator or a binary generator driven by hot water discharged from the steam-liquid separator of the geothermal fluid as set forth in claim 1 or claim 4, or by high-temperature heat contained in the steam, hot water, or heat medium obtained after driving the heat engine as set forth in claim 1 or claim 4, and the electricity obtained from the generator is supplied to one or more of the absorption chiller or adsorption chiller as set forth in claim 13, the measuring instrument as set forth in claim 16, or a flow control valve or a control device.

[0032] The invention described in claim 18 is The present invention is characterized in that it further comprises a hydroelectric generator driven by the flowing water after driving the hydraulic engine described in claim 2 or claim 5, and the electricity obtained from the generator is supplied to one or more of a water pump that supplies flowing water to the heat exchanger described in claim 14, a measuring instrument described in claim 16, a flow control valve, or a control device to operate them.

[0033] The invention described in claim 19 is The present invention is characterized in that a wind power generator is further provided in the vicinity of the wind engine described in claim 3 or claim 6, and the power obtained from the generator is supplied to one or more of the blower fan or electrically driven heat pump refrigerator mounted on the radiator described in claim 15, the measuring instrument described in claim 16, the flow control valve, or the control device to operate them.

[0034] The invention described in claim 20 is The fluid supplied to the intake port of the pump described in claims 1 to 6 is either biogas, combustion exhaust gas or air, and the separation membrane described in claims 1 to 7 is either a carbon dioxide separation membrane or a methane separation membrane.

[0035] The invention described in claim 21 is The fluid component concentration and recovery device is characterized by being a renewable energy-utilizing fluid component concentration and recovery device that separates and concentrates and recovers specific components contained in a fluid using renewable energy by applying the fluid component concentration and recovery method using renewable energy described in claims 1 to 20.

[0036] [Effects of the Invention]

[0037] According to the present invention, it is possible to concentrate specific components contained in fluids and separate and recover them with high purity, using a wide range of renewable energy sources, including not only geothermal steam, biomass combustion heat, or hydraulic power, but also solar heat and wind power, and targeting not only gases such as air containing carbon dioxide, combustion exhaust gas, and biogas, but also a variety of fluids including liquids containing specific components. [Brief explanation of the drawings]

[0038] [Figure 1] FIG. 1 is a schematic diagram showing a first embodiment of the present invention, which is an apparatus for liquefying and recovering carbon dioxide originating from biomass, which combines a biomass methane fermentation system with a carbon dioxide concentration and recovery apparatus that utilizes geothermal energy in multiple stages. [Figure 2]FIG. 10 is a schematic diagram showing a second embodiment of the present invention, which is an apparatus for liquefying and recovering carbon dioxide originating from biomass, which combines a steam turbine driven by a wood biomass combustion boiler and an apparatus for concentrating and recovering carbon dioxide from boiler exhaust gas. [Figure 3] FIG. 10 is a schematic diagram showing a third embodiment of the present invention, an apparatus for liquefying and recovering carbon dioxide from air, which is driven by a solar-powered steam turbine to concentrate and recover carbon dioxide from the air and liquefy it. [Figure 4] FIG. 10 is a schematic diagram showing an apparatus for liquefying and recovering carbon dioxide in the air, which is a fourth embodiment of the present invention and which concentrates, recovers, and liquefies carbon dioxide in the air by driving a water turbine. [Figure 5] FIG. 10 is a schematic diagram showing an apparatus for liquefying and capturing carbon dioxide in the air, which is a fifth embodiment of the present invention and is driven by a wind turbine to concentrate, capture, and liquefy carbon dioxide in the air. DETAILED DESCRIPTION OF THE INVENTION

[0039] The best mode for carrying out the present invention will be described below with reference to the drawings. The scope of the present invention is defined by the claims and is not limited to the present embodiment.

[0040] (First embodiment)

[0041] First, a biomass-origin carbon dioxide liquefaction and recovery system according to a first embodiment of the present invention, which combines a biomass methane fermentation system with a geothermal energy multistage carbon dioxide concentration and recovery system, will be described with reference to FIG.

[0042] As shown in Figure 1, this system consists of a high-temperature methane fermentation tank 2 that uses anaerobic methane fermentation bacteria to produce biogas composed primarily of methane and carbon dioxide from biomass resources 1 for methane fermentation, such as food waste, inedible agricultural parts, or livestock waste, and a carbon dioxide concentration and recovery system that uses geothermal energy in multiple stages. The carbon dioxide contained in the biogas produced in the methane fermentation tank is separated and concentrated using multiple carbon dioxide separation membranes, and then recovered as biomethane and liquefied carbon dioxide.

[0043] Here, the above-mentioned geothermal energy multistage carbon dioxide concentration and capture system is equipped with a steam turbine 5 driven by the geothermal steam obtained by introducing geothermal fluid 3 containing geothermal steam and hot water into a steam-liquid separator 4 to separate the geothermal fluid 3 into high-temperature, high-pressure geothermal steam and hot water, a geothermal steam turbine-driven multistage carbon dioxide concentration and capture system 6 comprising a plurality of rotating blades directly connected to the rotary drive shaft of the steam turbine and stator blades within an airtight pressure vessel, and a plurality of carbon dioxide separation membranes provided within the vessel, and a heat exchanger that cools and liquefies the high-purity, high-pressure carbon dioxide gas discharged from the outlet of this system with cold water obtained using geothermal energy.

[0044] Furthermore, this equipment is configured to extract and collect biomethane, which is the separation membrane off-gas generated in each compression and concentration process of the multistage carbon dioxide concentration and recovery equipment 6, and store it, and supply the highly concentrated carbon-neutral methane from which the inert gas carbon dioxide has been removed as fuel.This makes it possible to supply biogas derived from biomass as biomethane, which has high ignition and combustibility and a high calorific value, and as liquefied carbon dioxide, which is suitable for transportation and use.

[0045] The multistage carbon dioxide concentration and capture device 6 is configured so that biogas that has passed through a biogas purification filter 7 that removes hydrogen sulfide and excessive humidity contained in the biogas produced in the high-temperature methane fermentation tank 2 is supplied, and when the first-stage intake compression rotor blades 8 rotate by the rotary driving force of the steam turbine 5 to suck and compress the biogas at the intake port, the carbon dioxide gas in the biogas is selectively sucked and compressed by passing the gas through a first carbon dioxide separation membrane 9 provided at the intake port, and is supplied to the second-stage suction compression rotor blades 10.

[0046] Furthermore, the carbon dioxide gas discharged from the second-stage suction compression rotor blades 10 has higher selectivity but lower permeability than the first carbon dioxide separation membrane 9, and therefore requires a higher pressure gas supply and gas suction force.By passing the gas through the second carbon dioxide separation membrane 11 and then suction-supplying it to the third stage, carbon dioxide gas with higher purity and pressure than that of the second stage is supplied to the intake port of the third stage.

[0047] Similarly, the carbon dioxide gas discharged from the third-stage suction compression rotor blades is passed through third carbon dioxide separation membrane 13, which has higher selectivity but lower permeability than second carbon dioxide separation membrane 11, and therefore requires a higher-pressure gas supply and gas suction force.The carbon dioxide gas discharged from the third-stage suction compression rotor blades is then passed through fourth carbon dioxide separation membrane 14, which has higher selectivity but lower permeability than third carbon dioxide separation membrane 13, and therefore requires a higher-pressure gas supply and gas suction force.The pressure of the separated and recovered carbon dioxide gas increases in later stages, and as a result, a higher-pressure gas supply and higher suction force are required.By selecting and providing carbon dioxide separation membranes with higher selectivity in stages, the carbon dioxide gas discharged from the final stage of the device is configured to be high-pressure, high-purity carbon dioxide gas suitable for the cooling and liquefaction process in water-cooled heat exchanger 15.

[0048] In this system, the low-temperature steam discharged from the steam turbine 5 after driving it and the high-temperature water supplied from the steam-liquid separator 4 are supplied to a binary power generation system 16 to generate renewable energy. The electricity obtained is supplied to an absorption chiller 17 driven by the low-temperature steam and hot water after the binary power generation system is in operation, and its associated cooling tower, a cold water circulation pump 18 for circulating the cold water obtained from the chiller to the water-cooled heat exchanger 15, a gas blower 19 for biomethane recovery and storage, measuring devices 20, 21, and 22 that measure the temperature, concentration, and flow rate of the recovered carbon dioxide gas and liquefied carbon dioxide, and the biomethane extracted and recovered as off-gas, flow control valves 23, 24, and 25 that control the biogas supply amount, off-gas recovery amount, and liquefied carbon dioxide recovery flow rate based on the data obtained from the measuring devices, and a control device 26 that controls the opening of these control valves in accordance with the measurement results of the various measuring devices.

[0049] Here, the aperture adjustment of the flow control valve using the control device of this device is desirably controlled so as to maximize the concentration or flow rate of the carbon dioxide gas to be concentrated and recovered, depending on the flow rate and concentration of the carbon dioxide gas to be concentrated and recovered, and the pressure and flow rate in the gas flow path of the biomethane to be extracted and recovered. For example, if the gas flow path pressure of the biomethane to be extracted and recovered becomes excessively high, it will be more likely to be mixed in as an impurity that passes through the separation membrane. Therefore, when the concentration of the carbon dioxide gas to be concentrated and recovered decreases, the aperture of the flow control valve provided in the gas flow path of the biomethane to be extracted and recovered can be opened to reduce the pressure and increase the amount of biomethane to be extracted. This makes it possible to increase the concentration of carbon dioxide to be separated and concentrated while increasing the amount of biomethane to be extracted and recovered.

[0050] In addition, the hot water generated after the absorption chiller is put into operation is used to heat and keep the high-temperature methane fermentation tank 2 warm, promoting methane fermentation before being discharged.By effectively utilizing geothermal energy in multiple stages, including driving a steam turbine for separating and concentrating biogas, a binary power generation facility to supply power for running the system, and driving the absorption chiller to liquefy the separated and concentrated carbon dioxide and heating the methane fermentation tank, it is possible to separate the components of biogas and concentrate and recover carbon dioxide using geothermal energy without emitting carbon dioxide. (Second embodiment)

[0051] Next, a biomass-origin carbon dioxide liquefaction and recovery system according to a second embodiment of the present invention, which combines a woody biomass combustion boiler with a system for concentrating and recovering carbon dioxide from boiler combustion exhaust gas, will be described with reference to FIG.

[0052] As shown in Figure 2, the device of the second embodiment is different in that the carbon dioxide in the combustion exhaust gas generated from the boiler is compressed and supplied to each cylinder from separation membrane 9 to separation membrane 11 and separation membrane 13 by a multi-cylinder carbon dioxide concentration, capture and compression device 28 driven by a crankshaft connected to the rotating shaft of a steam turbine 5 that operates using steam generated by supplying woody biomass to a boiler 27 as a heat source, and the carbon dioxide is concentrated and compressed as it passes through the separation membranes.

[0053] This system is also different in that it is equipped with a woody biomass combustion exhaust gas purification device 29 such as a bag filter or electrostatic precipitator, in order to remove components such as dust and tar contained in the exhaust gas from woody biomass combustion, along with sulfur oxides and nitrogen oxides, before supplying it to the concentration and recovery compressor.In addition, the off-gas generated by the separation membranes between each cylinder is a gas mainly composed of nitrogen and oxygen that can be released into the atmosphere, so the off-gas from each cylinder is bled at the appropriate time by opening and closing control using a cam mechanism via a solenoid valve or crankshaft, and the bleed air is released into the atmosphere without being recovered.

[0054] With this configuration, in the carbon dioxide concentration and recovery process via a separation membrane, it is possible to efficiently concentrate carbon dioxide in combustion exhaust gas originating from woody biomass and recover it as liquefied carbon dioxide as a reciprocating piston compression engine with higher suction and compression efficiency than a non-positive displacement turbine compressor, without providing a large-area separation membrane.

[0055] In this configuration, the separation membranes provided in the connecting flow section between multiple cylinders may be multiple separation membranes with the same characteristics, layered from the upstream side to the downstream side. However, as in the first embodiment, it is preferable to provide a membrane with low selectivity and highest permeability at the most upstream side, and then provide membranes with gradually increasing selectivity and decreasing permeability from the second membrane onwards. (Third embodiment)

[0056] Next, a third embodiment of the present invention, an airborne carbon dioxide liquefaction and recovery system that concentrates, recovers, and liquefies carbon dioxide in the air by being driven by a solar-heat-utilizing steam turbine, will be described with reference to FIG.

[0057] As shown in Figure 3, this device uses solar thermal energy, the amount of energy that can be utilized varying depending on the time of day, weather, and season, to separate and concentrate carbon dioxide in the air and recover it as liquefied carbon dioxide. To this end, first-stage turbo pump 31 and second-stage turbo pump 32 are connected to the rotating shaft of steam turbine 5, which is driven by a continuous supply of solar thermal energy via a circulating heat medium from solar thermal collection system 30 having a heat medium thermal storage tank, and turbo compressor 33 pressurizes the concentrated and recovered carbon dioxide. Air that is purified and supplied through intake air dust removal filter 34 is concentrated and pressurized in stages through carbon dioxide separation membrane 9, separation membrane 11, and separation membrane 13 to become high-purity high-pressure carbon dioxide gas, but is otherwise the same as the other embodiments.

[0058] By adopting such an embodiment, it becomes possible to efficiently separate and capture carbon dioxide from the local outside air in places where solar radiation is available, and then concentrate and liquefy and recover it, without relying on renewable energy resources that are unevenly distributed in different regions, such as geothermal or hydroelectric power.This makes it possible to concentrate and recover carbon dioxide from the air simultaneously and in parallel over a wide area, thereby realizing fixation and resource utilization. (Fourth embodiment)

[0059] Next, a fourth embodiment of the present invention, an apparatus for liquefying and capturing carbon dioxide in the air, which is driven by a water turbine and concentrates and captures carbon dioxide in the air to liquefy it, will be described with reference to FIG.

[0060] As shown in Figure 4, this device uses the same method of concentrating, capturing, and liquefying carbon dioxide contained in the air using a turbo pump and compressor equipped with multiple separation membranes, but it differs in that it uses the energy of flowing river water and the cold energy contained in the river water as its driving source.

[0061] In other words, the driving force for the turbo pump that uses a turbo pump to supply gas to multiple separation membranes and the compressor that pressurizes the separated and concentrated carbon dioxide gas directly utilizes the rotational force of a waterwheel-type torque transmission device 35 installed on the river flow path, and to cool the concentrated high-pressure carbon dioxide gas, a gas cooler 36 that exchanges heat with river water is used, and renewable energy electricity obtained from a hydroelectric power generation facility 37 that generates electricity from the water flow after driving the waterwheel-type torque transmission device 35 is used to drive the pump for cooling with flowing water and to drive the measuring devices and control valves that measure the temperature, pressure, and flow rate of each part of the system.

[0062] With this configuration, it becomes possible to concentrate carbon dioxide in the air and recover it as liquefied carbon dioxide even in areas that lack geothermal or biomass resources but are rich in hydroelectric resources. (Fifth embodiment)

[0063] Next, an airborne carbon dioxide liquefaction and recovery device according to a fifth embodiment of the present invention, which is driven by a wind turbine to concentrate, recover, and liquefy carbon dioxide in the air, will be described with reference to FIG.

[0064] As shown in Figure 5, the device of the fifth embodiment also separates, concentrates, and liquefies carbon dioxide from the air for recovery. However, since the driving force of the turbo pump and compressor when concentrating and recovering carbon dioxide through multiple separation membranes is provided by the wind turbine-type torque transmission device 38, the device's operation is limited to times when the wind turbine is operating stably above a certain level.

[0065] Another difference is that the cold energy supply method used to cool and liquefy the concentrated and recovered high-pressure carbon dioxide gas is performed by an electric heat pump refrigerator 40 that is powered by electricity supplied from a wind power generation facility 39 installed near a windmill-type rotational force transmission device 38 used to operate the carbon dioxide separation and concentration device.

[0066] The operation of the device of the fifth embodiment will be limited to when the wind turbine is operating stably above a certain level. However, in order to ensure stable operation at all times of the measuring instruments and control systems for the temperature, gas concentration, flow rate, etc. of each part of the entire system, including the supply of cold heat to liquefy concentrated high-pressure carbon dioxide, it is desirable to install a large-capacity storage facility 41 next to the wind power generation facility 39 so that it can be used for charging and discharging.

[0067] By adopting such an embodiment, it becomes possible to liquefy and recover carbon dioxide from the air with high efficiency in areas where there are no geothermal or hydroelectric resources, but where the wind speed required to operate the device is stable.

[0068] As described above, in accordance with the diverse renewable energy sources distributed throughout the region, it will be possible to concentrate and recover carbon dioxide emissions from combustion exhaust gases resulting from the use of power generation facilities and heat utilization facilities, thereby suppressing their release into the atmosphere, or to efficiently recover carbon dioxide originating from biomass or carbon dioxide in the atmosphere as liquefied carbon dioxide, which can then be immobilized underground or used for commercial and industrial purposes such as dry ice, or transported and used as a raw material for producing carbon-neutral fuels, etc.

[0069] Furthermore, this technology is not limited to areas with geothermal resources, hydroelectric resources, or biomass resources, which can operate continuously day and night regardless of weather, but can be used in a wide range of regions, including areas where solar heat and wind power resources can be utilized, and will enable the concentration of carbon dioxide contained in the atmosphere and its recovery as liquefied carbon dioxide, which can be easily transported and used, in accordance with local renewable energy resources. [Industrial Applicability]

[0070] The present invention is not limited to the above-described embodiments, and is not limited to, for example, the separation of biogas components or the separation and recovery of carbon dioxide contained in combustion exhaust gas and air. The present technology can also be applied when concentrating and recovering a specific component from a liquid mixture of various components through a separation membrane, or when cooling and solidifying the concentrated and recovered liquid component, or when adiabatically expanding liquefied carbon dioxide to turn it into dry ice and transporting and using it as solid carbon dioxide.

[0071] As such, the above-described embodiments are merely illustrative, and anything that has substantially the same configuration as the technical idea described in the claims of the present invention and exhibits similar effects is included within the technical scope of the present invention. [Explanation of symbols]

[0072] 1. Biomass resources 2. High-temperature methane fermentation tank 3...geothermal fluid 4...Brackish liquid separator 5. Steam turbine 6. Multi-stage carbon dioxide concentration and recovery equipment 7. Biogas purification filter 8. First stage intake compressor blade 9. First carbon dioxide separation membrane 10. Second stage suction / compression rotor blade 11. Second carbon dioxide separation membrane 12. Third stage intake compressor blade 13. The third carbon dioxide separation membrane 14. The fourth carbon dioxide separation membrane 15...Water-cooled heat exchanger 16. Binary power generation facility 17...Adsorption refrigerator 18. Refrigerant Circulation Pump 19. Biomethane Gas Blower 20 Carbon dioxide gas characteristic measuring device 21. Liquefied carbon dioxide characteristic measuring device 22. Biomethane extraction characteristic measurement device 23 Biogas supply flow control valve 24. Off-gas recovery flow control valve 25. Liquefied carbon dioxide recovery flow control valve 26. Multi-stage carbon dioxide concentration and recovery control device 27 Wood biomass boiler 28. Multi-cylinder carbon dioxide concentration and capture compression device 29 Woody biomass combustion exhaust gas purification equipment 30. Solar heat collection system 31 First stage turbopump 32 Second stage turbopump 33 Carbon dioxide gas boost turbo compressor 34···Intake dust filter 35. Waterwheel torque transmission device 36 Gas Cooling Device 37 Hydroelectric Power Plant 38. Windmill-type torque transmission device 39. Wind power generation facilities 40 Electric heat pump refrigerator 41 Large-capacity energy storage facility

Claims

1. A method for concentrating and recovering a fluid component, comprising: a heat engine using geothermal fluid, biomass combustion heat, or solar heat as a heat source; and a multi-stage or multi-cylinder pump connected to and driven by the rotating shaft of the heat engine directly or via a transmission, the multi-stage or multi-cylinder pump having a plurality of separation membranes for separating specific components contained in the fluid on the fluid intake or fluid intake piping, the discharge outlet from the first stage or first cylinder being connected to the intake of the second stage or second cylinder or later, wherein the specific components contained in the fluid are recovered while being concentrated via the plurality of separation membranes.

2. A method for concentrating and recovering a fluid component, characterized in that the method comprises a hydraulic engine driven by a water flow as an energy source, and a multi-stage or multi-cylinder pump connected to the rotating shaft of the hydraulic engine directly or via a transmission, and equipped with a plurality of separation membranes for separating specific components contained in the fluid, such that the discharge outlet from the first stage or first cylinder is connected to the intake port of the second stage or second cylinder or later, thereby recovering the specific components contained in the fluid while concentrating them via the plurality of separation membranes.

3. A method for concentrating and recovering a fluid component, comprising: a wind engine driven by wind power as an energy source; and a multi-stage or multi-cylinder pump connected to the rotating shaft of the wind engine directly or via a transmission, the multi-stage or multi-cylinder pump having a plurality of separation membranes for separating specific components contained in the fluid, the discharge outlet from the first stage or first cylinder being connected to the intake port of the second stage or second cylinder or later, thereby recovering the specific components contained in the fluid while concentrating them via the plurality of separation membranes.

4. 4. The method for concentrating and recovering a fluid component according to claim 1, wherein the plurality of separation membranes are provided so that the permeability of the separation membranes for separating and recovering a specific component gradually decreases while the selectivity gradually increases from an inlet and upstream side for the fluid to an outlet and downstream side where the specific component has been separated and concentrated from the fluid.

5. 4. The method for concentrating and recovering a fluid component using renewable energy according to claim 1, further comprising a compressor connected to the outlet of the multi-stage or multi-cylinder pump, either directly or via a transmission, to the rotary shaft, for compressing the specific component separated and concentrated from the fluid and discharged from the outlet, and wherein the separated and concentrated specific component is pressurized or liquefied, thereby recovering it as a high-pressure gas or liquid.

6. 2. A method for concentrating and recovering a fluid component using renewable energy, as described in claim 1, characterized in that the heat engine is a turbine or reciprocating steam engine using geothermal fluid, biomass combustion heat, or solar heat as a heat source, or a turbine or reciprocating combustion engine driven by the combustion energy of biomass fuel.

7. 4. The method for concentrating and recovering a fluid component according to claim 1, wherein the pump is either a positive displacement pump classified as a reciprocating pump or a rotary pump, or a non-positive displacement turbo pump classified as a centrifugal pump, a mixed flow pump, or an axial flow pump. A method for concentrating and recovering a fluid component using renewable energy.

8. 6. The method for concentrating and recovering a fluid component using renewable energy according to claim 5, wherein the compressor is a positive displacement compressor classified as a reciprocating compressor, a swash plate compressor, a diaphragm compressor, a screw compressor, a scroll compressor, a rotary compressor, a rotary piston compressor, or a slide vane compressor, or a centrifugal or axial non-positive displacement turbo compressor. Recovery method.

9. 4. The method for concentrating and recovering a fluid component according to claim 1, further comprising providing a heat exchanger at the discharge port of the pump or in a piping flow path for the discharged fluid, and supplying to the heat exchanger one or more of cold energy contained in river water, lake water, or seawater, or cold energy contained in geothermal heat, groundwater heat, or snow and ice heat, or providing a radiator fan to cool the specific component concentrated and recovered from the fluid using outside air to lower its temperature, or to recover it by condensing, liquefying, or solidifying it.

10. 2. A method for concentrating and recovering a fluid component using renewable energy, as described in claim 1, characterized in that a heat exchanger is provided at the discharge port of the pump or in the piping flow path of the discharged fluid, and further provided with an absorption or adsorption refrigerator operated using as a heat source hot water discharged from a steam-liquid separator for the geothermal fluid, or the high-temperature heat contained in the steam, hot water, or heat medium obtained after driving the heat engine, and by supplying cold heat obtained from the refrigerator to the heat exchanger, the specific component concentrated and recovered from the fluid is cooled to lower its temperature, or is recovered by condensing, liquefying, or solidifying.

11. 3. A method for concentrating and recovering a fluid component using renewable energy, as described in claim 2, characterized in that a heat exchanger is provided in the discharge port of the pump or in the piping flow path of the discharged fluid, and cold heat obtained from the flowing water after driving the hydraulic engine is supplied to the heat exchanger, thereby cooling the specific component concentrated and recovered from the fluid to lower its temperature, or recovering it by condensing, liquefying, or solidifying it.

12. 4. A method for concentrating and recovering a fluid component using renewable energy, as described in claim 3, characterized in that the pump discharge port or the piping flow path of the discharged fluid is provided with one or more of a radiator that dissipates heat to outside air or an electrically driven heat pump refrigerator, and the specific component concentrated and recovered from the fluid is recovered by lowering the temperature by dissipating heat or blowing cold air, or by condensing, liquefying, or solidifying.

13. 4. The method for concentrating and recovering a fluid component using renewable energy according to claim 1, further comprising: a measuring device, disposed at the discharge port of the pump or in a piping flow path for the discharged fluid, for measuring one or more of the temperature, pressure, flow rate, and concentration of the concentrated and recovered fluid or the fluid of the non-specific component generated in the process of concentration and recovery; and one or more flow control valves disposed in the intake port, discharge port, or piping flow path through which the concentrated and recovered fluid or the fluid of the non-specific component generated in the process of concentration and recovery flows, and a control device for controlling one or more of the temperature, pressure, flow rate, and concentration of the fluid component to be concentrated and recovered by controlling the aperture of the flow control valve based on measurements obtained from the measuring device.

14. 2. The method for concentrating and recovering a fluid component according to claim 1, further comprising: a heat exchanger at the discharge port of the pump or in a piping flow path of the discharged fluid; an absorption or adsorption chiller that supplies cold heat to the heat exchanger; and a steam turbine generator or a binary generator that is driven using, as a heat source, hot water discharged from a steam-liquid separator for the geothermal fluid, or high-temperature heat contained in the steam, hot water, or heat medium obtained after driving the heat engine, and wherein electricity obtained from the generator is supplied to the absorption or adsorption chiller.

15. 12. The method for concentrating and recovering a fluid component using renewable energy as described in claim 11, further comprising a hydroelectric generator driven by the flowing water remaining after driving the hydraulic engine, wherein the electricity obtained from the generator is supplied to a water pump that supplies flowing water to the heat exchanger to operate the water pump.

16. 13. The method for concentrating and recovering a fluid component using renewable energy according to claim 12, further comprising a wind power generator located near the wind engine, and supplying electricity obtained from the generator to the blower fan mounted on the radiator or the electrically driven heat pump refrigerator to operate them.

17. 4. The method for concentrating and recovering a fluid component using renewable energy according to claim 1, wherein the fluid supplied to the suction port of the pump is any one of biogas, combustion exhaust gas, and air.

18. A fluid component concentration and recovery device that utilizes renewable energy, characterized in that by applying the fluid component concentration and recovery method described in any one of claims 1 to 3, specific components contained in a fluid are separated and concentrated and recovered using renewable energy.

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