KR20210039268A - Exhaust gas treatment apparatus - Google Patents

Abstract

Disclosed is an exhaust gas treatment apparatus. According to one embodiment of the present invention, the exhaust gas treatment apparatus includes: a gas-liquid reactor absorbing emission control gas included in exhaust gas by making the emission control gas come in contact with treatment liquid; a treatment liquid supply tank supplying the treatment liquid to the gas-liquid reactor; and a gas-liquid separation treatment liquid regeneration unit regenerating waste treatment liquid, which is the treatment liquid having absorbed the emission control gas, into treatment liquid which does not absorb the emission control gas, and supplying the regenerated treatment liquid to the treatment liquid supply tank. The gas-liquid separation treatment liquid regeneration unit includes a gas-liquid separation membrane through which gas can pass but liquid cannot pass, and the gas-liquid separation membrane divides a liquid flow path in which the waste treatment liquid flows, and a gas flow path in which the emission control gas flows, and the emission control gas having absorbed the waste treatment liquid flows to the gas flow path, in which low emission control gas partial-pressure is formed, through the gas-liquid separation membrane while flowing in the liquid flow path such that the emission control gas can be separated into emission control gas and treatment liquid.

Description

Exhaust gas treatment system {EXHAUST GAS TREATMENT APPARATUS}

The present invention relates to an exhaust gas treatment apparatus for treating exhaust gas.

As regulations on exhaust gas discharged from ships are increasingly being strengthened, there is a need to remove not only sulfur oxides but also carbon dioxide from the exhaust gas discharged from ships.

In order to treat the exhaust gas, an exhaust gas treatment device is installed on the ship, and the exhaust gas treatment device can treat the exhaust gas by injecting a treatment liquid into the exhaust gas. In the exhaust gas treatment system, seawater can be used as a treatment liquid. If seawater is used as a treatment liquid, sulfur oxides can be removed from the exhaust gas. However, since only a small amount of carbon dioxide can be removed, it has been difficult to realize the carbon dioxide reduction performance that can satisfy the Energy Efficiency Design Index of the International Maritime Organization under the UN. In addition, since a relatively large amount of seawater is required to treat exhaust gas, a facility for supplying and spraying a large amount of seawater is required.

In addition, an alkaline aqueous solution such as an aqueous sodium hydroxide solution may be used as the treatment liquid in the exhaust gas treatment apparatus. Although it is possible to treat the exhaust gas with a small amount, it is expensive. In order to reduce the cost, in the exhaust gas treatment apparatus, the waste treatment liquid treated with the exhaust gas can be regenerated and reused, but in the conventional exhaust gas treatment apparatus, the regeneration rate of the waste treatment liquid was low. Accordingly, since the treatment agent must be continuously supplied to the regenerated treatment liquid, the cost has not been greatly reduced. In addition, the equipment used to regenerate the waste treatment liquid is a large equipment applicable to some land, and it is difficult to apply the exhaust gas treatment equipment to the ship.

The present invention has been made by recognizing at least one of the demands or problems occurring in the prior art as described above.

One aspect of the object of the present invention is to reduce the cost for treating exhaust gas in an exhaust gas treatment apparatus.

Another aspect of the object of the present invention is to increase the regeneration rate of the waste treatment liquid treated with exhaust gas.

Another aspect of the object of the present invention is to allow the size of the exhaust gas treatment apparatus to be reduced.

The exhaust gas treatment apparatus according to an embodiment for realizing at least one of the above problems may include the following features.

An exhaust gas treatment apparatus according to an embodiment of the present invention includes a gas-liquid reactor for absorbing and removing the emission control gas by contacting the emission control gas contained in the exhaust gas with a treatment liquid; A treatment liquid supply tank for supplying the treatment liquid to the gas-liquid reactor; And a gas-liquid separation treatment liquid for regenerating the waste treatment liquid, which is a treatment liquid absorbing the discharge control gas, into a treatment liquid not absorbing the discharge control gas, and supplying the recycled treatment liquid to the treatment liquid supply tank. Regeneration unit; Including, wherein the gas-liquid separation treatment liquid regeneration unit includes a gas-liquid separation membrane that passes gas but does not pass liquid, and the gas-liquid separation membrane divides a liquid flow path through which waste treatment liquid flows and a gas flow path through which emission control gas flows And, the emission control gas absorbed in the waste treatment liquid may pass through the gas-liquid separation membrane while flowing through the liquid flow path and move to a gas flow path in which a low emission control gas partial pressure is formed, and may be separated into an emission control gas and a treatment liquid.

In this case, a waste treatment liquid drain pipe connected to the gas-liquid reactor may be connected to one side of the liquid flow path, and the other side of the liquid flow path may be connected to the treatment liquid supply tank by a treatment liquid recovery pipe.

In addition, the waste treatment liquid drain pipe may be provided with a filtration treatment unit for filtering contaminants other than the emission control gas contained in the waste treatment liquid.

In addition, a gas recovery pipe provided with a vacuum pump is connected to one side of the gas flow path so that a low partial pressure of the emission regulation gas is formed in the gas flow path.

In addition, an air inlet pipe provided with a flow control valve is connected to the other side of the gas flow path, so that the partial pressure of the emission regulation gas formed in the gas flow path can be adjusted.

In addition, the gas-liquid separation membrane may be a hollow fiber membrane in which the gas flow path or the liquid flow path is formed.

In addition, the gas-liquid reactor may include a housing connected to an exhaust gas discharge device, and a treatment liquid injection unit for injecting a treatment liquid into the exhaust gas flowing through the housing.

In addition, the treatment liquid injection unit is connected to the treatment liquid supply tank and passes through one surface of the housing, and a treatment liquid flow pipe provided inside the housing, and a treatment provided in a portion of the treatment liquid flow pipe provided inside the housing. It may include a liquid injection nozzle.

In addition, a heat exchanger may be connected to the treatment liquid supply tank to cool the treatment liquid stored in the treatment liquid supply tank.

In addition, the emission control gas may be sulfur oxide or carbon dioxide, and the treatment liquid may be seawater or an alkaline aqueous solution.

As described above, according to the embodiment of the present invention, the waste treatment liquid can be regenerated by the gas-liquid separation treatment liquid regeneration unit that separates the emission control gas from the waste treatment liquid treated with the exhaust gas.

In addition, according to an embodiment of the present invention, the regeneration rate of the waste treatment liquid treated with exhaust gas can be increased.

And also, according to the embodiment of the present invention, the cost for treating exhaust gas in the exhaust gas treatment apparatus can be reduced.

And also, according to the embodiment of the present invention, the size of the exhaust gas treatment apparatus can be reduced.

1 is a view showing a first embodiment of an exhaust gas treatment apparatus according to the present invention.
2 is a view showing another embodiment of the gas-liquid separation treatment liquid regeneration unit of the first embodiment of the exhaust gas treatment apparatus according to the present invention.
3 is a view showing an embodiment of a gas processing unit of the first embodiment of the exhaust gas processing apparatus according to the present invention.
4 is a view showing another embodiment of the gas treatment unit of the first embodiment of the exhaust gas treatment apparatus according to the present invention.
5 is a view showing a second embodiment of an exhaust gas treatment apparatus according to the present invention.
6 is a diagram showing a third embodiment of an exhaust gas treatment apparatus according to the present invention.
7 is a diagram showing a fourth embodiment of an exhaust gas treatment apparatus according to the present invention.

In order to help understand the features of the present invention as described above, an exhaust gas treatment apparatus related to an embodiment of the present invention will be described in more detail below.

The embodiments described below will be described on the basis of embodiments most suitable for understanding the technical features of the present invention, and the technical features of the present invention are not limited by the described embodiments, but will be described below. It is to illustrate that the present invention can be implemented as in the embodiments. Accordingly, the present invention can be variously modified within the technical scope of the present invention through the embodiments described below, and such modified embodiments will fall within the technical scope of the present invention. And, in the reference numerals in the accompanying drawings in order to help understand the embodiments described below, related elements among the elements that perform the same function in each embodiment are indicated by numbers on the same or extension lines.

First embodiment of the exhaust gas treatment apparatus

Hereinafter, a first embodiment of an exhaust gas treatment apparatus according to the present invention will be described with reference to FIGS. 1 to 4.

1 is a view showing a first embodiment of an exhaust gas treatment apparatus according to the present invention, and FIG. 2 is a view showing another embodiment of a gas-liquid separation treatment liquid regeneration unit of the first embodiment of the exhaust gas treatment apparatus according to the present invention. to be.

3 is a view showing an embodiment of the gas treatment unit of the first embodiment of the exhaust gas treatment apparatus according to the present invention, and FIG. 4 is a view showing the gas treatment unit of the first embodiment of the exhaust gas treatment apparatus according to the present invention. It is a diagram showing another embodiment.

The first embodiment of the exhaust gas treatment apparatus according to the present invention may include a gas-liquid reactor 200, a treatment liquid supply tank 300, and a gas-liquid separation treatment liquid regeneration unit 400.

In the gas-liquid reactor 200, exhaust gas discharged from an exhaust gas discharge device (not shown) such as an engine or a boiler may flow into the gas-liquid reactor 200. Further, in the gas-liquid reactor 200, the exhaust gas and the processing liquid are brought into contact with each other so that the emission control gas contained in the exhaust gas is absorbed and removed by the processing liquid. The emission control gas may be, for example, sulfur oxides or carbon dioxide. However, any emission regulation is possible as long as emission to the atmosphere such as nitrogen oxides is regulated. The gas-liquid reactor 200 may include a housing 210 and a treatment liquid injection unit 220.

The housing 210 may be connected to an exhaust gas discharge device. The housing 210 may be provided with an inlet 211, an outlet 212, and a drain 213. 1, the inlet 211 is provided on the lower side of the housing 210, the outlet 212 is provided on the upper surface of the housing 210, and the drain hole 213 is on the lower surface of the housing 210. It can be provided. However, the portion of the housing 210 in which the inlet 211, the outlet 212, or the drain 213 is provided is not particularly limited.

The inlet 211 may be connected to an exhaust gas discharge device. Accordingly, the exhaust gas discharged from the exhaust gas discharge device may flow into the housing 210 through the inlet 211 as shown in FIG. 1 and flow inside the housing 210.

A treatment liquid may be sprayed into the housing 210 by the treatment liquid injection unit 220 as shown in FIG. 1. Accordingly, the exhaust gas flowing into the housing 210 may contact the processing liquid. In this way, when the exhaust gas comes into contact with the treatment liquid, emission control gas contained in the exhaust gas, such as sulfur oxide or carbon dioxide, can be absorbed by the treatment liquid and removed from the exhaust gas. The exhaust gas from which the emission control gas has been removed may be discharged through the discharge port 212. In addition, the waste treatment liquid, which is a treatment liquid that has absorbed the discharge regulation gas, may be drained through the drain port 213.

A packing 230 may be provided inside the housing 210. The packing 230 may increase a contact area and a contact time between the exhaust gas and the treatment liquid. Accordingly, the treatment efficiency of the exhaust gas by the treatment liquid can be improved. The packing 230 may include a plurality of members having a plurality of holes formed thereon. In addition to the packing 230, a configuration in which the contact area and the contact time between the exhaust gas and the processing liquid may be increased, such as the packing 230, may be provided inside the housing 210.

The housing 210 may have a rectangular cross section. The housing 210 may be installed inside a stack (not shown) of, for example, a ship (not shown). The ship's stack may have a rectangular cross section. In addition, as described above, if the cross section of the housing 210 has a square shape, when the housing 210 is installed in the stack of a ship having a square cross section, the dead area, which is an unusable space, can be minimized. When installing the housing 210 on the stack of the ship, the stack may be extended, for example, in the fore or stern direction of the ship. If the cross-sectional shape of the housing 210 is rectangular, the dead area can be minimized when installed in the stack of a ship having a rectangular cross-section as described above, so that the expanded area of the stack for installation of the housing 210 can be minimized. have. Accordingly, it is possible to easily install the housing 210 of the ship's stack, save time and materials, etc. for installation of the housing 210 on the stack, and the space utilization of the ship may be improved. .

The treatment liquid injection unit 220 may inject the treatment liquid into the exhaust gas flowing through the housing 210. The treatment liquid injection unit 220 may include a treatment liquid flow pipe 221 and a treatment liquid injection nozzle 222.

The treatment liquid flow pipe 221 may be connected to the treatment liquid supply tank 300. The treatment liquid flow pipe 221 may be connected to the treatment liquid supply tank 300 by the treatment liquid supply pipe LP as shown in FIG. 1. A treatment liquid supply pump PP may be provided in the treatment liquid supply pipe LP. In addition, when the treatment liquid supply pump PP is driven, the treatment liquid stored in the treatment liquid supply tank 300 may flow through the treatment liquid flow pipe 221.

The treatment liquid flow pipe 221 may pass through one surface of the housing 210 and may be provided inside the housing 210. In addition, the treatment liquid injection nozzle 222 may be provided in a portion of the treatment liquid flow pipe 221 provided in the housing 210. Accordingly, the treatment liquid flowing through the treatment liquid flow pipe 221 may be injected into the exhaust gas flowing inside the housing 210 through the treatment liquid injection nozzle 222 as shown in FIG. 1.

The treatment liquid supply tank 300 may supply the treatment liquid to the gas-liquid reactor 200. The treatment liquid may be stored in the treatment liquid supply tank 300. The treatment liquid stored in the treatment liquid supply tank 300 may be, for example, seawater or an alkaline aqueous solution such as an aqueous sodium hydroxide solution. However, the treatment liquid stored in the treatment liquid supply tank 300 is not particularly limited, and the treatment liquid is injected into the exhaust gas and is in contact with the exhaust gas to absorb the emission regulation gas contained in the exhaust gas, and the gas-liquid separation treatment liquid regeneration unit 400 ), as long as the emission control gas can be separated and regenerated, anything known is possible.

One side of the treatment liquid supply pipe LP may be connected to the treatment liquid supply tank 300 as shown in FIG. 1. The other side of the treatment liquid supply pipe LP may be connected to the treatment liquid flow pipe 221 of the treatment liquid injection unit 220. And, when the treatment liquid supply pump (PP) of the treatment liquid supply pipe (LP) is driven, the treatment liquid from the treatment liquid supply tank 300 can be supplied to the treatment liquid injection unit 220 through the treatment liquid supply pipe (LP). have.

One side of the treatment liquid recovery pipe LR may be connected to the treatment liquid supply tank 300. The other side of the treatment liquid recovery pipe LR may be connected to the gas-liquid separation treatment liquid regeneration unit 400. In addition, the treatment liquid regenerated in the gas-liquid separation treatment liquid regeneration unit 400 may be supplied to and stored in the treatment liquid supply tank 300 through the treatment liquid recovery pipe LR as shown in FIG. 1.

Meanwhile, as shown in FIG. 1, the treatment agent supply tank 600 may be connected to the treatment liquid recovery pipe LR by the treatment agent supply pipe LT. Accordingly, a treatment agent stored in the treatment agent supply tank 600, for example, an alkali agent such as sodium hydroxide, may be supplied to the regenerated treatment liquid flowing through the treatment liquid recovery pipe LR through the treatment agent supply pipe LT. In addition, the treatment agent supply pipe (LT) is connected to the treatment liquid supply tank 300, not the treatment liquid recovery pipe (LR), as shown in FIG. 5, and the treatment agent supply tank to the treatment liquid stored in the treatment liquid supply tank 300. It is also possible to supply the treatment agent stored in 600.

A heat exchanger (HE) may be connected to the treatment liquid supply tank 300 as shown in FIG. 1. The heat exchanger (HE) may heat exchange with the treatment liquid stored in the treatment liquid supply tank 300 to cool the treatment liquid to a temperature that can relatively well absorb the emission control gas contained in the exhaust gas. The treatment liquid absorbs the emission control gas contained in the exhaust gas in the gas-liquid reactor 200 to become a waste treatment liquid, and the temperature may be increased by the hot exhaust gas. In this way, when the waste treatment liquid whose temperature is higher than that of the treatment liquid before being sprayed into the gas-liquid reactor 200 is regenerated in the gas-liquid separation treatment liquid regeneration unit 400, the regenerated treatment liquid is also before being sprayed into the gas-liquid reactor 200. The temperature may be higher than that of the treatment liquid. When the treatment liquid whose temperature has risen as described above is supplied to the treatment liquid supply tank 300, the temperature of the treatment liquid stored in the treatment liquid supply tank 300 rises, so that the absorption rate of the discharge regulation gas of the treatment liquid may be lowered. However, as described above, when the temperature of the treatment liquid stored in the treatment liquid supply tank 300 is cooled to a temperature capable of relatively well absorbing the emission control gas contained in the exhaust gas by the heat exchanger (HE), the treatment liquid Emission control gas absorption rate may not be lowered.

The gas-liquid separation treatment liquid regeneration unit 400 separates the discharge control gas from the waste treatment liquid, which is a treatment liquid that has absorbed the discharge control gas, drained from the gas-liquid reactor 200 and regenerates it as a treatment liquid, and treats the recycled treatment liquid. It can be supplied to the liquid supply tank 300. In this way, since the treatment liquid can be recycled and reused, the cost required to treat the exhaust gas can be reduced.

As shown in Fig. 1, one side of the waste treatment liquid drainage pipe LD is connected to the drain 213 of the gas-liquid reactor 200, and the other side of the waste treatment liquid drainage pipe LD is a gas-liquid separation treatment liquid regeneration unit 400. Can be connected to. Accordingly, the waste treatment liquid drained through the drain 213 of the gas-liquid reactor 200 may flow to the gas-liquid separation treatment liquid regeneration unit 400 through the waste treatment liquid drainage pipe LD. In this case, the waste treatment liquid drain pipe LD may be provided with a booster pump PB as shown in FIG. 4.

The waste treatment liquid drainage pipe LD may be provided with a filtration treatment unit (WTS) that filters and treats pollutants other than the emission control gas contained in the waste treatment liquid, as shown in FIG. 1. Pollutants other than emission control gas contained in the waste treatment liquid include particulate matter and oil. The filtration treatment unit (WTS) may filter pollutants excluding emission control gas contained in the waste treatment liquid flowing to the gas-liquid separation treatment liquid regeneration unit 400 through the waste treatment liquid drainage pipe LD. Accordingly, for example, particulate matter, oil, etc. contained in the waste treatment liquid are filtered by the filtration treatment unit (WTS), thereby minimizing pollutants contained in the treatment liquid regenerated in the gas-liquid separation treatment liquid regeneration unit 400 Accordingly, the performance of the gas-liquid separation membrane 420 included in the gas-liquid separation treatment liquid regeneration unit 400 can be protected. The filtration treatment unit (WTS) can filter particulate matter, oil, etc. from the waste treatment liquid using, for example, a filter (not shown) or centrifugal force. However, the configuration in which the filtration treatment unit (WTS) filters particulate matter, oil, etc. from the waste treatment liquid is not particularly limited, and any known configuration may be used.

As shown in FIG. 1, one side of the treatment liquid recovery pipe LR may be connected to the gas-liquid separation treatment liquid regeneration unit 400, and the other side of the treatment liquid recovery pipe LR may be connected to the treatment liquid supply tank 300. have. Accordingly, the treatment liquid regenerated in the gas-liquid separation treatment liquid regeneration unit 400 may be supplied to the treatment liquid supply tank 300 through the treatment liquid recovery pipe LR and may be reused as a treatment liquid.

The gas-liquid separation treatment liquid regeneration unit 400 includes a gas-liquid separation membrane 420 that passes gas but does not pass through the liquid. The flowing gas flow path 412 can be partitioned. The emission control gas passes through the gas-liquid separation membrane 420 of the present invention, but the waste treatment liquid does not pass through the gas-liquid separation membrane 420.

In addition, a low partial pressure of the emission regulation gas is formed in the gas flow path 412, so that the emission regulation gas absorbed in the waste treatment liquid flows through the liquid flow line 411 and passes through the gas-liquid separation membrane 420, thereby reducing the partial pressure of the emission regulation gas. By moving to the formed gas flow path 412, it is possible to separate the emission control gas and the treatment liquid. Low partial pressure of emission control gas means a state in which the concentration of emission control gas is low. When the carbon dioxide of the emission control gas is described as an example, the concentration of carbon dioxide is low in the gas flow path 412 and a low partial pressure of carbon dioxide is formed. The lower the partial pressure, the lower the solubility of the gas in the liquid, so that the emission control gas absorbed in the waste treatment liquid flows through the liquid flow path 411 and passes through the gas-liquid separation membrane 420 to form a gas flow with a low emission control gas partial pressure. It moves to the furnace 412. Negative pressure can be applied to create a low emission control gas partial pressure, or the emission control gas can be diluted with sweeping air. In this way, the emission control gas absorbed in the waste treatment liquid flows through the liquid flow path 411 and passes through the gas-liquid separation membrane 420 and moves to the gas flow path 412 where the partial pressure of the emission control gas is formed. The emission control gas can be easily separated from

A gas-liquid separation membrane 420 that passes gas but does not pass through a liquid is used, and a low emission control gas partial pressure is formed in the gas flow path 412 partitioned by the gas-liquid separation membrane 420, thereby separating the emission control gas from the waste treatment liquid. Thus, the waste treatment liquid can be regenerated into a treatment liquid that does not absorb the emission control gas. In the case of using such a method, since the amount of the treatment agent to be supplied to the regenerated treatment liquid can be reduced, the cost required to regenerate the waste treatment liquid can be reduced. Thus, the cost required to treat the exhaust gas can be reduced. In addition, since the size of the gas-liquid separation treatment liquid regeneration unit 400 can be made relatively small, the size of the exhaust gas treatment device 100 can be reduced. The device 100 can be easily installed.

The gas-liquid separation treatment liquid regeneration unit 400 may include a separation unit body 410 as shown in FIG. 1. The separation unit body 410 may be divided into a liquid flow path 411 and a gas flow path 412 by a gas-liquid separation membrane 420.

1, a waste treatment liquid drainage pipe LD connected to the drain 213 of the gas-liquid reactor 200 is connected to one side of the liquid flow path 411, and the other side of the liquid flow path 411 is processed. It may be connected to the treatment liquid supply tank 300 by the liquid recovery pipe LR. Accordingly, the waste treatment liquid drained through the drain 213 of the gas-liquid reactor 200 flows into the liquid flow path 411 to flow through the liquid flow path 411. And, while flowing through the liquid flow path 411, the discharge regulation gas is separated and the regenerated treatment liquid flows into the treatment liquid recovery pipe LR and flows to the treatment liquid supply tank 300 through the treatment liquid recovery pipe LR. can do.

A gas recovery pipe LG equipped with a vacuum pump PV may be connected to one side of the gas flow path 412 as shown in FIG. 1. Accordingly, when the vacuum pump PV is driven, a low partial pressure of the emission regulation gas may be formed in the gas flow path 412. In addition, an air inlet pipe LA provided with a flow control valve VC may be connected to the other side of the gas flow path 412. Thereby, while the vacuum pump (PV) is driven, by operating the flow control valve (VC) to control the flow rate of air flowing into the air inlet pipe (LA), The partial pressure of the emission control gas can be adjusted.

The gas-liquid separation membrane 420 may be a hollow fiber membrane in which a gas flow path 412 is formed as shown in FIG. 1. Accordingly, the internal space of the separation unit body 410 other than the gas-liquid separation membrane 420 may become the liquid flow path 411. In addition, the gas-liquid separation membrane 420 may be a hollow fiber membrane in which a liquid flow path 411 is formed, as shown in FIG. 2. In this case, the internal space of the separation unit body 410 other than the gas-liquid separation membrane 420 may be the gas flow path 412. However, the gas-liquid separation membrane 420 is not particularly limited, and the discharge regulation gas passes but the waste treatment liquid does not pass, and the liquid flow path 411 through which the waste treatment liquid flows through the separation unit body 410 and discharge control As long as it can be divided into the gas flow path 412 through which gas flows, any of the well-known things such as flat membranes may be used.

When high sulfur fuel is used in the exhaust gas discharge device, a relatively large amount of sulfur oxides is contained in the exhaust gas discharged from the exhaust gas discharge device. As such, when the exhaust gas containing a large amount of sulfur oxide flows into the housing 210 of the gas-liquid reactor 200, the treatment liquid injected into the exhaust gas by the treatment liquid injection unit 220 is sulfur oxide contained in the exhaust gas. Is mainly removed from the exhaust gas. That is, in the gas-liquid reactor 200, the exhaust gas is desulfurized by the treatment liquid. As described above, the waste treatment liquid from which the sulfur oxides are removed from the exhaust gas contains sulfur oxides, and the gas-liquid separation treatment liquid regeneration unit 400 separates the emission control gas, which is sulfur oxides such as sulfur dioxide, from the waste treatment liquid.

When low sulfur fuel is used in the exhaust gas discharge device, relatively little sulfur oxides are contained in the exhaust gas discharged from the exhaust gas discharge device. As described above, when the exhaust gas containing less sulfur oxide is introduced into the housing 210 of the gas-liquid reactor 200, the treatment liquid injected into the exhaust gas by the treatment liquid injection unit 220 absorbs carbon dioxide contained in the exhaust gas. It is mainly removed from exhaust gas. Carbon dioxide is included in the waste treatment liquid from which carbon dioxide is removed from the exhaust gas, and carbon dioxide is separated from the waste treatment liquid in the gas-liquid separation treatment liquid regeneration unit 400.

The first embodiment of the exhaust gas treatment apparatus 100 according to the present invention may further include a gas treatment unit 500. The gas treatment unit 500 may process emission control gas separated from the waste treatment liquid in the gas-liquid separation treatment liquid regeneration unit 400.

In the gas treatment unit 500, the emission control gas may be dissolved in seawater in an eco-friendly ionic state to be treated. For example, in the gas treatment unit 500, carbon dioxide, which is an emission control gas, can be treated by dissolving it in seawater with natural eco-friendly ionized substances such as carbonic acid, bicarbonate, and carbonate, and in the case of sulfur oxide, natural state such as sulfuric acid and sulfate. It can be treated by dissolving it in seawater as an eco-friendly ionizing material of

To this end, the gas treatment unit 500 may include a seawater flow pipe 510 to which seawater flows and a gas recovery pipe (LG) connected to the gas-liquid separation treatment liquid regeneration unit 400 is connected as shown in FIG. 3. have. The seawater flow pipe 510 may be, for example, a cooling water pipe, a ballast water pipe, or a sea chest provided on a ship. However, the seawater flow pipe 510 is not particularly limited, and any known one may be used as long as the seawater flows.

A portion of the seawater flow pipe 510 to which the gas recovery pipe LG is connected may be branched into a plurality as shown in FIG. 3. In addition, the gas recovery pipe LG may be branched and connected to portions of the branched seawater flow pipe 510, respectively.

As described above, when the seawater flow pipe 510 is branched into a plurality, the flow rate of seawater decreases, so that sufficient time for the emission control gas to be dissolved in the seawater in an eco-friendly ion state can be secured. Dissolution in seawater in an eco-friendly ionic state can be made better. In addition, as shown in Figure 3, the seawater flow pipe 510 may be provided with a pressure control device (VCP). Thereby, by increasing the pressure of the seawater flowing through the seawater flow pipe 510, the emission control gas can be easily dissolved in the seawater in an eco-friendly ion state.

The gas processing unit 500 may further include a microbubble generator 520 provided in the seawater flow pipe 510 to be connected to the gas recovery pipe LG as shown in FIG. 3. In the microbubble generator 520, the emission control gas may be mixed with the seawater flowing through the seawater flow pipe 510 as fine bubbles. For example, a plurality of micropores 521 are formed in the microbubble generator 520 so that the emission control gas flowing through the gas recovery pipe LG passes through the micropores 521 and flows through the seawater flow pipe 510 with microbubbles. It can be mixed in seawater. In this way, when the emission control gas is mixed with the seawater flowing through the seawater flow pipe 510 as fine bubbles, the dissolution of the emission control gas into the seawater in an eco-friendly ionic state can be made better.

The gas processing unit 500 may further include a gas mixer 530. The gas mixer 530 may be provided in a portion of the seawater flow pipe 510 next to the microbubble generator 520 in the flow direction of seawater as shown in FIG. 3. In addition, the emission control gas bubbles generated in the microbubble generator 520 and supplied to the seawater flowing through the seawater flow pipe 510 may be mixed with the seawater. For example, the gas mixer 530 may be provided so that the screw-shaped mixing member 531 rotates, so that the emission control gas bubbles supplied to the seawater of the seawater flow pipe 510 and seawater may be mixed. Accordingly, it is possible to better dissolve the emission control gas into seawater in an eco-friendly ionic state.

As described above, the branched seawater flow pipe 510 may be collected again and connected to the sea (SEA) as shown in FIG. 3. Accordingly, seawater in which the emission control gas is dissolved in an eco-friendly ionic state can be drained into the sea (SEA). As shown in FIG. 3, a water quality measurement sensor SP may be provided at a portion of the seawater flow pipe 510 through which seawater dissolved in an environment-friendly ionic state is discharged into the sea.

In addition, the gas treatment unit 500 may dissolve the emission control gas in the fresh water flowing through the fresh water flow pipe (not shown) in an eco-friendly ion state to be treated.

Meanwhile, the gas treatment unit 500 may store and treat the emission control gas separated from the waste treatment liquid in the gas-liquid separation treatment liquid regeneration unit 400. In some areas of the sea (SEA), a no-discharge condition is required in which no material is discharged from ships or the like. Accordingly, in the case of a ship running in such an area, the gas treatment unit 500 may store the emission control gas separated from the waste treatment liquid in the gas-liquid separation treatment liquid regeneration unit 400. In this way, the emission control gas stored in the gas processing unit 500 may be supplied to a place of use.

The gas processing unit 500 may include a gas storage tank 540 to which a gas recovery pipe LG is connected to store emission control gas, as shown in FIG. 4.

The emission control gas separated from the waste treatment liquid in the gas-liquid separation treatment liquid regeneration unit 400 may be stored in the gas storage tank 540 through a gas recovery pipe LG. In the gas storage tank 540, the emission control gas is cooled and compressed to liquefy the emission control gas, thereby storing the emission control gas in a liquid state. In this way, the emission control gas stored in a liquid state in the gas storage tank 540 may be supplied to a user.

Second Embodiment of Exhaust Gas Treatment System

Hereinafter, a second embodiment of an exhaust gas treatment apparatus according to the present invention will be described with reference to FIG. 5.

5 is a view showing a second embodiment of an exhaust gas treatment apparatus according to the present invention.

Here, the second embodiment of the exhaust gas treatment apparatus according to the present invention is the first embodiment of the exhaust gas treatment apparatus according to the present invention described with reference to FIGS. 1 to 4 above, and exhaust from the gas-liquid reactor 200. The difference is that the sulfur oxide contained in the gas is absorbed and removed by the first treatment liquid, and the carbon dioxide contained in the exhaust gas from which the sulfur oxide is removed is absorbed and removed by the second treatment liquid. And, for this purpose, a first removal region RR1 in which the exhaust gas and the first treatment liquid are in contact with the gas-liquid reactor 200 to remove sulfur oxide, and a second removal region RR1 in which the exhaust gas and the second treatment liquid are in contact with each other to remove carbon dioxide. The difference is that the removal region RR2 and the connection region RC connecting the first removal region RR1 and the second removal region RR2 are provided.

Therefore, hereinafter, the differentiated parts will be mainly described, and the remaining configurations may be replaced with those described with reference to FIGS. 1 to 4.

In the gas-liquid reactor 200 of the second embodiment of the exhaust gas treatment apparatus 100 according to the present invention, the sulfur oxide contained in the exhaust gas is absorbed and removed by the first treatment liquid, and carbon dioxide contained in the exhaust gas from which the sulfur oxide is removed. May be absorbed and removed by the second treatment liquid.

When a treatment liquid, for example an alkaline aqueous solution, is injected into the exhaust gas containing both sulfur oxide and carbon dioxide, the sulfur oxide may be first removed from the exhaust gas. Therefore, in order to remove carbon dioxide from the exhaust gas, sulfur oxides contained in the exhaust gas must be removed first. As described above, when the first treatment liquid absorbs and removes the sulfur oxide contained in the exhaust gas, and the second treatment liquid absorbs and removes the carbon dioxide contained in the exhaust gas from which the sulfur oxide has been removed, sulfur oxides and sulfur oxides from the exhaust gas and It can remove all carbon dioxide. In addition, even when the exhaust gas contains less sulfur oxides, since the sulfur oxides can be removed first, the carbon dioxide removal rate can be further improved.

The gas-liquid reactor 200 includes a first removal region RR1 in which sulfur oxides are removed by contacting the exhaust gas with the first treatment liquid, and a second removal region RR2 in which carbon dioxide is removed by contacting the exhaust gas with the second treatment liquid. ), and a connection region RC connecting the first removal region RR1 and the second removal region RR2.

To this end, the housing 210 of the gas-liquid reactor 200 has a first removal region RR1 and a second removal region RR2 and a connection region inside by a plurality of partition walls WD, as shown in FIG. 5. It can be divided into (RC).

In this case, in the first removal region RR1 and the second removal region RR2, the exhaust gas flows from the bottom to the top, and in the connection area RC, the exhaust gas flows from the top to the bottom. ) May be provided inside the housing 210.

For example, as shown in FIG. 5, two partition walls WD are provided inside the housing 210, respectively, so that the inside of the housing 210 is provided with a first removal region RR1 and a second removal region RR2. It can be divided into a connection area (RC). That is, one partition wall WD divides the interior of the housing 210 into the first removal region RR1 and partitions a part of the connection region RC, and the other partition wall WD controls the interior of the housing 210. 2 The remainder of the connection area RC may be divided while being divided into the removal area RR2.

In addition, the partition wall WD that divides the first removal region RR1 and a part of the connection region RC has an upper end of the housing 210 inside the housing 210 such that the upper end is spaced a predetermined distance apart from the upper end of the housing 210 as shown in FIG. 5. It can be provided in. In addition, the partition wall WD partitioning the second removal region RR2 from the rest of the connection region RC may be provided in the housing 210 so that the lower end is spaced apart from the lower end of the housing 210 by a predetermined distance.

In addition, the inlet 211 connected to the exhaust gas discharge device may be connected to the first removal region RR1, and the outlet 212 may be connected to the second removal region RR2. In addition, the housing 210 is provided with a first drain port 213 ′ and a second drain port 213 ″, respectively, and the first drain port 213 ′ is connected to the first removal area RR1 and the second drain port 213 ") may be connected to the second removal area RR2.

Thereby, it is possible to remove sulfur oxides or carbon dioxide while the exhaust gas flows from the bottom to the top in both the first removal area RR1 and the second removal area RR2. In the connection area RC, the first removal area The exhaust gas from which the sulfur oxides have been removed in RR1 may flow from the top to the bottom to flow into the second removal region RR2.

In addition, the gas-liquid separation treatment liquid regeneration unit 400 has a pretreatment configuration and a treatment liquid recovery configuration connected to the gas-liquid separation treatment liquid regeneration unit 400 for regeneration of the waste treatment liquid, and a configuration connected to a gas recovery pipe for separating carbon dioxide. It may include.

The gas-liquid reactor 200 of the second embodiment of the exhaust gas treatment apparatus 100 according to the present invention includes a first treatment liquid injection unit 220 ′ and a second treatment liquid injection unit 220 as shown in FIG. 5. ") can be included.

The first treatment liquid injection unit 220 ′ may inject the first treatment liquid into the exhaust gas flowing through the first removal region RR1 of the housing 210. The first treatment liquid injection unit 220 ′ may include a first treatment liquid flow pipe 221 ′ and a first treatment liquid injection nozzle 222 ′, as shown in FIG. 5.

The first treatment liquid flow pipe 221 ′ may pass through one surface of the housing 210 and may be provided in the first removal region RR1. In addition, the first treatment liquid injection nozzle 222 ′ may be provided in a portion of the first treatment liquid flow pipe 221 ′ provided in the first removal region RR1.

There may be a plurality of first treatment liquid spraying units 220 ′. In this case, the plurality of first treatment liquid spraying units 220 ′ may be disposed vertically at predetermined intervals. In addition, in the lowermost first treatment liquid injection unit 220 ′, a pretreatment of removing some sulfur oxides from the exhaust gas may be performed while cooling the temperature of the exhaust gas by the first treatment liquid to facilitate removal of sulfur oxides and carbon dioxide. . In addition, the remaining first treatment liquid injection unit 220 ′ may perform post-treatment to remove the remaining sulfur oxides from the exhaust gas. For example, as shown in FIG. 5, there may be two first treatment liquid spraying units 220'. However, the number of the first treatment liquid spraying units 220 ′ is not particularly limited, and any number may be used.

The first treatment liquid may be seawater. In this case, as shown in FIG. 5, the first treatment liquid supply pipe LP' connected to the ocean SEA may be connected to the first treatment liquid flow pipe 221 ′ of the first treatment liquid injection unit 220 ′. . A first treatment liquid supply pump PP' may be provided in the first treatment liquid supply pipe LP'. In addition, a first waste treatment liquid drain pipe LD' connected to the ocean SEA may be connected to the first drain 213 ′ connected to the first removal region RR1 of the housing 210.

Accordingly, when the first treatment liquid supply pump (PP') is driven, seawater flows through the first treatment liquid flow pipe 221 ′ of the first treatment liquid injection unit 220 ′ with the first treatment liquid to perform the first treatment. The exhaust gas flowing through the first removal region RR1 of the housing 210 may be injected through the liquid injection nozzle 222 ′. In addition, the first waste treatment liquid, which is seawater that has been injected into the first removal area RR1 of the housing 210 and absorbs sulfur oxides from the exhaust gas, is transferred to the sea through the first waste treatment liquid drainage pipe LD'. Can be drained. A water treatment unit (not shown) is provided in the first waste treatment liquid drainage pipe LD', so that the first waste treatment liquid, which is seawater that has absorbed sulfur oxides from the exhaust gas, is water treated and then discharged to the sea (SEA). have.

The second treatment liquid injection unit 220" may inject the second treatment liquid into the exhaust gas flowing through the second removal area RR2 of the housing 210. The second treatment liquid injection unit 220" As shown in FIG. 5, a second treatment liquid flow pipe 221" and a second treatment liquid injection nozzle 222" may be included.

The second treatment liquid flow pipe 221" may pass through the other surface of the housing 210 and may be provided in the second removal region RR2. And, the second treatment liquid injection nozzle 222" may be provided in the second removal region ( It may be provided in a portion of the second treatment liquid flow pipe 221" provided in RR2).

In the treatment liquid supply tank 300 of the second embodiment of the exhaust gas treatment apparatus 100 according to the present invention, the second treatment liquid may be supplied to the gas-liquid reactor 200. To this end, the second treatment liquid is stored in the treatment liquid supply tank 300, and a second treatment liquid supply pipe LP" connected to the treatment liquid supply tank 300 is provided with the second treatment liquid injection unit 220". 2 It may be connected to the treatment liquid flow pipe 221".

A second treatment liquid supply pump PP" may be provided in the second treatment liquid supply pipe LP". And, when the second treatment liquid supply pump (PP") is driven, the second treatment liquid stored in the treatment liquid supply tank 300 is transferred to the second treatment liquid flow pipe 221" of the second treatment liquid injection unit 220" By flowing, the exhaust gas flowing through the second removal area RR2 of the housing 210 may be injected through the second treatment liquid injection nozzle 222".

The second treatment liquid may be an alkaline aqueous solution such as an aqueous sodium hydroxide solution.

Gas-liquid separation treatment liquid of the second embodiment of the exhaust gas treatment apparatus 100 according to the present invention The regeneration unit 400 separates carbon dioxide from the second waste treatment liquid, which is a second treatment liquid that has absorbed carbon dioxide, drained from the gas-liquid reactor 200, and regenerates it as a second treatment liquid, and the recycled second treatment liquid is treated as a treatment liquid. It can be supplied to the supply tank 300.

For this purpose, gas-liquid separation treatment liquid The gas-liquid separation membrane 420 of the regeneration unit 400 may pass carbon dioxide but may not pass the second waste treatment liquid. And, the second waste treatment liquid drain pipe (LD") connected to the gas-liquid reactor 200 is a gas-liquid separation treatment liquid It may be connected to one side of the liquid flow path 411 of the regeneration unit 400. For example, as shown in FIG. 5, a second waste treatment liquid drainage pipe LD" is connected to the second drain 213" connected to the second removal area RR2 of the gas-liquid reactor 200, and the second waste treatment Liquid drainage pipe (LD") is a gas-liquid separation treatment liquid It may be connected to one side of the liquid flow path 411 of the regeneration unit 400. In addition, the other side of the liquid flow path 411 may be connected to the treatment liquid supply tank 300 by a treatment liquid recovery pipe LR.

Accordingly, the second waste treatment liquid drained through the second drainage port 213" of the gas-liquid reactor 200 is a gas-liquid separation treatment liquid through the second waste treatment liquid drainage pipe LD" While flowing through the liquid flow path 411 of the regeneration unit 400, carbon dioxide may be separated and regenerated as a second treatment liquid. The regenerated second treatment liquid may be supplied to the treatment liquid supply tank 300 through the treatment liquid recovery pipe LR.

And, gas-liquid separation treatment liquid Carbon dioxide separated from the second waste treatment liquid flowing through the liquid flow path 411 of the regeneration unit 400 and moved to the gas flow path 412 is passed through a gas return pipe (LG) connected to the gas flow path 412. It can be processed by flowing to the gas processing unit 500.

Third Embodiment of Exhaust Gas Treatment System

Hereinafter, a third embodiment of an exhaust gas treatment apparatus according to the present invention will be described with reference to FIG. 6.

6 is a diagram showing a third embodiment of an exhaust gas treatment apparatus according to the present invention.

Here, in the third embodiment of the exhaust gas treatment apparatus according to the present invention, the second embodiment of the exhaust gas treatment apparatus according to the present invention described with reference to FIG. 5 and the treatment liquid supply tank 300 is a gas-liquid reactor ( The first gas-liquid separation treatment liquid that supplies the first treatment liquid and the second treatment liquid to 200), and regenerates the first waste treatment liquid as the first treatment liquid The regeneration unit 400' and a second gas-liquid separation treatment liquid for regenerating the second waste treatment liquid as a second treatment liquid There is a difference in that it includes a regeneration unit 400".

Therefore, hereinafter, the differentiated parts will be mainly described, and the remaining configurations may be replaced with those described with reference to FIGS. 1 to 5.

The treatment liquid supply tank 300 of the third embodiment of the exhaust gas treatment apparatus 100 according to the present invention may supply the first treatment liquid and the second treatment liquid to the gas-liquid reactor 200, respectively.

To this end, the interior of the treatment liquid supply tank 300 includes a first storage area SS1 in which the first treatment liquid is stored, and a second storage area SS2 in which the second treatment liquid is stored, as shown in FIG. 6. As a result, it may be partitioned by the partition wall WD.

In addition, the first storage region SS1 is connected to the first treatment liquid injection unit 220 ′ of the gas-liquid reactor 200 by a first treatment liquid supply pipe LP′, and the second storage region SS2 is It may be connected to the second treatment liquid injection unit 220" of the gas-liquid reactor 200 by a second treatment liquid supply pipe LP".

Accordingly, when the first treatment liquid supply pump PP' provided in the first treatment liquid supply pipe LP' is driven, the first treatment liquid in the first storage area SS1 is transferred to the first treatment liquid supply pipe LP'. ) May be supplied to the first treatment liquid spraying unit 220 ′. The first treatment liquid supplied to the first treatment liquid injection unit 220 ′ may be injected into the exhaust gas flowing through the first removal region RR1 of the gas-liquid reactor 200.

In addition, when the second treatment liquid supply pump PP" provided in the second treatment liquid supply pipe LP" is driven, the second treatment liquid in the second storage area SS2 is transferred to the second treatment liquid supply pipe LP". It may be supplied to the second treatment liquid spraying unit 220" through. The second treatment liquid supplied to the second treatment liquid injection unit 220" may be injected into the exhaust gas flowing through the second removal region RR2 of the gas-liquid reactor 200.

Meanwhile, a plurality of first treatment liquid spraying units 220 ′ may be provided, and a packing 230 may be provided at a portion of the first removal region RR1 between the plurality of first treatment liquid spraying units 220 ′. For example, as shown in FIG. 6, two first treatment liquid spraying units 220' are disposed vertically at predetermined intervals, and a first removal area between the two first treatment liquid spraying units 220' ( The packing 230 may be provided in a portion of RR1).

1st gas-liquid separation treatment liquid The regeneration unit 400' separates sulfur oxides from the first waste treatment liquid, which is a first treatment liquid that has absorbed sulfur oxides, drained from the gas-liquid reactor 200, and regenerates them as a first treatment liquid. May be supplied to the treatment liquid supply tank 300.

To this end, the first gas-liquid separation treatment liquid In the regeneration unit 400', the first gas-liquid separation membrane 420', which passes the sulfur oxide but does not pass the first waste treatment liquid, is the first liquid flow path 411' and the sulfur oxide through which the first waste treatment liquid flows. This flowing first gas flow path 412' can be partitioned. In addition, a low partial pressure of sulfur oxides is formed in the first gas flow path 412 ′, so that the sulfur oxide contained in the first waste treatment liquid of the first liquid flow path 411 ′ is transferred to the first gas-liquid separation membrane 420 ′. It may pass through and move to the first gas flow path 412'.

1st gas-liquid separation treatment liquid The regeneration unit 400' is a first separation unit main body 410' whose internal space is divided into a first liquid flow path 411' and a first gas flow path 412' by a first gas-liquid separation membrane 420'. ) May be further included. In addition, a first waste treatment liquid drain pipe LD' connected to the first drain 213' of the gas-liquid reactor 200 is connected to one side of the first liquid flow path 411', and the first liquid flow path 411 The other side of') may be connected to the first storage area SS1 of the treatment liquid supply tank 300 by a first treatment liquid recovery pipe LR'. In addition, a first gas recovery pipe (LG') equipped with a vacuum pump (PV) is connected to one side of the first gas flow path 412', so that a low partial pressure of sulfur oxides is formed in the first gas flow path 412'. You can do it. In addition, the partial pressure of sulfur oxides formed in the first gas flow path 412' is connected to the first air inlet pipe LA' equipped with a flow control valve VC on the other side of the first gas flow path 412'. Can be adjusted. In addition, the first gas-liquid separation membrane 420 ′ may be a hollow fiber membrane in which the first gas flow path 412 ′ or the first liquid flow path 411 ′ is formed.

Second gas-liquid separation treatment liquid The regeneration unit 400" separates carbon dioxide from the second waste treatment liquid, which is a second treatment liquid that has absorbed carbon dioxide, drained from the gas-liquid reactor 200, and regenerates it as a second treatment liquid, and processes the recycled second treatment liquid. It can be supplied to the liquid supply tank 300.

To this end, the second gas-liquid separation treatment liquid In the regeneration unit 400", the second gas-liquid separation membrane 420", which passes carbon dioxide but does not pass through the second waste treatment liquid, flows into the second liquid flow path 411" through which the second waste treatment liquid flows. The second gas flow path 412" can be divided. In addition, a low partial pressure of carbon dioxide is formed in the second gas flow path 412", so that the carbon dioxide contained in the second waste treatment liquid of the second liquid flow path 411" passes through the second gas-liquid separation membrane 420". Thus, it can be moved to the second gas flow path 412".

Second gas-liquid separation treatment liquid The regeneration unit 400" is a second separation unit body 410" in which the internal space is divided into a second liquid flow path 411" and a second gas flow path 412" by a second gas-liquid separation membrane 420". In addition, a second waste treatment liquid drain pipe LD" connected to the second drain 213" of the gas-liquid reactor 200 is connected to one side of the second liquid flow path 411", , The other side of the second liquid flow path 411" may be connected to the second storage area SS2 of the treatment liquid supply tank 300 by a second treatment liquid recovery pipe LR". And, a second gas return pipe (LG") equipped with a vacuum pump (PV) is connected to one side of the second gas flow path 412" so that a low partial pressure of carbon dioxide is formed in the second gas flow path 412". In addition, a second air inlet pipe LA" equipped with a flow control valve VC is connected to the other side of the second gas flow path 412" to form in the second gas flow path 412". The lower partial pressure of carbon dioxide can be adjusted. In addition, the second gas-liquid separation membrane 420" may be a hollow fiber membrane in which the second gas flow path 412" or the second liquid flow path 411" is formed.

The first treatment liquid and the second treatment liquid may be an aqueous alkaline solution such as an aqueous sodium hydroxide solution. In this case, an alkali agent such as sodium hydroxide is stored in the treatment agent supply tank 600, and the treatment agent supply tank 600 is a treatment liquid supply tank ( They are connected to the first storage area SS1 and the second storage area SS2 of 300), respectively, so that an alkali agent may be supplied as a treatment agent.

However, the first treatment liquid and the second treatment liquid may be different from each other.

In addition, each of the first gas recovery pipe LG' and the second gas recovery pipe LG" may be connected to the gas processing unit 500.

Fourth Embodiment of Exhaust Gas Treatment System

Hereinafter, a fourth embodiment of an exhaust gas treatment apparatus according to the present invention will be described with reference to FIG. 7.

7 is a diagram showing a fourth embodiment of an exhaust gas treatment apparatus according to the present invention.

Here, the fourth embodiment of the exhaust gas treatment apparatus according to the present invention is the third and fourth embodiments of the exhaust gas treatment apparatus according to the present invention described with reference to FIGS. 5 and 6, and a gas-liquid reactor ( There is a difference in that the cross section of the housing 210 of 200) is circular or elliptical.

Therefore, hereinafter, the differences will be mainly described, and the remaining configurations may be replaced with those described with reference to FIGS. 1 to 6.

In the fourth embodiment of the exhaust gas treatment apparatus 100 according to the present invention, the cross section of the housing 210 of the gas-liquid reactor 200 may be circular or elliptical. Accordingly, the housing 210 may be a cylinder or an elliptical cylinder as shown in FIG. 7. The first removal area RR1 is located at the outermost side in the radial direction inside the housing 210, the connection area RC is located inside the first removal area RR1, and the second removal area RR2 is It may be located inside the connection area RC. To this end, the cross section of the first removal region RR1 and the connection region RC may be annular, and the cross section of the second removal region RR2 may be circular or elliptical. Accordingly, since the exhaust gas may flow smoothly, the exhaust gas may not flow biased to one side, the exhaust gas may be processed more smoothly.

A plurality of partition walls WD, which are cylindrical or elliptical, are provided inside the housing 210 to divide the interior of the housing 210 into a first removal region RR1, a connection region RC, and a second removal region RR2. I can. For example, as shown in FIG. 7, two partition walls WD, which are cylindrical or elliptical, are provided, so that the interior of the housing 210 includes a first removal region RR1, a connection region RC, and a second removal region RR2. ) Can be divided.

The plurality of partition walls WD are housings such that exhaust gas flows from the bottom to the top in the first removal area RR1 and the second removal area RR2, and the exhaust gas flows from the top to the bottom in the connection area RC. (210) It may be provided inside.

In the gas-liquid reactor 200 of the above-described configuration, the exhaust gas discharged from the exhaust gas discharge device is first formed on the outermost side in the radial direction inside the housing 210, and is connected to the inlet 211. 1 may be introduced into the removal region RR1 through the inlet 211. The exhaust gas introduced into the first removal region RR1 may be removed by the first treatment liquid injected into the first removal region RR1 while flowing through the first removal region RR1. The exhaust gas from which the sulfur oxide has been removed may flow into the second removal region RR2 inside the connection region RC through the connection region RC inside the first removal region RR1. Carbon dioxide may be removed while the exhaust gas introduced into the second removal region RR2 flows through the second removal region RR2. The exhaust gas from which carbon dioxide has been removed may be discharged through the outlet 212 connected to the second removal region RR2.

As described above, when the exhaust gas treatment apparatus according to the present invention is used, the gas-liquid separation treatment liquid that separates the emission control gas from the waste treatment liquid treated with the exhaust gas The waste treatment liquid can be regenerated by the regeneration unit, the regeneration rate of the waste treatment liquid treated with the exhaust gas can be increased, the cost for treating the exhaust gas in the exhaust gas treatment device can be reduced, and The size can be reduced.

The exhaust gas treatment apparatus described above is not limitedly applicable to the configuration of the above-described embodiments, but the embodiments may be configured by selectively combining all or part of each of the embodiments so that various modifications can be made. have.

100: exhaust gas treatment device 200: gas-liquid reactor
210: housing 211: inlet
212: outlet 213: drain
213': 1st drain 213": 2nd drain
220: treatment liquid injection unit 220': first treatment liquid injection unit
220": second treatment liquid injection unit 221: treatment liquid flow pipe
221': first treatment liquid flow pipe 221": second treatment liquid flow pipe
222: treatment liquid injection nozzle 222': first treatment liquid injection nozzle
222": second treatment liquid spray nozzle 230: packing
300: treatment liquid supply tank 400: gas-liquid separation treatment liquid Regeneration unit
400': first gas-liquid separation treatment liquid Regeneration unit 400": second gas-liquid separation treatment liquid Regeneration unit
410: separation unit body 410': first separation unit body
410": 2nd separation unit body 411: liquid flow path
411': first liquid flow path 411": second liquid flow path
412: gas flow path 412': first gas flow path
412": second gas flow path 420: gas-liquid separation membrane
420': first gas-liquid separation membrane 420": second gas-liquid separation membrane
500: gas treatment unit 510: seawater flow pipe
520: fine bubble generator 521: fine pores
530: gas mixer 531: mixing member
540: gas storage tank 600: treatment agent supply tank
LD: Waste treatment liquid drainage pipe LD': Waste treatment liquid drainage pipe 1
LD": 2nd waste treatment liquid drainage pipe LR: Treatment liquid recovery pipe
LR': first treatment liquid recovery pipe LR": second treatment liquid recovery pipe
LG: Gas collection pipe LG': First gas collection pipe
LG": 2nd gas recovery pipe LA: Air inlet pipe
LA': 1st air inflow pipe LA": 2nd air inflow pipe
LP: Treatment liquid supply pipe LP': First treatment liquid supply pipe
LP": 2nd treatment liquid supply pipe LT: Treatment agent supply pipe
LT': first treatment agent supply pipe LT": second treatment agent supply pipe
PV: Vacuum pump PB: Booster pump
PP: Treatment liquid supply pump PP': First treatment liquid supply pump
PP": 2nd treatment liquid supply pump VC: Flow control valve
VCP: Pressure control device WTS: Filtration treatment unit
HE: heat exchanger RR1: first removal zone
RR2: second removal area RC: connection area
WD: Partition wall SEA: Marine
SP: water quality measurement sensor SS1: first storage area
SS2: Second storage area

Claims (10)

A gas-liquid reactor for absorbing and removing the emission control gas by contacting the emission control gas contained in the exhaust gas with the treatment liquid;
A treatment liquid supply tank for supplying the treatment liquid to the gas-liquid reactor; And
A gas-liquid separation treatment liquid for regenerating the waste treatment liquid, which is a treatment liquid absorbing the discharge control gas, into a treatment liquid that does not absorb the discharge control gas, and supplying the recycled treatment liquid to the treatment liquid supply tank Regeneration unit; Including,
The gas-liquid separation treatment liquid regeneration unit includes a gas-liquid separation membrane that passes gas but does not pass liquid, and the gas-liquid separation membrane divides a liquid flow path through which waste treatment liquid flows and a gas flow path through which emission control gas flows,
The exhaust gas treatment device, wherein the emission control gas absorbed in the waste treatment liquid passes through the gas-liquid separation membrane while flowing through the liquid flow path, moves to a gas flow path in which a low emission control gas partial pressure is formed, and separates it into an emission control gas and a treatment liquid. The exhaust gas treatment of claim 1, wherein a waste treatment liquid drain pipe connected to the gas-liquid reactor is connected to one side of the liquid flow path, and the other side of the liquid flow path is connected to the treatment liquid supply tank by a treatment liquid recovery pipe. Device. The exhaust gas treatment apparatus according to claim 2, wherein the waste treatment liquid drain pipe is provided with a filtration treatment unit that filters pollutants excluding emission control gas contained in the waste treatment liquid. The exhaust gas treatment apparatus according to claim 1, wherein a gas recovery pipe equipped with a vacuum pump is connected to one side of the gas flow path so that a low partial pressure of emission control gas is formed in the gas flow path. The exhaust gas treatment apparatus according to claim 1, wherein an air inlet pipe provided with a flow control valve is connected to the other side of the gas flow path to adjust the partial pressure of the emission regulation gas formed in the gas flow path. The exhaust gas treatment apparatus according to claim 1, wherein the gas-liquid separation membrane is a hollow fiber membrane in which the gas flow path or the liquid flow path is formed. The exhaust gas treatment apparatus according to claim 1, wherein the gas-liquid reactor comprises a housing connected to an exhaust gas discharge device, and a treatment liquid injection unit for injecting a treatment liquid to exhaust gas flowing through the housing. The treatment liquid flow pipe of claim 7, wherein the treatment liquid injection unit is connected to the treatment liquid supply tank and passes through one surface of the housing and is provided in the housing, and a part of the treatment liquid flow pipe provided inside the housing. Exhaust gas treatment apparatus including a treatment liquid injection nozzle provided in the. The exhaust gas treatment apparatus according to claim 1, wherein a heat exchanger is connected to the treatment liquid supply tank to cool the treatment liquid stored in the treatment liquid supply tank. The exhaust gas treatment apparatus according to claim 1, wherein the emission control gas is sulfur oxide or carbon dioxide, and the treatment liquid is seawater or an alkaline aqueous solution.

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