Wet-type exhaust gas desulfurization system having a means for supplying air

Abstract: A wet-type exhaust gas desulfurization system comprises a reservoir (3) for trapping an absorbing solution (4)(7) which has absorbed SO₂ from exhaust gas; an absorbing solution circulating tank (6) disposed directly under the reservoir; a plurality of bottom pipes which are installed at the bottom of reservoir and extend downward into the absorbing solution in the circulating tank and whose lower end is open, or drop pipes which depend into the absorbing solution and whose lower ends are open; an air supply pipe (8) at least one end of which is open to the atmosphere; a pipe (9) for discharging the air above the surface of absorbing solution onto the surface of solution in the reservoir; and a pipe for supplying the absorbing solution in the circulating tank to a spray nozzle (2) at the upper part of the absorbing tower.

Description: This invention relates to a wet-type exhaust gas desulfurization system and, more particularly, to a wet-type exhaust gas desulfurization system which can recover gypsum by oxidizing sulfite produced in the absorbing solution by sulfur oxides (hereinafter abbreviated as SO₂) absorbed from exhaust gas. In the conventional wet-type exhaust gas desulfurization system in which exhaust gas desulfurization is performed with calcium compound being used as an absorbent to recover gypsum, a conventional method for producing gypsum from calcium sulfite formed by a reaction between calcium compound and SO₂ is to extract slurry containing gypsum or calcium sulfite of stoichiometric quantity corresponding to the quantity of absorbed SO₂ from a circulating tank, and to oxidize the slurry in a separate oxidizing tower to produce gypsum from calcium sulfite. A system in which, the separate oxidizing tower being omitted, air or O₂-containing gas is blown directly into a circulating tank to produce gypsum by oxidizing calcium sulfite in the circulating tank has been disclosed in the Japanese Patent Publication No.17318/1975 and the Japanese Patent Application No. 18269/1976. Further, a system in which an absorbing solution received by an absorbing solution receiving tank is re-sprayed into a circulating tank while air is supplied onto the surface of solution in the circulating tank has been disclosed in the Japanese Patent Publication No.37252/1983. Still further, a system in which air is blown onto the surface of solution flowing down in an absorbing tower to accelerate oxidation has been disclosed in the Japanese Patent Application No. 178326/1983 and the Japanese Patent Application No.167432/1986. These conventional systems, which produce gypsum by blowing air for the oxidation of calcium sulfite, need to supply air by means of a blower or the like. Therefore, they have a disadvantage of requiring the power for supplying air. As described above, the conventional systems, in which air is used to oxidize sulfite produced by the absorption of SO₂ in the absorbing tower, have a problem of requiring much power to supply air. In view of the foregoing, it is an object of this invention to provide a system which supplies air for oxidation to a wet-type exhaust gas desulfurization system without using power. According to this invention (the first embodiment), (1) In a wet-type exhaust gas desulfurization apparatus in which exhaust gas desulfurization is performed by gas-liquid contact between the exhaust gas containing sulfur oxides and an absorbing solution containing calcium compound in an absorbing tower, the wet-type exhaust gas desulfurization apparatus having a means for supplying air comprises, (a) a reservoir for trapping the absorbing solution, which has absorbed sulfur oxides from the exhaust gas, at the bottom of the absorbing tower, (b) an absorbing solution circulating tank disposed directly under the reservoir, (c) a plurality of bottom pipes which are installed at the bottom of the reservoir and extend into the absorbing solution in the circulating tank and whose lower ends are open, (d) an air supply pipe which is disposed so as to cross through the bottom pipe and has openings at the through portion inside the bottom pipe and at least one end of which opens to the atmosphere, (e) a pipe through which the air above the surface of absorbing solution in the circulating tank is discharged onto the surface of the solution stored in the reservoir, and (f) a pipe for supplying the absorbing solution in the circulating tank to a spray nozzle disposed at the upper part of the absorbing tower via a pump. (2) The wet-type exhaust gas desulfurization system having a means for supplying air described in (1) has a means for supplying water intermittently to the openings of the air supply pipe. The above configuration of this first embodiment has the following effects: When the absorbing solution which is stored in the reservoir and flows into the circulation tank through the bottom pipe passing through the side of the air supply pipe disposed through the bottom pipe, a negative pressure is produced on the lower surface of the air supply pipe by the separation of flow. This negative pressure acts on the openings which are positioned on the lower surface of air supply pipe in the bottom pipe; as a result, air is sucked from the one or both ends of air supply pipe which communicates with the atmosphere. The air is sucked by the absorbing solution in the bottom pipe through the openings of the air supply pipe. The air drops together with the absorbing solution into the circulating tank, where the oxygen in the air reacts with the sulfite produced by the absorption of SO₂ contained in the absorbing solution to form gypsum. In this embodiment, air is automatically sucked by using a negative pressure produced by the separation of flow occurring around an object at the downstream side of an object placed in the field of flow. Cleaning water is intermittently sprayed to prevent the clogging of openings of air supply pipe which is caused by the deposit of salts at the wet boundary produced by the back flow due to the surface tension of absorbing solution. According to this invention (the second embodiment), (1) In a wet-type exhaust gas desulfurization apparatus in which exhaust gas desulfurization is performed by gas-liquid contact between the exhaust gas containing sulfur oxides and an absorbing solution containing calcium compound in an absorbing tower, the wet-type exhaust gas desulfurization apparatus having a means for supplying air comprises, (a) a reservoir for trapping the absorbing solution, which has absorbed sulfur oxides from the exhaust gas, at the bottom of the absorbing tower, (b) an absorbing solution circulating tank disposed directly under the reservoir, (c) a plurality of bottom pipes which are installed at the bottom of the reservoir and extend into the absorbing solution in the circulating tank and whose lower ends are open, (d) an air supply pipe which is disposed opposite to the bottom pipe or inserted in the bottom pipe so as to be close to the upper end of bottom pipe and has an appropriate gap and the other end of which communicates with the atmosphere, (e) a pipe through which the air above the surface of absorbing solution in the circulating tank is discharged onto the surface of the solution stored in the reservoir, and (f) a pipe for supplying the absorbing solution in the circulating tank to a spray nozzle disposed at the upper part of the absorbing tower via a pump. (2) The wet-type exhaust gas desulfurization system having a means for supplying air described in (1) has a means for supplying water intermittently to the air supply pipe. (3) The wet-type exhaust gas desulfurization system having a means for supplying air described in (1) or (2) has a means for adjusting the positional relationship between the upper end of bottom pipe and the lower end of air supply pipe. (4) The wet-type exhaust gas desulfurization system having a means for supplying air described in (1), (2) or (3) has a means for spraying a pumped solution downward into the bottom pipe or the air supply pipe. The above configuration of this second embodiment has the following effects: The absorbing solution is allowed to flow through the gap between the bottom pipe and the air supply pipe by using the potential energy of absorbing solution stored in the reservoir. Because the cross section of solution passage expands suddenly at the lower end of the air supply pipe, the flow of solution flowing down in the bottom pipe is separated at the periphery of the air supply pipe, so that a negative pressure depending on the flow speed of the solution is produced. By the negative pressure, air is sucked via the air supply pipe and directed to the circulating tank together with the solution flowing down in the bottom pipe for the oxidation in the circulating tank. The air accumulating above the surface of absorbing solution in the circulating tank is discharged onto the surface of absorbing solution stored in the reservoir so that the air is absorbed by the absorbing solution which drops from the absorbing tower to the reservoir. This uses the oxygen in the air more efficiently. Cleaning is performed intermittently by supplying water via the air feeding pipe to prevent the clogging of air supply pipe due to the deposit of gypsum because gypsum is deposited at the wet boundary inside the air supply pipe due to the back flow of absorbing solution produced in the end of air supply pipe by the surface tension at the periphery of the air supply pipe. The gap between the bottom pipe and the air supply pipe is varied by providing a means for adjusting the positional relationship between the upper end of bottom pipe and the lower end of air supply pipe, so that the amount of absorbing solution stored in the reservoir can be controlled. The amount of sucked air can be controlled by spraying the pumped solution downward into the bottom pipe. According to this invention (the third embodiment), (1) In a wet-type exhaust gas desulfurization apparatus in which exhaust gas desulfurization is performed by gas-liquid contact between the exhaust gas containing sulfur oxides and an absorbing solution containing calcium compound in an absorbing tower, the wet-type exhaust gas desulfurization apparatus having a means for supplying air comprises, (a) a reservoir which traps the absorbing solution, which has absorbed sulfur oxides from the exhaust gas, at the bottom of the absorbing tower, and has bottom pipes at its bottom, (b) an absorbing solution circulating tank disposed directly under the reservoir, (c) a drop pipe which is installed downwardly through the ceiling of circulating tank and extends into the absorbing solution in the circulating tank, and into which the bottom pipe is inserted close to the increased-diameter portion at the upper side of a restriction means, (d) a pipe through which the air above the surface of absorbing solution in the circulating tank is discharged onto the surface of the solution stored in the reservoir, and (e) a pipe for supplying the absorbing solution in the circulating tank to a spray nozzle disposed at the upper part of the absorbing tower via a pump. (2) The wet-type exhaust gas desulfurization system having a means for supplying air described in (1) has a means for controlling the discharge amount of absorbing solution in the bottom pipe. (3) The wet-type exhaust gas desulfurization system having a means for supplying air described in (1) or (2) has a bottom pipe whose inside diameter is decreased gradually toward the lower end. The above configuration of this third embodiment has the following effects: When the absorbing solution stored in the reservoir flows down in the bottom pipe and is injected toward the drop pipe, a negative pressure is produced by an aspirator (water jet pump) action at the gap between the lower end of bottom pipe and the drop pipe. By the produced negative pressure, air is sucked from the clearance between the upper opening of drop pipe and the bottom pipe. Furthermore, the air accumulating above the surface of absorbing solution in the circulating tank is discharged onto the surface of absorbing solution stored in the reservoir so that the air is absorbed by the absorbing solution which drops from the absorbing tower to the reservoir. This uses the oxygen in the air more efficiently. The amount of absorbing solution flowing down in the bottom pipe can be controlled and the intermittent flow of absorbing solution in the bottom pipe can be performed in response to the variation in the amount of solution circulating in the absorbing tower by installing a control means such as a valve in the bottom pipe. Also, the absorbing solution can be injected as a jet flow from the bottom pipe into the drop pipe by downwardly decreasing the inside diameter of the bottom pipe. FIG.1 is a schematic view of the first embodiment of this invention, FIG.2 is a partially enlarged perspective view, FIG.3 is a sectional view taken in the direction of arrow X of FIG.2, FIG.4 is a sectional view taken in the direction of arrow Y of FIG.2, FIG.5 is a further sectional enlarged view, FIG.6 is a schematic view of the second embodiment of this invention, FIG.7 is a partially enlarged view, FIG.8 is a further partially enlarged view, FIG.9 is another partially enlarged view, FIG.10 is another partially enlarged view, FIG.11 is a schematic view of the third embodiment of this invention, and FIG.12 is a partially enlarged view. This invention will be described in detail on the basis of respective embodiments. The first embodiment of the invention will be described with reference to FIG.1 to FIG.5. Referring to FIG.1, exhaust gas A containing SO₂ is directed to an absorbing tower 1. Absorbing solution 7 stored in a circulating tank 6 of the absorbing tower 1 is supplied to a spray nozzle 2 by means of a circulating pump 10. The exhaust gas A is treated by gas-liquid contact with the absorbing solution containing calcium compound which is sprayed from the spray nozzle 2, and discharged as a treated exhaust gas B from the absorbing tower 1 after desulfurization. The absorbing solution which has absorbed SO₂ in the absorbing tower 1 drops into a reservoir 3 at the bottom of the absorbing tower 1 and stored therein. The stored solution 4 is directed to the circulating tank 6 through a bottom pipes 5 which are connected to the bottom of the reservoir 3 and pass through the ceiling of the circulating tank 6 directly under the reservoir 3. The lower ends of the bottom pipes 5 are submerged in the solution 7 stored in the circulating tank 6. At the intermediate part between the bottom of reservoir 3 and the ceiling of the circulating tank 6, an air supply pipe 8 is installed which crosses through the bottom pipe. At least one end of the air supply pipe communicates with the atmosphere, and the through portion of the bottom pipe 5 has at least one air supply port 9 at its bottom. To explain the details of the air supply pipe portion, the partially enlarged views are shown in FIGS.2 through 4. In FIG.2, the air supply pipe 8 installed through the bottom pipe 5 depending from the bottom of the reservoir 3 has the air supply ports 9 at the bottom of its through portion. Also, the end of the air supply pipe 8 communicates with the atmosphere as an air suction port 11. FIGS.3 and 4 are sectional views taken in the direction of arrow X and Y, respectively, of FIG.2. In FIG.3, when the stored solution 4 in the reservoir 3 flows down through the bottom pipe 5, it passes through a clearance passage 12 between the air supply pipe 8 and the bottom pipe 5, which produces the separation of flow on the outside diameter surface of air supply pipe 8. The separation of flow creates a negative pressure on the external lower surface of the air supply pipe 8. The negative pressure allows air to be sucked through the air suction port 11 of the air supply pipe 8, and the sucked air is supplied from the air supply ports 9 to the absorbing solution flowing down in the bottom pipe. The supplied air flows down together with the solution flowing down in the bottom pipe 5 into the stored solution 7 in the circulating tank 6, where the oxygen which is a component of the supplied air reacts with the sulfite contained in the solution flowing down in the bottom pipe 5 to form gypsum. FIG.5 is a typical view showing the cleaning system of air supply ports 9. The system has spray nozzles 14 over the entrances of the air supply ports in the air supply pipe 8. The cleaning is performed intermittently with water fed through a water feeding pipe 13 having a control valve 16 halfway by operating the valve 16 in accordance with a control signal 15. In the embodiment of this invention, the air supply pipe 8 has a circular cross section, but it may be differently shaped so that negative pressure is produced by the separation of flow; for example, it may have triangular or rectangular cross section or may be of cross arrangement or of multi-pipe system. Next, the second embodiment of the invention will be described with reference to FIG.6. to FIG.10. Referring to FIG.6, untreated exhaust gas A containing SO₂ is directed to an absorbing tower 101, and treated by gas-liquid contact with the absorbing solution containing calcium compound which is sprayed from the spray nozzle 102, in the same way as that of the above-described embodiment of the first invention, and discharged as a treated exhaust gas B from the absorbing tower 101 after desulfurization. In this figure, reference numeral 108 denotes a circulating pump, and 109 denotes a circulating line. The absorbing solution which has absorbed SO₂ in the absorbing tower 101 drops into a reservoir 104 at the bottom of the absorbing tower 101 and is stored therein. The stored solution 111 is directed to the circulating tank 106 through a bottom pipes 107 which are connected to the bottom of the reservoir 104 and pass through the ceiling of the circulating tank 106 directly under the reservoir 104. At the entrance of bottom pipe 107 into which the stored solution 111 in the reservoir 104 flows, an air supply pipe 105 is mounted opposite to the bottom pipe 107 as shown in FIG.7 or inserted in the bottom pipe 107 as shown in FIG.8. The air supply pipes 105 are branched from an air feeding pipe 103 whose one end opens to the atmosphere. When the stored solution 111 in the reservoir 104 flows down in the bottom pipe 107, the flow separates at the periphery of the end of air supply pipe 105, resulting in the production of negative pressure. The negative pressure acts on the inside of the air supply pipe 105; as a result, air is supplied into the solution through the air feeding pipe 103 and the air supply pipe 105. A proper depth of solution in the reservoir 104 is kept by the flow resistance of solution between the air supply pipe 105 and the bottom pipe 107. The supplied air drops together with the solution through the bottom pipe, and distributed in the circulating tank 106, where the oxygen in the air reacts with the sulfite produced by the absorption of SO₂ from the exhaust gas A to form gypsum. The air which rises from the absorbing solution 112 stored in the circulating tank 106 has a positive pressure in an air accumulation chamber 114, and discharged to above the surface of stored solution 111 in the reservoir 104 at the bottom of the absorbing tower 101 through an exhaust pipe 110. In the used air discharged from the air accumulation chamber 114 through the exhaust pipe 110, unreacted oxygen remains. By discharging the used air containing unreacted oxygen to above the surface of stored solution 111 in the reservoir 104 at the bottom of the absorbing tower 101, the used air is mixed into the stored solution 111 in the reservoir 104 by means of the drop energy of the absorbing solution dropping from the absorbing tower 101, so that the unreacted oxygen reacts with the sulfite in the same way as described above, which improves the utilization rate of oxygen in the supplied air. In this process, the bubble of the supplied air can be made fine by dividing into plurality the respective air supply pipe 105 whose end is opposite to or inserted in the entrance of the bottom pipe 107. To intermittently clean the absorbing solution which flows backward into the air supply pipe 105 by surface tension, water is supplied to the air supply pipe 105 via a water feeding pipe 115. FIG.9 shows a mechanism for adjusting the flow resistance of solution at the portion where the air supply pipe 105 is arranged opposite to the bottom pipe 107. Referring to FIG.9, an expansion cylinder 116 is connected to a fixing jig 117 joined to the external wall at the bottom of reservoir 104, and the other end of the cylinder 116 is connected to a fixing jig 118 joined to the bottom pipe 107. The cylinder 116 is driven along a guide 121 pneumatically or hydraulically in accordance with the pressure signals generated by a pressure unit 119. As a result, the bottom pipe 107 is moved up and down. This changes a gap h between the end of the air supply pipe 105 and the end of the bottom pipe 107, which in turn changes the resistance at the gap h so that the amount of absorbing solution flowing down in the bottom pipe 107 is controlled. Consequently, the level of solution stored in the reservoir 104 is properly maintained. Reference numeral 120 denotes an expansion joint. The bottom pipe 107 is moved in this embodiment, but the air supply pipe 105 may be moved because the purpose is the adjustment of the gap h. FIG.10 shows an embodiment in which a solution feeding pipe 122 which opens downward in the bottom pipe 107 and has a control valve 123 halfway therein, and the pumped solution is sprayed downward from the solution feeding pipe 122 so that flow rate of suction air is controlled. The pumped solution is sprayed in the bottom pipe 107 in this embodiment, but it may be sprayed downward in the air supply pipe 105 because the same effect is provided even when it is sprayed at the end portion of the air supply pipe 105. Next, the third embodiment of the invention will be described with reference to FIG.11 and FIG.12. As with the embodiments described above, exhaust gas A containing SO₂ is directed to an absorbing tower 201, treated by gas-liquid contact with the absorbing solution, and discharged as a treated exhaust gas B from the absorbing tower 201 after desulfurization. The absorbing solution which has absorbed SO₂ in the absorbing tower 201 drops into a reservoir 203 at the bottom of the absorbing tower 201 and stored therein. The stored solution 204 is injected toward a drop pipe 207 via a bottom pipe 205 which opens close to and opposite to the upper portion of the entrance increased-diameter portion of the drop pipe 207. The drop pipe 207 is connected to the bottom of the reservoir 203 and depends into the stored solution 210 stored in a circulating tank 208 through the ceiling 211 of the circulating tank 208. When the stored solution 204 is injected, a negative pressure is produced by an aspirator (water jet pump) action at the gap between the drop pipe 207 and the bottom pipe 205. This negative pressure draws air from the open end of the drop pipe 207. The air is distributed into the stored solution 210 in the circulating tank 208, so that the oxygen in the air reacts with the sulfite in the absorbing solution, which has flown down trough the drop pipe 207 into the stored solution 210 in the circulating tank 208, to form gypsum. Reference numeral 206 denotes a valve mounted in the bottom pipe 205. FIG.12 is a view for illustrating the details of the upper portion of the drop pipe 207 in relation to the bottom pipe 205 in this embodiment. In FIGS.11 and 12, the like numerals refer to like parts. With reference to FIG.12, the occurrence of aspirator action will be described in more detail. The bottom pipe 205 is tapered downward from the intermediate part and its lower end is close to and opposite to the upper portion of the restriction means 216 at the upper part of drop pipe 207 mounted to the ceiling 211 of the circulating tank. The solution flowing from the reservoir 203 is injected from the lower end of the bottom pipe 205, and passes through a passage 218 in the restriction means 216. When the solution passes through a increased-diameter portion 219 at the lower part of the restriction means, a suction force is exerted by the separation of flow. By a negative pressure caused by the suction force, air is sucked into the drop pipe 207 through the top opening 215 thereof, and is directed to the circulating tank 208 through an air passage 217 while being absorbed by the solution. In FIG.11, the circulating tank 208 is divided into two compartments by a partition plate 214 which depends into the stored solution 210 from the ceiling 211 of circulating tank 208. The first compartment (left compartment in the figure) has an air accumulation chamber 212 above the solution which drops from the reservoir 203, whereas the second compartment (right compartment in the figure) has a neutralizing chamber in which calcium compound absorbent is added. The exhaust gas from the air accumulation chamber 212 is discharged onto the surface of stored solution 204 in the reservoir 203 at the bottom of the absorbing tower 201 via an exhaust pipe 213 which has a plurality of openings above the surface of the stored solution 204 in the reservoir 203, which improves the utilization rate of air. According to the first embodiment, the absorbing solution sprayed in the absorbing tower is collected in the reservoir and then allowed to drop through the bottom pipe. By providing a means for separating the flow by utilizing the flow rate of solution dropping in the bottom pipe, a high negative pressure is produced. By using this negative pressure, air is automatically supplied from the atmosphere to oxidize sulfite for forming gypsum without using any power unit such as a blower or compressor. Furthermore, in order to automatically supply air in a stable manner for a long period of time, cleaning water is sprayed intermittently into the air supply ports so that the clogging of air supply port caused by the scale of gypsum is prevented. According to the second embodiment, the absorbing solution sprayed at the upper part of the absorbing tower is trapped temporarily in the reservoir disposed above the circulating tank. By using the negative pressure produced by the separation of flow of solution dropping into the circulating tank, air is sucked automatically without using any equipment such as a blower or compressor. A proper level of solution is maintained by arranging the air supply pipe close to and opposite to the bottom pipe or by inserting the air supply pipe in the bottom pipe, so that the drop speed of solution from the bottom pipe is sufficiently high. Furthermore, the upper part of the circulating tank is used as an air accumulation chamber, and the used air is discharged onto the surface of the stored solution in the reservoir. The used air enters the stored solution together with the absorbing solution sprayed at the upper part of the absorbing tower, so that the remaining oxygen in the used air is effectively used. According to the third embodiment, the absorbing solution sprayed at the upper part of the absorbing tower is trapped temporarily in the reservoir disposed in the absorbing tower, and injected from a specified pipe (bottom pipe). A negative pressure is produced by an aspirator (water jet pump) action caused by the separation of flow of solution at the restricted portion. By this negative pressure, air is automatically supplied for oxidation of sulfite without using any equipment such as a blower or compressor. In addition, the circulating tank is divided into two compartments. The upper part of the compartment into which air flows is used as an air accumulation chamber, from which the used air is discharged onto the surface of the stored solution in the reservoir. The used air enters the stored solution together with the absorbing solution sprayed at the upper part of the absorbing tower, so that the remaining oxygen in the used air is effectively used.

Claims: A a wet-type exhaust gas desulfurization apparatus in which exhaust gas desulfurization is performed by gas-liquid contact between the exhaust gas containing sulfur oxides and an absorbing solution containing calcium compound in an absorbing tower (1), said wet-type exhaust gas desulfurization apparatus having a means for supplying air comprising, (a) a reservoir (3) for trapping the absorbing solution, which has absorbed sulfur oxides from the exhaust gas, at the bottom of said absorbing tower, (b) an absorbing solution circulating tank (6) disposed directly under said reservoir, (c) a plurality of bottom pipes (5) which are installed at the bottom of said reservoir and extend into the absorbing solution in said circulating tank and whose lower ends are open, (d) an air supply pipe (8) which is disposed so as to cross through said bottom pipe and has openings (9) at the through portion inside said bottom pipe and at least one end (11) of which opens to the atmosphere, (e) a pipe through which the air above the surface of absorbing solution in said circulating tank is discharged onto the surface of the solution stored in said reservoir, and (f) a pipe for supplying the absorbing solution in said circulating tank to a spray nozzle (2) disposed at the upper part of said absorbing tower via a pump. A wet-type exhaust gas desulfurization system having a means for supplying air according to claim 1 wherein a means for supplying water intermittently to the openings of said air supply pipe is provided. A wet-type exhaust gas desulfurization apparatus in which exhaust gas desulfurization is performed by gas-liquid contact between the exhaust gas containing sulfur oxides and an absorbing solution containing calcium compound in an absorbing tower (101), said wet-type exhaust gas desulfurization apparatus having a means for supplying air comprising, (a) a reservoir (104) for trapping the absorbing solution, which has absorbed sulfur oxides from the exhaust gas, at the bottom of said absorbing tower, (b) an absorbing solution circulating tank (106) disposed directly under said reservoir, (c) a plurality of bottom pipes (107) which are installed at the bottom of said reservoir and extend into the absorbing solution in said circulating tank and whose lower ends are open, (d) an air supply pipe (105) which is disposed opposite to said bottom pipe or inserted in said bottom pipe so as to be close to the upper end of said bottom pipe and has an appropriate gap (h) and the other end of which communicates with the atmosphere, (e) a pipe (110) through which the air above the surface of absorbing solution in said circulating tank is discharged onto the surface of the solution stored (111) in said reservoir, and (f) a pipe (109) for supplying the absorbing solution in said circulating tank to a spray nozzle (102) disposed at the upper part of said absorbing tower via a pump (108). A wet-type exhaust gas desulfurization system having a means for supplying air according to claim 3 wherein a means for supplying water (115) intermittently to said air supply pipe is provided. A wet-type exhaust gas desulfurization system having a means for supplying air according to claim 3 or 4 wherein a means for adjusting the positional relationship between the upper end of said bottom pipe and the lower end of said air supply pipe is provided. A wet-type exhaust gas desulfurization system having a means for supplying air according to claim 3, 4 or 5 wherein a means (122) for spraying a pumped solution downward into said bottom pipe or said air supply pipe. A wet-type exhaust gas desulfurization apparatus in which exhaust gas desulfurization is performed by gas-liquid contact between the exhaust gas containing sulfur oxides and an absorbing solution containing calcium compound in an absorbing tower (201), said wet-type exhaust gas desulfurization apparatus having a means for supplying air comprising, (a) a reservoir (203) which traps the absorbing solution, which has absorbed sulfur oxides from the exhaust gas, at the bottom of said absorbing tower, and has bottom pipes (205) at its bottom, (b) an absorbing solution circulating tank (208) disposed directly under said reservoir, (c) a drop pipe (207) which is installed downwardly through the ceiling of said circulating tank and extends into the absorbing solution in said circulating tank, and into which the bottom pipe is inserted close to the increased-diameter portion at the upper side of a restriction means (216), (d) a pipe (213) through which the air above the surface of absorbing solution in said circulating tank is discharged onto the surface of the solution (204) stored in said reservoir, and (e) a pipe for supplying the absorbing solution in said circulating tank to a spray nozzle (202) disposed at the upper part of said absorbing tower via a pump (209). A wet-type exhaust gas desulfurization system having a means for supplying air according to claim 7 wherein a means for controlling the discharge amount of absorbing solution in said bottom pipe is provided. A wet-type exhaust gas desulfurization system having a means for supplying air according to claim 7 or 8 wherein the inside diameter of said bottom pipe is decreased gradually toward the lower end.

Inventors: INOUE KENJI C O HIROSHIMA TECH, OKINO SUSUMU C O HIROSHIMA TEC, ONIZUKA MASAKAZU C O HIROSHIMA, TAKASHINA TORU C O HIROSHIMA T, UKAWA NAOHIKO C O HIROSHIMA TE, INOUE, KENJI, C/O HIROSHIMA TECH. INSTITUTE, OKINO, SUSUMU, C/O HIROSHIMA TECH. INSTITUTE, ONIZUKA, MASAKAZU, C/O HIROSHIMA TECH. INSTITUTE, TAKASHINA, TORU, C/O HIROSHIMA TECH. INSTITUTE, UKAWA, NAOHIKO, C/O HIROSHIMA TECH. INSTITUTE
Applicants: MITSUBISHI HEAVY IND LTD, MITSUBISHI JUKOGYO KABUSHIKI KAISHA
Application year: 1991
Main classification: B01D53
IPC codes: B01D53, C01F11