A horizontal alkali washing device and a method of using the same

By designing a multi-stage stirring reaction chamber and alkali liquid circulation system in a horizontal alkali washing tower, the problem of insufficient contact time between alkali and acid gas is solved, the utilization efficiency of alkali liquid and the operation efficiency of the equipment is improved, and hazardous waste is reduced incur and operate costs.

CN118577115BActive Publication Date: 2024-12-13HAOPU NEW MATERIAL TECH CO LTD
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Patent Information

Application Number
CN202411059896.0
Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
Filing Date
2024-08-05
Publication Date
2024-12-13
Estimated Expiration
2044-08-05

AI Technical Summary

Technical Problem

The contact time between alkali and acid gas in traditional horizontal alkaline washing towers is insufficient, resulting in low alkali utilization efficiency, and large consumption of alkali liquid, resulting in a large amount of hazardous waste, which increases the treatment cost and environmental burden.

Method used

A horizontal alkaline washing device is designed, by fully contacting the acid gas absorbed by cold oil with the alkali liquid in a multi-stage stirring reaction chamber, and refluxing the separated alkali liquid into the horizontal tank using an alkali liquid circulation pump. Achieve the recycling of alkali liquid and reduce acid corrosion and waste alkali emissions.

Benefits of technology

It improves the utilization efficiency of lye, reduces the generation of hazardous waste, extends the operating cycle of the device, and saves resources and operating costs.

✦ Generated by Eureka AI based on patent content.

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Abstract

The present invention relates to the technical field of waste gas alkali washing, and in particular to a horizontal alkali washing device and a method for using the same, comprising a supporting base, a horizontal alkali washing mechanism and an air intake pipe, wherein the end of a salt cooling assembly is connected to the end of an alkali washing assembly, the end of the alkali washing assembly is connected to an oil-alkali separation assembly, and the oil-alkali separation assembly can return the separated alkali solution to the alkali washing assembly through an alkali solution circulation pump for recycling, and the air intake pipe is installed on a cold oil absorption assembly. In the horizontal alkali washing device and method for using the present embodiment, the separated alkali solution is returned to a horizontal tank with stirring through an alkali solution circulation pump for reuse. This recycling process not only saves resources, but also reduces operating costs. At the same time, through the cold oil absorption assembly, the salt cooling assembly and the alkali washing assembly, the acidic gas can be effectively converted into harmless substances during the multi-stage stirring and reaction process, while optimizing the efficiency of the use of the alkali solution.
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Description

Technical Field

[0001] The invention relates to the technical field of waste gas alkali washing, and in particular to a horizontal alkali washing device and a use method thereof. Background Art

[0002] In the prior art, the acid gas discharged from the top of the glue tank is usually treated by an alkali scrubber. The alkali scrubber is a device for gas purification, which mainly removes acidic substances in the gas through acid-base neutralization reaction. During operation, the gas phase in the glue tank enters from the middle and lower part of the tower, and the circulating alkali liquid is injected from the top of the tower through a circulating pump to form a top-down flow. In this way, the acid gas from the bottom to the top and the alkali liquid from the top to the bottom are fully contacted and the acid-base neutralization reaction is carried out on the tower plate;

[0003] Although alkali washing towers are widely used in industrial applications, they have several major problems. First, due to the relatively short residence time of the alkali solution in the tower, the alkali washing effect is usually not ideal. The contact time between the alkali solution and the acidic gas is not enough to achieve complete acid-base neutralization, so the utilization efficiency of the alkali is not high. Secondly, this operation mode leads to a large consumption of alkali solution, which in turn produces a large amount of alkali discharge and corresponding hazardous waste, increasing the treatment cost and environmental burden. Summary of the invention

[0004] The present application aims to solve one of the technical problems in the related art at least to some extent.

[0005] To this end, the first purpose of the present application is to solve the problem of traditional horizontal alkali washing device and its use method. The mixture of acidic gas and cold oil that has been fully alkali washed can be overflowed from the top of the last reaction chamber to the oil-alkali separation tank for separation, and the separated alkali liquid is returned to the horizontal tank with stirring through an alkali liquid circulation pump for recycling. Thus, the acid corrosion problem of the device is alleviated, and the utilization efficiency of the alkali is very high. It is only necessary to control the alkali concentration in the horizontal tank with stirring. When the alkali concentration is lower than the control range, a certain amount of alkali liquid can be added. There is no need to discharge the waste alkali regularly, the amount of hazardous waste is low, and the operation cycle is long.

[0006] To achieve the above-mentioned purpose, the first aspect of the present application proposes a horizontal alkali washing device and a method of using the same, comprising a supporting base, a horizontal alkali washing mechanism and an air intake pipe, wherein the horizontal alkali washing mechanism is installed on the top of the supporting base, and the air intake pipe is installed on the horizontal alkali washing mechanism. The horizontal alkali washing mechanism comprises a cold oil absorption component, a salt cooling component, an alkali washing component and an oil-alkali separation component, wherein the cold oil absorption component, the salt cooling component, the alkali washing component and the oil-alkali separation component are all installed on the supporting base, the end of the cold oil absorption component is connected to the end of the salt cooling component, the end of the salt cooling component is connected to the end of the alkali washing component, the end of the alkali washing component is connected to the oil-alkali separation component, and the oil-alkali separation component can return the separated alkali solution to the alkali washing component through an alkali solution circulation pump for recycling, and the air intake pipe is installed on the cold oil absorption component.

[0007] In the horizontal alkali washing device and the use method thereof of the embodiment of the present application, the waste gas is sequentially treated through a cold oil absorption component, a salt cooling component, an alkali washing component and an oil-alkali separation component, and then the alkali liquid separated by the oil-alkali separation component is returned to the horizontal tank with stirring through an alkali liquid circulation pump for reuse. This recycling process not only saves resources but also reduces operating costs. At the same time, through the cold oil absorption component, the salt cooling component and the alkali washing component, the acidic gas can be effectively converted into harmless substances in the multi-stage stirring and reaction process, and the use efficiency of the alkali liquid is optimized.

[0008] In addition, the horizontal alkali washing device and the method for using the same proposed in the present application may also have the following additional technical features:

[0009] As a preferred solution of the present invention, the cold oil absorption component includes an assembly plate, a cold oil bin, a first pump body, a spray plate, a spray pipe and a connecting piece, wherein the assembly plate is fixedly connected to one side of the top of the support base, the cold oil bin is fixedly connected to the top of the assembly plate, the first pump body is installed on the top of the cold oil bin, and the input end of the first pump body passes through the top of the cold oil bin, the spray plate is embedded in the outer wall of the air intake pipe, the spray pipe is arranged between the spray plate and the first pump body, and they are connected through the spray pipe, and the connecting piece is arranged between the end of the air intake pipe and the salt cooling assembly, and they are connected through the connecting piece.

[0010] As a preferred solution of the present invention, the connecting member includes a second pump body and a connecting pipe, wherein the second pump body is installed on the top of the support base and opposite to one side of the assembly plate, and the connecting pipe is arranged between the second pump body and the salt-cooling cooling assembly, and they are connected through the connecting pipe.

[0011] As a preferred scheme of the present invention, the salt-cooled cooling assembly includes a first support frame, a cooling tank, a third pump body, an input pipe and an output pipe, wherein the first support frame is fixedly connected to the other side of the top of the support base, the cooling tank is clamped on the inner wall of the first support frame, one end of the cooling tank is connected to one end of the connecting pipe, the third pump body is installed on the top of the support base, and relative to one side of the first support frame, the other end of the cooling tank is provided with the input pipe between the third pump body, and the two are connected through the input pipe, and the output pipe is provided between the alkali washing assembly and the third pump body, and the two are connected through the output pipe.

[0012] As a preferred scheme of the present invention, the alkali washing assembly includes a second support frame, an alkali washing tank, a partition, a connecting groove and a stirring member, wherein the second support frame is fixedly connected to the top of the support base, the alkali washing tank is clamped on the inner wall of the second support frame, one end of the output pipe passes through one end of the outer wall of the alkali washing tank, a plurality of partitions are fixedly connected to the inner wall of the alkali washing tank and separate the interior of the alkali washing tank into a plurality of reaction chambers, the connecting grooves are all opened at the bottom of the partition, and the stirring member is installed on the partition.

[0013] As a preferred solution of the present invention, the stirring member includes a driving motor, a driving rod, a fixed sleeve, a stirring plate and a through hole, wherein the driving motor is installed at the end of the outer wall of the alkali cleaning tank, one end of the driving rod is fixedly connected to the output end of the driving motor, the other end of the driving rod passes through a plurality of the partitions in sequence, and is rotatably connected to one end of the inner wall of the alkali cleaning tank, the plurality of fixed sleeves are respectively located in the corresponding reaction chambers and fixedly sleeved on the outer wall of the driving rod, the plurality of stirring plates are fixedly connected to the outer wall of the fixed sleeve in a circular array, and the through holes are evenly opened on the side walls of the stirring plates.

[0014] As a preferred solution of the present invention, the oil-alkali separation assembly includes a fixed seat, an oil-alkali separation tank, a reflux pipe and an overflow pipe, wherein the fixed seat is fixedly connected to one end of the top of the support base, the oil-alkali separation tank is clamped on the inner wall of the fixed seat, one end of the reflux pipe is connected to the outer wall of the alkali washing tank through a circulating pump, and the reflux pipe is arranged between the other end of the outer wall of the alkali washing tank and the oil-alkali separation tank, and is connected through the reflux pipe.

[0015] As a preferred solution of the present invention, a liquid inlet pipe is installed on the top of the alkali cleaning tank.

[0016] As a preferred solution of the present invention, a plurality of spray heads are installed at equal intervals on the bottom of the spray plate.

[0017] As a preferred solution of the present invention, the following steps are included:

[0018] S1. Preliminary treatment of acid gas. First, the acid gas discharged from the top of the glue tank is guided to the cold oil absorption system, and the acid gas is initially purified by the absorption effect of the cold oil;

[0019] S2, temperature adjustment, the gas after being absorbed by cold oil is further sent to the salt cooling system;

[0020] S3, entering the stirring horizontal tank, the cooled gas is then introduced into the first stirring reaction chamber, the gas enters from the top of the reaction chamber, and begins to react with the alkali solution pre-filled in the horizontal tank;

[0021] S4, multi-stage neutralization reaction, the mixture in the first reaction chamber flows into the second reaction chamber through the gap under the partition, and the alkali solution continues to react with the incompletely neutralized acidic gas in multiple reaction chambers;

[0022] S5, gas-liquid separation, the fully reacted mixture overflows from the top of the third reaction chamber and is then transported to the oil-alkali separation tank, where the alkali solution is separated from the cold oil to obtain clean alkali solution and oil;

[0023] S6, alkali solution circulation, the separated alkali solution is sent back to the horizontal tank with stirring through the alkali solution circulation pump.

[0024] Additional aspects and advantages of the present application will be given in part in the description below, and in part will become apparent from the description below, or will be learned through the practice of the present application.

[0025] Compared with the prior art, the present invention has the following beneficial effects:

[0026] 1. In the present invention, the waste gas after being absorbed by the cold oil enters from the top of the first reaction chamber, and after fully reacting with the alkali solution in the alkali washing tank under the stirring action of the stirring member, enters the second reaction chamber from the gap at the bottom of the partition for neutralization reaction. Similarly, the mixture of acidic gas and cold oil after sufficient alkali washing overflows from the top of the third reaction chamber to the oil-alkali separation component for separation. Therefore, in the multi-stage stirring and reaction process, the acidic gas can be effectively converted into harmless substances, and the use efficiency of the alkali solution is optimized.

[0027] 2. In the present invention, the other end of the driving rod passes through a plurality of partitions in sequence and is rotatably connected to one end of the inner wall of the alkali washing tank. A plurality of fixed sleeves are respectively located in corresponding reaction chambers and are fixedly sleeved on the outer wall of the driving rod. A plurality of stirring plates are fixedly connected to the outer wall of the fixed sleeve in a circular array. Through holes are evenly arranged on the side wall of the stirring plate. Then, the driving rod can be driven to rotate by starting the driving motor. Thus, under the action of the fixed sleeve, the stirring plate can be driven to stir the alkali solution in the alkali washing tank, so that the exhaust gas can fully react with the alkali solution in the alkali washing tank.

[0028] 3. In the present invention, the fixing seat is fixedly connected to one end of the top of the supporting base, the oil-alkali separation tank is clamped on the inner wall of the fixing seat, one end of the reflux pipe is connected to the outer wall of the alkali washing tank through a circulation pump, and a reflux pipe is arranged between the other end of the outer wall of the alkali washing tank and the oil-alkali separation tank, and they are connected through the reflux pipe, and then separated through the oil-alkali separation tank, and the separated alkali liquid is returned to the alkali washing tank through the alkali liquid circulation pump for recycling. BRIEF DESCRIPTION OF THE DRAWINGS

[0029] Figure 1 It is a structural schematic diagram of a horizontal alkali washing device and a method of using the same according to one embodiment of the present application;

[0030] Figure 2 It is a structural schematic diagram of a salt cooling assembly of a horizontal alkali washing device and a method of using the same according to one embodiment of the present application;

[0031] Figure 3 It is a structural schematic diagram of a cold oil bin of a horizontal alkali washing device and a method of using the same according to one embodiment of the present application;

[0032] Figure 4 A horizontal alkali cleaning device and a method for using the same according to an embodiment of the present application Figure 3 The enlarged structural diagram at A in the middle;

[0033] Figure 5 It is a schematic diagram of the structure inside the alkali washing tank of a horizontal alkali washing device and a method of using the same according to one embodiment of the present application;

[0034] Figure 6 It is a structural schematic diagram of a partition of a horizontal alkali washing device and a method of using the same according to one embodiment of the present application;

[0035] Figure 7 It is a structural schematic diagram of an oil-alkali separation tank of a horizontal alkali washing device and a method of using the same according to one embodiment of the present application;

[0036] Figure 8 A horizontal alkali cleaning device and a method for using the same according to an embodiment of the present application Figure 6 Schematic diagram of the enlarged structure at point B.

[0037] In the figure:

[0038] 1. Support base;

[0039] 2. Horizontal alkali cleaning mechanism; 21. Cold oil absorption assembly; 211. Assembly plate; 212. Cold oil tank; 213. First pump body; 214. Spray plate; 215. Spray pipe; 216. Connector; 2161. Second pump body; 2162. Connecting pipe; 22. Salt cooling assembly; 221. First support frame; 222. Cooling tank; 223. Third pump body; 224. Input pipe; 225. Output pipe; 23. Alkali washing assembly; 231, second support frame; 232, alkali washing tank; 2321, liquid inlet pipe; 233, partition; 234, connecting groove; 235, stirring element; 2351, driving motor; 2352, driving rod; 2353, fixed sleeve; 2354, stirring plate; 2355, through hole; 24, oil-alkali separation assembly; 241, fixed seat; 242, oil-alkali separation tank; 243, reflux pipe; 244, overflow pipe;

[0040] 3. Air intake duct. DETAILED DESCRIPTION

[0041] Embodiments of the present application are described in detail below, and examples of the embodiments are shown in the accompanying drawings, wherein the same or similar reference numerals throughout represent the same or similar elements or elements with the same or similar functions. The embodiments described below with reference to the accompanying drawings are exemplary and are intended to be used to explain the present application, and should not be construed as limitations on the present application. On the contrary, the embodiments of the present application include all changes, modifications and equivalents that fall within the spirit and connotation of the appended claims.

[0042] The horizontal alkali washing device and its use method of the embodiment of the present application are described below with reference to the accompanying drawings.

[0043] The embodiments of the present application provide a horizontal alkali washing device and a method of using the same. The device can separate a mixture of acidic gas and cold oil that has been sufficiently alkali washed by overflowing from the top of the last reaction chamber to the oil-alkali separation tank 242. The separated alkali liquid is returned to the horizontal tank with stirring through an alkali liquid circulation pump for recycling. Thus, the acid corrosion problem of the device is alleviated, and the utilization efficiency of the alkali is very high. It is only necessary to control the alkali concentration in the horizontal tank with stirring. When the alkali concentration is lower than the control range, a certain amount of alkali liquid can be added. There is no need to discharge the waste alkali regularly, the amount of hazardous waste is low, and the operation cycle is long.

[0044] like Figure 1-Figure 8 As shown, the horizontal alkali cleaning device and the use method thereof of the embodiment of the present application may include a supporting base 1, a horizontal alkali cleaning mechanism 2 and an air intake duct 3.

[0045] The horizontal alkali cleaning mechanism 2 is installed on the top of the supporting base 1 , and the air inlet pipe 3 is installed on the horizontal alkali cleaning mechanism 2 .

[0046] It should be noted that the support base 1 described in this embodiment is symmetrically fixedly connected to the two sides with guardrails, and one end of the air intake pipe 3 is connected to the top of the glue tank, so that the exhaust gas discharged from the top of the glue tank can be transported through the air intake pipe 3.

[0047] The horizontal alkali washing mechanism 2 comprises a cold oil absorption component 21 , a salt cooling component 22 , an alkali washing component 23 and an oil-alkali separation component 24 .

[0048] Among them, the cold oil absorption component 21, the salt cooling component 22, the alkali washing component 23 and the oil-alkali separation component 24 are all installed on the supporting base 1, the end of the cold oil absorption component 21 is connected to the end of the salt cooling component 22, the end of the salt cooling component 22 is connected to the end of the alkali washing component 23, the end of the alkali washing component 23 is connected to the oil-alkali separation component 24, and the oil-alkali separation component 24 can return the separated alkali solution to the alkali washing component 23 through the alkali solution circulation pump for recycling.

[0049] It should be noted that the exhaust gas described in this embodiment passes through the cold oil absorption component 21, the salt cooling component 22, the alkali washing component 23 and the oil-alkali separation component 24 in sequence, thereby effectively improving the effect of alkali washing. At the same time, the oil-alkali separation component 24 returns the separated alkali liquid to the alkali washing component 23 through the alkali liquid circulation pump for recycling. Therefore, the utilization efficiency of the alkali is very high. It is only necessary to control the alkali concentration of the alkali washing component 23. When the alkali concentration is lower than the control range, a certain amount of alkali liquid can be added. There is no need to discharge the waste alkali regularly, and the amount of hazardous waste is low.

[0050] The air intake pipe 3 is mounted on the cold oil absorption assembly 21 .

[0051] It should be noted that, when the exhaust gas is transported through the air intake pipe 3 as described in this embodiment, the exhaust gas can be cooled by the cold oil absorption component 21. At the same time, the acidic gas on the top of the glue tank can also be absorbed by the cold oil, and the acidic components in the gas are dissolved and absorbed by the cold oil, thereby purifying the gas.

[0052] Specifically, the waste gas is processed in turn through the cold oil absorption component 21, the salt cooling component 22, the alkali washing component 23 and the oil-alkali separation component 24, and then the alkali solution separated by the oil-alkali separation component 24 is returned to the horizontal tank with stirring through the alkali solution circulation pump for reuse. This recycling process not only saves resources but also reduces operating costs. At the same time, through the cold oil absorption component 21, the salt cooling component 22 and the alkali washing component 23, the acidic gas can be effectively converted into harmless substances in the multi-stage stirring and reaction process, and the utilization efficiency of the alkali solution is optimized.

[0053] In order to clearly illustrate the above embodiment, in one example of the present application, Figure 1-Figure 8 As shown, the cold oil absorption component 21 includes an assembly plate 211, a cold oil tank 212, a first pump body 213, a spray plate 214, a spray pipe 215 and a connector 216, wherein the assembly plate 211 is fixedly connected to one side of the top of the support base 1, the cold oil tank 212 is fixedly connected to the top of the assembly plate 211, the first pump body 213 is installed on the top of the cold oil tank 212, and the input end of the first pump body 213 passes through the top of the cold oil tank 212, the spray plate 214 is embedded in the outer wall of the air intake pipe 3, a spray pipe 215 is arranged between the spray plate 214 and the first pump body 213, and they are connected through the spray pipe 215, and a connector 216 is arranged between the end of the air intake pipe 3 and the salt cooling component 22, and they are connected through the connector 216.

[0054] It should be noted that the first pump body 213 described in this embodiment is fixedly connected to the top of the cold oil tank 212 by bolts, and an oil extraction pipeline is fixedly connected to the input end of the first pump body 213, and the cold oil tank 212 is integrally sleeved on the air intake pipe 3.

[0055] Furthermore, if Figure 4 As shown, a plurality of spray heads are installed at equal intervals at the bottom of the spray plate 214 .

[0056] Specifically, when the exhaust gas is transported through the air intake pipe 3, inside the cold oil tank 212, the exhaust gas in the air intake pipe 3 is first cooled by the cold oil in the cold oil tank 212. At the same time, when the exhaust gas is transported, the cold oil can be extracted through the first pump body 213 and sprayed through multiple spray heads. Therefore, after the acidic gas is absorbed by the cold oil, the acidic components in the gas are dissolved and absorbed by the cold oil, thereby purifying the gas, and the exhaust gas can also be cooled synchronously.

[0057] In one example of the present application, Figure 1-Figure 8 As shown, the connecting member 216 includes a second pump body 2161 and a connecting pipe 2162, wherein the second pump body 2161 is installed on the top of the support base 1 and relative to one side of the assembly plate 211, and a connecting pipe 2162 is provided between the second pump body 2161 and the salt cooling component 22, and they are connected through the connecting pipe 2162.

[0058] It should be noted that the connecting pipe 2162 described in this embodiment is a U-shaped pipe, so that the cold oil absorption component 21 and the salt cooling component 22 can be located on both sides of the alkali washing component 23, thereby effectively utilizing the processing space.

[0059] Specifically, after the exhaust gas passes through the air intake pipe 3 and is sprayed with cold oil, since the second pump body 2161 is installed on the top of the support base 1 and on one side relative to the assembly plate 211, a connecting pipe 2162 is provided between the second pump body 2161 and the salt cooling component 22, and they are connected through the connecting pipe 2162, and then by starting the second pump body 2161, the exhaust gas can be sent into the salt cooling component 22 through the connecting pipe 2162 for cooling operation.

[0060] In one embodiment of the present application, Figure 1-Figure 8 As shown, the salt-cooled cooling component 22 includes a first support frame 221, a cooling tank 222, a third pump body 223, an input pipe 224 and an output pipe 225, wherein the first support frame 221 is fixedly connected to the other side of the top of the support base 1, the cooling tank 222 is clamped on the inner wall of the first support frame 221, one end of the cooling tank 222 is connected to one end of the connecting pipe 2162, the third pump body 223 is installed on the top of the support base 1, and relative to one side of the first support frame 221, an input pipe 224 is arranged between the other end of the cooling tank 222 and the third pump body 223, and they are connected through the input pipe 224, and an output pipe 225 is arranged between the alkali washing component 23 and the third pump body 223, and they are connected through the output pipe 225.

[0061] It should be noted that the first support frame 221 described in this embodiment may include a support platform and multiple support frames, and the multiple support frames are fixedly connected to the top of the support platform at equal intervals, and the tops of the multiple support frames are provided with assembly grooves, so that the cooling tank 222 can be engaged in the assembly grooves.

[0062] As a possible situation, a spiral pipe is installed inside the cooling tank 222, and the two ends of the spiral pipe are respectively connected to one end of the input pipe 224 and one end of the connecting pipe 2162. The spiral pipe can increase the residence time of the exhaust gas in the cooling tank 222, thereby improving the cooling effect.

[0063] Specifically, in order to cool the exhaust gas and thus ensure the effect of subsequent alkali washing, the exhaust gas can be cooled by salt cooling through the cooling tank 222, and then under the action of the third pump body 223, the cooled exhaust gas can be transported to the alkali washing component 23 through the output pipe 225 for subsequent operations, thereby effectively improving the effect of alkali washing.

[0064] In one embodiment of the present application, Figure 1-Figure 8As shown, the alkali washing assembly 23 includes a second support frame 231, an alkali washing tank 232, a partition 233, a connecting groove 234 and a stirring member 235, wherein the second support frame 231 is fixedly connected to the top of the support base 1, the alkali washing tank 232 is clamped on the inner wall of the second support frame 231, one end of the output pipe 225 passes through one end of the outer wall of the alkali washing tank 232, a plurality of partitions 233 are fixedly connected to the inner wall of the alkali washing tank 232, and separate the interior of the alkali washing tank 232 into a plurality of reaction chambers, the connecting grooves 234 are all opened at the bottom of the partition 233, and the stirring member 235 is installed on the partition 233.

[0065] It should be noted that the second support frame 231 described in this embodiment includes a support platform and multiple support frames, the multiple support frames are fixedly connected to the top of the support platform at equal intervals, and the tops of the multiple support frames are provided with assembly grooves, so that the alkali washing tank 232 can be engaged in the assembly grooves.

[0066] Specifically, in order to improve the effect of alkali washing, the second support frame 231 is fixedly connected to the top of the support base 1, the alkali washing tank 232 is clamped on the inner wall of the second support frame 231, one end of the output pipe 225 passes through one end of the outer wall of the alkali washing tank 232, and a plurality of partitions 233 are fixedly connected to the inner wall of the alkali washing tank 232, and the interior of the alkali washing tank 232 is separated into a plurality of reaction chambers, and the connecting grooves 234 are all opened at the bottom of the partition 233, and the stirring member 235 is installed on the partition 233, so that the cooled exhaust gas enters the alkali washing tank 232, and the alkali washing tank 232 is used The partition 233 separates multiple reaction chambers with stirring. The waste gas after being absorbed by the cold oil enters from the top of the first reaction chamber, and under the stirring action of the stirring member 235, after fully reacting with the alkali solution in the alkali washing tank 232, enters the second reaction chamber from the gap at the bottom of the partition 233 for neutralization reaction. Similarly, the mixture of acidic gas and cold oil that has been fully alkali washed overflows from the top of the third reaction chamber to the oil-alkali separation component 24 for separation. Therefore, in the multi-stage stirring and reaction process, the acidic gas can be effectively converted into harmless substances, and the utilization efficiency of the alkali solution is optimized.

[0067] In one embodiment of the present application, Figure 1-Figure 8As shown, the stirring member 235 includes a driving motor 2351, a driving rod 2352, a fixed sleeve 2353, a stirring plate 2354 and a through hole 2355, wherein the driving motor 2351 is installed on the end of the outer wall of the alkali washing tank 232, one end of the driving rod 2352 is fixedly connected to the output end of the driving motor 2351, the other end of the driving rod 2352 passes through a plurality of partitions 233 in sequence, and is rotatably connected to one end of the inner wall of the alkali washing tank 232, a plurality of fixed sleeves 2353 are respectively located in corresponding reaction chambers, and are fixedly sleeved on the outer wall of the driving rod 2352, a plurality of stirring plates 2354 are fixedly connected to the outer wall of the fixed sleeve 2353 in a circular array, and through holes 2355 are evenly opened on the side wall of the stirring plate 2354.

[0068] It should be noted that a sealing rubber pad is installed at the intersection of the driving rod 2352 and the partition plate 233 described in this embodiment.

[0069] Specifically, by starting the driving motor 2351, the driving rod 2352 can be driven to rotate, thereby driving the stirring plate 2354 to stir the alkali solution in the alkali washing tank 232 under the action of the fixed sleeve 2353, so that the exhaust gas can fully react with the alkali solution in the alkali washing tank 232.

[0070] In one embodiment of the present application, Figure 1-Figure 8 As shown, the oil-alkali separation component 24 includes a fixed seat 241, an oil-alkali separation tank 242, a reflux pipe 243 and an overflow pipe 244, wherein the fixed seat 241 is fixedly connected to one end of the top of the support base 1, the oil-alkali separation tank 242 is clamped on the inner wall of the fixed seat 241, one end of the reflux pipe 243 is connected to the outer wall of the alkali washing tank 232 through a circulating pump, and a reflux pipe 243 is arranged between the other end of the outer wall of the alkali washing tank 232 and the oil-alkali separation tank 242, and is connected through the reflux pipe 243.

[0071] Specifically, separation is carried out in the oil-alkali separation tank 242, and the separated alkali solution is returned to the alkali washing tank 232 through an alkali solution circulation pump for recycling.

[0072] It should be understood that a liquid inlet pipe 2321 is installed on the top of the alkali cleaning tank 232 .

[0073] In one embodiment of the present application, Figure 1-Figure 8 As shown, the fall support alarm method for isolation facilities includes the following steps:

[0074] S1. Preliminary treatment of acidic gas. First, the acidic gas discharged from the top of the glue tank is guided to the cold oil absorption system. In this system, the acidic gas is initially purified by the absorption of cold oil. This process is mainly to remove the acidic components in the gas.

[0075] S2. Temperature regulation: the gas after being absorbed by cold oil is further sent to the salt cooling system. Through this process, the temperature of the gas is reduced to below 40 degrees. This step is necessary because lower temperature helps the efficiency of subsequent chemical reactions.

[0076] S3, enters the stirring horizontal tank, and the cooled gas is then introduced into the first stirring reaction chamber, where the gas enters from the top of the reaction chamber and begins to react with the alkali solution pre-filled in the horizontal tank. The function of the agitator is to ensure sufficient contact between the gas and the exhaust gas to promote the reaction;

[0077] S4, multi-stage neutralization reaction, the mixture in the first reaction chamber flows into the second reaction chamber through the gap under the separation plate, and so on, in multiple reaction chambers, the alkali solution continues to react with the incompletely neutralized acidic gas. This step increases the contact time between the gas and the alkali solution and improves the neutralization efficiency;

[0078] S5, gas-liquid separation, the fully reacted mixture overflows from the top of the third reaction chamber and is then transported to a separation tank, where the alkali solution is separated from the cold oil to obtain clean alkali solution and oil;

[0079] S6, alkali solution circulation: the separated alkali solution is sent back to the horizontal tank with stirring through the alkali solution circulation pump for reuse. This recycling process not only saves resources, but also reduces operating costs.

[0080] In summary, in the horizontal alkali washing device and the method of using the same in the embodiments of the present application, the waste gas is sequentially treated by the cold oil absorption component 21, the salt cooling component 22, the alkali washing component 23 and the oil-alkali separation component 24, and then the alkali liquid separated by the oil-alkali separation component 24 is returned to the horizontal tank with stirring through the alkali liquid circulation pump for reuse. This recycling process not only saves resources but also reduces operating costs. At the same time, through the cold oil absorption component 21, the salt cooling component 22 and the alkali washing component 23, the acidic gas can be effectively converted into harmless substances in the multi-stage stirring and reaction process, and the utilization efficiency of the alkali liquid is optimized.

[0081] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A horizontal alkali cleaning device, comprising a support base (1), a horizontal alkali cleaning mechanism (2) and an air intake pipe (3), characterized in that: It also includes a horizontal alkali washing mechanism (2); The horizontal alkali cleaning mechanism (2) is mounted on the top of the support base (1), and the air intake pipe (3) is mounted on the horizontal alkali cleaning mechanism (2); The horizontal alkali washing mechanism (2) comprises a cold oil absorption component (21), a salt cooling component (22), an alkali washing component (23) and an oil-alkali separation component (24), wherein: The cold oil absorption component (21), the salt cooling component (22), the alkali washing component (23) and the oil-alkali separation component (24) are all installed on the support base (1); The end of the cold oil absorption component (21) is connected to the end of the salt cooling component (22), and the end of the salt cooling component (22) is connected to the end of the alkali washing component (23); The end of the alkali washing component (23) is connected to the oil-alkali separation component (24), and the oil-alkali separation component (24) can return the separated alkali liquid to the alkali washing component (23) through an alkali liquid circulation pump for recycling; The air intake pipe (3) is installed on the cold oil absorption component (21); The alkali washing assembly (23) comprises a second support frame (231), an alkali washing tank (232), a partition (233), a connecting groove (234) and a stirring member (235), wherein: The second support frame (231) is fixedly connected to the top of the support base (1), and the alkali cleaning tank (232) is clamped on the inner wall of the second support frame (231); The plurality of partitions (233) are fixedly connected to the inner wall of the alkali washing tank (232) and separate the interior of the alkali washing tank (232) into a plurality of reaction chambers, and the connecting grooves (234) are all opened at the bottom of the partitions (233); The stirring member (235) is mounted on the partition (233); The stirring member (235) comprises a driving motor (2351), a driving rod (2352), a fixing sleeve (2353), a stirring plate (2354) and a through hole (2355), wherein: The driving motor (2351) is mounted on the end of the outer wall of the alkali washing tank (232); one end of the driving rod (2352) is fixedly connected to the output end of the driving motor (2351); the other end of the driving rod (2352) sequentially passes through the plurality of partitions (233) and is rotatably connected to one end of the inner wall of the alkali washing tank (232); The plurality of fixed sleeve plates (2353) are respectively located in the corresponding reaction chambers and are fixedly sleeved on the outer wall of the driving rod (2352); The plurality of stirring plates (2354) are fixedly connected to the outer wall of the fixed sleeve plate (2353) in a circular array, and the through holes (2355) are evenly opened on the side walls of the stirring plates (2354).

2. The horizontal alkali cleaning device according to claim 1 is characterized in that: The cold oil absorption assembly (21) comprises an assembly plate (211), a cold oil tank (212), a first pump body (213), a spray plate (214), a spray pipe (215) and a connecting piece (216), wherein: The assembly plate (211) is fixedly connected to one side of the top of the support base (1), and the cold oil tank (212) is fixedly connected to the top of the assembly plate (211); The first pump body (213) is installed on the top of the cold oil bin (212), and the input end of the first pump body (213) passes through the top of the cold oil bin (212); the spray plate (214) is embedded in the outer wall of the air inlet pipe (3); the spray pipe (215) is provided between the spray plate (214) and the first pump body (213), and they are connected via the spray pipe (215); The connecting piece (216) is provided between the end of the air intake pipe (3) and the salt cooling assembly (22), and they are connected via the connecting piece (216).

3. The horizontal alkali cleaning device according to claim 2 is characterized in that: The connecting member (216) comprises a second pump body (2161) and a connecting pipe (2162), wherein: The second pump body (2161) is mounted on the top of the support base (1) and on one side opposite to the assembly plate (211); The connecting pipe (2162) is provided between the second pump body (2161) and the salt cooling component (22), and the second pump body (2161) and the salt cooling component (22) are connected via the connecting pipe (2162).

4. The horizontal alkali cleaning device according to claim 3 is characterized in that: The salt cooling assembly (22) comprises a first support frame (221), a cooling tank (222), a third pump body (223), an input pipeline (224) and an output pipeline (225), wherein: The first support frame (221) is fixedly connected to the other side of the top of the support base (1), the cooling tank (222) is clamped on the inner wall of the first support frame (221), and one end of the cooling tank (222) is connected to one end of the connecting pipe (2162); The third pump body (223) is installed on the top of the support base (1), and relative to one side of the first support frame (221), and the input pipe (224) is provided between the other end of the cooling tank (222) and the third pump body (223), and they are connected via the input pipe (224); The output pipe (225) is provided between the alkali washing component (23) and the third pump body (223), and the two are connected via the output pipe (225); One end of the output pipe (225) passes through one end of the outer wall of the alkali washing tank (232).

5. The horizontal alkali cleaning device according to claim 4 is characterized in that: The oil-alkali separation component (24) comprises a fixing seat (241), an oil-alkali separation tank (242), a return pipe (243) and an overflow pipe (244), wherein: The fixing seat (241) is fixedly connected to one end of the top of the supporting base (1), and the oil-alkali separation tank (242) is clamped on the inner wall of the fixing seat (241); One end of the reflux pipe (243) is connected to the outer wall of the alkali washing tank (232) via a circulation pump; The reflux pipe (243) is provided between the other end of the outer wall of the alkali washing tank (232) and the oil-alkali separation tank (242), and the two are connected via the reflux pipe (243).

6. The horizontal alkali cleaning device according to claim 5, characterized in that: A liquid inlet pipe (2321) is installed on the top of the alkali washing tank (232).

7. The horizontal alkali cleaning device according to claim 2 is characterized in that: A plurality of spray heads are installed at equal intervals on the bottom of the spray plate (214).

8. The method for using the horizontal alkali cleaning device according to any one of claims 1 to 7, characterized in that: The following steps are involved: S1. Preliminary treatment of acid gas. First, the acid gas discharged from the top of the glue tank is guided to the cold oil absorption system, and the acid gas is initially purified by the absorption effect of the cold oil; S2, temperature adjustment, the gas after being absorbed by cold oil is further sent to the salt cooling system; S3, entering the stirring horizontal tank, the cooled gas is then introduced into the first stirring reaction chamber, the gas enters from the top of the reaction chamber, and begins to react with the alkali solution pre-filled in the horizontal tank; S4, multi-stage neutralization reaction, the mixture in the first reaction chamber flows into the second reaction chamber through the gap under the partition, and the alkali solution continues to react with the incompletely neutralized acidic gas in multiple reaction chambers; S5, gas-liquid separation, the fully reacted mixture overflows from the top of the third reaction chamber and is then transported to the oil-alkali separation tank, where the alkali solution is separated from the cold oil to obtain clean alkali solution and oil; S6, alkali solution circulation, the separated alkali solution is sent back to the horizontal tank with stirring through the alkali solution circulation pump.