Salt-containing wastewater and waste gas combined incineration treatment device and method

Abstract

The invention relates to the technical field of waste incineration, in particular to a salt-containing waste water and waste gas combined incineration treatment device and method.The method comprises the steps that waste gas and salt-containing waste water are monitored through a VOCs concentration sensor at an inlet and enter waste salt treatment assemblies at all levels according to the concentration to be treated, it is guaranteed that treatment reaches the standard, and combustion resources are saved; the incineration treatment device is high in heat recovery efficiency, the waste salt treatment energy efficiency is greatly improved through concentration-based treatment, the whole system achieves co-treatment of waste gas and salt-containing waste water, meanwhile, stable operation of the device is guaranteed, it is guaranteed that treatment reaches the standard, combustion resources are saved, and by dynamically adjusting the size of the combustion chamber, waste gas and waste water are optimized and matched; according to the invention, sufficient combustion is ensured, fuel waste is reduced, the overall combustion efficiency is improved, waste gas and waste water of different types and components are treated, the adaptability is high, the complex working condition requirements can be flexibly met, and meanwhile, the temperature of the connected regenerative chambers is reduced, the temperature difference is reduced, and the damage to the heat accumulators is prevented.

Description

Technical Field

[0001] The present invention relates to the technical field of waste incineration, and in particular to a device and method for combined incineration treatment of saline wastewater and waste gas. Background Art

[0002] The specific composition of industrial waste salt varies depending on its source, but it usually contains a large amount of organic matter that is difficult to separate, tends to release strong irritating odors and is even highly toxic. The pharmaceutical industry mainly produces waste gas and saline wastewater in the production process, with large emissions and a wide range of organic matter concentrations and types, including benzene, toluene, ethanol, ethyl acetate, hydrogen chloride, etc.

[0003] In the process of waste salt disposal, common treatment methods include physical treatment, chemical treatment, biological treatment and membrane separation technology. Physical treatment involves phase separation, precipitation, filtration, incineration and other steps, aiming to remove solid particles and suspended matter in waste salt; chemical treatment promotes the precipitation or coagulation of organic matter and heavy metal ions by adding chemical agents such as aluminum sulfate and polyaluminum chloride; biological treatment uses microorganisms to degrade organic matter and oxidized salts; membrane separation technology further removes organic components in waste salt and dissolves internal particles through reverse osmosis, nanofiltration and other technical means. For the treatment of waste salt, it also involves evaporation and salt separation process, which requires analysis of the composition of the waste salt solution, calculation and control of the salt separation temperature and salt-nitrogen ratio based on the mass percentage and solubility of the inorganic salt, and precise control of the endpoint concentration of each evaporation. In some cases, if the content of a certain inorganic salt in the waste salt solution has a large advantage, it can be considered to separate and recover the component by direct evaporation and crystallization. However, these conventional treatment technologies mainly focus on the treatment of saline wastewater, while the treatment of waste gas usually involves more complex technologies and process flows. Therefore, in the face of complex waste salt disposal scenarios, most waste salt treatment technologies tend to only treat either waste gas or saline wastewater, with a single use occasion, which greatly increases the treatment cost. In addition, large pharmaceutical companies often need to treat large quantities of waste salt, and the above technologies often have problems such as high disposal costs, large construction costs, low waste salt treatment efficiency, and low intelligence level.

[0004] The incineration of waste salt is an important waste salt treatment technology. The organic matter in the waste salt is decomposed by high temperature to achieve harmless and resource utilization of the waste salt. The main process of waste salt incineration is to heat the waste salt to a high temperature, usually above 800°C, so that the inorganic salt melts and flows into the bottom of the furnace, while the organic matter volatilizes and decomposes at high temperature. This method can effectively remove the organic matter in the waste salt, while recovering the inorganic salt to achieve resource utilization of the waste salt. However, incineration treatment requires a lot of energy to increase the incineration temperature, the energy consumption is high, and the heating process in the furnace is slow, the heat utilization rate is low, and in addition, the waste salt after high temperature treatment is deposited on the bottom and wall of the furnace body, which will have a great impact on the system pipelines, equipment and waste salt treatment quality, and reduce the service life of the equipment and the treatment yield. Each maintenance and cleaning requires a lot of manpower and material resources, and the recovery and treatment cycle is long, which delays normal operation. Therefore, in order to ensure the efficient and stable incineration of waste salt, it is necessary to optimize and improve the incineration treatment device and working method.

[0005] The existing patent with publication number CN115751342A discloses a combined incineration device for acrylonitrile waste gas and waste liquid, comprising: a burner for treating fuel and high calorific value waste liquid; a high-temperature reduction zone for treating high calorific value waste liquid and a small amount of low calorific value waste water, and configured with preheated combustion air or a small amount of preheated waste gas; a low-temperature reduction zone for treating low calorific value waste water, and configured with preheated combustion air or a small amount of preheated waste gas; a high-temperature mixer, provided with a preheated air distributor, a preheated waste gas distributor, and an ammonia distribution pipe; a high-temperature oxidation zone, providing space for upstream reduced flue gas or waste gas to undergo chemical reactions; a medium-temperature mixer, provided with a normal-temperature air distributor, a preheated waste gas distributor, and an ammonia distribution pipe; a low-temperature oxidation zone, providing space for upstream flue gas or waste gas to undergo chemical reactions; a low-temperature mixer, provided with a normal-temperature air distributor; a solid salt temperature adjustment zone, providing space for upstream flue gas cooling and uniformly distributing flue gas flow rate, so as to achieve the purpose of controlling fuel-type NOx, with a longer flue gas residence time and a better mixing effect.

[0006] However, the above invention does not perform diversion treatment according to the concentration of exhaust gas and waste water, and the degree of refinement is low. The combustion chamber cannot adjust the chamber size and cannot adapt to exhaust gas and waste water of different concentrations and flow rates. Simple mixing of waste water and waste liquid cannot achieve uniform distribution, which has a certain impact on combustion efficiency. Summary of the invention

[0007] In view of the above problems in the prior art, the present invention is proposed.

[0008] In order to solve the above technical problems, the present invention provides the following technical solutions: a device for combined incineration of saline wastewater and waste gas, comprising an incinerator, a combustion chamber arranged at the lower part of the incinerator, and a burner arranged at the top of the combustion chamber, wherein an annular spray assembly is arranged inside the combustion chamber; It also includes a heat storage chamber disposed above the combustion chamber, the heat storage chamber including a primary heat storage chamber and a secondary heat storage chamber separated by a flow balancing orifice plate, and a wastewater inlet pipe disposed inside the heat storage chamber, the wastewater inlet pipe being used to preheat wastewater; A zeolite wheel molecular sieve assembly is provided upstream of the incinerator, an activated carbon filter assembly is provided upstream of the zeolite wheel molecular sieve assembly, a waste gas flow inlet and a waste water flow inlet are provided on the incinerator, a fan is provided at the waste gas flow inlet to drive the waste gas to flow along the waste gas transmission pipe, and a water pump is provided at the waste water flow inlet to drive the waste water to flow into the incinerator; VOCs concentration sensors are installed at the waste gas inlet and wastewater inlet to monitor the content of organic components so that they can be incinerated according to their concentration.

[0009] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, wherein: the combustion chamber is located in the lower area of ​​the incinerator and a flow balancing orifice plate is provided between the combustion chamber and the primary heat storage chamber, and an axial through hole is provided on the surface of the flow balancing orifice plate; The two ends of the flow balancing orifice plate are provided with telescopic devices for adjusting the internal space of the combustion chamber; and the inner wall surface of the combustion chamber is provided with an annular spray assembly.

[0010] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, the secondary heat storage chamber is composed of a plurality of phase-change heat storage bodies, and the surface of the phase-change heat storage body is staggered and axially distributed with gas-liquid through holes at equal intervals, and the apertures of the gas-liquid through holes are the same; Heat exchange fins are evenly arranged along the inner wall of the gas-liquid through hole, and serpentine tubes are evenly spaced inside the phase change heat storage body. The inlet end of the serpentine tube is connected to the wastewater inlet pipe, and the outlet end is connected to the annular spray assembly.

[0011] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, the annular spray assembly includes a waste gas inlet, a waste gas outer pipe, a waste water inner pipe, a first waste gas outlet, a waste water outlet, a through pipe and a nozzle, one end of the waste gas inlet is connected to the waste gas outer pipe, and the waste water inner pipe is coaxially sleeved in the waste gas outer pipe; The wastewater inner pipe and the waste gas outer pipe are provided with through pipes at equal intervals, the through pipes connect the wastewater outlet and the nozzle, the nozzle includes a diffusion chamber, a contraction chamber and a slit nozzle, one end of the nozzle is sealed and connected to the waste gas outer pipe, and the slit nozzle is located at the other end of the nozzle.

[0012] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, the zeolite rotor molecular sieve assembly includes a desorption chamber, a desorption waste gas inlet, a desorption fan, an adsorption fan, a rotor, a crawler, a motor, and a fixed bracket; The rotating wheel is fixed on the fixing bracket, and desorption chambers are provided on both sides of the rotating wheel and are connected to the secondary heat storage chamber.

[0013] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, the activated carbon filter assembly includes an air supply port, a settling port, a second waste gas outlet, a second air storage chamber, a receiving plate and a filter layer, and the filter layer includes a primary filter layer, a secondary filter layer and a tertiary filter layer from bottom to top; An air supply port is provided at the bottom of the activated carbon filter component, a filter mesh is radially provided at the air supply port, a second air storage chamber is provided at the top of the activated carbon filter component and is connected to the second exhaust gas outlet, a second pressure sensor is provided on the outside of the activated carbon filter component and is externally connected to a control unit; the control unit sets a pressure difference alarm value, and when the pressure difference in the activated carbon filter component reaches a first-level pressure difference alarm value, it reminds you to replace the filter material, and when it reaches a second-level pressure difference alarm value, it reminds you to release the pressure in the activated carbon filter component, and when it reaches a third-level pressure difference alarm value, it starts the emergency emptying mode.

[0014] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, the telescopic device comprises a slideway penetrating the outer wall of the incinerator, a positioning cover is provided outside the slideway, a connecting rod is slidably provided inside the slideway, a bracket is fixedly provided on the outer wall of the positioning cover, and a sliding rod is provided on the outer wall of the bracket; A lifting sleeve is slidably provided on the slide rod, and the lifting sleeve is fixedly connected to the connecting rod. One end of the connecting rod penetrates into the incinerator and is fixedly connected to the flow equalizing orifice plate, so that when the lifting sleeve is raised or lowered, the flow equalizing orifice plate is driven to rise and fall through the connecting rod.

[0015] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, wherein: an impeller is rotatably arranged in the waste gas inlet, a rotating shaft is fixedly arranged at the center of the impeller, the rotating shaft rotates and penetrates outside the waste gas inlet and is provided with an eccentric fan; The outer wall of the slide rod is also fixedly engaged with a fixing rod, the fixing rod is fixedly connected to the outer wall of the incinerator, the fixing rod is vertically provided with a support rod, the support rod is rotatably provided with an amplitude modulation rod, the amplitude modulation rod is parallelly provided with an amplitude modulation groove, and a slider is slidably provided in the amplitude modulation groove; A pull rod is provided on the end surface of the slider, a swing arm is rotatably provided in the lifting sleeve, an arc groove is opened on the swing arm, and a cylinder is provided at the end of the amplitude modulation rod, and the cylinder is slidably arranged on the arc groove.

[0016] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, wherein: the first-level heat storage chamber and the second-level heat storage chamber are respectively connected with a first branch pipe and a second branch pipe, the first branch pipe and the second branch pipe are respectively provided with a connecting pipe, and the two connecting pipes are arranged in parallel; A floating ball is slidably disposed in the connecting tube, and a rack is slidably disposed on the outer wall of the connecting tube. One end of the rack slides through the connecting tube and is fixedly connected to the outer wall of the floating ball.

[0017] As a preferred solution of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention, two racks are meshed with gears at the same time, a balance bar is provided for rotating the gear axis, an inclined block is provided at one end of the balance bar, and the inclined block slides through the pull rod.

[0018] The present invention also discloses a method for treating saline wastewater and waste gas by combined incineration, which is implemented based on the above-mentioned saline wastewater and waste gas combined incineration treatment device, and the steps of the method include: S1. Divert and preliminarily treat the waste gas, including: S1.1. A first concentration sensor is arranged in the exhaust gas transmission pipe, and the exhaust gas concentration is monitored based on the first concentration sensor, and the exhaust gas is divided into two parts: high-concentration exhaust gas and low-concentration exhaust gas; S1.2. A second fan is set to pump low-concentration exhaust gas into the activated carbon filter assembly; the activated carbon filter assembly transmits gas through the air supply port, and the low-concentration exhaust gas passes through the filter mesh to form an upward flow field inside the activated carbon filter assembly, and then passes through the primary filter layer, the secondary filter layer, and the tertiary filter layer in turn for preliminary filtration to remove large particle impurities; S2. Adsorption and desorption treatment of waste gas, including: S2.1. The low-concentration exhaust gas after preliminary filtration enters the zeolite rotor molecular sieve assembly through the adsorption fan for organic matter adsorption; S2.2. After the exhaust gas adsorption is completed, a third concentration sensor is set in the exhaust gas pipe of the desorption chamber to monitor the exhaust gas concentration. When the concentration reaches the standard, the exhaust gas is discharged; S2.3. If the exhaust gas concentration exceeds the standard or is incompletely adsorbed, the desorption fan introduces part of the gas into the desorption chamber to desorb the zeolite rotor molecular sieve assembly. The desorption chamber is connected to an exhaust gas ring pipe, and the exhaust gas after desorption returns to the combustion chamber through the exhaust gas ring pipe for incineration purification; S3. Incineration of high-concentration waste gas, including: S3.1, the high-concentration exhaust gas is pumped by the first fan and directly sent into the combustion chamber of the incinerator through the exhaust gas ring pipe; S3.2, spraying combustion aids through burners to assist in the incineration of high-concentration waste gas; S4. Discharge and heat storage treatment of the incineration waste gas obtained from incineration, including: S4.1. The incineration waste gas enters the primary heat storage chamber and the secondary heat storage chamber through the equalizing orifice plate, exchanges heat with the phase change heat storage body, and completes the heat storage process; S4.2. A guide orifice plate is provided on the inner wall of the incinerator. Most of the incineration waste gas after heat storage enters the gas storage chamber on the top of the incinerator through the guide orifice plate. A fourth concentration sensor is provided in the gas storage chamber to monitor the waste gas concentration. The gas is discharged after reaching the standard. S4.3. Another part of the exhaust gas enters the desorption chamber through the desorption fan to desorb the zeolite rotor molecular sieve assembly. The exhaust gas after desorption enters the combustion chamber again through the exhaust gas ring pipe for secondary incineration treatment.

[0019] S5. Pre-treatment of organic wastewater by diversion and incineration, including: S5.1. A second concentration sensor is provided in the organic wastewater flow channel to monitor the concentration of organic components and divert the wastewater according to the concentration of organic components; S5.2, the organic wastewater is pumped into the wastewater inlet pipe by a water pump, and flows into the primary heat storage chamber and the secondary heat storage chamber in sequence, and is preheated by the phase change heat storage body; S6. Incineration and purification of organic wastewater, including: S6.1. The preheated organic wastewater enters the annular spray assembly and is evenly sprayed into the combustion chamber for incineration and purification. S6.2. A fifth concentration sensor is installed in the flow channel of the purified wastewater to monitor the concentration, and the wastewater is discharged after reaching the standard; S7. Perform temperature monitoring and control, including: S7.1. Temperature sensors are installed on the side walls of the primary heat storage chamber and the secondary heat storage chamber to monitor the temperature of the phase change heat storage body; S7.2. When the temperature difference exceeds 100°C, the control unit adjusts the flow of the water pump to accelerate the flow rate of the wastewater through the wastewater inlet pipe to reduce the temperature difference; when the temperature difference is less than 100°C, the flow of the water pump is reduced to maintain the heat storage effect and protect the phase change heat storage body.

[0020] Beneficial effects of the present invention: an adjustable chamber combustion chamber is arranged inside the incinerator, and a two-stage heat storage chamber is arranged above the combustion chamber, so as to realize the cascade utilization of waste heat resources and reduce energy consumption. The annular spray assembly is located inside the combustion chamber, which is an inner and outer outer tube structure, realizing uniform spraying while realizing the coordinated treatment of waste gas and waste water. The waste gas and saline waste water are monitored by the VOCs concentration sensor at the inlet, and enter the waste salt treatment components of each level to complete the treatment according to the concentration, so as to ensure that the treatment meets the standard and save combustion resources. The incineration treatment device of the present invention has a high heat recovery efficiency, and the concentration treatment greatly improves the energy efficiency of waste salt treatment. The coordinated treatment of waste gas and saline waste water is realized in an overall and systematic manner, and the stable operation of the device is also ensured. By dynamically adjusting the size of the combustion chamber, the waste gas and waste water are optimized and matched to ensure full combustion, reduce fuel waste, realize uniform spraying of waste liquid, and fully and evenly mix with waste gas, improve the overall combustion efficiency, and at the same time realize the reduction of the temperature of the connected heat storage chamber, reduce the temperature difference, and prevent the damage of the heat storage body. BRIEF DESCRIPTION OF THE DRAWINGS

[0021] In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following briefly introduces the drawings required for describing the embodiments. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without creative work. Among them: Figure 1 This is a working principle diagram of the combined incineration treatment device for salt-containing wastewater and waste gas of the present invention; Figure 2 It is a structural schematic diagram of the secondary heat storage chamber of the present invention; Figure 3 It is a top view of the cross-section of the secondary heat storage chamber of the present invention; Figure 4 It is a side cross-sectional view of the secondary heat storage chamber of the present invention; Figure 5 It is a schematic structural diagram of the phase change thermal storage body of the present invention; Figure 6 is an axial cross-sectional view of the phase change thermal storage body of the present invention; Figure 7 It is a structural schematic diagram of the flow balancing orifice plate of the present invention; Figure 8 It is a structural schematic diagram of the annular spray assembly of the present invention; Fig. 9 It is a nozzle structure diagram of the annular spray assembly of the present invention; Fig.10 It is a schematic structural diagram of the zeolite wheel molecular sieve assembly of the present invention; Fig.11 It is a schematic structural diagram of the activated carbon filter assembly of the present invention; Fig.12 It is the overall schematic diagram of the incinerator in the present invention; Fig.13 For the present invention Fig.12 Schematic diagram of the structure of the middle A area; Fig.14 It is an enlarged schematic diagram of the interior of the incinerator in the present invention; Fig.15 For the present invention Fig.14 A magnified view of the structure of region B; Fig.16 For the present invention Fig.14 A magnified view of the C region structure; Fig.17 For the present invention Fig.14 A magnified view of the D region structure; Fig.18 The present invention is a flow chart of a method for combined incineration treatment of saline wastewater and waste gas.

[0022] Reference numerals: 1, incinerator; 2, zeolite rotor molecular sieve assembly; 2-1, desorption chamber; 2-2, desorption exhaust gas inlet; 2-3, desorption fan; 2-4, adsorption fan; 2-5, rotor; 2-6, crawler; 2-7, motor; 2-8, fixed bracket; 3. Activated carbon filter assembly; 3-1. Air supply port; 3-2. Settling port; 3-3. Second exhaust gas outlet; 3-4. Second air storage chamber; 3-5. Receiver plate; 3-6. Third-level filter layer; 3-6a. Microporous activated carbon; 3-7. Secondary filter layer; 3-7a. Transition pore activated carbon; 3-8. First-level filter layer; 3-8a. Macroporous activated carbon; 4. First fan; 5. Second fan; 6. Water pump; 7. First concentration sensor; 8. Second concentration sensor; 9. First gas stop valve; 10. Second gas stop valve; 11. Third concentration sensor; 12. Fourth concentration sensor; 13. Fifth concentration sensor; 14. Third gas stop valve; 15. Fourth gas stop valve; 16. Burner; 17. Gas storage chamber; 18. Combustion chamber; 19. Primary heat storage chamber; 20, secondary heat storage chamber; 20-1, phase change heat storage body; 20-1a, gas-liquid through hole; 20-1b, heat exchange fin; 20-2, desorption gas inlet; 20-3, guide cover; 20-4, desorption gas pipe; 21, first liquid stop valve; 22, second liquid stop valve; 23, flow equalizing orifice plate; 23-1, through hole; 24, guide orifice plate; 25, telescopic device; 251, slideway; 252, positioning cover; 253, connecting rod; 254, bracket; 255, sliding rod; 256, lifting sleeve; 257, impeller; 258, rotating shaft; 259, eccentric fan; 2511, fixing rod; 2512, supporting rod; 2513, amplitude modulation rod; 2514, amplitude modulation groove; 2515, sliding block; 2516, pulling rod; 2517, cylinder; 2518, first branch pipe; 2519, second branch pipe; 2521, connecting pipe; 2523, rack; 2524, gear; 2525, balance rod; 2526, inclined block; 26, annular spray assembly; 26-1, exhaust gas inlet; 26-10, annular pipe bracket; 26-2, exhaust gas outer pipe; 26-3, wastewater inner pipe; 26-4, wastewater outlet; 26-5, first exhaust gas outlet; 26-6, diffusion chamber; 26-7, contraction chamber; 26-8, slit outlet; 26-9, through pipe; 27. First pressure sensor; 28. First temperature sensor; 29. ​​Second temperature sensor; 30. Third temperature sensor; 31. Fourth temperature sensor; 32. Second pressure sensor; 33. Third pressure sensor; 34. Wastewater inlet pipe. DETAILED DESCRIPTION

[0023] In order to make the above-mentioned objects, features and advantages of the present invention more obvious and easy to understand, the specific implementation methods of the present invention are described in detail below in conjunction with the accompanying drawings.

[0024] In the following description, many specific details are set forth to facilitate a full understanding of the present invention, but the present invention may also be implemented in other ways different from those described herein, and those skilled in the art may make similar generalizations without violating the connotation of the present invention. Therefore, the present invention is not limited to the specific embodiments disclosed below.

[0025] Secondly, the term "one embodiment" or "embodiment" as used herein refers to a specific feature, structure, or characteristic that may be included in at least one implementation of the present invention. The term "in one embodiment" that appears in different places in this specification does not necessarily refer to the same embodiment, nor does it refer to a separate or selective embodiment that is mutually exclusive with other embodiments.

[0026] Example 1 Reference Figure 1 to Figure 17 , which is the first embodiment of the present invention, provides a device for combined incineration treatment of salt-containing wastewater and waste gas.

[0027] Specifically, a salt-containing wastewater and waste gas combined incineration treatment device comprises: an incinerator 1, a combustion chamber 18 arranged at the lower part of the incinerator 1, a burner 16 arranged at the top of the combustion chamber 18, an annular spray assembly 26 arranged inside the combustion chamber 18, and a heat storage chamber arranged above the combustion chamber 18, wherein the heat storage chamber comprises a primary heat storage chamber 19 and a secondary heat storage chamber 20 separated by a flow balancing orifice plate 23; a desorption gas inlet 20-2, a guide cover 20-3, and a desorption gas pipe 20-4 are arranged above the secondary heat storage chamber 20; A wastewater inlet pipe 34 is provided inside the primary heat storage chamber 19 and the secondary heat storage chamber 20. The device also includes a zeolite wheel molecular sieve assembly 2 arranged upstream of the incinerator 1, an activated carbon filter assembly 3 arranged upstream of the zeolite wheel molecular sieve assembly 2, and the incinerator 1 is provided with a waste gas flow inlet and a wastewater flow inlet. A fan is provided at the waste gas flow inlet to drive the waste gas to flow along the waste gas transmission pipe, and the waste gas transmission pipe is used to transmit the waste gas. A water pump 6 is provided at the wastewater flow inlet to drive the wastewater flow along the wastewater flow channel into the incinerator 1; VOCs concentration sensors are installed at the waste gas flow inlet and the wastewater flow inlet. The VOCs concentration sensors are used to monitor the content of organic components and send them into each device for incineration treatment according to their concentrations. When the content of organic waste components is lower than 1.5 times the allowable emission concentration, it is a low concentration, and greater than or equal to 1.5 times the allowable emission concentration is a high concentration. The allowable emission concentration refers to the volatile organic compound unorganized emission control standard.

[0028] Better yet, see Figures 1 to 7In this embodiment: the combustion chamber 18 is located in the lower area of ​​the incinerator 1 and is provided with a flow equalizing orifice plate 23 between the combustion chamber 18 and the primary heat storage chamber 19. Axial through holes 23-1 are evenly spaced and staggered on the surface of the flow equalizing orifice plate 23. The exhaust gas after combustion first enters the primary heat storage chamber 19 through the through hole 23-1 to complete heat storage, and then enters the gas storage chamber 17 at the top of the incinerator 1 after heat storage in the secondary heat storage chamber 20 and is discharged.

[0029] Preferably, telescopic devices 25 are provided at both ends of the flow equalizing orifice plate 23 to adjust the size of the internal space of the combustion chamber 18 and improve the combustion temperature and efficiency; an annular spray assembly 26 is provided along the inner wall of the upper part of the combustion chamber 18, and a triangular ring tube bracket 26-10 is welded between the annular spray assembly 26 and the inner wall of the incinerator 1.

[0030] The secondary heat storage chamber 20 is composed of a plurality of phase-change heat storage bodies 20-1. The surface of the phase-change heat storage body 20-1 is axially distributed with gas-liquid through holes 20-1a at equal intervals and the apertures of the gas-liquid through holes 20-1a are the same.

[0031] More preferably, heat exchange fins 20-1b are evenly arranged along the inner wall of the gas-liquid through hole 20-1a. The heat exchange fins 20-1b are longitudinal tree-shaped straight fins. Each group of fins includes left and right fins and upper and lower fins. The fins are staggered and arranged at equal intervals. The sum of the maximum transverse diameters between the heat exchange fins 20-1b is smaller than the inner diameter of the through hole 20-1a.

[0032] Among them, serpentine pipes are arranged at equal intervals inside the phase change heat storage body 20-1, the inlet end of the serpentine pipe is connected to the wastewater inlet pipe 34, and the outlet end is connected to the annular spray assembly 26; the component size and structure of the lower first-level heat storage chamber 19 and the second-level heat storage chamber 20 are completely consistent.

[0033] It should be noted that the phase change thermal storage body 20 - 1 material includes but is not limited to ceramic thermal storage material, molten salt thermal storage material, concrete thermal storage material, alkaline earth metal composite phase change thermal storage material, etc.

[0034] For further information, see Figure 1 , Figure 8 and Fig. 9 In this embodiment: the annular spray assembly 26 includes an exhaust gas inlet 26-1, an exhaust gas outer pipe 26-2, a wastewater inner pipe 26-3, a first exhaust gas outlet 26-5, a wastewater outlet 26-4, a through pipe 26-9 and a nozzle, one end of the exhaust gas inlet 26-1 is connected to the exhaust gas outer pipe 26-2, the wastewater inner pipe 26-3 is coaxially sleeved in the exhaust gas outer pipe 26-2, and the wastewater inlet pipe 34 extends from the first-level heat storage chamber 19, passes through the flow balancing orifice plate 23 and is sealed and connected to the wastewater inner pipe 26-3.

[0035] Among them, through pipes 26-9 are opened vertically downward at equal intervals between the wastewater inner pipe 26-3 and the exhaust gas outer pipe 26-2 along the pipe section direction. The length of the through pipe 26-9 is equal to the distance between the pipe walls of the wastewater inner pipe 26-3 and the exhaust gas outer pipe 26-2. The through pipe 26-9 connects the wastewater outlet 26-4 with the nozzle. Four first exhaust gas outlets 26-5 are opened on the outer pipe side walls on both sides of the through pipe 26-9 and are connected to the nozzle.

[0036] More preferably, the nozzle includes a diffusion chamber 26-6, a contraction chamber 26-7 and a slit nozzle 26-8. One end of the nozzle is sealed and connected to the exhaust gas outer pipe 26-2. The port diameter of the nozzle is the sum of the diameter of the through pipe 26-9 and the diameter of the first exhaust gas outlet 26-5. The other end is provided with a slit nozzle 26-8. The diameter of the slit nozzle 26-8 is 1 / 3 or 1 / 4 of the diameter of the through pipe 26-9. The length of the slit is 1 / 2 of the diameter of the through pipe 26-9. The pipe mouth and the slit nozzle 26-8 are connected in sequence through the diffusion chamber 26-6 and the contraction chamber 26-7. The width of the diffusion chamber 26-6 is slightly larger than the diameter of the nozzle port, and the height is 2 to 3 times the diameter of the pipe mouth of the through pipe 26-9. The diffusion chamber 26-6 is approximately truncated cone in shape as a whole, and slit outlets 26-8 with the same width as the pipe mouth of the through pipe 26-9 are opened on the walls on both sides as pressure relief diversion ports. The axial section of the contraction chamber 26-7 is in the shape of an inverted trapezoid, and its height is equal to the diameter of the pipe mouth of the through pipe 26-9.

[0037] It should be noted that the outer wall of the outer exhaust pipe 26-2 in the annular spray assembly 26 is arc sprayed with a high temperature and corrosion resistant metal coating, and the base material of the metal coating includes but is not limited to nickel, copper, tungsten carbide and nano-metal ceramics.

[0038] Example 2 Reference Figure 1 to Figure 10 , which is the second embodiment of the present invention, and this embodiment is based on the previous embodiment.

[0039] For details, please refer to Figure 1 and Fig. 9 In this embodiment, the zeolite rotor molecular sieve assembly 2 includes a desorption chamber 2-1, a desorption exhaust gas inlet 2-2, a desorption fan 2-3, an adsorption fan 2-4, a rotor 2-5, a track 2-6, a motor 2-7, and a fixed bracket 2-8; the rotor 2-5 is fixed on the fixed bracket 2-8, and the motor 2-7 drives the track 2-6 to drive the rotor 2-5 to work, and the exhaust gas is discharged after purification is completed.

[0040] More preferably, desorption chambers 2-1 are provided on both sides of the upper part of the wheel 2-5 and are connected to the secondary heat storage chamber 20. After the purified exhaust gas that has released heat in the secondary heat storage chamber 20 completes the desorption work, it circulates into the combustion chamber 18 again to complete the purification. The motor 2-7 drives the crawler 2-6 and then drives the wheel 2-5 to work.

[0041] The desorption waste gas inlet 2-2 is connected to the interior of the desorption chamber 2-1, part of the waste gas enters the desorption chamber 2-1 through the desorption fan 2-3, and part of the waste gas enters the zeolite rotor molecular sieve assembly 2 through the adsorption fan 2-4.

[0042] Preferably, the zeolite rotor molecular sieve assembly 2 is connected to a third concentration sensor 11 for monitoring the exhaust gas concentration. The organic exhaust gas discharged from the adsorption chamber is discharged after being monitored by the third concentration sensor 11 and meeting the standards.

[0043] See also Figure 1 and Fig.10 In this embodiment, the activated carbon filter assembly 3 includes an air supply port 3-1, a sedimentation port 3-2, a second exhaust gas outlet 3-3, a second air storage chamber 3-4, a receiving plate 3-5 and a filter layer; the filter layer includes a primary filter layer 3-8, a secondary filter layer 3-7, and a tertiary filter layer 3-6 from bottom to top; an air supply port 3-1 is provided at the bottom of the activated carbon filter assembly 3, and a filter mesh is radially provided at the air supply port 3-1.

[0044] Among them, the filter layers are arranged axially at equal intervals inside the activated carbon filter assembly 3, and a sedimentation port 3-2 is provided outside each filter layer for replacing the filter material, and visible impurities can also be separated and discharged. The filter layer is a grid structure, which can be used as a diverter plate to guide the exhaust gas to flow upward. Activated carbon is laid on the filter layer. The first-level filter layer 3-8 includes macroporous activated carbon 3-8a, the second-level filter layer 3-7 includes transitional pore activated carbon 3-7a, and the third-level filter layer 3-6 includes microporous activated carbon 3-6a.

[0045] Among them, the incoming exhaust gas must first be diverted through the first concentration sensor 7. The diversion threshold of the first concentration sensor 7 is the exhaust gas particle size value allowed to be discharged, and is transported to the first fan 4 and the second fan 5 respectively. The first fan 4 and the second fan 5 are respectively provided with a first gas shut-off valve 9 and a second gas shut-off valve 10 for switching control of the gas flow passing through.

[0046] More preferably, if Figure 1 As shown, the salt-containing wastewater and waste gas combined incineration treatment device of the present invention also includes a third gas stop valve 14, a fourth gas stop valve 15, a first liquid stop valve 21, and a second liquid stop valve 22; a first pressure sensor 27 and a third pressure sensor 33, each stop valve is used to control the waste gas and wastewater flow, and the pressure sensor is used to measure the pressure size of each position area. Various stop valves and pressure sensors are referenced by those skilled in the art. Figure 1 It can be installed in the middle position, or you can choose the installation position according to the needs of the site.

[0047] Among them, as shown in the attached manual Fig.11As shown, a pressure mark P is provided on the first pressure sensor 27, indicating that the purpose of the first pressure sensor 27 is to measure pressure.

[0048] Preferably, a second gas storage chamber 3-4 is provided on the top of the activated carbon filter assembly 3 and connected to the second exhaust gas outlet 3-3. A second pressure sensor 32 is provided on the outside of the activated carbon filter assembly 3 and is externally connected to a control unit. The control unit sets a pressure differential alarm value. When the pressure differential in the activated carbon filter assembly 3 reaches the first-level pressure differential alarm value, it reminds the filter material to be replaced. When the second-level pressure differential alarm value is reached, it reminds the activated carbon filter assembly 3 to release the pressure. When the third-level pressure differential alarm value is reached, the emergency emptying mode is started. At this time, the second gas shut-off valve 10 is closed, the first gas shut-off valve 9 is opened, and the adsorption fan 2-4 is adjusted to operate at the rated maximum power until the third-level pressure differential alarm is released. The pressure differential alarm value includes the first-level pressure differential alarm value, the second-level pressure differential alarm value, and the third-level pressure differential alarm value, which are determined by those skilled in the art according to actual conditions.

[0049] Example 3 Reference Figure 1 to Figure 8 , which is the third embodiment of the present invention, and this embodiment is based on the previous embodiment.

[0050] Specifically, the telescopic device 25 includes a slide 251 that penetrates the outer wall of the incinerator 1, a positioning cover 252 is provided outside the slide 251, a connecting rod 253 is slidably provided inside the slide 251, a bracket 254 is fixedly provided on the outer wall of the positioning cover 252, and a sliding rod 255 is provided on the outer wall of the bracket 254.

[0051] Among them, a lifting sleeve 256 is slidably provided on the sliding rod 255, and the lifting sleeve 256 is fixedly connected to the connecting rod 253. One end of the connecting rod 253 penetrates into the incinerator 1 and is fixedly connected to the flow equalizing orifice plate 23, so that when the lifting sleeve 256 is raised or lowered, the flow equalizing orifice plate 23 is driven to rise and fall through the connecting rod 253.

[0052] Among them, during the up and down movement of the flow equalizing orifice plate 23, not only the size of the combustion chamber 18 will be changed according to the amount of exhaust gas to improve the combustion efficiency, but also the inner wall of the combustion chamber 18 of the incinerator 1 will be rubbed to scrape and remove the impurities attached to the inner wall of the combustion chamber 18 after combustion. The greater the exhaust gas intake, the greater the scraping frequency to prevent impurities from accumulating and agglomerating.

[0053] Preferably, an impeller 257 is rotatably provided in the exhaust gas inlet 26 - 1 , a rotating shaft 258 is fixedly provided at the center of the impeller 257 , and the rotating shaft 258 rotates and penetrates outside the exhaust gas inlet 26 - 1 and is provided with an eccentric fan 259 .

[0054] More preferably, the slide bar 255 is arranged parallel to the axial direction of the incinerator 1, the bracket 254 is a rectangular frame, the connecting rod 253 slides through the positioning cover 252 and is sealed therewith to prevent the heat and waste water and exhaust gas from escaping, and the other end of the rotating shaft 258 is meshed with the outer wall of the annular spray assembly 26 through a bevel gear, so that when the rotating shaft 258 rotates, it can also drive the annular spray assembly 26 to rotate on the inner wall of the incinerator 1, so as to achieve uniform spraying of the waste liquid, fully and evenly mix it with the exhaust gas, and improve the combustion efficiency.

[0055] Among them, the outer wall of the sliding rod 255 is also fixedly engaged with a fixing rod 2511, and the fixing rod 2511 is fixedly connected to the outer wall of the incinerator 1. The fixing rod 2511 is vertically provided with a support rod 2512, and an amplitude modulation rod 2513 is rotatably provided on the support rod 2512. The amplitude modulation rod 2513 is parallelly provided with an amplitude modulation groove 2514, and a slider 2515 is slidably provided in the amplitude modulation groove 2514.

[0056] Preferably, a pull rod 2516 is provided on the end face of the slider 2515, a swing arm is rotatably provided in the lifting sleeve 256, an arc groove is provided on the swing arm, and a cylinder 2517 is provided at the end of the amplitude modulation rod 2513, and the cylinder 2517 is slidably provided on the arc groove.

[0057] The rotation speed of the impeller 257 is related to the exhaust gas flow rate at the exhaust gas inlet 26-1, so the faster the exhaust gas flow rate, the faster the annular spray assembly 26 rotates. Among them, the arc groove and the swing trajectory of the swing arm do not overlap, so when the cylinder 2517 moves with the swing arm, the fulcrum position of the arc groove itself during rotation and swinging changes, thereby changing the lifting amplitude of the lifting sleeve 256. The larger the lifting amplitude, the larger the scraping range, and the maximum and minimum values ​​of the internal space of the combustion chamber 18 also change accordingly.

[0058] Preferably, the first heat storage chamber 19 and the second heat storage chamber 20 are connected with a first branch pipe 2518 and a second branch pipe 2519 respectively, and the first branch pipe 2518 and the second branch pipe 2519 are respectively provided with a connecting pipe 2521, and the two connecting pipes 2521 are arranged in parallel.

[0059] A floating ball is slidably disposed inside the connecting tube 2521 , and a rack 2523 is slidably disposed on the outer wall of the connecting tube 2521 . One end of the rack 2523 slides through the connecting tube 2521 and is fixedly connected to the outer wall of the floating ball.

[0060] The rack 2523 is sealed to the connecting pipe 2521 to prevent gas or liquid leakage. The floating ball is made of heat-resistant rubber. When the temperature in the primary heat storage chamber 19 and the secondary heat storage chamber 20 increases, the gas expands and pushes the floating ball toward one of the heat storage chambers.

[0061] More preferably, the two racks 2523 are meshed with the gear 2524 at the same time. The gear 2524 is provided with a balance bar 2525 rotatably axially. An inclined block 2526 is provided at one end of the balance bar 2525 . The inclined block 2526 slides through the pull rod 2516 .

[0062] The inclined block 2526 is a parallelogram, and a parallelogram groove is also provided in the pull rod 2516, so that when the balance bar 2525 moves up and down, the pull rod 2516 is driven to move left and right, thereby adjusting the swinging and floating of the swing arm.

[0063] Preferably, when the temperatures in the primary heat storage chamber 19 and the secondary heat storage chamber 20 change synchronously, the two floating balls move up and down in the same proportion, thereby synchronously driving the gear 2524 to rotate. When there is a temperature difference between the two, the floating ball on the side with higher temperature moves more greatly, so that the rack 2523 on this side descends more greatly, driving the gear 2524 to roll downward along the rack 2523 on the other side for a distance, and at the same time moves downward through the balance rod 2525, driving the pull rod 2516 to move outward, so that the swing amplitude of the swing arm changes.

[0064] It should be noted that, in the present embodiment, the annular spray assembly 26 is also provided with an upwardly directed nozzle, so that when the swing amplitude of the swing arm increases, the waste liquid can also be sprayed upward to spray and cool the equalizing orifice plate 23 connected to the primary heat storage chamber 19, thereby lowering the temperature of the connected heat storage chambers, reducing the temperature difference, and preventing damage to the heat storage body.

[0065] Example 4 Reference Figure 1-Figure 18 , which is the fourth embodiment of the present invention, and this embodiment provides a method for treating saline wastewater and waste gas by combined incineration, and the method is implemented based on the above-mentioned device for treating saline wastewater and waste gas by combined incineration.

[0066] Specifically, a method for treating salt-containing wastewater and waste gas by combined incineration includes: the waste gas is monitored and diverted by a first concentration sensor 7, and low-concentration waste gas is pumped into an activated carbon filter assembly 3 by a second fan 5. The lower side wall of the activated carbon filter assembly 3 is provided with an air supply port 3-1 and a filter mesh is provided radially to preliminarily screen out large particles of impurities visible in the waste gas. The waste gas forms an upward flow field inside, and passes through a primary filter layer 3-8, whose surface is paved with macroporous activated carbon 3-8a; a secondary filter layer 3-7, whose surface is paved with transitional pore activated carbon 3-7a; a tertiary filter layer 3-6, whose surface is paved with microporous activated carbon 3-6a. The filter layer is a grid structure, which can be used as a diverter plate to guide the waste gas to flow upward, guide the waste gas to form an upward circulation, a uniform flow field, and improve the filtering efficiency of the gas. The waste gas coming out of the waste gas outlet 3-3 enters the zeolite rotor molecular sieve assembly 2 through the adsorption fan 2-4, and after the organic adsorption is completed, it is discharged after the third concentration sensor 11 monitors and meets the standard; Another part of the high-concentration exhaust gas is pumped by the first fan 4 through the exhaust gas ring pipe and directly sent into the combustion chamber 18 in the incinerator 1. At the same time, the burner 16 sprays the combustion aid to assist the incineration of the waste salt. After the incineration and purification is completed, the exhaust gas flows upward from the equalizing orifice plate 23 and enters the primary heat storage chamber 19 and the secondary heat storage chamber 20 in turn, and exchanges heat with the phase change heat storage body 20-1 to complete the heat storage process.

[0067] Most of the exhaust gas finally enters the gas storage chamber 17 at the top of the incinerator 1 through the guide orifice plate 24, and is then discharged after being monitored by the fourth concentration sensor 12 to meet the standard; the other part of the exhaust gas enters the desorption chamber 2-1 through the desorption fan 2-3 to desorb the zeolite rotor molecular sieve component 2, and after desorption is completed, it circulates through the exhaust gas ring pipe into the combustion chamber 18 for incineration purification treatment.

[0068] The organic wastewater at the other end is monitored and diverted by the second concentration sensor 8, and the organic components are pumped from high to low by the water pump 6, and enter the first-level heat storage chamber 19 and the second-level heat storage chamber 20 through the wastewater inlet pipe 34, and pass through the heat storage body to complete preheating, and then flow downward into the annular spray assembly 26 and evenly sprayed into the combustion chamber 18 until it is purified and discharged after being monitored by the fifth concentration sensor 13 to meet the standards.

[0069] The first temperature sensor 28 and the second temperature sensor 29 are deeply inserted into the upper and lower parts of the side of the first heat storage chamber 19, respectively. Similarly, the third temperature sensor 30 and the fourth temperature sensor 31 are deeply inserted into the upper and lower parts of the side of the second heat storage chamber 20, respectively. The four groups of temperature sensors are connected to the control unit. When the temperature difference between the first temperature sensor 28 and the second temperature sensor 29 (or the third temperature sensor 30 and the fourth temperature sensor 31) exceeds 100°C, in order to prevent the phase change heat storage body 20-1 from being damaged, the flow rate of the water pump 6 is increased to enable the wastewater to quickly pass through the wastewater inlet pipe 34 and complete the heat exchange, thereby reducing the temperature difference. Otherwise, the flow rate of the water pump 6 is reduced.

[0070] Importantly, it should be noted that the construction and arrangement of the present application shown in a number of different exemplary embodiments are only exemplary. Although only a few embodiments are described in detail in this disclosure, it should be readily understood by those who refer to this disclosure that many modifications are possible (e.g., the size, scale, structure, shape and proportion of various elements, and parameter values ​​(e.g., temperature, pressure, etc.), mounting arrangements, use of materials, color, changes in orientation, etc.) without substantially departing from the novel teachings and advantages of the subject matter described in the application. For example, an element shown as integrally formed may be composed of multiple parts or elements, the position of the element may be inverted or otherwise changed, and the nature or number or position of the discrete element may be altered or changed. Therefore, all such modifications are intended to be included within the scope of the present invention. The order or sequence of any process or method steps may be changed or reordered according to an alternative embodiment. In the claims, any "device plus function" clause is intended to cover the structure described herein that performs the function, and is not only structurally equivalent but also equivalent structure. Other substitutions, modifications, changes and omissions may be made in the design, operating conditions and arrangement of the exemplary embodiments without departing from the scope of the present invention. Therefore, the invention is not limited to a specific embodiment, but extends to numerous modifications still falling within the scope of the appended claims.

[0071] It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention rather than to limit it. Although the present invention has been described in detail with reference to the preferred embodiments, those skilled in the art should understand that the technical solutions of the present invention may be modified or replaced by equivalents without departing from the spirit and scope of the technical solutions of the present invention, which should all be included in the scope of the claims of the present invention.

Claims

1. A device for combined incineration of saline wastewater and waste gas, characterized in that: include: An incinerator (1), a combustion chamber (18) disposed at the bottom of the incinerator (1), and a burner (16) disposed at the top of the combustion chamber (18), wherein an annular spray assembly (26) is disposed inside the combustion chamber (18); It also includes a heat storage chamber disposed above the combustion chamber (18), the heat storage chamber including a primary heat storage chamber (19) and a secondary heat storage chamber (20) separated by a flow balancing orifice plate (23), and a wastewater inlet pipe (34) disposed inside the heat storage chamber, the wastewater inlet pipe (34) being used to preheat wastewater; A zeolite wheel molecular sieve assembly (2) is provided upstream of the incinerator (1), an activated carbon filter assembly (3) is provided upstream of the zeolite wheel molecular sieve assembly (2), a waste gas flow inlet and a waste water flow inlet are provided on the incinerator (1), a fan is provided at the waste gas flow inlet to drive the waste gas to flow along a waste gas transmission pipe, the waste gas transmission pipe is used to transmit the waste gas, and a water pump (6) is provided at the waste water flow inlet to drive the waste water to flow along the waste water flow channel into the incinerator (1); VOCs concentration sensors are installed at the waste gas inlet and wastewater inlet to monitor the content of organic components so that they can be incinerated according to their concentration.

2. The device for combined incineration of saline wastewater and waste gas according to claim 1, characterized in that: The combustion chamber (18) is located in the lower area of ​​the incinerator (1) and is provided with a flow balancing orifice plate (23) between the combustion chamber (18) and the first-level heat storage chamber (19), and an axial through hole (23-1) is provided on the plate surface of the flow balancing orifice plate (23); Telescopic devices (25) are provided at both ends of the flow balancing orifice plate (23) for adjusting the internal space of the combustion chamber (18).

3. The device for combined incineration of saline wastewater and waste gas according to claim 2, characterized in that: The secondary heat storage chamber (20) is composed of a plurality of groups of phase-change heat storage bodies (20-1), the surface of the phase-change heat storage body (20-1) is provided with gas-liquid through holes (20-1a) axially distributed at equal intervals and staggered, and the gas-liquid through holes (20-1a) have the same aperture; Heat exchange fins (20-1b) are evenly arranged inside the gas-liquid through hole (20-1a) along the inner wall of the hole, and serpentine tubes are evenly spaced inside the phase-change heat storage body (20-1), wherein the inlet end of the serpentine tube is connected to the wastewater inlet pipe (34) and the outlet end is connected to the annular spray assembly (26).

4. The combined incineration treatment device for salt-containing wastewater and waste gas according to claim 3 is characterized in that: The annular spray assembly (26) comprises an exhaust gas inlet (26-1), an exhaust gas outer pipe (26-2), a waste water inner pipe (26-3), a first exhaust gas outlet (26-5), a waste water outlet (26-4), a through pipe (26-9) and a spray head; one end of the exhaust gas inlet (26-1) is connected to the exhaust gas outer pipe (26-2), and the waste water inner pipe (26-3) is coaxially sleeved in the exhaust gas outer pipe (26-2); Through pipes (26-9) are provided at equal intervals between the wastewater inner pipe (26-3) and the waste gas outer pipe (26-2); the through pipes (26-9) connect the wastewater outlet (26-4) and the nozzle; the nozzle comprises a diffusion chamber (26-6), a contraction chamber (26-7) and a slit-type nozzle (26-8); one end of the nozzle is sealedly connected to the waste gas outer pipe (26-2); and the slit-type nozzle (26-8) is located at the other end of the nozzle.

5. The combined incineration treatment device for salt-containing wastewater and waste gas according to claim 4 is characterized in that: The zeolite rotor molecular sieve assembly (2) comprises a desorption chamber (2-1), a desorption exhaust gas inlet (2-2), a desorption fan (2-3), an adsorption fan (2-4), a rotor (2-5), a crawler (2-6), a motor (2-7), and a fixing bracket (2-8); The rotating wheel (2-5) is fixed on the fixed bracket (2-8), and desorption chambers (2-1) are provided on both sides of the rotating wheel (2-5) and are connected to the secondary heat storage chamber (20).

6. The device for combined incineration of saline wastewater and waste gas according to claim 5, characterized in that: The activated carbon filter assembly (3) comprises an air supply port (3-1), a settling port (3-2), a second exhaust gas outlet (3-3), a second air storage chamber (3-4), a receiving plate (3-5), and a filter layer; the filter layer comprises, from bottom to top, a primary filter layer (3-8), a secondary filter layer (3-7), and a tertiary filter layer (3-6); The activated carbon filter assembly (3) is provided with an air supply port (3-1) at the bottom, and a filter mesh is radially provided at the air supply port (3-1). The activated carbon filter assembly (3) is provided with a second air storage chamber (3-4) at the top and is connected to the second exhaust gas outlet (3-3). The activated carbon filter assembly (3) is provided with a second pressure sensor (32) outside and is externally connected to a control unit; the control unit sets a pressure differential alarm value, and when the pressure differential in the activated carbon filter assembly (3) reaches a first-level pressure differential alarm value, it reminds to replace the filter material; when it reaches a second-level pressure differential alarm value, it reminds to release the pressure in the activated carbon filter assembly (3); when it reaches a third-level pressure differential alarm value, it starts an emergency emptying mode.

7. The device for combined incineration of saline wastewater and waste gas according to claim 6, characterized in that: The telescopic device (25) comprises a slideway (251) penetrating through the outer wall of the incinerator (1); a positioning cover (252) is provided outside the slideway (251); a connecting rod (253) is slidably provided inside the slideway (251); a bracket (254) is fixedly provided on the outer wall of the positioning cover (252); and a sliding rod (255) is provided on the outer wall of the bracket (254); A lifting sleeve (256) is slidably provided on the slide rod (255), and the lifting sleeve (256) is fixedly connected to the connecting rod (253). One end of the connecting rod (253) passes through the incinerator (1) and is fixedly connected to the flow balancing orifice plate (23), so that when the lifting sleeve (256) is raised or lowered, the flow balancing orifice plate (23) is driven to be raised or lowered through the connecting rod (253).

8. The device for combined incineration of saline wastewater and waste gas according to claim 7, characterized in that: An impeller (257) is rotatably provided inside the exhaust gas inlet (26-1), a rotating shaft (258) is fixedly provided at the center of the impeller (257), and the rotating shaft (258) rotatably penetrates outside the exhaust gas inlet (26-1) and is provided with an eccentric fan (259); The outer wall of the slide bar (255) is also fixedly engaged with a fixing rod (2511), the fixing rod (2511) is fixedly connected to the outer wall of the incinerator (1), the fixing rod (2511) is vertically provided with a support rod (2512), the support rod (2512) is rotatably provided with an amplitude modulation rod (2513), the amplitude modulation rod (2513) is parallelly provided with an amplitude modulation groove (2514), and a sliding block (2515) is slidably provided in the amplitude modulation groove (2514); The end surface of the slider (2515) is provided with a pull rod (2516), a swing arm is rotatably provided in the lifting sleeve (256), an arc-shaped groove is provided on the swing arm, and a cylinder (2517) is provided at the end of the amplitude modulation rod (2513), and the cylinder (2517) is slidably arranged on the arc-shaped groove.

9. The device for combined incineration of saline wastewater and waste gas according to claim 8, characterized in that: The first-stage heat storage chamber (19) and the second-stage heat storage chamber (20) are respectively connected with a first branch pipe (2518) and a second branch pipe (2519); the first branch pipe (2518) and the second branch pipe (2519) are respectively provided with a connecting pipe (2521); the two connecting pipes (2521) are arranged in parallel; A floating ball is slidably disposed inside the connecting tube (2521), and a rack (2523) is slidably disposed on the outer wall of the connecting tube (2521). One end of the rack (2523) slides through the connecting tube (2521) and is fixedly connected to the outer wall of the floating ball.

10. The device for combined incineration of saline wastewater and waste gas according to claim 9, characterized in that: The two racks (2523) are meshed with the gear (2524) at the same time. The gear (2524) is provided with a balance bar (2525) for axial rotation. An inclined block (2526) is provided at one end of the balance bar (2525). The inclined block (2526) slides through the pull rod (2516).

11. A method for treating saline wastewater and waste gas by combined incineration, which is implemented based on the device for treating saline wastewater and waste gas by combined incineration according to claim 10, characterized in that: The method comprises: S1. Divert and preliminarily treat the waste gas, including: S1.

1. A first concentration sensor (7) is arranged in the exhaust gas transmission pipe, and the exhaust gas concentration is monitored based on the first concentration sensor (7), so as to divide the exhaust gas into two parts: high-concentration exhaust gas and low-concentration exhaust gas; S1.2, a second fan (5) is provided to pump low-concentration exhaust gas into the activated carbon filter assembly (3); the activated carbon filter assembly (3) carries out gas transmission through the air supply port (3-1), and the low-concentration exhaust gas passes through the filter mesh, forms an upward flow field inside the activated carbon filter assembly (3), and passes through the primary filter layer (3-8), the secondary filter layer (3-7), and the tertiary filter layer (3-6) in sequence for preliminary filtration to remove large particle impurities; S2. Adsorption and desorption treatment of waste gas, including: S2.1, the low-concentration exhaust gas after preliminary filtration enters the zeolite rotor molecular sieve assembly (2) through the adsorption fan (2-4) to adsorb organic matter; S2.2, after the exhaust gas adsorption is completed, a third concentration sensor (11) is arranged in the exhaust gas discharge pipe of the desorption chamber (2-1) to monitor the exhaust gas concentration, and when the concentration reaches the standard, the exhaust gas is discharged; S2.

3. If the exhaust gas concentration exceeds the standard or is incompletely adsorbed, the desorption fan (2-3) introduces part of the gas into the desorption chamber (2-1) to desorb the zeolite rotor molecular sieve assembly (2). The desorption chamber (2-1) is connected to an exhaust gas ring pipe, and the exhaust gas after desorption is returned to the combustion chamber (18) through the exhaust gas ring pipe for incineration purification; S3. Incineration of high-concentration waste gas, including: S3.1, high-concentration exhaust gas is pumped by the first fan (4) and directly sent into the combustion chamber (18) of the incinerator (1) through the exhaust gas ring pipe; S3.2, spraying a combustion aid through a burner (16) to assist in the incineration of high-concentration exhaust gas; S4. Discharge and heat storage treatment of the incineration waste gas obtained from incineration, including: S4.1, the incineration waste gas enters the primary heat storage chamber (19) and the secondary heat storage chamber (20) through the flow-averaging orifice plate (23), exchanges heat with the phase-change heat storage body (20-1), and completes the heat storage process; S4.

2. A guide orifice plate (24) is provided on the inner wall of the incinerator (1). Most of the incineration waste gas after heat storage passes through the guide orifice plate (24) and enters the gas storage chamber (17) at the top of the incinerator (1). A fourth concentration sensor (12) is provided in the gas storage chamber (17) to monitor the waste gas concentration. The gas is discharged after reaching the standard. S4.

3. Another part of the waste gas enters the desorption chamber (2-1) through the desorption fan (2-3) to desorb the zeolite rotor molecular sieve assembly (2). The desorbed waste gas enters the combustion chamber (18) again through the waste gas ring pipe for secondary incineration treatment.

12. A method for treating saline wastewater and waste gas by combined incineration according to claim 11, characterized in that: The method further comprises: S5. Pre-treatment of organic wastewater by diversion and incineration, including: S5.

1. A second concentration sensor (8) is provided in the organic wastewater flow channel to monitor the concentration of organic components and to divert the wastewater according to the concentration of organic components; S5.2, the organic wastewater is pumped into the wastewater inlet pipe (34) by the water pump (6), and flows into the primary heat storage chamber (19) and the secondary heat storage chamber (20) in sequence, and is preheated by the phase change heat storage body (20-1); S6. Incineration and purification of organic wastewater, including: S6.1, the preheated organic wastewater enters the annular spray assembly (26) and is evenly sprayed into the combustion chamber (18) for incineration and purification; S6.

2. A fifth concentration sensor (13) is provided in the flow channel of the purified wastewater to monitor the concentration, and the wastewater is discharged after reaching the standard; S7. Perform temperature monitoring and control, including: S7.1, temperature sensors are respectively installed on the side walls of the primary heat storage chamber (19) and the secondary heat storage chamber (20) to monitor the temperature of the phase change heat storage body (20-1); S7.

2. When the temperature difference exceeds 100° C., the control unit adjusts the flow rate of the water pump (6) to accelerate the flow rate of the wastewater through the wastewater inlet pipe (34) to reduce the temperature difference; when the temperature difference is less than 100° C., the flow rate of the water pump (6) is reduced to maintain the heat storage effect and protect the phase change heat storage body (20-1).

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