Box type waste liquid treatment device
By designing a box-type waste liquid treatment device, using the combination of evaporation components and dehumidification components, the problem of small-scale industrial enterprises being difficult to deal with waste water is solved, efficient evaporation and moisture removal of waste liquid is achieved, and storage and treatment costs are reduced.
Patent Information
- Application Number
- CN202421682646.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-07-16
- Publication Date
- 2025-06-27
- Estimated Expiration
- 2034-07-16
AI Technical Summary
Small-scale industrial enterprises find it difficult to effectively deal with the wastewater they generate, resulting in large storage space, high costs and high outsourcing treatment costs.
A box-type waste liquid treatment device is designed, including a drying box, an evaporation assembly and a dehumidification assembly. The evaporation assembly is arranged intersecting with the evaporation trough through a tortuous airflow channel to promote the evaporation of the waste liquid; the dehumidification assembly is formed by the compressed air drying unit and the heating unit to continuously evaporate the moisture in the waste liquid through the evaporation cycle.
Effectively extend the contact time between the airflow and the waste liquid, promote the evaporation and moisture removal of the waste liquid, reduce storage and treatment costs, and is suitable for small-scale industrial enterprises.
Smart Images

Figure CN223033152U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of environmental protection treatment of industrial waste liquid, in particular to a box-type waste liquid treatment device. Background Technique
[0002] At present, industrial wastewater is extremely harmful to the environment and society, and will have direct or indirect impacts on rivers and groundwater. If the pollution is serious, it will cause serious harm to soil, aquatic plants, and crops. At the same time, industrial wastewater has a certain volatility, will produce irritating odors, and will cause a certain degree of pollution to air quality. Then, harmful chemical substances enter the human body through the respiratory tract, and long-term accumulation will cause various diseases, posing a serious threat to people's life and health.
[0003] For some small-scale enterprises, the discharge volume of their wastewater is small, and the scale of waste liquid treatment required is small. Generally, the generated wastewater is stored, and after a certain amount of wastewater is accumulated, it is entrusted to an external party for centralized treatment. The required storage space is large, the storage cost is high, and the external treatment cost is large. Content of the Utility Model
[0004] In view of this, it is necessary to provide a box-type waste liquid treatment device to solve the problem that it is difficult to treat the small-scale wastewater generated by existing enterprises.
[0005] The utility model provides a box-type waste liquid treatment device. It includes:
[0006] A drying box body, in which a relatively isolated evaporation chamber and a dehumidification chamber are formed;
[0007] An evaporation component, the evaporation component includes a tortuously arranged air flow channel and an evaporation drawer for storing waste liquid. The air flow channel is arranged in the evaporation chamber, and a plurality of the evaporation drawers are movably inserted into the drying box body. The air flow channel intersects with the evaporation drawer to promote the evaporation of the waste liquid;
[0008] A dehumidification component, arranged in the dehumidification chamber. The dehumidification component includes a dehumidification pipeline and a compressed air drying unit and a heating unit arranged on the dehumidification pipeline. The two ends of the dehumidification pipeline are respectively communicated with the two ends of the air flow channel; the heating unit includes a heating shell and high-temperature filler, and the filler is filled in the heating shell. The compressed air drying unit can pressurize, heat up and dehumidify the wet air from the evaporation chamber.
[0009] Furthermore, the dehumidification component further includes a heating unit, and the heating unit includes a plurality of heating rods inserted into the heating shell, and the heating rods can heat the filler.
[0010] Further, the filler is a metal oxide or nitride filler.
[0011] Further, the heating housing includes an air inlet and an air outlet communicating with the dehumidification duct, and an openable and closable pressure relief port. The pressure relief port communicates with the outside through a duct, and the pressure relief port can relieve pressure overload.
[0012] Further, the compressed air drying unit includes a compressor and an adsorption dryer. Both the compressor and the adsorption dryer are connected to the dehumidification duct. The compressor can heat and pressurize the air, and the adsorption dryer can absorb moisture in the air.
[0013] Further, a solid moisture absorbent capable of desorbing moisture is provided inside the adsorption dryer.
[0014] Further, at least one partition is provided inside the evaporation drawer. The partition is fixedly connected to the evaporation drawer, and the partition can separate the inner cavity of the evaporation drawer.
[0015] Further, the partition is arranged perpendicular to the flow direction of the air flow channel.
[0016] Further, communication holes are provided on the partition.
[0017] Further, a liquid delivery pipe is provided in the evaporation chamber opposite to the evaporation drawer. The liquid delivery pipe can input waste water from the outside into the evaporation drawer.
[0018] Compared with the prior art, the beneficial effects of the present utility model are as follows:
[0019] (1) A box-type waste liquid treatment device of the present utility model is provided with an evaporation assembly. The evaporation assembly includes an air flow channel and an evaporation drawer for storing waste liquid. The air flow channel is arranged in the evaporation chamber, and a plurality of evaporation drawers are movably inserted into the drying box body. The air flow channel intersects with the evaporation drawer, and the air flow channel is relatively tortuous, which can extend the path of the air flow, increase the contact time between the air flow and the waste liquid, and promote the evaporation of the waste liquid.
[0020] (2) A box-type waste liquid treatment device of the present utility model is provided with a dehumidification assembly. The dehumidification assembly is arranged in the dehumidification chamber. The dehumidification assembly includes a dehumidification duct and a compressed air drying unit and a heating unit arranged on the dehumidification duct. The dehumidification duct can sequentially input the humid air into the compressed air drying unit and the heating unit to complete the heating and dehumidification of the air. The two ends of the dehumidification duct are respectively communicated with the two ends of the air flow channel. The dehumidification duct can draw the humid air from the evaporation chamber to flow through the compressed air drying unit and the heating unit and then return to the evaporation chamber to form an evaporation cycle, continuously evaporating the moisture in the waste liquid and promoting the crystallization of substances in the waste liquid.
[0021] (3) A box - type waste liquid treatment device of the present utility model is provided with a heating unit. The heating unit includes a heating housing and high - heat filler. The filler is filled in the heating housing, and the heating housing can keep the filler warm to inhibit heat dissipation. The high - heat filler can heat the passing air to increase the air temperature and further promote the evaporation process of the waste liquid. BRIEF DESCRIPTION OF THE DRAWINGS
[0022] The drawings described herein are used to provide a further understanding of the present utility model and form a part of this application. The schematic embodiments of the present utility model and their descriptions are used to explain the present utility model and do not constitute an improper limitation to the present utility model. In the drawings:
[0023] Figure 1 is a schematic structural diagram of the whole of the present utility model;
[0024] Figure 2 is a schematic structure of the heating unit and the heat - generating unit in the present utility model Figure 1 ;
[0025] Figure 3 is a schematic structure of the heating unit and the heat - generating unit in the present utility model Figure 2 ;
[0026] Figure 4 is a schematic structural diagram of the evaporation drawer in the present utility model.
[0027] In the figure, 100, drying box body; 110, evaporation chamber; 120, dehumidification chamber; 130, infusion pipe;
[0028] 200, evaporation assembly; 210, air flow channel; 220, evaporation drawer; 221, partition board; 222, communication hole;
[0029] 300, dehumidification assembly; 310, dehumidification pipeline; 320, compressed air drying unit; 321, compressor; 322, adsorption dryer; 330, heating unit; 331, heating housing; 331a, air inlet; 331b, air outlet; 331c, pressure relief port; 332, filler; 340, heat - generating unit; 341, heating rod. DETAILED DESCRIPTION OF THE EMBODIMENTS
[0030] The following will specifically describe the preferred embodiments of the present utility model with reference to the drawings. The drawings form a part of this application and are used together with the embodiments of the present utility model to explain the principle of the present utility model, and are not used to limit the scope of the present utility model.
[0031] A box-type waste liquid treatment device in this embodiment relates to the technical field of environmental protection treatment of industrial waste liquid. A compressed air drying unit 320 and a heating unit 330 are arranged in a drying box body 100, which can remove moisture in the air while raising the temperature, inhibit heat dissipation, and improve the utilization efficiency of air thermal energy. The heating unit 330 is provided with high-temperature filler 332. When air flows through the filler 332, the filler 332 can heat the air, thereby improving the conduction efficiency of heating.
[0032] Please refer to Figures 1 to 4 , a box-type waste liquid treatment device in this embodiment includes a drying box body 100, an evaporation assembly 200, and a dehumidification assembly 300. Among them, a relatively isolated evaporation chamber 110 and a dehumidification chamber 120 are formed in the drying box body 100, which can separate the evaporation process of the waste liquid and the water vapor separation process to avoid mutual interference between the two. At the same time, the drying box body 100 provides a closed environment, limiting the waste liquid treatment process in the drying box body 100, thereby avoiding the overflow of waste gas.
[0033] The evaporation assembly 200 includes an air flow channel 210 and an evaporation drawer 220 for storing waste liquid. The air flow channel 210 is arranged in the evaporation chamber 110. A plurality of evaporation drawers 220 are movably inserted into the drying box body 100. The air flow channel 210 intersects with the evaporation drawer 220. The air flow channel 210 is relatively tortuous, which can extend the path of the air flow, increase the contact time between the air flow and the waste liquid, and promote the evaporation of the waste liquid.
[0034] The dehumidification assembly 300 is arranged in the dehumidification chamber 120. The dehumidification assembly 300 includes a dehumidification pipeline 310 and a compressed air drying unit 320 and a heating unit 330 arranged on the dehumidification pipeline 310. The dehumidification pipeline 310 can sequentially input the humid and hot air into the compressed air drying unit 320 and the heating unit 330 to complete the heating and dehumidification of the air. Both ends of the dehumidification pipeline 310 are communicated with both ends of the air flow channel 210. The dehumidification pipeline 310 can draw the humid and hot air from the evaporation chamber 110 to flow through the compressed air drying unit 320 and the heating unit 330 and then return to the evaporation chamber 110 to form an evaporation cycle, continuously evaporating the moisture in the waste liquid and promoting the crystallization of substances in the waste liquid.
[0035] The heating unit 330 includes a heating housing 331 and high-temperature filler 332. The filler 332 is filled in the heating housing 331. The heating housing 331 can keep the filler 332 warm and inhibit heat dissipation. The high-temperature filler 332 can heat the passing air, raise the temperature of the air, and further promote the evaporation process of the waste liquid.
[0036] It should be noted that an air compressor 321 is provided in the compressed air drying unit 320, which can pressurize the air, increase the temperature and pressure of the air, promote the high-speed flow of the air, and provide power for the air to flow in the air flow channel 210.
[0037] In some embodiments, referring to Figures 1 to 3 , the dehumidification component 300 further includes a heating unit 340. The heating unit 340 includes a plurality of heating rods 341. The heating rods 341 are electric heating rods 341, and the electric heating rods 341 are directly inserted into the heating housing 331 to heat the packing 332 and keep the packing 332 in a high-temperature state. When the air passes through the gaps between the packings 332, the packings 332 can heat the air, increase the temperature of the air entering the evaporation chamber 110, and promote the evaporation of the waste liquid.
[0038] In the specific implementation process, the packing 332 is a metal oxide or nitride packing 332. Specifically, the packing 332 is alumina, magnesia, zinc oxide, aluminum nitride, boron nitride, silicon carbide, etc. The packings 332 are spaced apart from each other to form a flow gap, and the air can pass through the flow gap.
[0039] In some embodiments, referring to Figure 2 and Figure 3 , the heating housing 331 includes an air inlet 331a and an air outlet 331b communicating with the dehumidification pipeline 310 and an openable and closable pressure relief port 331c. The air dehumidified by the compressed air drying unit 320 enters the heating housing 331 from the air inlet 331a, is heated by the packing 332 in the heating housing 331, and then is discharged from the air outlet 331b into the evaporation chamber 110. The pressure relief port 331c is communicated with the outside through a pipeline. When the gas pressure in the heating housing 331 is too high due to temperature rise, the excess gas can be discharged from the pressure relief port 331c to achieve the purpose of pressure relief.
[0040] In some embodiments, referring to Figure 1 , the compressed air drying unit 320 includes a compressor 321 and an adsorption dryer 322. Both the compressor 321 and the adsorption dryer 322 are communicated with the dehumidification pipeline 310. The compressor 321 can heat and pressurize the air, increase the air temperature and pressure, and make the moisture in the air easier to evaporate and separate. The adsorption dryer 322 absorbs the moisture in the air through the adsorption material, further reduces the air humidity, and realizes efficient air drying. The combined action of the compressor 321 and the adsorption dryer 322 ensures that the air humidity is stably maintained at a low level and improves the overall effect of the dehumidification component 300.
[0041] In the specific implementation process, the adsorption dryer 322 is internally provided with a solid moisture absorbent that can desorb moisture. The main adsorbents used are silica gel, alumina gel, and molecular sieve. These adsorbents have a large number of pores, so they have a large specific surface area. When the vapor partial pressure on the surface of the adsorption material is less than the vapor surface partial pressure in the air, the moisture in the compressed air is adsorbed. However, when the adsorbent adsorbs enough moisture and becomes saturated, desorption regeneration must be carried out in order to adsorb again so that the dryer can work continuously. The adsorption dryer 322 has two towers. One tower is under working pressure to adsorb and dry the air, and the other tower is under normal pressure for desorption regeneration. Thus, the two towers carry out drying and regeneration under the control of the electric controller and work alternately to continuously provide dry compressed air.
[0042] In some embodiments, referring to Figure 1 and Figure 4 , at least one partition 221 is provided inside the evaporation drawer 220. The partition 221 is fixedly connected to the evaporation drawer 220, and the partition 221 can separate the inner cavity of the evaporation drawer 220. The fixed connection between the partition 221 and the evaporation drawer 220 can enhance the overall structural stability of the evaporation drawer 220 and prevent structural deformation or damage caused by air flow impact. The partition 221 can divide the inner cavity of the evaporation drawer 220 into several independent regions, preventing the waste liquid from fluctuating violently as the air flows and overflowing from the evaporation drawer 220.
[0043] In a further embodiment, the partition 221 is arranged perpendicular to the flow direction of the air flow channel 210. The vertically arranged partition 221 will force the air flow to generate disturbances during the flow process, increasing the contact opportunity between the air flow and the adsorption material and improving the adsorption efficiency. When the air flow encounters the partition 221 perpendicular to the flow direction, it will be forced to disperse and redirect, generating disturbances. The disturbances can accelerate the air flow on the surface of the waste liquid and promote the evaporation of the waste liquid.
[0044] The partition 221 is provided with communication holes 222. The communication holes 222 can communicate the chambers separated by the partition 221 to realize the liquid flow between the chambers, so that the liquid levels in the chambers are kept at the same height, avoiding inconsistent evaporation amounts in the chambers.
[0045] In some embodiments, referring to Figure 1 , an infusion tube 130 is provided in the evaporation chamber 110 opposite to the evaporation drawer 220. The infusion tube 130 can input the waste water from the outside into the evaporation drawer 220. The waste water is introduced into the evaporation drawer 220 through the infusion tube 130. During the evaporation process, the moisture in the waste water is removed, and the remaining solid substances can be further processed or utilized. The infusion tube 130 can intermittently transport the waste liquid into the evaporation drawer 220 to promote the crystallization of the waste liquid.
[0046] As described above, it is only the preferred specific embodiment of the present utility model, but the protection scope of the present utility model is not limited thereto. Any changes or substitutions that can be easily thought of by those skilled in the art within the technical scope disclosed by the present utility model should be covered within the present utility model.
Claims
1. A box-type waste liquid treatment device, characterized in that: include: A drying box body, wherein a relatively isolated evaporation chamber and a dehumidification chamber are formed in the drying box body; An evaporation component, the evaporation component comprising a zigzag airflow channel and an evaporation tray for storing waste liquid, the airflow channel is arranged in the evaporation chamber, a plurality of the evaporation trays are movably inserted in the drying box, and the airflow channel and the evaporation trays are arranged to intersect to promote the evaporation of the waste liquid; A dehumidification component is arranged in the dehumidification chamber, and the dehumidification component includes a dehumidification pipe and a compressed air drying unit and a heating unit arranged on the dehumidification pipe. The two ends of the dehumidification pipe are respectively connected to the two ends of the air flow channel; the heating unit includes a heating shell and a high-temperature filler, and the filler is filled in the heating shell. The compressed air drying unit can pressurize and heat the humid air from the evaporation chamber for dehumidification.
2. A box-type waste liquid treatment device according to claim 1, characterized in that: The dehumidification assembly further includes a heating unit, which includes a plurality of heating rods inserted into the heating shell, and the heating rods can heat the filler.
3. A box-type waste liquid treatment device according to claim 2, characterized in that: The filler is a metal oxide or nitride filler.
4. A box-type waste liquid treatment device according to claim 1, characterized in that: The heating shell includes an air inlet and an air outlet connected to the dehumidification pipe and an openable and closable pressure relief port. The pressure relief port is connected to the outside through a pipe, and the pressure relief port can relieve overload pressure.
5. A box-type waste liquid treatment device according to claim 1, characterized in that: The compressed air drying unit comprises a compressor and an adsorption dryer, both of which are connected to the dehumidification pipeline. The compressor can heat and pressurize the air, and the adsorption dryer can absorb moisture in the air.
6. A box-type waste liquid treatment device according to claim 5, characterized in that: The adsorption dryer is provided with a solid moisture absorbent capable of desorbing moisture.
7. A box-type waste liquid treatment device according to claim 1, characterized in that: At least one partition is arranged inside the evaporating drawer, and the partition is fixedly connected to the evaporating drawer, and the partition can separate the inner cavity of the evaporating drawer.
8. A box-type waste liquid treatment device according to claim 7, characterized in that: The partition is arranged perpendicular to the flow direction of the air flow channel.
9. A box-type waste liquid treatment device according to claim 8, characterized in that: The partition is provided with a communicating hole.
10. The box-type waste liquid treatment device according to claim 1, characterized in that: The evaporation chamber is provided with a liquid infusion tube arranged opposite to the evaporation drawer, and the liquid infusion tube can input waste water from the outside into the evaporation drawer.