A device for removing organic matter from industrial waste salt and a method for removing organic matter from waste salt

Abstract

The invention discloses an industrial waste salt organic matter removal device, comprising a main body component, including a tower body, an exhaust pipe connected to the upper end of the tower body, a first air inlet pipe connected to the lower part of the tower body, a liquid inlet pipe connected to the tower body above the first air inlet pipe, and the liquid inlet pipe can be connected to the inner cavity of the tower body; an air distribution component, including a lower air distribution plate connected to the tower body, an upper air distribution plate connected to the tower body above the lower air distribution plate, a plurality of wind caps with downward hollow cavities arranged on the upper air distribution plate, a plurality of wind holes arranged on the wind cap above the upper air distribution plate, a wind chamber is formed between the upper air distribution plate, an upper wall of the tower body and the lower air distribution plate, a plurality of upper slag discharge holes arranged on the upper air distribution plate, a plurality of slag discharge pipes corresponding to the upper slag discharge holes are arranged between the upper air distribution plate and the lower air distribution plate, a lower slag discharge hole is provided on the lower air distribution plate at the lower side of the slag discharge pipe, and the first air inlet pipe can be connected to the wind chamber; the invention can not only carry out organic matter removal treatment on high-salt organic wastewater, but also carry out organic matter removal treatment on waste salt solid waste.

Description

Technical Field

[0001] The invention relates to the technical field of environmental protection, in particular to an industrial waste salt organic matter removal device and a method for removing organic matter from waste salt. Background Art

[0002] With the rapid development of modern chemical industry, the output of industrial waste salt is increasing day by day, and industrial waste salt is rich in organic pollutants. If it is dumped at will, it will inevitably damage the ecological environment. At present, the main methods for treating industrial waste salt are landfill, incineration and harmless comprehensive utilization. Among them, the landfill method requires a large amount of space, and the waste salt may penetrate into the underground soil layer and endanger the groundwater system, so this treatment method is a temporary expedient; the incineration method will cause the problem of inorganic salt melting. The molten inorganic salt will cause strong corrosion to the equipment, often blocking the pipeline and paralyzing the equipment. The entrainment of inorganic salts in its flue gas is also serious, and its flue gas needs to be specially treated. Therefore, the incineration treatment method is technically difficult, costly and not often used; harmless comprehensive utilization is the direction of industrial waste salt treatment in the future. It not only solves the dilemma of increasing industrial waste salt and difficult treatment, but also turns industrial waste salt into treasure. The key to the resource utilization of industrial waste salt is the removal of organic pollutants. Therefore, it is urgent to develop a device for removing organic matter from industrial waste salt. Summary of the invention

[0003] The purpose of this section is to summarize some aspects of embodiments of the present invention and briefly introduce some preferred embodiments. Some simplifications or omissions may be made in this section and the specification abstract and the invention title of this application to avoid blurring the purpose of this section, the specification abstract and the invention title, and such simplifications or omissions cannot be used to limit the scope of the present invention.

[0004] In view of the above and / or existing problems in removing organic matter from existing industrial waste salts, the present invention is proposed.

[0005] Therefore, the purpose of the present invention is to provide an industrial waste salt organic matter removal device, which can not only remove organic matter from high-salt organic wastewater, but also remove organic matter from waste salt solid waste, and can effectively remove organic pollutants in industrial waste salt, which is more environmentally friendly.

[0006] In order to solve the above technical problems, the present invention provides the following technical solutions: an industrial waste salt organic matter removal device, comprising:

[0007] The main body assembly includes a tower body, wherein the upper end of the tower body is connected to an exhaust pipe, the lower part of the tower body is connected to a first air inlet pipe, the first air inlet pipe is connected to a first air inlet control valve, the tower body above the first air inlet pipe is connected to a liquid inlet pipe, the liquid inlet pipe is connected to a liquid inlet control valve, and when the liquid inlet control valve is opened, the liquid inlet pipe is connected to the inner cavity of the tower body;

[0008] An air distribution assembly includes a lower air distribution plate connected to the tower body, an upper air distribution plate connected to the tower body above the lower air distribution plate, a plurality of wind hoods with downward hollow cavities are arranged on the upper air distribution plate, a plurality of air holes are arranged on the wind hood above the upper air distribution plate, an air chamber is formed between the lower side of the upper air distribution plate, the inner wall of the tower body and the upper side of the lower air distribution plate, a plurality of upper slag discharge holes are arranged on the upper air distribution plate, a plurality of slag discharge pipes corresponding to the upper slag discharge holes are arranged between the upper air distribution plate and the lower air distribution plate, a lower slag discharge hole is provided on the lower air distribution plate on the lower side of the slag discharge pipe, and when the first air inlet control valve is opened, the first air inlet pipe is connected to the air chamber.

[0009] As a preferred solution of the device for removing organic matter from industrial waste salt in the present invention, the axis of the air hole is arranged to be inclined upward from the inside to the outside.

[0010] As a preferred solution of an industrial waste salt organic matter removal device in the present invention, wherein: a liquid ventilation ring is connected to the tower body above the air distribution component, the outer edge of the liquid ventilation ring is a curved surface concave toward the center of the liquid ventilation ring, the outer edges of the upper and lower ends of the liquid ventilation ring are fitted to the inner wall of the tower body to form a closed liquid and air inlet channel between the curved surface and the inner wall of the tower body, a plurality of atomizing nozzles are arranged on the liquid ventilation ring, the liquid and air inlet channels are connected with the inner cavity through the atomizing nozzles, and the liquid inlet pipe can be connected with the liquid and air inlet channels.

[0011] As a preferred solution of an industrial waste salt organic matter removal device in the present invention, the tower body is also connected to a second air inlet pipe, and the second air inlet pipe is connected to a second air inlet control valve. When the second air inlet control valve is opened, the second air inlet pipe is connected to the liquid and air inlet channels.

[0012] As a preferred solution of the device for removing organic matter from industrial waste salt in the present invention, the tower body is also connected to a first pressure relief valve which is in communication with the liquid and air inlet passages.

[0013] As a preferred solution of an industrial waste salt organic matter removal device in the present invention, wherein: a feed pipe is connected to the tower body above the liquid inlet pipe, and a feed control valve is connected to the feed pipe. When the feed control valve is opened, the feed pipe and the inner cavity are connected.

[0014] As a preferred scheme of the industrial waste salt organic matter removal device in the present invention, wherein: a circular purge pipe is connected to the tower body above the upper air distribution plate, the purge pipe has a closed annular air intake space, the tower body is connected to a purge air intake pipe, the purge air intake pipe is connected to a purge air intake valve, one end of the purge air intake pipe is outside the tower body, and the other end of the purge air intake pipe is connected to the purge pipe and connected to the air intake space, and a plurality of purge holes connected to the air intake space are arranged on the inner wall of the purge pipe.

[0015] As a preferred solution of an industrial waste salt organic matter removal device in the present invention, wherein: a lower head is fixed on the tower body at the lower side of the lower air distribution plate, and the lower end of the lower head is fixedly connected with a discharge pipe; an upper head is fixed at the upper end of the tower body, and both the lower head and the upper head are conical, the outer diameter of the lower end of the lower head is smaller than the outer diameter of the upper end of the lower head, the outer diameter of the lower end of the upper head is larger than the outer diameter of the upper end of the upper head, and the exhaust pipe is fixed at the upper end of the upper head.

[0016] As a preferred solution of the industrial waste salt organic matter removal device in the present invention, the upper head is connected to an upper pressure relief valve, the lower head is connected to a lower pressure relief valve, and the tower body at the wind chamber is connected to a second pressure relief valve.

[0017] As another object of the present invention, the present invention provides a method for removing organic matter from waste salt using a removal device, wherein the organic matter removal treatment of high-salt organic wastewater comprises the following steps:

[0018] Open the first air inlet control valve, and the external high-temperature air enters the air chamber through the first air inlet pipe, and is blown upward into the inner cavity through the hollow cavity and the air hole in sequence;

[0019] Open the liquid inlet control valve, and the pressurized high-salt organic wastewater from the outside enters the liquid inlet and air inlet channel through the liquid inlet pipe, and is sprayed into the liquid and air ring through the atomizing nozzle and instantly atomized. The organic matter is pyrolyzed and carbonized, the water evaporates into water vapor, and the inorganic salt crystallizes and solidifies into salt slag. The mixed gas is discharged from the exhaust pipe, and the salt slag and carbide are discharged from the discharge pipe;

[0020] During operation, the purge air inlet valve is controlled to open at a set interval to prevent salt slag from depositing on the upper side of the upper air distribution plate;

[0021] When the operation is completed, close the liquid inlet control valve, cut off the high-salt wastewater supply, close the first air inlet control valve, open the gap control purge air inlet valve, ventilate the purge pipe, blow air through the purge hole, blow the residual salt slag into the slag discharge pipe, and discharge the salt slag out of the discharge pipe;

[0022] The removal of waste salt, solid waste and organic matter includes the following steps:

[0023] Open the first air inlet control valve, and the external high-temperature air enters the air chamber through the first air inlet pipe and is evenly blown into the inner cavity through the air holes;

[0024] Open the second air inlet control valve, and the external high-temperature air enters the liquid and air passage through the second air inlet pipe, and is sprayed into the liquid and air ring through the atomizing nozzle;

[0025] Open the feed control valve, and the external waste salt particles are fed into the tower body through the feed pipe. They are fully fluidized under the action of the high-temperature fluidizing air in the tower body, and the fully pyrolyzed and carbonized salt slag falls to the bottom and is discharged from the tower body through the slag discharge pipe and the discharge pipe in turn, and the mixed gas is discharged from the exhaust pipe;

[0026] During operation, the purge air inlet valve is controlled to open at a set interval to prevent salt slag from depositing on the upper side of the upper air distribution plate;

[0027] When the operation is completed, close the feed control valve to cut off the high-salt particle supply, close the second air inlet control valve to cut off the high-temperature air supply, open the gap-controlled purge air inlet valve, and blow the gas into the purge pipe through the purge hole to blow the residual salt slag into the slag discharge pipe, so that the salt slag is discharged from the discharge pipe.

[0028] Compared with the prior art, the present invention has the following technical effects: the air distribution component integrates the air distribution and slag discharge functions, and realizes real-time slag discharge while achieving air distribution; the pipelines for introducing wastewater and solid waste particles are designed separately, so as to achieve the removal of organic matter in wastewater or solid waste particles and improve the scope of application; through the joint arrangement of the tower body and the liquid ventilation ring, it can be used as a wastewater sprayer and as a mixer for enhanced mixing. The middle of the liquid ventilation ring is a narrow opening, which increases the air flow rate and has an obvious chimney effect, which can effectively reduce the power consumption of the air inlet fan; it can be used to remove organic matter from industrial waste salt. BRIEF DESCRIPTION OF THE DRAWINGS

[0029] 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 labor. Among them:

[0030] Figure 1 It is the internal structure diagram of the present invention.

[0031] Figure 2 for Figure 1 A partial enlarged view of point A in the middle.

[0032] Figure 3 It is a top view of the upper air distribution plate in the present invention.

[0033] Figure 4 for Figure 3 The view from the center BB.

[0034] Figure 5 It is a top view of the lower air distribution plate in the present invention.

[0035] Figure 6 It is a structural diagram of the air distribution hood in the present invention.

[0036] Figure 7 It is a three-dimensional structural diagram of the purge tube in the present invention.

[0037] Figure 8It is a three-dimensional structural diagram of the liquid and ventilation ring in the present invention.

[0038] In the figure, 100 is a main assembly, 101 is a first air inlet pipe, 102 is a first air inlet control valve, 103 is a tower body, 103a is a lower end cap, 103b is an upper end cap, 103c is an inner cavity, 103d is a discharge pipe, 103e is a wind chamber, 104 is a liquid inlet pipe, 105 is a liquid inlet control valve, 106 is a feed pipe, 107 is a feed control valve, 108 is a velocity measuring air pipe, 109 is an exhaust pipe, 110 is an upper pressure relief valve, 111 is a second air inlet control valve, 112 is a second air inlet pipe, 200 is a liquid ventilation ring, 201 is a liquid ventilation ring, 202 is a liquid ventilation ring, 203 is a liquid ventilation ring, 204 is a liquid ventilation ring, 205 is a liquid ventilation ring, 206 is a liquid ventilation ring, 207 is a liquid ventilation ring, 208 is a liquid ventilation ring, 209 is a liquid ventilation ring, 201 is a liquid ventilation ring, 201 is a liquid ventilation ring, 202 is a liquid ventilation ring, 203 is a liquid ventilation ring, 204 is a liquid ventilation ring, 205 is a liquid ventilation ring, 206 is a liquid ventilation ring, 207 is a liquid ventilation ring, 208 is a liquid ventilation ring, 209 is a liquid ventilation ring, 20 Atomizing nozzle, 202 curved surface, 300 first pressure relief valve, 400 temperature sensor, 500 purge pipe, 501 air intake space, 502 purge hole, 600 purge air intake pipe, 700 purge air intake valve, 800 air distribution assembly, 801 wind hood, 801a hollow cavity, 801b air hole, 802 upper air distribution plate, 802a upper slag discharge hole, 802b threaded hole, 802c through hole, 803 slag discharge pipe, 804 lower air distribution plate, 804a lower slag discharge hole, 900 second pressure relief valve. DETAILED DESCRIPTION

[0039] 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.

[0040] 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.

[0041] 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.

[0042] Example 1

[0043] Reference Figures 1 to 8 This embodiment provides an industrial waste salt organic matter removal device, which can achieve the removal of organic matter. The salt slag after the organic matter is removed is discharged through a discharge pipe for further recycling, which is more environmentally friendly.

[0044] An industrial waste salt organic matter removal device includes a main body component 100, the main body component 100 includes a tower body 103, the upper end of the tower body 103 is connected to an exhaust pipe 109, the lower part of the tower body 103 is connected to a first air inlet pipe 101, the first air inlet pipe 101 is connected to a first air inlet control valve 102, the tower body 103 above the first air inlet pipe 101 is connected to a liquid inlet pipe 104, the liquid inlet pipe 104 is connected to a liquid inlet control valve 105, when the liquid inlet control valve 105 is opened, the liquid inlet pipe 104 is connected to the inner cavity 103c of the tower body 103, in order to further realize the salt slag discharge after the organic matter is removed, the tower body at the lower side of the lower air distribution plate 804 is connected to the lower part of the tower body 103. A lower head 103a is fixed on 103, and a discharge pipe 103d is fixedly connected to the lower end of the lower head 103a; an upper head 103b is fixed to the upper end of the tower body 103, and both the lower head 103a and the upper head 103b are conical, the outer diameter of the lower end of the lower head 103a is smaller than the outer diameter of the upper end of the lower head 103a, and the outer diameter of the lower end of the upper head 103b is larger than the outer diameter of the upper end of the upper head 103b, an exhaust pipe 109 is fixed to the upper end of the upper head 103b, an upper pressure relief valve 110 and a speed measuring air pipe 108 are connected to the upper head 103b, and a lower pressure relief valve is connected to the lower head 103a; an air distribution component 800 is connected inside the tower body 103.

[0045] Furthermore, the air distribution assembly 800 includes a lower air distribution plate 804 connected to the tower body 103, an upper air distribution plate 802 is connected to the tower body 103 above the lower air distribution plate 804, a plurality of threaded holes 802b are arranged on the upper air distribution plate 802, a through hole 802c connected to the air chamber 103e is opened on the upper air distribution plate 802 below the threaded hole 802b, the upper air distribution plate 802 is threadedly connected to a hood 801 having a downward hollow cavity 801a through the threaded hole 802b, and a plurality of air holes 801b are arranged on the hood 801 above the upper air distribution plate 802 A wind chamber 103e is formed between the lower side of the upper air distribution plate 802, the inner wall of the tower body 103 and the upper side of the lower air distribution plate 804, a plurality of upper slag discharge holes 802a are arranged on the upper air distribution plate 802, a plurality of slag discharge pipes 803 corresponding to the upper slag discharge holes 802a are arranged between the upper air distribution plate 802 and the lower air distribution plate 804, and lower slag discharge holes 804a are provided on the lower air distribution plate 804 at the lower side of the slag discharge pipes 803. When the first air inlet control valve 102 is opened, the first air inlet pipe 101 is connected to the wind chamber 103e, and the axis of the air hole 801b is inclined upward from the inside to the outside.

[0046] A liquid ventilation ring 200 is connected to the tower body 103 above the air distribution assembly 800. The outer edge of the liquid ventilation ring 200 is a curved surface 202 that is recessed toward the center of the liquid ventilation ring 200. The outer edges of the upper and lower ends of the liquid ventilation ring 200 are fitted to the inner wall of the tower body 103 to form a closed liquid and air inlet channel between the curved surface 202 and the inner wall of the tower body 103. A plurality of atomizing nozzles 201 are arranged on the liquid ventilation ring 200. The liquid and air inlet channels are connected to the inner cavity 103c via the atomizing nozzles 201, and the liquid inlet pipe 104 can be connected to the liquid and air inlet channels.

[0047] A temperature sensor 400 is connected to the tower body 103 above the upper air distribution plate 802; in the initial state, all control valves are in a closed state; when removing organic matter from high-salinity wastewater, the first air inlet control valve 102 is opened, and high-temperature gas is introduced into the first air inlet pipe 101, and the external high-temperature air enters the wind chamber 103e through the first air inlet control valve 102. The temperature is measured by the temperature sensor 400, and the air inlet temperature is controlled between 500°C and 700°C according to different working conditions. Pressurized high-salinity organic wastewater is introduced into the liquid inlet pipe 104, and the high-salinity organic wastewater enters the liquid and ventilation channel, and is sprayed into the liquid and ventilation channel through a plurality of atomizing nozzles 201 arranged in an array on the curved surface 202. The liquid is instantly atomized in the middle channel of the ring 200, and the atomizing nozzle 201 is shaped like a Venturi nozzle, which can enhance the liquid atomization effect. The atomized wastewater and the high-temperature fluidized air intake are mixed and contacted to quickly pyrolyze and carbonize. The middle channel of the liquid and ventilation ring 200 is narrow in the middle and wide at the upper and lower ends, which has the effect of increasing the air flow velocity and has an obvious chimney effect, which can reduce the power consumption of the air intake fan. During operation, the organic matter in the atomized wastewater is pyrolyzed and carbonized, the water evaporates into water vapor, and the inorganic salt crystallizes and solidifies into salt slag. The mixed gas is discharged from the exhaust pipe 109, and the salt slag and carbide are discharged from the discharge pipe 103d. Since the organic matter is fully pyrolyzed and carbonized, the salt slag discharged from the discharge pipe 103d can be recycled.

[0048] In order to further improve the scope of application, the tower body 103 is also connected to a second air inlet pipe 112, and the second air inlet control valve 111 is connected to the second air inlet pipe 112. When the second air inlet control valve 111 is opened, the outer end of the second air inlet pipe 112 is connected to the liquid inlet and air inlet channels, and when the second air inlet control valve 111 is closed, the outer end of the second air inlet pipe 112 is isolated from the liquid inlet and air inlet channels; the tower body 103 is also connected to a first pressure relief valve 300 connected to the liquid inlet and air inlet channels, a second pressure relief valve 900 is connected to the tower body 103 at the wind chamber 103e, a feed pipe 106 is connected to the tower body 103 above the liquid inlet pipe 104, and a feed control valve 107 is connected to the feed pipe 106. When the feed control valve 107 is opened, the feed pipe 106 is connected to the inner cavity 103c, and when the feed control valve 107 is closed, the feed pipe 106 is isolated from the inner cavity 103c.

[0049] When removing organic matter from waste salt solid waste, the first air inlet control valve 102 is opened, and the external high-temperature air enters the air chamber 103e through the first air inlet pipe 101, and is evenly blown into the inner cavity 103c through the plurality of air holes 801b arranged on the plurality of air caps 801. The temperature is measured by the temperature sensor 400, and the air inlet temperature is controlled between 600°C and 800°C according to the different feed materials. The wind speed is measured by the speed measuring air pipe 108, and the air inlet speed is controlled according to the working conditions. The second air inlet control valve 111 is opened, and the external high-temperature air enters the liquid and air passage through the second air inlet pipe 112, and is sprayed into the middle passage through the atomizing nozzle 201, and the atomizing nozzle 201 is used to spray the atomizing nozzle 201 into the middle passage. The air pressure at the nozzle 201 is controlled to be 10% of the air pressure in the wind chamber 103e. The airflow ejected from the atomizing nozzle 201 is conducive to the fluidization of the waste salt particles and can also effectively prevent the atomizing nozzle 201 from being blocked. The feed control valve 107 is opened, and the waste salt particles are introduced into the feed pipe 106 and input into the tower body 103. Under the action of the high-temperature fluidizing wind in the tower body 103, they are fully fluidized, and the heat of the fluidizing air is fully mixed with the waste salt particles, which improves the efficiency of heat and mass transfer, so that the organic matter in the waste salt is fully oxidized and pyrolyzed, and the fully pyrolyzed and carbonized salt slag falls to the bottom and is discharged from the tower body 103 through the slag discharge pipe 803, the lower head 103a, and then through the discharge pipe 103d.

[0050] During the organic matter removal process, overpressure at any point will trigger the corresponding pressure relief valve to open and release pressure.

[0051] In order to further avoid the deposition of salt slag on the upper air distribution plate 802, a circular purge pipe 500 is connected to the tower body 103 above the upper air distribution plate 802, and the purge pipe 500 has a closed annular air intake space 501. The tower body 103 is connected to a purge air intake pipe 600, and the purge air intake pipe 600 is connected to a purge air intake valve 700. One end of the purge air intake pipe 600 is outside the tower body 103, and the other end of the purge air intake pipe 600 is connected to the purge pipe 500 and connected to the air intake space 501. The inner wall of the purge pipe 500 is provided with a plurality of purge holes 502 connected to the air intake space 501.

[0052] During the organic matter removal process, the purge air inlet valve 700 is intermittently controlled to open several times, and gas is introduced into the purge air inlet pipe 600, and air is blown onto the upper wind plate through the purge hole 502 to prevent residue from being deposited on the upper wind plate, and the residual salt residue is blown into the slag discharge pipe 803. At the same time, it can also promote the salt residue in the lower cone head to be discharged faster along the discharge pipe 103d.

[0053] Example 2

[0054] Reference Figures 1 to 8 This embodiment is based on Example 1, and the difference from Example 1 is that this embodiment of the present invention provides a method for removing organic matter from waste salt using a removal device, which can further achieve the removal of organic matter from high-salt organic wastewater and waste salt solid waste.

[0055] When removing organic matter from high-salt organic wastewater, the following steps are included:

[0056] The first air inlet control valve 102 is opened, and the external high-temperature air enters the air chamber 103e through the first air inlet pipe 101, and the air is blown upward into the inner cavity 103c through the hollow cavity 801a and the air hole 801b in sequence. The temperature sensor 400 detects the temperature inside the tower body 103 above the upper wind plate, and controls the air inlet temperature to be between 500°C and 700°C according to different working conditions. The wind speed is measured by the speed measuring air pipe 108, and the air inlet speed is adjusted and controlled according to the working conditions;

[0057] Open the liquid inlet control valve 105, and the pressurized high-salt organic wastewater from the outside enters the liquid inlet and air inlet channel through the liquid inlet pipe 104, and is sprayed into the liquid and air ring 200 through the atomizing nozzle 201 and instantly atomized, the organic matter is pyrolyzed and carbonized, the water evaporates into water vapor, the inorganic salt crystallizes and solidifies into salt slag, and the mixed gas is discharged from the exhaust pipe 109, and the salt slag and carbide are discharged from the discharge pipe 103d;

[0058] During operation, the purge air inlet valve 700 is controlled to open at a set interval to prevent salt slag from being deposited on the upper side of the upper air distribution plate 802;

[0059] When the operation is completed, the liquid inlet control valve 105 is closed, the high-salt wastewater supply is cut off, the first air inlet control valve 102 is closed, the gap control purge air inlet valve 700 is opened, air is ventilated into the purge pipe 500, and air is blown through the purge hole 502 to blow the residual salt slag into the slag discharge pipe 803, so that the salt slag is discharged from the discharge pipe 103d;

[0060] The process of removing organic matter from waste salt solid waste includes the following steps:

[0061] The first air inlet control valve 102 is opened, and the external high-temperature air enters the air chamber 103e through the first air inlet pipe 101, and is evenly blown to the inner cavity 103c through the air holes 801b. The temperature sensor 400 detects the temperature inside the tower body 103 above the upper wind plate, and controls the air inlet temperature to be between 600°C and 800°C according to different working conditions. The wind speed is measured by the speed measuring air pipe 108, and the air inlet speed is adjusted and controlled according to the working conditions.

[0062] The second air inlet control valve 111 is opened, and the external high-temperature air enters the liquid ventilation channel through the second air inlet pipe 112, and is sprayed into the liquid ventilation ring 200 through the atomizing nozzle 201. By controlling the air pressure entering the second air inlet pipe 112 and the first air inlet pipe 101, the air pressure at the atomizing nozzle 201 is controlled to be 10% of the air pressure of the wind chamber 103e. The airflow sprayed from the atomizing nozzle 201 helps the fluidization of the waste salt particles and effectively prevents the atomizing nozzle 201 from being blocked.

[0063] Open the feed control valve 107, and the external waste salt particles are fed into the tower body 103 through the feed pipe 106. Under the action of the high-temperature fluidizing air in the tower body 103, the salt slag that is fully pyrolyzed and carbonized falls to the bottom and is discharged from the tower body 103 through the slag discharge pipe 803 and the discharge pipe 103d in turn, and the mixed gas is discharged from the exhaust pipe 109;

[0064] During operation, the purge air inlet valve 700 is controlled to open at a set interval to prevent salt slag from being deposited on the upper side of the upper air distribution plate 802;

[0065] When the operation is completed, the feed control valve 107 is closed to cut off the high-salt particle supply, the second air inlet control valve 111 is closed to cut off the high-temperature air supply, the gap control purge air inlet valve 700 is opened, and the gas entering the purge pipe 500 is blown through the purge hole 502 to blow the residual salt slag into the slag discharge pipe 803, so that the salt slag is discharged from the discharge pipe 103d.

[0066] 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. An industrial waste salt organic matter removal device, characterized in that: These include, The main body component (100) comprises a tower body (103), wherein the upper end of the tower body (103) is connected to an exhaust pipe (109), the lower part of the tower body (103) is connected to a first air inlet pipe (101), the first air inlet pipe (101) is connected to a first air inlet control valve (102), the tower body (103) above the first air inlet pipe (101) is connected to a liquid inlet pipe (104), the liquid inlet pipe (104) is connected to a liquid inlet control valve (105), and when the liquid inlet control valve (105) is opened, the liquid inlet pipe (104) is connected to an inner cavity (103c) of the tower body (103); The air distribution assembly (800) comprises a lower air distribution plate (804) connected to the tower body (103); an upper air distribution plate (802) is connected to the tower body (103) above the lower air distribution plate (804); a plurality of wind caps (801) with downwardly facing hollow cavities (801a) are arranged on the upper air distribution plate (802); a plurality of air holes (801b) are arranged on the wind cap (801) above the upper air distribution plate (802); the lower side of the upper air distribution plate (802), the inner wall of the tower body (103) and the lower air distribution plate (804) are connected to the tower body (103); A wind chamber (103e) is formed between the upper and lower sides of the first air distribution plate (804), a plurality of upper slag discharge holes (802a) are arranged on the upper air distribution plate (802), a plurality of slag discharge pipes (803) corresponding to the upper slag discharge holes (802a) are arranged between the upper air distribution plate (802) and the lower air distribution plate (804), and a lower slag discharge hole (804a) is provided on the lower air distribution plate (804) below the slag discharge pipe (803), and when the first air inlet control valve (102) is opened, the first air inlet pipe (101) and the wind chamber (103e) are connected; A liquid-passing and air-venting ring (200) is connected to the tower body (103) above the air distribution assembly (800). The outer edge of the liquid-passing and air-venting ring (200) is a curved surface (202) that is concave toward the center of the liquid-passing and air-venting ring (200). The outer edges of the upper and lower ends of the liquid-passing and air-venting ring (200) are attached to the inner wall of the tower body (103) so that a closed liquid-inlet and air-inlet channel is formed between the curved surface (202) and the inner wall of the tower body (103). A plurality of atomizing nozzles (201) are arranged on the liquid-passing and air-venting ring (200). The liquid-inlet and air-inlet channels are connected to the inner cavity (103c) via the atomizing nozzles (201). The liquid inlet pipe (104) can be connected to the liquid inlet and air inlet channel, the tower body (103) is also connected to a second air inlet pipe (112), the second air inlet pipe (112) is connected to a second air inlet control valve (111), when the second air inlet control valve (111) is opened, the second air inlet pipe (112) and the liquid inlet and air inlet channel are connected, the tower body (103) above the liquid inlet pipe (104) is connected to a feed pipe (106), the feed pipe (106) is connected to a feed control valve (107), when the feed control valve (107) is opened, the feed pipe (106) and the inner cavity (103c) are connected.

2. The device for removing organic matter from industrial waste salt according to claim 1, characterized in that: The axis of the air hole (801b) is arranged to be inclined upward from the inside to the outside.

3. An industrial waste salt organic matter removal device as claimed in claim 1 or 2, characterized in that: The tower body (103) is also connected to a first pressure relief valve (300) which is in communication with the liquid and gas inlet passages.

4. The device for removing organic matter from industrial waste salt according to claim 1 or 2, characterized in that: A circular purge pipe (500) is connected to the tower body (103) above the upper air distribution plate (802), and the purge pipe (500) has a closed annular air intake space (501). A purge air intake pipe (600) is connected to the tower body (103), and a purge air intake valve (700) is connected to the purge air intake pipe (600). One end of the purge air intake pipe (600) is outside the tower body (103), and the other end of the purge air intake pipe (600) is connected to the purge pipe (500) and communicates with the air intake space (501). The inner wall of the purge pipe (500) is provided with a plurality of purge holes (502) that are communicated with the air intake space (501).

5. The device for removing organic matter from industrial waste salt according to claim 4, characterized in that: A lower end cap (103a) is fixed on the tower body (103) at the lower side of the lower air distribution plate (804), and a discharge pipe (103d) is fixedly connected to the lower end of the lower end cap (103a); an upper end cap (103b) is fixed to the upper end of the tower body (103), and both the lower end cap (103a) and the upper end cap (103b) are conical, and the outer diameter of the lower end of the lower end cap (103a) is smaller than the outer diameter of the upper end of the lower end cap (103a), and the outer diameter of the lower end of the upper end cap (103b) is larger than the outer diameter of the upper end of the upper end cap (103b), and an exhaust pipe (109) is fixed to the upper end of the upper end cap (103b).

6. The device for removing organic matter from industrial waste salt according to claim 5, characterized in that: The upper end cap (103b) is connected to an upper pressure relief valve (110), the lower end cap (103a) is connected to a lower pressure relief valve, and the tower body (103) at the wind chamber (103e) is connected to a second pressure relief valve (900).

7. A method for removing organic matter from waste salt using the removal device as claimed in claim 6, characterized in that: The removal of organic matter from high-salt organic wastewater includes the following steps: The first air inlet control valve (102) is opened, and the external high-temperature air enters the air chamber (103e) through the first air inlet pipe (101), and is blown upwardly into the inner cavity (103c) through the hollow cavity (801a) and the air hole (801b) in sequence; The liquid inlet control valve (105) is opened, and the external pressurized high-salt organic wastewater enters the liquid inlet and air inlet passage through the liquid inlet pipe (104), and is sprayed into the liquid and air circulation ring (200) through the atomizing nozzle (201) to be instantly atomized, the organic matter is pyrolyzed and carbonized, the water evaporates into water vapor, the inorganic salt crystallizes and solidifies into salt residue, and the mixed gas is discharged through the exhaust pipe (109), and the salt residue and carbide are discharged through the discharge pipe (103d); During operation, the purge air inlet valve (700) is controlled to open at a set interval to prevent salt slag from being deposited on the upper side of the upper air distribution plate (802); When the operation is completed, the liquid inlet control valve (105) is closed, the high-salt organic wastewater supply is cut off, the first air inlet control valve (102) is closed, the gap control purge air inlet valve (700) is opened, air is ventilated into the purge pipe (500), and air is blown through the purge hole (502) to blow the residual salt residue into the slag discharge pipe (803), so that the salt residue is discharged from the discharge pipe (103d); The removal of waste salt, solid waste and organic matter includes the following steps: The first air inlet control valve (102) is opened, and the external high-temperature air enters the air chamber (103e) through the first air inlet pipe (101), and is evenly blown into the inner cavity (103c) through the air holes (801b); The second air inlet control valve (111) is opened, and the external high-temperature air enters the liquid and air passage through the second air inlet pipe (112), and is sprayed into the liquid and air ring (200) through the atomizing nozzle (201); Open the feed control valve (107), and the external waste salt particles are fed into the tower body (103) through the feed pipe (106). The waste salt particles are fully fluidized under the action of the high-temperature fluidizing air in the tower body (103) 1, and the fully pyrolyzed and carbonized salt slag falls to the bottom and is discharged from the tower body (103) through the slag discharge pipe (803) and the discharge pipe (103d) in sequence, and the mixed gas is discharged from the exhaust pipe (109); During operation, the purge air inlet valve (700) is controlled to open at a set interval to prevent salt slag from being deposited on the upper side of the upper air distribution plate (802); When the operation is completed, the feed control valve (107) is closed to cut off the supply of waste salt particles, the second air inlet control valve (111) is closed to cut off the supply of high-temperature air, the gap control purge air inlet valve (700) is opened, and the gas introduced into the purge pipe (500) is blown through the purge hole (502) to blow the residual salt slag into the slag discharge pipe (803), so that the salt slag is discharged from the discharge pipe (103d).

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