CN214307135U - High-efficient processing apparatus of organic waste liquid - Google Patents
High-efficient processing apparatus of organic waste liquid Download PDFInfo
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- CN214307135U CN214307135U CN202120131552.1U CN202120131552U CN214307135U CN 214307135 U CN214307135 U CN 214307135U CN 202120131552 U CN202120131552 U CN 202120131552U CN 214307135 U CN214307135 U CN 214307135U
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Abstract
The utility model discloses an organic waste liquid high-efficiency processing device, which comprises a shell, an organic waste liquid conveying assembly is sequentially arranged along the inner side of the shell from inside to outside, a transition channel, a temperature adjusting channel, a coal powder conveying channel, a combustion air channel and an adherence air channel, the organic waste liquid high-efficiency processing device can introduce air into the organic waste liquid high-efficiency processing device through the adherence air channel, the air can flow along the peripheral wall to form an air cooling layer, the air cooling layer can well reduce the temperature of the peripheral wall, the temperature of the peripheral wall can be kept stable, the phenomena of dust deposition and coking corrosion on the surface of the peripheral wall are avoided, the service life of the organic waste liquid high-efficiency processing device is favorably prolonged, the organic waste liquid is processed through coal powder combustion through the coal powder conveying channel, the original heat value of the organic waste liquid is fully utilized, the effect of adjusting the temperature of a combustion area is achieved through changing the gas composition and the flow velocity in the temperature adjusting channel, effectively decompose organic matters in the waste liquid, and solve the problems of difficult combustion and low treatment efficiency.
Description
Technical Field
The utility model relates to a waste incineration's technical field, more specifically relates to an organic waste liquid high efficiency processing apparatus.
Background
Chemical organic waste liquid widely exists in industries such as basic chemical raw material manufacturing, coal chemical industry, petrochemical industry and the like, is high-concentration salt-containing polluting waste liquid, has huge production amount, complex components and special physicochemical characteristics, such as low heat value, low ash melting point, high corrosive substance content and the like, and the chemical organic waste liquid treatment is basically performed by a chemical reaction method, a physical separation method, a landfill method and combustion treatment at present, wherein the combustion treatment is a relatively universal low-cost and low-pollution mode, but the problems of difficult combustion, low treatment efficiency, short service life of equipment and the like still exist in the treatment process.
SUMMERY OF THE UTILITY MODEL
The present invention aims at solving at least one of the technical problems in the related art to a certain extent.
Therefore, the embodiment of the utility model provides an organic waste liquid high-efficient processing apparatus, this organic combustion waste liquid treater handles organic waste liquid with pulverized coal combustion, has fully utilized the original calorific value of organic waste liquid, through changing the gas composition and the velocity of flow in the passageway that adjusts the temperature, plays the effect of adjusting the combustion zone temperature, effectively decomposes the organic matter in the waste liquid, has solved difficult combustion and the problem of treatment inefficiency; this organic combustion waste liquid treater has set up combustion-supporting wind passageway and adherence wind passageway, can make the air divide into combustion-supporting wind and adherence wind and get into respectively in the organic waste liquid high efficiency processing device, not only make the air give in organic waste liquid high efficiency processing device in grades and reduce nitrogen oxide, combustion-supporting wind combines together with the transition passageway and makes gas-liquid solid fuel and air intensive mixing stable combustion, and adherence wind can form the cooling air bed that flows along the perisporium inner peripheral surface in first intracavity, with the cooling perisporium, not only can cancel water cooling plant, and avoid the emergence of perisporium surface deposition coking corrosion phenomenon.
According to the utility model discloses organic waste liquid high efficiency processing device includes: the shell is provided with a first cavity and a peripheral wall enclosing the first cavity, and the first cavity comprises an air guide cavity, a combustion stabilizing cavity and a rectifying cavity which are sequentially communicated; an organic waste liquid conveying assembly arranged in the center of the first cavity; the first air duct is sleeved at the liquid inlet end of the organic waste liquid conveying component, one end, close to the liquid inlet end of the organic waste liquid conveying component, is open, one end, far away from the liquid inlet end of the organic waste liquid conveying component, is closed, and a transition channel is formed between the inner circumferential surface of the first air duct and the outer circumferential surface of the organic waste liquid conveying component; the second air duct is arranged in the air guide cavity, and an adherence air channel is formed between the outer peripheral surface of the second air duct and the inner peripheral surface of the peripheral wall; the third air duct is arranged in the air guide cavity, and a combustion-supporting air channel is formed between the outer peripheral surface of the third air duct and the inner peripheral surface of the second air duct; and one of the outer peripheral surface of the fourth air duct and the inner peripheral surface of the third air duct and the inner peripheral surface of the fourth air duct and the outer peripheral surface of the first air duct is a pulverized coal conveying channel, and the other is a temperature regulating channel.
According to the embodiment of the utility model, set up the first air duct, the second air duct, the third air duct, fourth air duct and organic waste liquid transport assembly that establish each other in organic waste liquid high efficiency processing device, wherein organic waste liquid transport assembly is coaxial with the organic waste liquid combustion processor, in the radial direction of organic waste liquid high efficiency processing device, first air duct cover is established on organic waste liquid transport assembly, form transition passageway between the inside of first air duct and the outside of organic waste liquid transport assembly, form adherence wind channel between second air duct outer peripheral face and the perisporium medial surface, form combustion-supporting wind between third air duct outer peripheral face and the second air duct medial surface and arrive simultaneously, fourth air duct medial surface and first air duct lateral surface, between fourth air duct lateral surface and the third air duct medial surface, one of them is buggy conveying channel, another forms the passageway that adjusts the temperature, the utility model discloses an organic waste liquid high efficiency processing apparatus can be according to the temperature of organic waste liquid high efficiency processing apparatus's perisporium, let in the air in to organic waste liquid high efficiency processing apparatus through adherence wind passageway, this air can flow in order to form the air cooling layer along the perisporium, the temperature of the reduction perisporium that this air cooling layer can be fine, make the temperature of perisporium remain stable, the emergence of perisporium surface deposition coking and corrosion phenomena has been avoided, be favorable to prolonging organic waste liquid high efficiency processing apparatus's life, through buggy transfer passage with the organic waste liquid of buggy combustion processing, make full use of the original calorific value of organic waste liquid, constitute and the velocity of flow through the gas that changes in the passageway that adjusts the temperature, play the effect of adjusting the combustion area temperature, effectively decompose the organic matter in the waste liquid, the problem that difficult combustion and treatment effeciency are low is solved.
In some embodiments, organic waste liquid transport assembly includes organic waste liquid conveyer pipe, reflux cap and atomizing nozzle assembly, organic waste liquid conveyer pipe with the coaxial setting in first chamber, the reflux cap is established the play liquid end of organic waste liquid conveyer pipe, the reflux cap is the cylindric, the export orientation of reflux cap the inlet end of organic waste liquid conveyer pipe, atomizing nozzle assembly sets up the exit of reflux cap.
In some embodiments, the atomizing nozzle assembly comprises a fixed disk, the fixed disk is sleeved outside the liquid outlet end of the organic waste liquid conveying pipe, the outer peripheral surface of the fixed disk is connected with the inner edge of the outlet end of the backflow cap, and the fixed disk is provided with a plurality of injection holes penetrating through the fixed disk.
In some embodiments, an impeller assembly is arranged in each of the combustion air channel and the temperature adjusting channel.
In some embodiments, the second air duct includes a barrel, a flexible portion sleeved on an outer circumferential surface of the barrel, and an adjusting assembly, the adjusting assembly includes an adjusting piece and a sealing washer, a plurality of mounting holes are formed in the barrel at intervals along a circumferential direction of the barrel, one adjusting assembly is correspondingly arranged in each mounting hole, a first portion of the adjusting piece penetrates through the flexible portion and is arranged in the mounting hole, a second portion of the adjusting piece is pressed on the outer circumferential surface of the flexible portion, and the sealing washer is arranged between the second portion of the adjusting piece and the outer circumferential surface of the flexible portion.
In some embodiments, an igniter and a flame detector are disposed within the transition passage.
In some embodiments, a plurality of density separation structures are arranged on the inner side of the pulverized coal conveying channel along the circumferential direction of the pulverized coal conveying channel.
Drawings
Fig. 1 is a first perspective view of a cross-sectional view of an apparatus for efficiently treating organic waste liquid according to an embodiment of the present invention.
Fig. 2 is a second perspective view of the cross-sectional view of the device for efficiently treating organic waste liquid according to the embodiment of the present invention.
Fig. 3 is a third perspective view of the cross-sectional view of the device for efficiently treating organic waste liquid according to the embodiment of the present invention.
Fig. 4 is a perspective view of an apparatus for efficiently treating organic waste liquid according to an embodiment of the present invention.
Fig. 5 is a front view of an atomizing nozzle assembly according to an embodiment of the present invention.
Fig. 6 is a perspective view of an atomizing nozzle assembly according to an embodiment of the present invention.
Fig. 7 is a cross-sectional view of fig. 6.
Fig. 8 is a sectional view of a second air duct according to an embodiment of the present invention
Reference numerals:
the device comprises a shell 1, a first air duct 2, a second air duct 3, a cylinder 301, a flexible part 302, a regulating part 303, a sealing washer 304, a third air duct 4, a fourth air duct 5, a stable combustion chamber 6, a rectification chamber 7, an organic waste liquid conveying pipe 8, a backflow cap 9, a fixed disc 10, an injection hole 11, a transition passage 12, an adherence air passage 13, a combustion-supporting air passage 14, a pulverized coal conveying passage 15 and a temperature adjusting passage 16.
Detailed Description
Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings. The embodiments described below with reference to the drawings are exemplary and intended to be used for explaining the present invention, and should not be construed as limiting the present invention.
As shown in fig. 1-7, the device for efficiently treating organic waste liquid according to the embodiment of the present invention includes a housing 1, a first air duct 2, a second air duct 3, a third air duct 4, a fourth air duct 5, and an organic waste liquid conveying assembly.
The casing 1 is provided with a first cavity and a peripheral wall enclosing the first cavity, the first cavity comprises a combustion stabilizing cavity 6 in the middle, an air guide cavity positioned on the left side of the combustion stabilizing cavity 6 and a rectifying cavity 7 positioned on the right side of the combustion stabilizing cavity 6, the peripheral wall corresponding to the combustion stabilizing cavity 6 is a conical surface, the diameter of a left end port is smaller than that of a right end port, the air guide cavity and the rectifying cavity 7 are cylindrical, and the first air guide cylinder 2, the second air guide cylinder 3, the third air guide cylinder 4 and the fourth air guide cylinder 5 are arranged in the air guide cavity;
the organic waste liquid conveying assembly comprises an organic waste liquid conveying pipe 8, a backflow cap 9 and an atomizing nozzle assembly, the organic waste liquid conveying pipe 8 is coaxially arranged with the first cavity, the liquid inlet end of the organic waste liquid conveying pipe 8 is located in the air guide cavity, the liquid outlet end of the organic waste liquid conveying pipe is located at the outlet end of the rectifying cavity 7, the backflow cap 9 is of a cylindrical structure with one closed end and one open end, the backflow cap 9 is coaxially arranged with the organic waste liquid conveying pipe 8, the backflow cap 9 is located at the liquid outlet end of the organic waste liquid conveying pipe 8, the open end faces the liquid inlet end of the organic waste liquid conveying pipe 8, the atomizing nozzle assembly comprises a fixed disc 10, the fixed disc 10 is sleeved at the liquid outlet end of the organic waste liquid conveying pipe 8, the outer circumferential surface of the fixed disc 10 is connected with the open end of the backflow cap 9, and the fixed disc 10 is provided with a plurality of injection holes 11 penetrating through the fixed disc 10;
the first air duct 2 is a blunt body with a conical shape, an oval shape, a cylindrical shape or other arbitrary curves, the first air duct 2 is sleeved outside the organic waste liquid conveying pipe 8 and is coaxially arranged with the organic waste liquid conveying pipe, one end of the first air duct 2 close to the stable combustion cavity 6 is closed, the closed end is provided with a plurality of through holes (not shown in the figure), one end far away from the stable combustion cavity 6 is opened, the organic waste liquid conveying pipe 8 penetrates through one end, close to the stable combustion cavity 6, of the first air duct 2 and enters the stable combustion cavity 6, a transition channel 12 is formed between the inner side face of the first air duct 2 and the outer side face of the organic waste liquid conveying pipe 8, an igniter (not shown in the figure) is arranged in the transition channel 12, flame of the igniter penetrates through the through holes and then is injected into the first cavity, a flame detector (not shown in the figure) can be further arranged in the transition channel, the widest diameter of the transition channel 12 is smaller than the inner diameter of the fourth air duct 5, and the narrowest diameter is larger than the largest diameter of the igniter and/or the flame detector;
an adherence air channel 13 is formed between the outer side surface of the second air duct 3 and the inner side surface of the peripheral wall, the second air duct 3 comprises a cylinder 301 and a plurality of movable positioning assemblies which are arranged outside the cylinder 301 and distributed along the circumferential direction, the movable positioning assemblies are used for adjusting the sectional area of the adherence air channel 13, each movable positioning assembly comprises a flexible portion 302 sleeved on the outer circumferential surface of the cylinder 301 and an adjusting assembly, each adjusting assembly comprises an adjusting piece 303 and a sealing washer 304, a plurality of mounting holes are formed in the cylinder 301 at intervals along the circumferential direction of the cylinder 301, the mounting holes can be threaded holes, the adjusting pieces 303 can be adjusting bolts, each threaded hole is correspondingly provided with one adjusting bolt, a plurality of unthreaded holes corresponding to the mounting holes are formed in the flexible portions 302, and the threaded ends of the adjusting bolts penetrate through the sealing washers 304 and the unthreaded holes of the flexible portions 302 and are finally screwed into the threaded holes of the cylinder 301 for connection;
a combustion-supporting air channel 14 is formed between the outer side surface of the third air duct 4 and the inner side surface of the second air duct 3;
the fourth air duct 5 is positioned between the third air duct 4 and the first air duct 2, and the inner side and the outer side of the fourth air duct 5 correspond to two channels, wherein one channel can be a pulverized coal conveying channel 15, and the other channel can be a temperature adjusting channel 16;
axial impeller components can be arranged in the combustion-supporting air channel 14 and the temperature adjusting channel 16, a movable axial impeller component (not shown in the figure) which is easy to detach is arranged in the temperature adjusting channel 16 and is used for enabling combustible combustion-supporting gas or inert flame-retardant gas to form rotary airflow with tangential speed after passing through the movable axial impeller component, and a movable axial impeller component (not shown in the figure) which is easy to detach is arranged in the combustion-supporting air channel 14 and is used for enabling combustion-supporting air to form rotary airflow with tangential speed after passing through the movable axial impeller component;
the coal powder conveying channel 15 can be internally provided with a detachable shade separation structural member (not shown in the figure), the shade separation structural member can be divided into a reducing shape, a gear shape and a petal shape, threaded holes are arranged at corresponding positions of the shade separation structural member and the coal powder conveying channel 15, and the shade separation structural member is fixed in the coal powder conveying channel 15 through bolts, sealing gaskets and threaded holes.
The utility model discloses organic waste liquid high efficiency processing apparatus's application method, including following step:
selecting an organic waste liquid conveying pipe 8 with a proper diameter, an atomizing nozzle component with proper atomizing characteristics and a concentration separation component according to the heat value of the organic waste liquid, the waste liquid amount and the coal type, and selecting a reducing type concentration separator or a gear type concentration separator by the concentration separation component if the coal type has high volatile components and high heat value; if the coal type is low in volatile component and low in heat value, the concentration separation component selects a petal-shaped concentration separator;
air is introduced in two paths, one path of air passes through a movable axial impeller assembly (not shown in the figure) in a combustion-supporting air channel 14 to form a rotating airflow with tangential speed to directly enter a combustion stabilizing cavity 6, and the combustion-supporting air channel 14 and a transition channel 12 act together to form an embedded high-temperature backflow area; the other path of the wall-attached air forms wall-attached air through the wall-attached air channel 13, one part of the wall-attached air forms a cooling air layer flowing along the wall surface of the stable combustion cavity 6 so as to cool the stable combustion cavity 6 and the rectification cavity 7, the wall surface temperature of the stable combustion cavity 6 and the rectification cavity 7 is lower than 40 ℃, the other part of the wall-attached air and the main flame form high-speed jet flame of air-wrapped fire through the rectification cavity 7 to enter the hearth, therefore, not only is the fuel stably combusted, but also the phenomenon of ash deposition, coking and corrosion in the shell 1 and the hearth is avoided;
the wind speed of the wall attaching wind is larger than that of the combustion supporting wind and is controlled to be more than 20m/s, the proportion of the combustion supporting wind and the wall attaching wind is preferably 1:2, the proportion can ensure that fuel is stably combusted, the combustion supporting wind is mixed with main flame layer by layer to reduce nitrogen oxides, and the wall attaching wind has enough momentum to cool the combustion stabilizing cavity 6 and the rectifying cavity 7;
meanwhile, the organic waste liquid enters a high-temperature reflux zone through a reflux channel consisting of an organic waste liquid conveying pipe 8, a reflux cap 9 and an atomizing nozzle assembly, wherein the inlet pressure of the organic waste liquid conveying pipe 8 is required to be greater than the pressure inside an organic waste liquid combustor, the pressure is controlled to be 0.3-0.5 MPa to prevent the atomizing nozzle from being blocked, and the organic waste liquid high-efficiency treatment device is not corroded, the organic waste liquid is preheated through the high-temperature reflux zone, a proper combustion temperature is selected according to the heat value of the waste liquid and the waste liquid amount, the temperature adjusting channel 16 can be introduced with oxidizing gas (including but not limited to air and oxygen), combustible gas (including but not limited to H2, CH4 and natural gas) and inert gas (including but not limited to CO2 and N2), if the temperature of the combustion zone is lower, the oxidizing gas or the combustible gas is introduced, if the temperature is higher, the inert gas is introduced to maintain the temperature of the combustion zone between 700-1600 ℃, the pulverized coal is combusted in the high temperature recirculation zone, the organic waste liquid passes through the atomizing nozzle assembly to form a droplet flow, and is mixed with the combustion-supporting air and the temperature-adjusting gas at the closed end of the transition passage 122 to form a multi-layer main flame.
The utility model discloses owing to take above technical scheme, it has following advantage: 1. the utility model treats the organic waste liquid by burning the pulverized coal, fully utilizes the original heat value of the organic waste liquid, plays the role of adjusting the temperature of a combustion area by changing the gas composition and the flow rate in the temperature adjusting channel 16, ensures that the temperature of the combustion area is between 700 and 1600 ℃, and effectively decomposes organic matters in the waste liquid; 2. the utility model discloses set up combustion-supporting wind passageway 14 and adherence wind passageway 13, can make the air divide into combustion-supporting wind and adherence wind and get into the burning processor body respectively, not only make the air give the burning processor in grades and reduce nitrogen oxide, combustion-supporting wind combines together with transition passageway 12 and makes the gaseous-liquid solid fuel and air intensive mixing stable combustion, and adherence wind can form the cooling air bed that flows along the steady burning chamber 6 wall in the steady burning chamber 6, in order to cool steady burning chamber 6 and rectification chamber 7, make the wall temperature of steady burning chamber 6 and rectification chamber 7 be less than 40 ℃ all the time, not only can cancel the water cooling plant of steady burning chamber 6, and avoid the emergence of the ash deposition coking corrosion phenomenon of the steady burning chamber 6 wall; 3. the utility model discloses can adjust the sectional area of adherence wind passageway 13 through movable locating component, and then adjust the wind speed of adherence wind, the mixing rate of the combustion-supporting wind of control and adherence wind, thereby control the combustion process of gas-liquid solid fuel in organic waste liquid high-efficient processing apparatus, form an inside hypoxemia, high temperature, outside hyperoxia, microthermal environment in surely firing chamber 6 from this, this kind of temperature distribution and atmosphere distribution, not only can reach the effect of high combustion efficiency and low nitrogen, widen the load adjustment range and the coal type adaptability of combustion processor, and can effectually solve phenomena such as stable combustion chamber wall high temperature corrosion, deposition and coking, reduce the maintenance frequency of combustion processor, prolong the life of combustion processor; 4. the utility model discloses still adopted transition passageway 12's design, this transition passageway 12 not only can embed ignition oil gun and igniter, transition passageway 12 can also produce the recirculation zone of a high turbulence intensity with the combustion-supporting wind passageway 14 combined action of built-in movable axial impeller moreover, and the mixing rate of reinforcing gas-liquid solid fuel and air improves the burn-off rate of fuel under the underload operating mode.
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", and the like, indicate the orientation or positional relationship indicated based on the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.
Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In the description of the present invention, "a plurality" means at least two, e.g., two, three, etc., unless specifically limited otherwise.
In the present invention, unless otherwise expressly stated or limited, the terms "mounted," "connected," and "fixed" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally formed; may be mechanically coupled, may be electrically coupled or may be in communication with each other; they may be directly connected or indirectly connected through intervening media, or they may be connected internally or in any other suitable relationship, unless expressly stated otherwise. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.
In the present application, unless expressly stated or limited otherwise, the first feature may be directly on or directly under the second feature or indirectly via intermediate members. Also, a first feature "on," "over," and "above" a second feature may be directly or diagonally above the second feature, or may simply indicate that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature may be directly under or obliquely under the first feature, or may simply mean that the first feature is at a lesser elevation than the second feature.
In the present disclosure, the terms "one embodiment," "some embodiments," "an example," "a specific example," or "some examples" or the like mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present disclosure. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.
Although embodiments of the present invention have been shown and described, it is understood that the above embodiments are exemplary and should not be construed as limiting the present invention, and that variations, modifications, substitutions and alterations can be made to the above embodiments by those of ordinary skill in the art without departing from the scope of the present invention.
Claims (7)
1. An organic waste liquid high-efficiency treatment device is characterized by comprising:
the shell is provided with a first cavity and a peripheral wall enclosing the first cavity, and the first cavity comprises an air guide cavity, a combustion stabilizing cavity and a rectifying cavity which are sequentially communicated;
an organic waste liquid conveying assembly arranged in the center of the first cavity;
the first air duct is sleeved at the liquid inlet end of the organic waste liquid conveying component, one end, close to the liquid inlet end of the organic waste liquid conveying component, is open, one end, far away from the liquid inlet end of the organic waste liquid conveying component, is closed, and a transition channel is formed between the inner circumferential surface of the first air duct and the outer circumferential surface of the organic waste liquid conveying component;
the second air duct is arranged in the air guide cavity, and an adherence air channel is formed between the outer peripheral surface of the second air duct and the inner peripheral surface of the peripheral wall;
the third air duct is arranged in the air guide cavity, and a combustion-supporting air channel is formed between the outer peripheral surface of the third air duct and the inner peripheral surface of the second air duct;
and one of the outer peripheral surface of the fourth air duct and the inner peripheral surface of the third air duct and the inner peripheral surface of the fourth air duct and the outer peripheral surface of the first air duct is a pulverized coal conveying channel, and the other is a temperature regulating channel.
2. The apparatus according to claim 1, wherein the organic waste liquid delivery assembly comprises an organic waste liquid delivery pipe, a backflow cap and an atomizing nozzle assembly, the organic waste liquid delivery pipe is disposed coaxially with the first cavity, the backflow cap is disposed at a liquid outlet end of the organic waste liquid delivery pipe, the backflow cap is cylindrical, an outlet of the backflow cap faces a liquid inlet end of the organic waste liquid delivery pipe, and the atomizing nozzle assembly is disposed at an outlet of the backflow cap.
3. The device for high-efficiency treatment of organic waste liquid as claimed in claim 2, wherein the atomizing nozzle assembly comprises a fixed disk, the fixed disk is sleeved outside the liquid outlet end of the organic waste liquid conveying pipe, the outer circumferential surface of the fixed disk is connected with the inner edge of the outlet end of the reflux cap, and the fixed disk is provided with a plurality of injection holes penetrating through the fixed disk.
4. The device for efficiently treating the organic waste liquid according to claim 1, wherein axial impeller assemblies are arranged in the combustion-supporting air channel and the temperature adjusting channel.
5. The device for efficiently treating organic waste liquid according to claim 1, wherein the second air duct comprises a barrel, a flexible portion sleeved on the outer peripheral surface of the barrel, and an adjusting assembly, the adjusting assembly comprises an adjusting piece and a sealing washer, a plurality of mounting holes are formed in the barrel at intervals along the circumferential direction of the barrel, each mounting hole is provided with one adjusting piece, a first portion of the adjusting assembly penetrates through the flexible portion and is arranged in the mounting hole, a second portion of the adjusting piece is pressed on the outer peripheral surface of the flexible portion, and the sealing washer is arranged between the second portion of the adjusting piece and the outer peripheral surface of the flexible portion.
6. The apparatus for treating organic waste liquid with high efficiency as claimed in claim 1, wherein an igniter and a flame detector are arranged inside the temperature adjusting channel.
7. The device for efficiently treating the organic waste liquid according to claim 1, wherein a plurality of concentration separation structural members are arranged on the inner side of the pulverized coal conveying channel along the circumferential direction of the pulverized coal conveying channel.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120131552.1U CN214307135U (en) | 2021-01-18 | 2021-01-18 | High-efficient processing apparatus of organic waste liquid |
| PCT/CN2022/072508 WO2022152311A1 (en) | 2021-01-18 | 2022-01-18 | Waste gas/waste liquid/solid waste combustion treatment device and use method therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120131552.1U CN214307135U (en) | 2021-01-18 | 2021-01-18 | High-efficient processing apparatus of organic waste liquid |
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| CN214307135U true CN214307135U (en) | 2021-09-28 |
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| CN202120131552.1U Active CN214307135U (en) | 2021-01-18 | 2021-01-18 | High-efficient processing apparatus of organic waste liquid |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022152311A1 (en) * | 2021-01-18 | 2022-07-21 | 煤科院节能技术有限公司 | Waste gas/waste liquid/solid waste combustion treatment device and use method therefor |
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2021
- 2021-01-18 CN CN202120131552.1U patent/CN214307135U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022152311A1 (en) * | 2021-01-18 | 2022-07-21 | 煤科院节能技术有限公司 | Waste gas/waste liquid/solid waste combustion treatment device and use method therefor |
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Address after: 102600 No.5, Yulong Street, Caiyu Economic Development Zone, Caiyu Town, Daxing District, Beijing Patentee after: Beijing Tiandi Sunac Technology Co.,Ltd. Patentee after: TIANJIN THERMAL POWER CO.,LTD. Address before: 102600 No.5, Yulong Street, Caiyu Economic Development Zone, Caiyu Town, Daxing District, Beijing Patentee before: CHINA COAL RESEARCH INSTITUTE (CCRI) ENERGY SAVING TECHNOLOGY CO.,LTD. Patentee before: TIANJIN THERMAL POWER CO.,LTD. |
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