CN218860535U

CN218860535U - Sectional type electric induction pyrolysis carbonization device for sludge

Info

Publication number: CN218860535U
Application number: CN202320221945.0U
Authority: CN
Inventors: 朱君亮
Original assignee: Shanghai Lianghui Technology Co ltd
Current assignee: Shanghai Lianghui Technology Co ltd
Priority date: 2023-02-15
Filing date: 2023-02-15
Publication date: 2023-04-14
Anticipated expiration: 2033-02-15

Abstract

The utility model discloses a mud sectional type electric induction pyrolysis carbonization device, including the conveyer, install at the left driving motor of conveyer, set up the conveying pole of being connected inside the conveyer and with the driving motor transmission, the surface intercommunication of conveyer has the mud ascending pipe, the surface of conveyer is provided with the carbonization and preheats the structure, the fixed surface of conveyer is connected with the electromagnetic heating system who is located carbonization and preheats structure right side, the surface of conveyer has set gradually main carbonization structure and the cooling structure that is located electromagnetic heating system right side, the top intercommunication of conveyer has the combustible gas discharge pipe that is located the cooling structure right side, the bottom intercommunication of conveyer has the carbonization mud delivery pipe that is located combustible gas discharge pipe bottom. The utility model discloses can increase the mode of current heating burning, the user of being convenient for carries out the accuracy to heating temperature and masters, and mud can obtain abundant decomposition at the in-process that slowly heaies up simultaneously.

Description

Sectional type electric induction pyrolysis carbonization device for sludge

Technical Field

The utility model relates to a sludge treatment technical field specifically is a mud sectional type electric induction pyrolysis carbonization device.

Background

The sludge pyrolysis is to utilize the thermal instability of organic matters in the sludge, heat the organic matters under the anaerobic condition to thermally crack the organic matters, and crack the organic matters according to the carbon-hydrogen ratio to form gas phase and solid phase with higher utilization value.

Mainly decompose through the mode of heating burning among the sludge treatment process, but the mode of current heating burning is comparatively single, and the user of being inconvenient for carries out the accuracy to heating temperature and masters, and mud can't obtain abundant decomposition at rapid heating up's in-process simultaneously.

Therefore, the design and modification of the sludge sectional type electric induction pyrolysis carbonization device are needed.

SUMMERY OF THE UTILITY MODEL

For solving the problem that proposes in the above-mentioned background art, the utility model aims to provide a mud sectional type electric induction pyrolysis carbonization device possesses the advantage that improves sludge treatment and decomposes the effect, has solved the mode of current heating burning comparatively single, and the not convenient to use user carries out the accuracy and masters to heating temperature, and mud can't obtain the problem of abundant decomposition at rapid heating up's in-process simultaneously.

In order to achieve the above purpose, the utility model provides a following technical scheme: a sectional type electric induction pyrolysis carbonization device for sludge comprises a conveyor;

a driving motor installed at the left side of the conveyor;

the conveying rod is arranged in the conveyor and is in transmission connection with the driving motor;

the utility model discloses a cooling device for a motor vehicle, including conveyer, surface intercommunication of conveyer have the mud filling tube, the surface of conveyer is provided with the carbonization and preheats the structure, the fixed surface of conveyer is connected with the electromagnetic heating system that is located the carbonization and preheats structure right side, the surface of conveyer has set gradually main carbonization structure and the cooling structure that is located the electromagnetic heating system right side, the top intercommunication of conveyer has the combustible gas discharge pipe that is located the cooling structure right side, the bottom intercommunication of conveyer has the carbonization mud delivery pipe that is located combustible gas discharge pipe bottom, the surface of mud filling tube and carbonization mud delivery pipe all communicates there is the transport paddle.

As the utility model discloses preferred, the carbonization preheats the structure and includes that fixed connection presss from both sides the cover in preheating on the conveyer surface, it is located electromagnetic heating system's left side to preheat to press from both sides the cover.

As the utility model discloses preferred, main carbonization structure includes that fixed connection presss from both sides the cover at the main heating on conveyer surface, the quantity that main heating pressed from both sides the cover is two, main heating presss from both sides the cover and is located electromagnetic heating system's right side.

As the utility model discloses preferred, cooling structure includes the cooling jacket of fixed connection on the conveyer surface, the cooling jacket is located the right side that the main heating pressed from both sides the cover.

As the utility model discloses preferred, the output and the input that preheat the clamp cover and main heating clamp cover all communicate there is high temperature fluid pipeline, the output and the input that the cooling presss from both sides the cover all communicate there is cooling water piping.

As the utility model discloses preferred, preheat the surface that presss from both sides cover, electromagnetic heating system, main heating jacket and cooling jacket and all communicate temperature monitoring module.

Compared with the prior art, the beneficial effects of the utility model are as follows:

1. the utility model discloses can increase the mode of current heating burning, the user of being convenient for carries out the accuracy to heating temperature and masters, and mud can obtain abundant decomposition at the in-process that slowly heaies up simultaneously.

2. The utility model discloses a set up and preheat the clamp cover, can preheat mud to do benefit to mud carbonization at the back.

Drawings

FIG. 1 is a schematic structural view of the present invention;

fig. 2 is a schematic view of the local structure section of the present invention.

In the figure: 1. a conveyor; 2. a drive motor; 3. a conveying rod; 4. a sludge injection pipe; 5. an electromagnetic heating system; 6. a combustible gas discharge pipe; 7. carbonizing the sludge discharge pipe; 8. conveying the blades; 9. preheating a jacket; 10. a primary heating jacket; 11. a cooling jacket; 12. a high temperature fluid conduit; 13. a cooling water pipeline; 14. and a temperature monitoring module.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

As shown in fig. 1 and fig. 2, the present invention provides a sectional type electric induction pyrolysis carbonization apparatus for sludge, which comprises a conveyor 1;

a driving motor 2 installed at the left side of the conveyor 1;

the conveying rod 3 is arranged in the conveyor 1 and is in transmission connection with the driving motor 2;

conveyer 1's surface intercommunication has mud filling tube 4, conveyer 1's surface is provided with the carbonization and preheats the structure, conveyer 1's fixed surface is connected with the electromagnetic heating system 5 that is located the carbonization and preheats the structure right side, conveyer 1's surface has set gradually main carbonization structure and the cooling structure that is located electromagnetic heating system 5 right side, conveyer 1's top intercommunication has combustible gas discharge pipe 6 that is located the cooling structure right side, conveyer 1's bottom intercommunication has the carbonization mud delivery pipe 7 that is located combustible gas discharge pipe 6 bottom, the surface of mud filling tube 4 and carbonization mud delivery pipe 7 all communicates has transport paddle 8.

Referring to fig. 1, the carbonizing preheating structure includes a preheating jacket 9 fixedly attached to the surface of the conveyor 1, and the preheating jacket 9 is located at the left side of the electromagnetic heating system 5.

As a technical optimization scheme of the utility model, preheat through the setting and press from both sides cover 9, can preheat mud to do benefit to the mud carbonization at the back.

Referring to fig. 1, the main carbonization structure includes two main heating jackets 10 fixedly attached to the surface of the conveyor 1, and the main heating jackets 10 are located at the right side of the electromagnetic heating system 5.

As a technical optimization scheme of the utility model, press from both sides cover 10 through setting up the main heating, guarantee that mud has abundant time to carry out the pyrolysis, the heat that the combustible gas of production produced after the burning provides the heat to outside fluid heat source, and the organic matter falls to below 1.0% after the mud carbonization.

Referring to fig. 1, the cooling structure includes a cooling jacket 11 fixedly attached to the surface of the conveyor 1, the cooling jacket 11 being located on the right side of the main heating jacket 10.

As a technical optimization scheme of the utility model, through setting up cooling jacket 11, can cool off mud fast, the mud recovery after being convenient for handle.

Referring to fig. 1, the output end and the input end of the preheating jacket 9 and the main heating jacket 10 are both communicated with a high-temperature fluid pipeline 12, and the output end and the input end of the cooling jacket 11 are both communicated with a cooling water pipeline 13.

As a technical optimization scheme of the utility model, through setting up high temperature fluid pipeline 12 and cooling water piping 13, can improve fluid injection efficiency, prevent that the energy is extravagant.

Referring to fig. 1, the surfaces of the preheating jacket 9, the electromagnetic heating system 5, the main heating jacket 10 and the cooling jacket 11 are communicated with a temperature monitoring module 14.

As the utility model discloses a technical optimization scheme, through setting up temperature monitoring module 14, the user of can being convenient for carries out the accuracy to the temperature and masters, and the user of being convenient for carries out nimble regulation to the temperature.

The utility model discloses a theory of operation and use flow: when the device is used, the solid sludge drives the conveying rod 3 to rotate under the rotation of the external driving motor 2, and the sludge is uniformly conveyed forwards from the carbonization preheating structure → the electromagnetic heating system 5 → the main carbonization structure → the cooling structure, and the like, in the conveying process, the carbonization preheating structure can utilize a fluid heat source which is sent from the outside and is about 350 ℃ to heat the conveyor 1, the temperature of the sludge reaches 300 ℃ under the heating of the conveyor 1 so as to be beneficial to the subsequent sludge carbonization, the electromagnetic heating system 5 utilizes the electromagnetic heating principle to heat the conveyor 1 to about 650 ℃, the sludge in the conveyor 1 is heated to more than 600 ℃, the sludge is carbonized and is cracked into gaseous and solid products, the gaseous products are pyrolysis gas and are combustible gas, the pyrolysis gas generated from the pyrolysis device contains certain harmful substances and can be combusted, so that the energy can be utilized, at the same time, harmful substances are converted into completely oxidized flue gas, the pyrolysis is carried out along with the forward feeding of the sludge, the heating mode at this stage is mainly that an external fluid heat source heats the conveyor 1 to about 600 ℃, the sludge is guaranteed to have sufficient time for pyrolysis, the heat generated by the combustion of the generated combustible gas provides heat for the external fluid heat source, the organic matters after the carbonization of the sludge are reduced to below 1.0 percent, the sludge after the carbonization of the sludge is cooled by a main cooling jacket 11, the cooling is that the carbonized sludge is cooled to 300 ℃ by a cooling circulating tower, the carbonized material is cooled to below 150 ℃ in the section under the spiral conveying, the cooling is that the carbonized sludge is cooled by the cooling circulating tower, the material conveyed to the tail part enters a carbonized sludge discharge pipe 7, and the material is conveyed out of a slag discharge port under the rotation of a conveying blade 8 in the carbonized sludge discharge pipe 7, the recoverable gas rises through the combustible gas discharge pipe 6 and is discharged.

In summary, the following steps: this mud sectional type electric induction pyrolysis carbonization device can increase the mode of current heating burning, and the user of being convenient for carries out the accuracy to heating temperature and masters, and mud can obtain abundant decomposition at the in-process that slowly heaies up simultaneously.

It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.

Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims

1. A sectional type electric induction pyrolysis carbonization device for sludge, which comprises a conveyor (1);

a driving motor (2) arranged on the left side of the conveyor (1);

the conveying rod (3) is arranged in the conveyor (1) and is in transmission connection with the driving motor (2);

the method is characterized in that: the surface intercommunication of conveyer (1) has mud ascending pipe (4), the surface of conveyer (1) is provided with the carbonization and preheats the structure, the fixed surface of conveyer (1) is connected with electromagnetic heating system (5) that are located the carbonization and preheat the structure right side, the surface of conveyer (1) has set gradually main carbonization structure and the cooling structure that is located electromagnetic heating system (5) right side, the top intercommunication of conveyer (1) has combustible gas discharge pipe (6) that are located the cooling structure right side, the bottom intercommunication of conveyer (1) has carbonization mud delivery pipe (7) that are located combustible gas discharge pipe (6) bottom, the surface of mud ascending pipe (4) and carbonization mud delivery pipe (7) all communicates has transport thick liquid leaf (8).

2. The sludge segmented electric induction pyrolysis carbonization device according to claim 1, characterized in that: the carbonization preheating structure comprises a preheating jacket (9) fixedly connected to the surface of the conveyor (1), and the preheating jacket (9) is positioned on the left side of the electromagnetic heating system (5).

3. The sectional electric induction pyrolysis carbonization device for sludge according to claim 2, wherein: the main carbonization structure comprises two main heating jackets (10) fixedly connected to the surface of the conveyor (1), and the main heating jackets (10) are positioned on the right side of the electromagnetic heating system (5).

4. The segmented electric induction pyrolysis carbonization device for sludge according to claim 3, wherein: the cooling structure comprises a cooling jacket (11) fixedly connected to the surface of the conveyor (1), and the cooling jacket (11) is positioned on the right side of the main heating jacket (10).

5. The sludge segmented electric induction pyrolysis carbonization device according to claim 4, characterized in that: the output end and the input end of the preheating jacket (9) and the main heating jacket (10) are both communicated with a high-temperature fluid pipeline (12), and the output end and the input end of the cooling jacket (11) are both communicated with a cooling water pipeline (13).

6. The sludge segmented electric induction pyrolysis carbonization device according to claim 5, characterized in that: the surfaces of the preheating jacket (9), the electromagnetic heating system (5), the main heating jacket (10) and the cooling jacket (11) are communicated with a temperature monitoring module (14).