CN204569823U - A kind of pulverized coal pyrolysis rotary kiln - Google Patents

Abstract

The utility model relates to a pulverized coal pyrolysis rotary furnace. The pulverized coal pyrolysis rotary furnace involved comprises a rotary furnace body, and the rotary furnace body is provided with a preheating section, a pyrolysis section and a cooling section; the preheating section and the pyrolysis section are equipped with a plurality of heat exchange tubes, and the The cooling section is equipped with multiple semi-coke cooling heat exchange tubes. At least two hot flue gas inlets are arranged at intervals on the heat exchange tube of the pyrolysis section to facilitate adjustment of the temperature distribution in the furnace length direction. The use of heat exchange tubes greatly increases the heat exchange area. The heat exchange tube rotary furnace of the utility model has a large heat exchange area, a large amount of pulverized coal to be processed, and a simple structure, which is suitable for large-scale pyrolysis production of more than one million tons of pulverized coal.

Description

A pulverized coal pyrolysis rotary furnace

technical field

The utility model relates to a large-scale pulverized coal pyrolysis rotary furnace device, in particular to a pulverized coal pyrolysis rotary furnace.

Background technique

The existing external heating pulverized coal pyrolysis rotary furnace has the problems of complex structure, high cost, small heat transfer area, low thermal efficiency and low output.

Contents of the invention

Aiming at the defects or deficiencies of the prior art, the utility model provides a new type of external heating pulverized coal pyrolysis rotary kiln.

The pulverized coal pyrolysis rotary furnace of the utility model comprises a rotary furnace body, and the rotary furnace body is provided with a preheating section, a pyrolysis section and a cooling section; the preheating section and the pyrolysis section are fixedly installed with a plurality of Heat exchange tubes, the cooling section is fixedly installed with a plurality of heat exchange tubes for semi-coke cooling.

Furthermore, the length direction of the heat exchange tubes for heating pulverized coal and the heat exchange tubes for semi-coke cooling of the utility model is arranged along the axial direction of the rotary furnace body.

Further, in the utility model, multiple heat exchange tubes for heating pulverized coal and multiple heat exchange tubes for cooling semi-coke each form an annular tube layer in the radial section of the rotary furnace body, and around the center of the rotary furnace, 1-4 layers of heat exchange tubes are arranged. Heat pipe.

Furthermore, at least two hot flue gas inlets are arranged axially on the heat exchange tubes in the pyrolysis section in the rotary furnace body of the utility model, through which hot flue gas is provided for the heat exchange tubes in the pyrolysis section.

Further, a combustion chamber is installed at the entrance of the hot flue gas of the utility model, and the combustion chamber can use coal gas, or pulverized coal, and coke powder as the combustion chamber fuel; Preheat the air.

Furthermore, a material guide screw is installed in the rotary furnace body of the utility model, and the heat exchange tube is fixedly installed on the material guide screw and rotates together with the rotary furnace.

Further, an anti-lifting device is installed on the outer wall of the heat exchange tube for pulverized coal heating and the heat exchange tube for semi-coke cooling in the present invention, and the length direction of the anti-dust device extends along the axial direction of the radiation pyrolysis tube. The anti-dust device is provided with a mounting surface and a vertex, the mounting surface is installed on the outer wall of the radiation pyrolysis tube, the vertex is opposite to the mounting surface, and the vertex on the dust preventing device points to the The rotation direction of the pulverized coal pyrolysis radiant tube rotary furnace is the same or parallel.

Furthermore, the anti-lifting device of the present invention is formed by welding two rectangular plates on the outer wall of the radiant tube, the cross section of which is triangular, and the vertex of the triangle points to the same or parallel to the rotation direction of the pulverized coal pyrolysis rotary furnace.

Further, the gas outlet on the rotary furnace body of the utility model is set at the semi-coke outlet end, and the hot gas generated by the pyrolysis of pulverized coal is discharged from the furnace above the semi-coke discharge hood.

Further, the hot flue gas outlet of the heat exchange tube for heating pulverized coal in the utility model is set at the raw coal feed end of the rotary furnace, and the hot flue gas in the heat exchange tube in the furnace fully exchanges heat with the pulverized coal and is discharged from the feed end of the rotary furnace .

The beneficial effects of the utility model are:

(1) The rotary furnace of the utility model greatly improves the heat transfer area of the rotary furnace, and the external heating type rotary furnace with the same diameter increases the heat transfer area by 2-8 times, and greatly increases the production capacity;

(2) The heat supply of the rotary furnace of the utility model can be provided by gaseous fuel, solid fuel or liquid fuel, especially the use of solid fuel can greatly reduce the fuel cost of pyrolysis.

(3) The multi-combustion chamber of the rotary furnace of the utility model realizes the problem of adjusting the temperature distribution of the rotary furnace along the furnace length direction, and can conveniently control the thermal system.

(4) The rotary kiln of the utility model adopts the method of air indirect cooling to recover the waste heat of semi-coke, saves energy, and has no coke-quenching sewage.

(5) The rotary furnace of the utility model combines the material guide screw with the heat exchange tube support, and the furnace body is placed horizontally to avoid the inclined design of the kiln body, which is convenient for the operation of the kiln body and simplifies the structure.

(6) The anti-lifting device welded on the heat exchange tube in the rotary furnace of the utility model is beneficial to high-temperature dust removal for reducing the gas dust removal load.

In summary, the pulverized coal pyrolysis rotary furnace of the utility model has a large heat transfer area, a large amount of pulverized coal to be processed, and a simple structure, and is suitable for large-scale pyrolysis production of pulverized coal of more than one million tons.

Description of drawings

Fig. 1 is the structural reference schematic diagram of pulverized coal pyrolysis rotary furnace of the present utility model;

Fig. 2 is a reference schematic diagram of the structure of the lifting prevention device of the present invention.

Detailed ways

The existing external heating pulverized coal pyrolysis rotary furnace has the problems of small heat transfer area and low thermal efficiency. In order to increase the heat transfer area, improve heat transfer efficiency, and increase the pyrolysis output per unit volume of the pyrolysis furnace, it is proposed to use radiant tube technology for The external heating rotary pyrolysis furnace can improve the heating efficiency of the rotary furnace and greatly increase the production capacity. However, the existing radiant tubes are all fixed heating elements. How to apply the radiant tubes to the rotary furnace and rotate together with the rotary furnace is the primary problem. Secondly, the length of the rotary furnace is relatively long, requiring longer radiant tubes The traditional radiant tube is short, how to solve the length direction of the smoke radiant tube to ensure a long effective wall temperature distribution is the second problem faced. Thirdly, the straight type of radiant tube generally uses gas as fuel, and each radiant tube corresponds to a burner. Large-scale rotary furnaces have too many burners, and the failure rate is high, which is inconvenient to manage and control. Fourth, the pulverized coal moves in the gap of the radiant tubes in the rotary drum, and is easily carried by the radiant tubes to form lifting materials, resulting in a series of problems such as excessive dust in the rotary furnace and excessive load of gas filtration and dust removal.

In the rotary furnace of the utility model, the single combustion of gas radiant tubes is changed to burning in combustion chambers to produce high-temperature flue gas, which is then fed into each radiant tube, and the radiant tubes are turned into simple heat exchange tubes. By increasing the number of combustion chambers, the To meet the problem that the temperature distribution of the heat exchange tube is not easy to control along the length direction, obtain uniform heat distribution and heat the tube wall of the heat exchange tube, and the tube wall of the heat exchange tube transfers heat to the heated material through radiation heat transfer, of course, including material contact The outer wall of the radiant tube transfers the heat inside the tube to the heated material through conduction heat transfer.

Example:

With reference to Fig. 1-Fig. 2, the structure of the rotary kiln device provided by this embodiment includes: a pulverized coal feeding device 11, a rotary kiln body 7, supporting wheels (5, 13) and a transmission device 14;

The rotary furnace body 7 is provided with a hot gas outlet 2, a flue gas outlet 10 and a semi-coke outlet 19; a material guide screw 15 is installed in the rotary furnace body 7;

The pulverized coal feeding device 11 is sealed and connected with the rotary furnace body 7 through the feeding sealing device 12; the flue gas outlet 10 is sealed and connected with the rotary furnace body through the flue gas sealing device 9; a discharge cover 1 is installed at the semi-coke outlet 19;

The rotary furnace body 7 is provided with a preheating section, a pyrolysis section and a cooling section sequentially along the feeding direction of pulverized coal, wherein;

The preheating section and the pyrolysis section are equipped with heat exchange tubes 16, and three groups of hot flue gas inlets 4 are arranged on the heat exchange tubes 16 along the axial interval, and combustion chambers (3, 6, 8 ), each combustion chamber is sealed and connected with the rotary furnace body by combustion sealing device 17;

The heat exchange tubes 16 are arranged parallel to the axial direction of the rotary furnace, forming an annular radiant tube layer in the radial section of the rotary furnace. Depending on the size of the cross-sectional area of the rotary furnace, 1-4 layers of heat exchange tubes are arranged around the center of the rotary furnace to greatly improve heat transfer. Area, pulverized coal is heated, dried, pyrolyzed, cooled and then transported out of the rotary furnace with the flow of the rotary body in the gap between the heat exchange tubes. Depending on the diameter of the kiln body and the requirements of the heat transfer surface, heat exchange tubes with a diameter of 80-200mm are arranged.

The cooling section is equipped with heat exchange tubes for semi-coke cooling. The heat exchange tubes for semi-coke cooling are provided with an air inlet 18, and the semi-coke is cooled by normal temperature air; the installation method of the cooling heat exchange tubes in the rotary furnace body is the same as The installation method of the heating heat exchange tube in the furnace body is the same.

And each radiant pyrolysis tube is welded with an anti-lifting device 20 to avoid lifting during rotation and suppress dust generation. The cross-section of the anti-lifting device is a triangular structure, and the direction of the apex of the triangle is consistent with the rotation direction of the radiant tube installed in the rotary drum. The triangular structure is formed by two rectangular plates welded on the outer wall of the radiant tube, which ensures that when the radiant tube installed in the rotary cylinder rotates with the cylinder body, it is not easy to carry the materials in the cylinder, avoiding material lifting and avoiding damage caused by material lifting. Lots of dust.

The heat exchange tube adjusts the temperature distribution along the axial direction of the rotary furnace through the adjustment of the fuel supply to each combustion chamber. The heat exchange tube is fixed on the blade of the material guide screw on the inner wall of the rotary furnace, so that the material guide screw not only plays the role of material guide, but also plays the role of supporting the radiant tube.

The working process of the pulverized coal pyrolysis rotary furnace:

The rotary furnace body rotates counterclockwise, and the pulverized coal runs from the preheating section to the pyrolysis section and the cooling section, and the drying and preheating process is realized by exchanging heat with the radiant tube in the preheating section; the flue gas in the radiant tube is cooled and discharged outside the furnace; The heated pulverized coal continues to run and enters the pyrolysis section. The high-temperature flue gas in the radiant tube is used to pyrolyze the preheated pulverized coal. After the pulverized coal is pyrolyzed, it becomes semi-coke and enters the cooling section. Radiant tube heat exchange, combustion-supporting air and gas are preheated for combustion in the combustion chamber, semi-coke is cooled and discharged out of the furnace. The hot gas is exported from the cooling section and enters the downstream gas dust removal and purification section.

Specific instructions: Pulverized coal at room temperature is sent into the sealed rotary furnace body through a screw conveyor, enters the gap between the heat exchange tubes in the rotary furnace, and exchanges heat with the heat exchange tubes. When the raw coal is dried and preheated to about 300°C, it enters the heat Decomposition section, heat exchange with heat exchange tubes, heated to above 450-500°C, pulverized coal is pyrolyzed to generate gas, which itself becomes semi-coke powder, stays in the pyrolysis section for more than 30 minutes, and is sent to the cooling section and air The heat exchange tube is cooled to below 300°C and discharged out of the furnace. The gas generated by pyrolysis is discharged from the semi-coke discharge hood at the cooling end. The gas discharge temperature is about 300°C and enters the dust removal, purification and cooling section.

After the semi-coke powder is finely ground and less than 75 microns, it is sprayed into the combustion chamber and the combustion-supporting air after heat exchange in the cooling section is mixed and burned in the combustion chamber. The heat exchange tube in the furnace has a wall temperature of 500-700°C in the pyrolysis section, which is used to pyrolyze pulverized coal. After exchanging heat with pulverized coal, the temperature of the hot air will drop to about 200°C and be discharged out of the furnace to realize separation and separation. indirect heat exchange.

Claims (10)

1. A pulverized coal pyrolysis rotary furnace is characterized in that, comprising a rotary furnace body, the rotary furnace body is provided with a preheating section, a pyrolysis section and a cooling section; The preheating section and the pyrolysis section are fixedly installed with multiple heat exchange tubes for heating pulverized coal, and the cooling section is fixedly installed with multiple heat exchange tubes for semi-coke cooling. 2. The pulverized coal pyrolysis rotary furnace according to claim 1, characterized in that the length direction of the heat exchange tubes for heating pulverized coal and the heat exchange tubes for semi-coke cooling is arranged along the axial direction of the rotary furnace body. 3. The pulverized coal pyrolysis rotary furnace as claimed in claim 2 is characterized in that, the plurality of pulverized coal heating heat exchange tubes and the plurality of semi-coke cooling heat exchange tubes are respectively formed in the radial section of the rotary furnace body Ring tube layer, and around the center of the rotary furnace, 1-4 layers of heat exchange tubes are arranged. 4. The pulverized coal pyrolysis rotary furnace as claimed in claim 1, wherein at least two hot flue gas inlets are provided at least two hot flue gas inlets at intervals along the axial direction on the pulverized coal heating heat exchange tube, through which the hot flue gas inlet is used for pyrolysis. The heat exchange tubes in the section provide hot flue gas. 5. The pulverized coal pyrolysis rotary furnace according to claim 4, characterized in that a combustion chamber is installed at the inlet of the hot flue gas. 6. The pulverized coal pyrolysis rotary furnace according to claim 1, characterized in that, a material guide screw is installed in the rotary furnace body, and the heat exchange tube is fixedly installed on the material guide screw. 7. The pulverized coal pyrolysis rotary furnace as claimed in claim 1, characterized in that, an anti-lifting device is installed on the outer wall of the heat exchange tube for heating the pulverized coal and the heat exchange tube for cooling the semi-coke, the anti-lifting device The length direction of the dust-raising device extends along the axial direction of the radiation pyrolysis tube. The dust-proof device is provided with a mounting surface and a top angle, and the installation surface is installed on the outer wall of the radiation pyrolysis tube. The mounting surface is opposite to the above-mentioned installation surface, and the top angle on the dust prevention device is directed to be the same as or parallel to the rotation direction of the pulverized coal pyrolysis radiant tube rotary kiln. 8. The pulverized coal pyrolysis rotary furnace as claimed in claim 7, wherein the anti-lifting device is formed by welding two rectangular plates on the outer wall of the radiant tube, the cross section of which is triangular, and the apex of the triangle is pointing to be the same as or parallel to the rotation direction of the pulverized coal pyrolysis rotary kiln. 9. The pulverized coal pyrolysis rotary furnace according to claim 1, characterized in that the gas outlet on the rotary furnace body is set at the semi-coke outlet end. 10. The pulverized coal pyrolysis rotary kiln according to claim 1, characterized in that the hot flue gas outlet of the pulverized coal heating heat exchange tube is arranged at the raw coal feed end of the rotary kiln.