Regeneration of high-temperature oil cracking steam condensing equipment

Abstract

The utility model relates to the technical field of steam condensation, and disclose a kind of regeneration pyrolysis high-temperature oil steam condensing equipment, including reaction component, separation component, temperature control component, filter component and tank body component, separation component is arranged in the inside of reaction component, temperature control component is installed in the outside of reaction component, filter component is arranged in the outside of one side of reaction component, tank body component is arranged in one side of filter component;By being provided with reaction component and separation component, it is favorable to remove solid particles and liquid pollutants in high-temperature oil vapor, avoid its into subsequent processing procedure, to reduce the occurrence of pipeline blockage problem, and ensure oil quality;By being provided with reaction component and filter component, it is favorable to maintenance personnel can be easily removed and installed filter plate without using tool, greatly reduce the time required for replacement, to reduce the downtime caused by maintenance, improve production efficiency.

Description

Technical Field

[0001] This utility model relates to the field of steam condensation technology, and more specifically to a regenerated pyrolysis high-temperature oil steam condensation device. Background Technology

[0002] With the increasing popularity of automobiles, the number of waste tires is increasing year by year. The pyrolysis treatment of waste tires can not only solve the environmental pollution problem caused by their long-term accumulation, but also transform them into useful chemical raw materials, realizing resource recycling and reuse.

[0003] Existing cracked oil vapor condensation equipment has shortcomings in oil-gas separation, which affects the quality of oil products. It may not be able to effectively remove impurities and moisture from oil vapor, thus affecting the purity and stability of the oil products. Since oil vapor contains impurities such as carbon black dust, these impurities are prone to accumulate inside pipelines and equipment, causing pipeline blockage and affecting the normal operation of the equipment. Utility Model Content

[0004] In order to overcome the above-mentioned defects of the prior art, the present invention provides a regenerated pyrolysis high-temperature oil vapor condensation device to solve the problems existing in the background art.

[0005] This utility model provides the following technical solution: a regenerative pyrolysis high-temperature oil vapor condensation device, comprising a reaction component, a separation component, a temperature control component, a filter component, and a tank component. The separation component is disposed inside the reaction component, the temperature control component is disposed outside the reaction component, the filter component is disposed on one side of the reaction component, and the tank component is disposed on one side of the filter component. The filter component includes a valve, a lug, a filter plate, a collar, a buckle, and a sealing ring. The valve is fixedly installed outside the gas supply pipe, and lugs are symmetrically arranged on the outside of the valve. The filter plate is movably snapped into one side of the gas supply pipe, and a sealing ring is fixedly sleeved on the outside of the filter plate. The collar is fixedly sleeved on one side of the tank component, and buckles are symmetrically installed on both sides of the collar. Preferably, the reaction assembly includes a reaction vessel, a support, a sealing cap, a first oil outlet pipe, and a gas supply pipe. The support is evenly installed at the bottom of the reaction vessel and the tank assembly. The sealing cap is installed at the top of the reaction vessel. The first oil outlet pipe is fixedly connected to the bottom of the reaction vessel. The gas supply pipe is fixedly connected to one side of the reaction vessel.

[0006] Preferably, the separation assembly includes a motor, fan blades, and carbon plates. The motor is nested inside the sealing cover, and the output shaft of the motor is fixedly connected to the fan blades via a coupling. The carbon plates are evenly distributed at the bottom of the inner wall of the reactor.

[0007] Preferably, the temperature control assembly includes a digital controller, a heating element, a thermometer, and a condenser. The digital controller is fixedly installed on the outside of the reactor, the heating element is nested in the inner wall of the reactor, the thermometer is fixedly installed on the inner wall of the reactor, and the condenser is located on one side of the tank assembly.

[0008] Preferably, the tank assembly includes a condenser, an air inlet pipe, and a second oil outlet pipe. The condenser is located on one side of the reactor. One end of the air inlet pipe is movably engaged in the inner wall of one side of the gas delivery pipe, and the other end of the air inlet pipe is fixedly connected to one side of the condenser. The second oil outlet pipe is located at the bottom of the air inlet pipe.

[0009] The technical effects and advantages of this utility model are as follows: This invention, by incorporating a reaction component and a separation component, facilitates the removal of solid particles and liquid contaminants from high-temperature oil vapor, preventing them from entering subsequent processing steps, thereby reducing pipeline blockage and ensuring oil quality.

[0010] This invention, by incorporating a reaction component and a filter component, allows maintenance personnel to easily remove and install the filter plate without using tools, greatly reducing the time required for replacement, thereby minimizing downtime due to maintenance and improving production efficiency. Attached Figure Description

[0011] Figure 1 This is a schematic diagram of the overall structure of this utility model.

[0012] Figure 2 This is a schematic diagram of the overall structure and some cross-sectional views of the present invention.

[0013] Figure 3 This is a schematic diagram of the reaction assembly, filter assembly, and tank assembly of this utility model.

[0014] Figure 4 For the present utility model Figure 3 Schematic diagram of structure A in the middle.

[0015] The attached diagram is labeled as follows: 1. Reaction assembly; 101. Reactor; 102. Support; 103. Sealing cap; 104. First oil outlet pipe; 105. Gas supply pipe; 2. Separation assembly; 201. Motor; 202. Fan blade; 203. Carbon plate; 3. Temperature control assembly; 301. CNC controller; 302. Heating element; 303. Thermometer; 304. Condenser; 4. Filter assembly; 401. Valve; 402. Lug; 403. Filter plate; 404. Collar; 405. Snap-fit; 406. Sealing ring; 5. Tank assembly; 501. Condenser tank; 502. Gas inlet pipe; 503. Second oil outlet pipe. Detailed Implementation

[0016] The technical solution of this utility model will be clearly and completely described below with reference to the accompanying drawings. In addition, the forms of the various structures described in the following embodiments are merely illustrative. The regenerative pyrolysis high-temperature oil vapor condensation equipment involved in this utility model is not limited to the structures described in the following embodiments. All other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of this utility model.

[0017] Reference Figure 1-4 This utility model provides a regenerative pyrolysis high-temperature oil vapor condensation device, including a reaction component 1, a separation component 2, a temperature control component 3, a filter component 4, and a tank component 5. The separation component 2 is located inside the reaction component 1, the temperature control component 3 is installed outside the reaction component 1, the filter component 4 is located outside one side of the reaction component 1, and the tank component 5 is located on one side of the filter component 4. The reaction assembly 1 includes a reaction vessel 101, a support 102, a sealing cap 103, a first oil outlet pipe 104, and a gas supply pipe 105. The support 102 is evenly installed at the bottom of the reaction vessel 101 and the tank assembly 5. The sealing cap 103 is installed at the top of the reaction vessel 101. The first oil outlet pipe 104 is fixedly connected to the bottom of the reaction vessel 101. The gas supply pipe 105 is fixedly connected to one side of the reaction vessel 101.

[0018] The separation component 2 includes a motor 201, a fan blade 202, and a carbon plate 203. The motor 201 is nested inside the sealing cover 103, and the output shaft of the motor 201 is fixedly connected to the fan blade 202 via a coupling. The carbon plate 203 is evenly distributed at the bottom of the inner wall of the reactor 101, which facilitates the starting of the motor 201. The output shaft of the motor 201 drives the transmission shaft to rotate, and the transmission shaft drives the fan blade 202 to rotate, generating wind power. This blows up some of the fine impurities after the tires inside the reactor 101 are heated and decomposed, and they are absorbed by the carbon plate 203, thus improving the separation effect.

[0019] The temperature control assembly 3 includes a digital controller 301, a heating element 302, a thermometer 303, and a condenser 304. The digital controller 301 is fixedly installed on the outside of the reactor 101, the heating element 302 is nested in the inner wall of the reactor 101, the thermometer 303 is fixedly installed on the inner wall of the reactor 101, and the condenser 304 is located on one side of the tank assembly 5, which facilitates the heating element 302 to heat the tire inside the reactor 101. The temperature inside the reactor 101 is monitored by the thermometer 303 and displayed on the display screen of the digital controller 301.

[0020] The filter assembly 4 includes a valve 401, a lug 402, a filter plate 403, a collar 404, a snap fastener 405, and a sealing ring 406. The valve 401 is fixedly installed on the outside of the gas supply pipe 105, and the lugs 402 are symmetrically arranged on the outside of the valve 401. The filter plate 403 is movably snapped into the inside of one side of the gas supply pipe 105, and the sealing ring 406 is fixedly sleeved on the outside of the filter plate 403. The collar 404 is fixedly sleeved on the outside of one side of the tank assembly 5, and the snap fasteners 405 are symmetrically installed on both sides of the collar 404. This allows the collar 404, snap fasteners 405, and tank assembly 5 to be removed from one side of the gas supply pipe 105 by opening the snap fasteners 405 on both sides, and then the filter plate 403 and collar 404 can be removed and replaced. This prevents the gas supply pipe 105 from becoming blocked after the equipment has been working for a long time, which would affect the condensation effect.

[0021] The tank assembly 5 includes a condenser 501, an air inlet pipe 502, and a second oil outlet pipe 503. The condenser 501 is located on one side of the reactor 101. One end of the air inlet pipe 502 is movably clamped into the inner wall of one side of the gas supply pipe 105, and the other end of the air inlet pipe 502 is fixedly connected to one side of the condenser 501. The second oil outlet pipe 503 is located at the bottom of the air inlet pipe 502.

[0022] The working principle of this utility model: First, open the sealing cover 103, put the waste tire into the reactor 101, close the sealing cover 103, and start the heating tube 302 through the CNC 301 to heat and decompose the tire inside the reactor 101. Next, the motor 201 is started. The output shaft of the motor 201 drives the transmission shaft to rotate. The transmission shaft drives the fan blades 202 to rotate and generate wind. This wind blows up some of the fine impurities after the tires inside the reactor 101 are heated and decomposed. These impurities are absorbed by the carbon plate 203, improving the separation effect. Some oil stains are discharged from the first oil outlet pipe 104. The oil and gas generated by the pyrolysis are discharged into the gas supply pipe 105 under the action of wind. The fine carbon black dust is filtered by the filter plate 403 and then transported into the condenser 501 through the air inlet pipe 502. The condenser 304 is started to cool and condense the oil and gas generated by the pyrolysis into liquid oil, which is then output from the second oil outlet pipe 503. Finally, after the equipment has been working for a long time, open the buckles 405 on both sides, remove the collar 404, buckle 405 and tank assembly 5 from one side of the gas supply pipe 105, and remove and replace the filter plate 403 and collar 404 to avoid clogging of the filter plate 403 and affecting the condensation effect.

[0023] Finally, the following points should be noted: First, in the description of this application, it should be noted that, unless otherwise specified and limited, the terms "installation", "connection", and "linkage" should be interpreted broadly, and can be mechanical or electrical connections, or internal connections between two components, or direct connections. "Up", "down", "left", "right", etc. are only used to indicate relative positional relationships. When the absolute position of the described object changes, the relative positional relationship may change. Secondly: The accompanying drawings of the embodiments disclosed in this utility model only involve the structures involved in the embodiments disclosed in this utility model. Other structures can refer to the general design. In the absence of conflict, the same embodiment and different embodiments of this utility model can be combined with each other. Finally: The above description is only a preferred embodiment of the present utility model and is not intended to limit the present utility model. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present utility model should be included within the protection scope of the present utility model.

Claims

1. A regenerative pyrolysis high-temperature oil vapor condensation device, comprising a reaction assembly (1), a separation assembly (2), a temperature control assembly (3), a filtration assembly (4), and a tank assembly (5), characterized in that: The separation component (2) is located inside the reaction component (1), the temperature control component (3) is installed outside the reaction component (1), the filter component (4) is located outside one side of the reaction component (1), and the tank component (5) is located on one side of the filter component (4). The filter component (4) includes a valve (401), a lug (402), a filter plate (403), a collar (404), a buckle (405), and a sealing ring (406). The valve (401) is fixedly installed outside the gas supply pipe (105), and the lug (402) is symmetrically arranged outside the valve (401). The filter plate (403) is movably snapped inside one side of the gas supply pipe (105), and the sealing ring (406) is fixedly sleeved on the outside of the filter plate (403). The collar (404) is fixedly sleeved on one side of the tank component (5), and the buckles (405) are symmetrically installed on both sides of the collar (404).

2. The regenerative pyrolysis high-temperature oil vapor condensation equipment according to claim 1, characterized in that: The reaction assembly (1) includes a reaction vessel (101), a support (102), a sealing cap (103), a first oil outlet pipe (104), and a gas supply pipe (105). The support (102) is evenly installed at the bottom of the reaction vessel (101) and the tank assembly (5). The sealing cap (103) is installed at the top of the reaction vessel (101). The first oil outlet pipe (104) is fixedly connected to the bottom of the reaction vessel (101). The gas supply pipe (105) is fixedly connected to one side of the reaction vessel (101).

3. The regenerative pyrolysis high-temperature oil vapor condensation equipment according to claim 2, characterized in that: The separation component (2) includes a motor (201), a fan blade (202) and a carbon plate (203). The motor (201) is nested inside the sealing cover (103), and the output shaft of the motor (201) is fixedly connected to the fan blade (202) through a coupling. The carbon plate (203) is evenly arranged at the bottom of the inner wall of the reactor (101).

4. The regenerative pyrolysis high-temperature oil vapor condensation equipment according to claim 2, characterized in that: The temperature control assembly (3) includes a digital controller (301), a heating tube (302), a thermometer (303), and a condenser (304). The digital controller (301) is fixedly installed on the outside of the reactor (101), the heating tube (302) is nested in the inner wall of the reactor (101), the thermometer (303) is fixedly installed on the inner wall of the reactor (101), and the condenser (304) is located on one side of the tank assembly (5).

5. The regenerative pyrolysis high-temperature oil vapor condensation equipment according to claim 2, characterized in that: The tank assembly (5) includes a condenser (501), an air inlet pipe (502), and a second oil outlet pipe (503). The condenser (501) is located on one side of the reactor (101). One end of the air inlet pipe (502) is movably clamped into the inner wall of one side of the gas transmission pipe (105), and the other end of the air inlet pipe (502) is fixedly connected to one side of the condenser (501). The second oil outlet pipe (503) is located at the bottom of the air inlet pipe (502).

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