CN214863438U

CN214863438U - Coke oven gas desulfurization decarbonization compression synthesizer

Info

Publication number: CN214863438U
Application number: CN202120667716.2U
Authority: CN
Inventors: 汪群
Original assignee: Chongqing Langfu Environmental Protection Technology Co ltd
Current assignee: Chongqing Langfu Environmental Protection Technology Co ltd
Priority date: 2021-03-31
Filing date: 2021-03-31
Publication date: 2021-11-26
Anticipated expiration: 2031-03-31

Abstract

The utility model relates to a coke oven technical field just discloses a coke oven gas desulfurization decarbonization compression synthesizer, the on-line screen storage device comprises a base, the last fixed surface of base is connected with the casing, the last fixed surface of base is connected with annular oil tank. This kind of coke oven gas desulfurization decarbonization compression synthesizer, through setting up heating device, make annular heat conduction pole at the in-process of work, can effectual and the inside conduction oil fully contact of annular oil tank, the heating effect of conduction oil has been improved, the heat conduction piece of annular heat conduction pole lateral wall can effectual improvement conduction oil the efficiency of being heated simultaneously, slow down the device through setting up, make the conduction oil when entering annular oil tank inside through the oil feed nozzle, can effectually slow down the impact force of conduction oil, the inside conduction oil of annular oil tank has been avoided being driven, mix fast with oil feed nozzle spun conduction oil, result in the inside conduction oil of annular oil tank to appear ephemeral cooling, the heating effect of conduction oil to the conversion jar has further been influenced.

Description

Coke oven gas desulfurization decarbonization compression synthesizer

Technical Field

The utility model relates to a coke oven technical field specifically is a coke oven gas desulfurization decarbonization compression synthesizer.

Background

In the prior art, a reformer for coke oven gas is provided in the patent technology of patent No. CN211463087U, which includes a furnace body, a heating mechanism is sleeved on the outer surface of the furnace body, the heating mechanism includes a polyester ammonia heat insulation sleeve, an electric heating pipe, an oil storage chamber, an annular liquid guide pipe and a circulating pump, the polyester ammonia heat insulation sleeve is sleeved on the outer surface of the furnace body, the electric heating pipe is installed at the corresponding position on both sides of the bottom end of the inner wall of the polyester ammonia heat insulation sleeve, the oil storage chamber is installed at the corresponding position of the electric heating pipe on the bottom end of the furnace body, the annular liquid guide pipe is uniformly sleeved on the inner wall of the furnace body, and the circulating pump is installed at the connection position of the annular liquid guide pipe and the oil storage chamber; the reforming furnace for coke oven gas solves the problem of uneven heating of the furnace body by arranging the heating mechanism, and improves the production efficiency of environment-friendly gas.

However, among the above-mentioned technical scheme, because electric heating pipe is located the below setting in oil storage chamber, electric heating pipe is not in the in-process of work and the inside conduction oil in oil storage chamber fully contact, lead to the inside conduction oil of oil storage chamber to heat up slowly, and along with the circulation returns the inside conduction oil temperature decline in oil storage chamber, drive about down at the circulating pump and carry out the flash mixed with the inside conduction oil in oil storage chamber, cause the inside conduction oil temperature in oil storage chamber to appear the difference in temperature of short-lived, further influenced the heating effect to the furnace body.

SUMMERY OF THE UTILITY MODEL

Technical problem to be solved

Aiming at the defects of the prior art, the utility model provides a coke oven gas desulfurization and decarburization compression synthesizer, which solves the problem provided by the background technology.

(II) technical scheme

In order to achieve the above object, the present invention provides the following technical solutions: the utility model provides a coke oven gas desulfurization decarbonization compression synthesizer, includes the base, the last fixed surface of base is connected with the casing, the last fixed surface of base is connected with annular oil tank, the inside conduction oil that is provided with of annular oil tank, the inside of casing is provided with the retort, the retort is located fixed surface on the annular oil tank and is connected, the last fixed surface of annular oil tank is connected with the retort, the lateral wall of annular oil tank is provided with oil inlet nozzle and play oil nozzle, the lateral wall cover of retort is equipped with spiral defeated oil pipe, spiral defeated oil pipe's both ends respectively with the one end fixed connection who advances oil nozzle and play oil nozzle, spiral defeated oil pipe is provided with the circulating pump with a play oil nozzle junction, the inside heating device that is provided with of annular oil tank, the inside of annular oil tank is provided with slows down the device.

(III) advantageous effects

Compared with the prior art, the utility model discloses possess following beneficial effect:

1. this kind of coke oven gas desulfurization decarbonization compression synthesizer, through setting up heating device, make annular heat conduction pole at the in-process of work, can effectual and the inside conduction oil fully contact of annular oil tank, the heating effect of conduction oil has been improved, the heat conduction piece of annular heat conduction pole lateral wall can effectual improvement conduction oil the efficiency of being heated simultaneously, slow down the device through setting up, make the conduction oil when entering annular oil tank inside through the oil feed nozzle, can effectually slow down the impact force of conduction oil, the inside conduction oil of annular oil tank has been avoided being driven, mix fast with oil feed nozzle spun conduction oil, result in the inside conduction oil of annular oil tank to appear ephemeral cooling, the heating effect of conduction oil to the conversion jar has further been influenced.

2. This kind of coke oven gas desulfurization decarbonization compression synthesizer, through setting up the guide plate, make the conduction oil follow the inside back that flows in U-shaped groove, through the guide plate, with the position of conduction oil drainage to annular heat conduction pole and conducting strip, the conducting strip blocks the conduction oil, and heat it, the flow velocity of the inside conduction oil of circulation loop annular oil tank has further been delayed, through setting up fixed block and U-shaped groove into the metal material, make the conduction oil get into the inside back of U-shaped groove, can effectually preheat the conduction oil, further improve the heating efficiency to the conduction oil.

Drawings

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

FIG. 2 is a front view of the cutting structure of the present invention;

FIG. 3 is a schematic view of the overlooking and sectioning structure of the annular oil tank of the present invention

FIG. 4 is a front view of the ring-shaped fuel tank of the present invention

FIG. 5 is a schematic view of the structure of the slowing device of the present invention

Fig. 6 is a front view of the slowing device of the present invention.

In the figure: 1. a base; 2. a housing; 3. an annular fuel tank; 4. a conversion tank; 5. an oil inlet nozzle; 6. an oil outlet nozzle; 7. a spiral oil delivery pipe; 8. a heating device; 801. an annular heat conducting rod; 802. a fixed block; 803. a heat conductive sheet; 9. a mitigation device; 901. a U-shaped groove; 10. a baffle; 11. and a circulating pump.

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.

Examples

Please refer to fig. 1-6, a coke oven gas desulfurization decarbonization compression synthesizer, which comprises a base 1, the upper surface of the base 1 is fixedly connected with a shell 2, the upper surface of the base 1 is fixedly connected with an annular oil tank 3, heat conducting oil is arranged inside the annular oil tank 3, a conversion tank 4 is arranged inside the shell 2, the conversion tank 4 is located on the annular oil tank 3 and is fixedly connected with the upper surface, an oil inlet nozzle 5 and an oil outlet nozzle 6 are arranged on the outer side wall of the annular oil tank 3, a spiral oil conveying pipe 7 is sleeved on the outer side wall of the conversion tank 4, two ends of the spiral oil conveying pipe 7 are respectively fixedly connected with one end of the oil inlet nozzle 5 and one end of the oil outlet nozzle 6, a circulating pump 11 is arranged at the joint of the spiral oil conveying pipe 7 and the oil outlet nozzle 6, a heating device 8 is arranged inside the annular oil tank 3, and a slowing device 9 is arranged inside the annular oil tank 3.

Further, as shown in fig. 2, fig. 3 and fig. 4, heating device 8 includes annular heat conduction rod 801, annular heat conduction rod 801 is located the inside setting of annular oil tank 3, a plurality of fixed blocks 802 of the lateral wall fixedly connected with of annular heat conduction rod 801, the one end of fixed block 802 and the inside wall fixed connection of annular oil tank 3, a plurality of conducting strips 803 of the lateral wall fixedly connected with of annular heat conduction rod 801, make annular heat conduction rod 801 at the in-process of work, can effectual and the inside conduction oil of annular oil tank 3 fully contact, the heating effect of conduction oil has been improved, the efficiency of being heated of conduction oil can effectually be improved to the conducting strip 803 of annular heat conduction rod 801 lateral wall simultaneously.

Further, as shown in fig. 2, fig. 3, fig. 5 and fig. 6, the slowing device 9 includes the U-shaped groove 901, the one end of U-shaped groove 901 and the one end fixed connection of fixed block 802, make the conduction oil get into annular oil tank 3 inside through oil feed nozzle 5 when, can effectually slow down the impact dynamics of conduction oil, avoided the inside conduction oil of annular oil tank 3 to be driven, mix with 5 spun conduction oil of oil feed nozzle fast, lead to the inside conduction oil of annular oil tank 3 to appear transient cooling, the heating effect of conduction oil to conversion tank 4 has been guaranteed.

Further, as shown in fig. 2 and 3, the inside wall of the annular oil tank 3 is symmetrically provided with the guide plates 10, and the symmetrically arranged guide plates 10 are located on two sides of the oil inlet nozzle 5, so that after the heat transfer oil flows out from the inside of the U-shaped groove 901, the heat transfer oil is guided to the positions of the annular heat conducting rod 801 and the heat conducting fins 803 through the guide plates 10, the heat conducting fins 803 block the heat transfer oil and heat the heat transfer oil, and the flowing speed of the heat transfer oil circulating back to the inside of the annular oil tank 3 is further delayed.

Further, as shown in fig. 2, 3 and 4, the fixing block 802 and the U-shaped groove 901 are both made of metal, so that the heat transfer oil can be effectively preheated after entering the U-shaped groove 901, and the heating efficiency of the heat transfer oil is further improved.

The working principle is as follows: when the annular oil tank is used, the annular heat conducting rod 801 is opened at first, and the annular heat conducting rod 801 heats heat conducting oil in the annular oil tank 3 in the working process; after the temperature of the heat conduction oil inside the annular oil tank 3 reaches a specified value, the circulating pump 11 is turned on, the circulating pump 11 drives the heat conduction oil inside the annular oil tank 3 to enter the inside of the spiral oil delivery pipe 7 through the oil outlet nozzle 6, the heat conduction oil enters the inside of the U-shaped groove 901 through the oil inlet nozzle 5 after circulating inside the spiral oil delivery pipe 7, the heat conduction oil entering the inside of the U-shaped groove 901 overflows from the outlet of the U-shaped groove 901 to the periphery, the heat conduction oil overflows through the guide plate 10 and flows to the positions of the annular heat conduction rod 801 and the heat conduction sheet 803, the heat conduction sheet 803 stops the heat conduction oil again, and the flow rate of the heat conduction oil is delayed, so that the annular heat conduction rod 801 and the heat conduction sheet 803 have sufficient time to heat the heat conduction oil.

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 coke oven gas desulfurization, decarburization and compression synthesis device comprises a base (1), wherein the upper surface of the base (1) is fixedly connected with a shell (2);

the method is characterized in that:

the upper surface of the base (1) is fixedly connected with an annular oil tank (3), heat conducting oil is arranged in the annular oil tank (3), a conversion tank (4) is arranged in the shell (2), the conversion tank (4) is fixedly connected with the upper surface of the annular oil tank (3), the upper surface of the annular oil tank (3) is fixedly connected with a conversion tank (4), the outer side wall of the annular oil tank (3) is provided with an oil inlet nozzle (5) and an oil outlet nozzle (6), the outer side wall of the conversion tank (4) is sleeved with a spiral oil delivery pipe (7), two ends of the spiral oil delivery pipe (7) are respectively fixedly connected with one end of the oil inlet nozzle (5) and one end of the oil outlet nozzle (6), a circulating pump (11) is arranged at the joint of the spiral oil delivery pipe (7) and the oil outlet nozzle (6), the annular oil tank (3) is internally provided with a heating device (8), and the annular oil tank (3) is internally provided with a retarding device (9).

2. The coke oven gas desulfurization, decarburization and compression synthesis device of claim 1, which is characterized in that: heating device (8) are including annular heat conduction pole (801), annular heat conduction pole (801) are located the inside setting of annular oil tank (3), a plurality of fixed blocks (802) of lateral wall fixedly connected with of annular heat conduction pole (801), the one end of fixed block (802) and the inside wall fixed connection of annular oil tank (3), a plurality of conducting strips (803) of lateral wall fixedly connected with of annular heat conduction pole (801).

3. The coke oven gas desulfurization, decarburization and compression synthesis device as claimed in claim 1 or 2, characterized in that: the slowing device (9) comprises a U-shaped groove (901), and one end of the U-shaped groove (901) is fixedly connected with one end of the fixing block (802).

4. The coke oven gas desulfurization, decarburization and compression synthesis device as claimed in claim 1 or 2, characterized in that: the inner side wall of the annular oil tank (3) is symmetrically provided with guide plates (10), and the guide plates (10) which are symmetrically arranged are arranged on two sides of the oil inlet nozzle (5).

5. The coke oven gas desulfurization, decarburization and compression synthesis device as claimed in claim 3, wherein: the inner side wall of the annular oil tank (3) is symmetrically provided with guide plates (10), and the guide plates (10) which are symmetrically arranged are arranged on two sides of the oil inlet nozzle (5).

6. The coke oven gas desulfurization, decarburization and compression synthesis device of claim 2, which is characterized in that: the fixing block (802) and the U-shaped groove (901) are both made of metal materials.