CN214438913U

CN214438913U - Oil-sealed waste material catalytic control device

Info

Publication number: CN214438913U
Application number: CN202120129842.2U
Authority: CN
Inventors: 孙亮; 张春海; 陆培华; 穆祥; 许志林
Original assignee: Hongji Formosa Petrochemical Co Zhejiang
Current assignee: Hongji Formosa Petrochemical Co Zhejiang
Priority date: 2021-01-18
Filing date: 2021-01-18
Publication date: 2021-10-22
Anticipated expiration: 2031-01-18

Abstract

The utility model provides an oil seal formula waste material catalytic control device belongs to waste material processing technology field. The catalytic reactor comprises a waste treatment barrel provided with an air blocking agent, a catalyst arranged in the waste treatment barrel, and a catalytic device connected with the waste treatment barrel, wherein the catalytic device comprises a catalytic gas spray gun inserted into the waste treatment barrel, the top end of the catalytic gas spray gun is connected with a first air inlet pipe, and a cooling cavity is arranged in the waste treatment barrel. Air separation agent can separate catalyst and air, prevents the spontaneous combustion of catalyst, and the external nitrogen oxygen mist of intake pipe, when handling the waste material, nitrogen gas and oxygen can let in to air separation agent and contact with the catalyst through intake pipe and catalytic gas spray gun, thereby make catalyst and oxygen and nitrogen gas reaction handle the waste material, and it can cool down to the waste material processing barrel to lead to the coolant liquid to the cooling intracavity.

Description

Oil-sealed waste material catalytic control device

Technical Field

The utility model belongs to the technical field of the waste material is handled, a oil seal formula waste material catalytic control device is related to.

Background

The waste materials are sometimes treated by catalyst catalysis in industry, but some catalysts have spontaneous combustion phenomenon in air, and the catalytic reaction speed is difficult to control.

In order to overcome the defects of the prior art, people continuously explore and propose various solutions, for example, chinese patent discloses a controllable reaction device for producing hydrogen from sodium borohydride [ application number: 201621041339.7], comprising a hydrogen production reaction chamber, a manual control system, a catalyst placing element and a gas filtering mechanism; the hydrogen production reaction chamber is provided with a hydrogen output port, the manual control system is connected with the hydrogen production reaction chamber, and the reaction rate is controlled by controlling the height of the catalyst immersed in the solution; the bottom of the hydrogen production reaction chamber is provided with a waste liquid discharge port; the ports are hermetically connected in a threaded mode; the catalyst placing element is composed of a screen; the upper end of the catalyst placing element is connected with the control system through a hard rod; the control system is positioned on a hydrogen output port on the hydrogen production reaction chamber, and the manual control system consists of a regulating device of a catalyst placing element and an air flow speed display element. The utility model has the advantages of being simple in structure and convenient in operation, reactor internal pressure is low and safe in utilization, can effectually carry out manual, automatic control reaction rate, can high-efficiently retrieve the catalyst to can not cause fuel cell electrode catalyst's poisoning.

SUMMERY OF THE UTILITY MODEL

The utility model aims at the above-mentioned problem, provide an oil seal formula waste material catalytic control device.

In order to achieve the above purpose, the utility model adopts the following technical proposal:

the utility model provides an oil seal formula waste material catalytic control device, is including the waste material processing barrel that is equipped with the air separation agent, and the catalyst setting still includes the catalytic unit who promotes that links to each other with the waste material processing barrel in the waste material processing barrel, the catalytic unit that promotes including inserting the catalytic gas spray gun in the waste material processing barrel, catalytic gas spray gun top even have an intake pipe, the waste material processing barrel in be equipped with the cooling chamber.

In the oil-sealed waste material catalysis control device, the catalysis promoting device further comprises a connecting seat, a valve is arranged on the connecting seat, and one end, far away from the catalysis gas spray gun, of the first air inlet pipe is connected with the valve.

In the oil-sealed waste catalyzing and controlling device, the connecting seat comprises a base, a connecting rod vertically arranged is arranged on the base, a display panel is arranged at the top of the connecting rod, and the valve is arranged on the connecting rod.

In foretell oil seal formula waste material catalysis controlling means, display panel on still be equipped with gas flowmeter, gas flowmeter bottom link to each other with the valve through No. two intake pipes, gas flowmeter top still link to have No. three intake pipes.

In foretell oil seal formula waste material catalysis controlling means, the waste material processing barrel on still be equipped with the liquid inlet joint that links to each other with the cooling chamber and go out the liquid hole, liquid inlet joint be located the well upper side of waste material processing barrel lateral wall, the liquid hole be located the downside of waste material processing barrel lateral wall.

In the oil-sealed waste material catalysis control device, the waste material treatment barrel comprises an inner barrel and an outer barrel, the cooling cavity is positioned between the inner barrel and the outer barrel, and the catalysis gas spray gun is inserted into the inner barrel.

In the oil-sealed waste material catalysis control device, the inner barrel is detachably arranged in the outer barrel, and a circumferential limit structure is arranged between the outer barrel and the inner barrel.

In the oil-sealed waste material catalysis control device, the circumferential limiting structure comprises a sealing baffle plate which is welded on the outer barrel and has an annular cross section, a plurality of limiting grooves are uniformly arranged on the sealing baffle plate at intervals along the circumferential direction, a plurality of limiting blocks corresponding to the limiting grooves are arranged on the inner barrel, and the limiting blocks are inserted into the limiting grooves and are in sliding connection with the limiting grooves.

In the oil-sealed waste material catalytic control device, the bottom of the cooling cavity is welded with a plurality of supporting blocks, the supporting blocks are uniformly arranged at intervals along the circumferential direction, and the tops of the supporting blocks are abutted against the inner barrel.

In the oil-sealed waste catalyzing and controlling device, a thermometer is also arranged on the side wall of the outer barrel, and a temperature display connected with the thermometer is also arranged on the display panel.

Compared with the prior art, the utility model has the advantages of:

1. air separation agent can separate catalyst and air, prevents the spontaneous combustion of catalyst, and the external nitrogen oxygen mist of intake pipe, when handling the waste material, nitrogen gas and oxygen can let in to air separation agent and contact with the catalyst through intake pipe and catalytic gas spray gun, thereby make catalyst and oxygen and nitrogen gas reaction handle the waste material, and it can cool down to the waste material processing barrel to lead to the coolant liquid to the cooling intracavity.

2. The thermometer can detect the temperature of the inner barrel, the temperature display can display the temperature detected by the thermometer on the display panel, the observation is convenient, the speed of the catalytic reaction can be judged according to the temperature of the inner barrel, and then the oxygen amount and the nitrogen amount introduced into the air blocking agent are adjusted according to the reaction speed.

Additional advantages, objects, and features of the invention will be set forth in part in the description which follows and in part will become apparent to those having ordinary skill in the art upon examination of the following or may be learned from practice of the invention.

Drawings

Fig. 1 is a schematic diagram of the overall structure provided by the present invention;

FIG. 2 is a schematic view of the internal structure of the waste disposal cask;

figure 3 is a top view of the waste disposal bin.

Detailed Description

As shown in fig. 1-3, an oil-sealed waste catalytic control device comprises a waste treatment barrel 2 provided with an air blocking agent 1, a catalyst arranged in the waste treatment barrel 2, and a catalytic promotion device 3 connected with the waste treatment barrel 2, wherein the catalytic promotion device 3 comprises a catalytic gas spray gun 4 inserted into the waste treatment barrel 2, the top end of the catalytic gas spray gun 4 is connected with a first air inlet pipe 5, and a cooling cavity 6 is arranged in the waste treatment barrel 2.

In this embodiment, air separation agent 1 can separate catalyst and air, prevents the catalyst spontaneous combustion, and the external nitrogen oxygen mist of intake pipe 5, during the processing waste material, nitrogen gas and oxygen can let in to the air separation agent and contact with the catalyst through intake pipe and catalysis gas spray gun 4, thereby make catalyst and oxygen and nitrogen gas reaction handle the waste material, and it can cool down waste material treatment barrel 2 to lead to the coolant liquid to the cooling intracavity.

It will be understood by those skilled in the art that the air blocking agent 1 may be white oil, etc., and the coolant may be tap water, etc.

Preferably, as shown in fig. 1-3, the catalytic device 3 further includes a connecting seat 7, a valve 8 is disposed on the connecting seat 7, and one end of the first air inlet pipe 5, which is far away from the catalytic gas spray gun 4, is connected to the valve 8. The valve 8 can be used for introducing air into the oxygen quantity and the nitrogen quantity in the waste treatment barrel 2.

As shown in fig. 1-3, the connection seat 7 includes a base 9, a connection rod 10 vertically disposed is disposed on the base 9, a display panel 11 is disposed on the top of the connection rod 10, and the valve 8 is disposed on the connection rod 10. Still be equipped with gas flowmeter 12 on display panel 11, gas flowmeter 12 bottom link to each other with valve 8 through No. two intake pipe 13, gas flowmeter 12 top still link to each other and have No. three intake pipe 14. The gas flow meter 12 can detect the gas flow rate introduced into the waste treatment barrel 2 and display the gas flow rate on the display panel 11, so that the gas flow rate can be observed conveniently.

As shown in fig. 1-3, the waste treatment barrel 2 is further provided with a liquid inlet connector 15 and a liquid outlet hole 16 connected with the cooling cavity 6, the liquid inlet connector 15 is located at the upper middle side of the side wall of the waste treatment barrel 2, and the liquid outlet hole 16 is located at the lower side of the side wall of the waste treatment barrel 2. The external water pipe of liquid inlet joint 15, the water pipe can let in the cooling intracavity with the running water from liquid inlet joint 15, cools down waste treatment bucket 2, and the running water of cooling intracavity passes through the drain hole and discharges.

As shown in fig. 1-3, the waste treatment barrel 2 comprises an inner barrel 17 and an outer barrel 18, the cooling chamber 6 is located between the inner barrel 17 and the outer barrel 18, and the catalytic gas spray gun 4 is inserted into the inner barrel 17. The inner barrel 17 is detachably arranged in the outer barrel 18, and a circumferential limiting structure 19 is further arranged between the outer barrel 18 and the inner barrel 17. Interior bucket 17 detachable sets up and is conveniently wasing, and circumference limit structure 19 can be spacing to interior bucket 17 circumference.

As shown in fig. 1-3, the circumferential limiting structure 19 includes a closed baffle 20 welded on the outer barrel 18 and having an annular cross section, a plurality of limiting grooves 21 are uniformly arranged on the closed baffle 20 at intervals along the circumferential direction, a plurality of limiting blocks 22 corresponding to the limiting grooves 21 are arranged on the inner barrel 17, and the limiting blocks 22 are inserted into the limiting grooves 21 and slidably connected with the limiting grooves 21. A plurality of supporting blocks 23 are further welded at the bottom of the cooling cavity 6, the supporting blocks 23 are uniformly arranged at intervals along the circumferential direction, and the tops of the supporting blocks 23 are abutted to the inner barrel 17. The limiting groove 21 is matched with the limiting block 22 to limit the inner barrel 17, and the closed baffle 20 can seal the cooling cavity.

As shown in fig. 1-3, a thermometer 24 is further disposed on the side wall of the outer tub 18, and a temperature display 25 connected to the thermometer 24 is further disposed on the display panel 11. The thermometer 24 can detect the temperature of the inner barrel, the temperature display 25 can display the temperature detected by the thermometer 24 on the display panel, so that the observation is convenient, the speed of catalytic reaction can be judged according to the temperature of the inner barrel, and the oxygen amount and the nitrogen amount introduced into the air blocking agent are adjusted according to the reaction speed.

The utility model discloses a theory of operation is: the air separation agent 1 can separate a catalyst from air to prevent the catalyst from spontaneous combustion, the air inlet pipe 5 is externally connected with nitrogen-oxygen mixed gas, when waste materials are treated, nitrogen and oxygen can be introduced into the air separation agent through the air inlet pipe and the catalytic gas spray gun 4 and are contacted with the catalyst, the catalyst is enabled to react with the oxygen and the nitrogen to treat the waste materials, cooling liquid is introduced into a cooling cavity to cool the waste material treatment barrel 2, the valve 8 can be used for introducing the oxygen and the nitrogen into the waste material treatment barrel 2, the gas flowmeter 12 can be used for detecting the gas flow introduced into the waste material treatment barrel 2 and displaying the gas flow on the display panel 11 to facilitate observation, the thermometer 24 can be used for detecting the temperature at the inner barrel, the temperature display 25 can be used for displaying the temperature detected by the thermometer 24 on the display panel to facilitate observation, and the catalytic reaction rate can be judged according to the temperature at the inner barrel, and then the amount of oxygen and the amount of nitrogen introduced into the air blocking agent are adjusted according to the reaction rate.

The specific embodiments described herein are merely illustrative of the spirit of the invention. Various modifications, additions and substitutions for the specific embodiments described herein may be made by those skilled in the art without departing from the spirit of the invention or exceeding the scope of the invention as defined in the accompanying claims.

Claims

1. The utility model provides an oil seal formula waste material catalysis controlling means, is including waste material processing barrel (2) that is equipped with air barrier agent (1), and the catalyst setting is in waste material processing barrel (2), its characterized in that still includes and urge catalytic unit (3) that link to each other with waste material processing barrel (2), urge catalytic unit (3) including inserting catalysis gas spray gun (4) in waste material processing barrel (2), catalysis gas spray gun (4) top even have intake pipe (5) No. one, waste material processing barrel (2) in be equipped with cooling chamber (6).

2. The oil-sealed waste catalytic control device according to claim 1, characterized in that the catalytic device (3) further comprises a connecting seat (7), a valve (8) is arranged on the connecting seat (7), and one end of the first air inlet pipe (5) far away from the catalytic gas spray gun (4) is connected with the valve (8).

3. The oil-sealed waste catalytic control device according to claim 2, wherein the connecting base (7) comprises a base (9), a connecting rod (10) is vertically arranged on the base (9), a display panel (11) is arranged on the top of the connecting rod (10), and the valve (8) is arranged on the connecting rod (10).

4. The oil-sealed waste catalytic control device according to claim 3, characterized in that a gas flowmeter (12) is further arranged on the display panel (11), the bottom of the gas flowmeter (12) is connected with the valve (8) through a second gas inlet pipe (13), and a third gas inlet pipe (14) is further connected to the top of the gas flowmeter (12).

5. The oil-sealed waste catalytic control device according to claim 4, wherein the waste treatment barrel (2) is further provided with a liquid inlet joint (15) and a liquid outlet hole (16) connected with the cooling cavity (6), the liquid inlet joint (15) is located on the middle upper side of the side wall of the waste treatment barrel (2), and the liquid outlet hole (16) is located on the lower side of the side wall of the waste treatment barrel (2).

6. The oil-sealed catalytic control device for wastes according to claim 5, characterized in that said waste treatment tank (2) comprises an inner tank (17) and an outer tank (18), said cooling chamber (6) is located between the inner tank (17) and the outer tank (18), said catalytic gas lance (4) is inserted into the inner tank (17).

7. The catalytic control device of claim 6, wherein the inner barrel (17) is detachably disposed in the outer barrel (18), and a circumferential limiting structure (19) is disposed between the outer barrel (18) and the inner barrel (17).

8. The oil-sealed waste catalytic control device according to claim 7, characterized in that the circumferential limiting structure (19) comprises a closed baffle (20) welded on the outer barrel (18) and having an annular cross section, a plurality of limiting grooves (21) are uniformly arranged on the closed baffle (20) along the circumferential direction at intervals, a plurality of limiting blocks (22) corresponding to the limiting grooves (21) are arranged on the inner barrel (17), and the limiting blocks (22) are inserted into the limiting grooves (21) and are slidably connected with the limiting grooves (21).

9. The oil-sealed waste catalytic control device according to claim 8, wherein a plurality of support blocks (23) are welded at the bottom of the cooling chamber (6), the support blocks (23) are uniformly arranged along the circumferential direction at intervals, and the tops of the support blocks (23) are abutted against the inner barrel (17).

10. The oil-sealed waste catalytic control device according to claim 9, characterized in that a thermometer (24) is further disposed on the side wall of the outer tub (18), and a temperature display (25) connected to the thermometer (24) is further disposed on the display panel (11).