CN210934110U

CN210934110U - Separator for synthetic ammonia workshop section

Info

Publication number: CN210934110U
Application number: CN201921493674.4U
Authority: CN
Inventors: 金康
Original assignee: Wuhan Bolang Qingneng Environmental Protection Engineering Co ltd
Current assignee: Wuhan Bolang Qingneng Environmental Protection Engineering Co ltd
Priority date: 2019-09-06
Filing date: 2019-09-06
Publication date: 2020-07-07
Anticipated expiration: 2029-09-06

Abstract

The utility model discloses a separator for synthetic ammonia workshop section, including support, baffle, ware body, isolating construction, top cap, bottom and separator body, the separator body includes ware body, top cap and bottom, gas inlet has been seted up to the left end face of ware body, gas outlet has been seted up to the right-hand member face of ware body, the up end of ware body is connected with the top cap, the gas vent has been seted up in the middle of the up end of top cap, the lower terminal surface of ware body is connected with the bottom, the leakage fluid dram has been seted up in the middle of the lower terminal surface of bottom, the inboard upper portion of ware body is connected with isolating construction, the inboard sub-unit connection of ware body has the baffle, the bottom face of separator body is connected with the support. The utility model discloses a set up ware body and isolating construction, solved in the transform workshop section because the inside pressure ratio of current separator is higher, lead to using the conventional silk screen demister of usefulness to have the problem that has the restriction requirement to the flow rate.

Description

Separator for synthetic ammonia workshop section

Technical Field

The utility model relates to the technical field of gas-liquid separation, in particular to a separator for a synthetic ammonia workshop section.

Background

The development of projects of coal-to-olefin, coal-to-oil, coal-to-ethylene glycol and coal-to-natural gas in China all have matched ammonia synthesis sections, and the conversion and separation of coal gas are involved in the sections.

However, the prior art has the following disadvantages: in a conversion section, due to the fact that the pressure in the equipment is high, a conventional wire mesh demister has the problem that the flow rate is limited, and therefore a novel separator is provided for solving the problem of gas-liquid separation in a gas conversion section.

SUMMERY OF THE UTILITY MODEL

Technical problem to be solved

To the deficiency of the prior art, the utility model provides a separator for synthetic ammonia workshop section has solved in the transform workshop section, because the equipment internal pressure is than higher, the silk screen demister of conventional usefulness exists the problem that has the restriction requirement to the flow rate.

(II) technical scheme

In order to achieve the above object, the utility model provides a following technical scheme: a separator for a synthetic ammonia workshop section comprises a support, a baffle, a separator body, a separation structure, a top cover, a bottom cover and a separator body, wherein the separator body comprises the separator body, the top cover and the bottom cover, a gas inlet is formed in the left end face of the separator body, a gas outlet is formed in the right end face of the separator body, the top cover is connected to the upper end face of the separator body, an exhaust port is formed in the middle of the upper end face of the top cover, the bottom cover is connected to the lower end face of the separator body, a liquid discharge port is formed in the middle of the lower end face of the bottom cover, the separation structure is connected to the upper portion of the inner side of the separator body, the baffle is connected to the lower portion of the inner side.

Preferably, the outer side of the gas inlet is connected with a gas inlet pipe, and the gas inlet pipe is connected with a first valve.

Preferably, the outer side of the exhaust port is connected with an exhaust pipe, and the exhaust pipe is connected with a second valve.

Preferably, a first conduit is connected to the outer side of the gas outlet, and a third valve is connected to the first conduit.

Preferably, a second conduit is connected to the outer side of the liquid outlet, and a fourth valve is connected to the second conduit.

Preferably, a transverse plate is welded at the upper end of the baffle plate, and the left end face of the transverse plate is connected to the lower portion of the inner left side wall of the transformer body.

Preferably, a flow guide pipe is connected in the middle of the lower end face of the separation structure, connecting rods are welded on the right end face of the separation structure in an up-and-down symmetrical mode, and the right end face of each connecting rod is connected to the upper portion of the right side wall of the inside of the device body.

(III) advantageous effects

The utility model provides a separator for synthetic ammonia workshop section possesses following beneficial effect:

the utility model, through the device body and the separation structure, the separation structure is arranged inside the device body, so that the utility model can meet the requirements under high pressure working condition, the separation structure in the utility model adopts the folded plate separation technology, the gas-liquid separation efficiency can be improved, the gas flow rate is large, the capacity of treating gas is large, the separation efficiency is improved by five times to ten times compared with the separation efficiency of a common silk screen demister, the system resistance is reduced, the system energy consumption is reduced, the energy-saving effect is achieved, the general resistance is reduced between one hundred pa and one hundred fifty pa, the resistance is reduced by about one time to two times compared with the conventional separator, the separation efficiency reaches nineteen percent for droplet particles with more than 5um, compared with similar products, the utility model has the characteristics of large capacity of treating gas, small occupied area, high separation efficiency, small investment and convenient installation and maintenance, the exhaust port is only used in the pressure test and exhaust of the system, the screen demister is not used in the normal driving process, and the problem that the conventional screen demister has a limit requirement on the flow rate due to high pressure in equipment in a conversion section is solved.

Drawings

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

fig. 2 is an enlarged schematic view of the structure of the middle separation structure of the present invention;

fig. 3 is an enlarged schematic view of the structure at a in fig. 1 according to the present invention;

fig. 4 is an enlarged schematic view of the structure at B in fig. 1 according to the present invention;

fig. 5 is an enlarged schematic view of the structure at C in fig. 1 according to the present invention.

The reference numbers in the figures are: 1. a support; 2. a gas inlet; 3. a baffle plate; 4. a body; 5. a separation structure; 6. an exhaust port; 7. a gas outlet; 8. a liquid discharge port; 9. a top cover; 10. a bottom cover; 11. a separator body; 12. an air inlet pipe; 13. a first valve; 14. an exhaust pipe; 15. a second valve; 16. a first conduit; 17. a third valve; 18. a second conduit; 19. a fourth valve; 20. a transverse plate; 21. a flow guide pipe; 22. a connecting rod.

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.

Referring to fig. 1-5, the present invention provides an embodiment: the utility model provides a synthetic ammonia separator for workshop section, including support 1, baffle 3, ware body 4, separation structure 5, top cap 9, bottom 10 and separator body 11, separator body 11 includes ware body 4, top cap 9 and bottom 10, gas inlet 2 has been seted up to the left end face of ware body 4, gas outlet 7 has been seted up to the right-hand member face of ware body 4, the up end of ware body 4 is connected with top cap 9, gas vent 6 has been seted up in the middle of the up end of top cap 9, the lower terminal surface of ware body 4 is connected with bottom 10, leakage fluid dram 8 has been seted up in the middle of the lower terminal surface of bottom 10, the inboard upper portion of ware body 4 is connected with separation structure 5, the inboard sub-unit connection of ware body 4 has baffle 3, the bottom face of separator body 11 is connected with support.

Further, the outside of gas inlet 2 is connected with intake pipe 12, is connected with first valve 13 on the intake pipe 12, and steerable gas-liquid mixture gets into the inboard of ware body 4.

Further, an exhaust pipe 14 is connected to the outside of the exhaust port 6, and a second valve 15 is connected to the exhaust pipe 14 to control the exhaust of the separated gas.

Further, a first conduit 16 is connected to the outside of the gas outlet 7, and a third valve 17 is connected to the first conduit 16, so that the gas-liquid mixture can be controlled to leave the inside of the vessel body 4.

Further, a second pipe 18 is connected to the outside of the liquid discharge port 8, and a fourth valve 19 is connected to the second pipe 18, thereby controlling the discharge of the separated liquid.

Further, a transverse plate 20 is welded to the upper end of the baffle plate 3, and the left end surface of the transverse plate 20 is connected to the lower portion of the inner left side wall of the vessel body 4, so that the baffle plate 3 is connected to the inner side of the vessel body 4.

Furthermore, a draft tube 21 is connected in the middle of the lower end face of the separation structure 5, a connecting rod 22 is welded on the right end face of the separation structure 5 in an up-and-down symmetrical manner, and the right end face of the connecting rod 22 is connected to the upper portion of the right side wall inside the vessel body 4, so that the separation structure 5 is connected inside the vessel body 4.

The working principle is as follows: when the device is used, a user opens the first valve 13, the second valve 15, the third valve 17 and the fourth valve 19 in sequence, then water gas in a conversion section enters the gas inlet 2 through the gas inlet 12, then the water gas flows into the inside of the device body 4 through the gas inlet 2, then the flow direction of the water gas is changed through the baffle 3, the water gas is deflected downwards and flows upwards, then the water gas is separated through the separation structure 5, separated gas is discharged into the inside of the first conduit 16 through the gas outlet 7, then the separated gas is discharged through the first conduit 16, captured liquid drops flow to the bottom of the inner side of the device body 4 through the flow guide pipe 21 at the lower part of the separation structure 5, then the liquid drops are discharged into the inside of the second conduit 18 through the liquid discharge port 8, and then the liquid drops are discharged through the second conduit 18.

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. The utility model provides a separator for synthetic ammonia workshop section, includes support (1), baffle (3), ware body (4), separation structure (5), top cap (9), bottom (10) and separator body (11), its characterized in that: the separator body (11) comprises a separator body (4), a top cover (9) and a bottom cover (10), a gas inlet (2) is formed in the left end face of the separator body (4), a gas outlet (7) is formed in the right end face of the separator body (4), the top cover (9) is connected to the upper end face of the separator body (4), a gas exhaust port (6) is formed in the middle of the upper end face of the top cover (9), the bottom cover (10) is connected to the lower end face of the separator body (4), a liquid discharge port (8) is formed in the middle of the lower end face of the bottom cover (10), a separation structure (5) is connected to the upper portion of the inner side of the separator body (4), a baffle (3) is connected to the lower portion of the inner side of the separator body (4), and a support (1.

2. The separator for the section of ammonia synthesis according to claim 1, characterized in that: the outside of gas inlet (2) is connected with intake pipe (12), be connected with first valve (13) on intake pipe (12).

3. The separator for the section of ammonia synthesis according to claim 1, characterized in that: the outside of gas vent (6) is connected with blast pipe (14), be connected with second valve (15) on blast pipe (14).

4. The separator for the section of ammonia synthesis according to claim 1, characterized in that: the outer side of the gas outlet (7) is connected with a first conduit (16), and the first conduit (16) is connected with a third valve (17).

5. The separator for the section of ammonia synthesis according to claim 1, characterized in that: the outer side of the liquid outlet (8) is connected with a second conduit (18), and the second conduit (18) is connected with a fourth valve (19).

6. The separator for the section of ammonia synthesis according to claim 1, characterized in that: the upper end of the baffle (3) is welded with a transverse plate (20), and the left end face of the transverse plate (20) is connected to the lower portion of the inner left side wall of the transformer body (4).

7. The separator for the section of ammonia synthesis according to claim 1, characterized in that: the honeycomb duct (21) is connected in the middle of the lower end face of the separating structure (5), connecting rods (22) are symmetrically welded on the upper portion and the lower portion of the right end face of the separating structure (5), and the right end face of each connecting rod (22) is connected to the upper portion of the inner right side wall of the body (4).