CN216825265U

CN216825265U - Shunting condensing equipment and remove liquid equipment thereof

Info

Publication number: CN216825265U
Application number: CN202123430591.0U
Authority: CN
Inventors: 陈发忠; 韩忠娟; 陈文照; 李鹏程
Original assignee: Fujian Hengjia Environmental Protection Equipment Co ltd
Current assignee: Fujian Hengjia Environmental Protection Equipment Co ltd
Priority date: 2021-12-30
Filing date: 2021-12-30
Publication date: 2022-06-28
Anticipated expiration: 2031-12-30

Abstract

The utility model relates to a reposition of redundant personnel condensing equipment and remove liquid equipment thereof, including removing fluid reservoir and defroster, be provided with on the lateral wall of removing the fluid reservoir except that the fluid reservoir air intake and remove the fluid reservoir air outlet, the bottom of removing the fluid reservoir is provided with the liquid outlet, removes the fluid reservoir air outlet and removes the fluid reservoir air intake and sets up respectively in the upper and lower below of defroster, removes fluid reservoir air intake department tangential connection and has the air-supply line for the wind that gets into through removing the fluid reservoir air intake can be rotatory along removing the fluid reservoir inner wall. Organic waste gas gets into except that the fluid reservoir through except that fluid reservoir air intake, because organic waste gas tangential gets into except that the fluid reservoir, organic waste gas can form the whirlwind in removing the fluid reservoir, under the centrifugal force effect, the steam in the waste gas is got rid of on the jar wall of removing the fluid reservoir, leaves along the jar wall again, and through the liquid outlet discharge, waste gas then leaves from except that the fluid reservoir air outlet after the defroster defogging in removing the fluid reservoir. The liquid removing equipment can effectively remove water vapor in organic waste gas and has the advantages of simple structure and low manufacturing cost.

Description

Shunting condensing equipment and remove liquid equipment thereof

Technical Field

The utility model relates to a technical field that organic waste gas administered especially relates to a reposition of redundant personnel condensing equipment and remove liquid equipment thereof.

Background

The bypass condenser is a device for condensing part of VOCs gas into substances such as ethyl acetate, benzene and the like through a built-in condenser. The VOCs waste gas air quantity passing through the condenser is controlled by adjusting a manual valve at the front end of the condenser, so that the function of condensing partial waste gas is achieved. The application of the traditional shunt condenser has a problem in the VOCs treatment process: the condensed low-temperature waste gas and the high-temperature waste gas which is not subjected to condensation treatment are mixed to generate a large amount of water vapor.

Volatile Organic Compounds, commonly referred to as VOCs, are called Volatile Organic Compounds in english, and in China, VOCs refer to Organic Compounds having a saturated vapor pressure of more than 70Pa at normal temperature and a boiling point of 260 ℃ or less at normal pressure, or all Organic Compounds having a vapor pressure of 10Pa or more and volatility at 20 ℃.

SUMMERY OF THE UTILITY MODEL

Therefore, a shunting condensing device and a liquid removing device thereof are needed to solve the problem that a large amount of water vapor is generated after the condensed low-temperature waste gas and the high-temperature waste gas which is not subjected to condensation treatment are mixed.

To achieve the above object, the inventors provide a liquid removing apparatus comprising: remove the fluid reservoir and violently locate the defroster in removing the fluid reservoir, it is that the cross-section is circular shape tank structure to remove the fluid reservoir, it removes the fluid reservoir air intake and removes the fluid reservoir air outlet to be provided with on the lateral wall of fluid reservoir, the bottom that removes the fluid reservoir is provided with the liquid outlet, it sets up respectively in the upper and lower below of defroster to remove the fluid reservoir air outlet and remove the fluid reservoir air intake, it is connected with the air-supply line to remove fluid reservoir air intake department tangential for the wind that gets into through removing the fluid reservoir air intake can be rotatory along removing the fluid reservoir inner wall.

Further, still be provided with the awl fill in the fluid reservoir, the awl is fought and is set up in the below of defroster, the upper and lower both ends that the awl was fought all are provided with the opening, the great opening one end that the awl was fought sets up, and the less opening one end that the awl was fought sets up down.

Further, the cone hopper is connected below the demister.

Further, the bottom of the liquid removing tank is of a conical structure.

Further, the liquid outlet is arranged in the center of the bottom of the liquid removing tank.

Further, the demister is a wire mesh demister.

Further, a liquid outlet pipe is connected to the liquid outlet.

The inventor still provides a reposition of redundant personnel condensing equipment, including reposition of redundant personnel condenser and remove liquid equipment, remove liquid equipment for the liquid equipment that removes among the above-mentioned arbitrary technical scheme, remove liquid equipment and connect in reposition of redundant personnel condenser's air outlet.

Different from the prior art, the technical scheme has the following advantages: organic waste gas gets into except that the fluid reservoir through except that fluid reservoir air intake, because organic waste gas tangential gets into except that the fluid reservoir, organic waste gas can form the whirlwind in removing the fluid reservoir, under the centrifugal force effect, the steam in the waste gas is got rid of on the jar wall of removing the fluid reservoir, leaves along the jar wall again, and through the liquid outlet discharge, waste gas then leaves from except that the fluid reservoir air outlet after the defroster defogging in removing the fluid reservoir. The liquid removing equipment can effectively remove water vapor in organic waste gas and has the advantages of simple structure and low manufacturing cost.

Drawings

FIG. 1 is a perspective view of a fluid removing apparatus according to the present embodiment;

FIG. 2 is a side view of a liquid removing apparatus according to the present embodiment;

FIG. 3 is a cross-sectional view taken at A-A of FIG. 2;

FIG. 4 is a schematic diagram of an internal structure of a liquid removing apparatus according to the present embodiment;

fig. 5 is a schematic structural diagram of a split-flow condensing device according to the present embodiment.

Description of the reference numerals:

01. liquid removal equipment;

1. a liquid removing tank;

11. an air inlet of the liquid removal tank;

12. an air outlet of the liquid removal tank;

131. a left side plate;

132. a right side plate;

133. an upper side plate;

134. a lower side plate;

14. a liquid outlet pipe;

15. a pillar;

2. a demister;

3. a conical hopper;

4. an air inlet pipe;

5. an air outlet pipe;

6. a first pipeline;

7. a second pipeline;

8. a condenser;

9. a manual butterfly valve.

Detailed Description

To explain in detail the possible application scenarios, technical principles, and practical embodiments of the present application, and to achieve the objectives and effects thereof, the following detailed description is given with reference to the accompanying drawings. The embodiments described herein are merely for more clearly illustrating the technical solutions of the present application, and therefore, the embodiments are only used as examples, and the scope of the present application is not limited thereby.

Reference herein to "an embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment can be included in at least one embodiment of the application. The appearances of the phrase "an embodiment" in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or related to other embodiments specifically defined. In principle, in the present application, the technical features mentioned in the embodiments can be combined in any manner to form a corresponding implementable technical solution as long as there is no technical contradiction or conflict.

Unless defined otherwise, technical terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs; the use of relational terms herein is intended only to describe particular embodiments and is not intended to limit the present application.

In the description of the present application, the term "and/or" is a expression for describing a logical relationship between objects, meaning that three relationships may exist, for example a and/or B, meaning: there are three cases of A, B, and both A and B. In addition, the character "/" herein generally indicates that the former and latter associated objects are in a logical relationship of "or".

In this application, terms such as "first" and "second" are 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.

Without further limitation, in this application, the use of "including," "comprising," "having," or other similar expressions in phrases and expressions of "including," "comprising," or "having," is intended to cover a non-exclusive inclusion, and such expressions do not exclude the presence of additional elements in a process, method, or article that includes the recited elements, such that a process, method, or article that includes a list of elements may include not only those elements but also other elements not expressly listed or inherent to such process, method, or article.

As is understood in the examination of the guidelines, the terms "greater than", "less than", "more than" and the like in this application are to be understood as excluding the number; the expressions "above", "below", "within" and the like are understood to include the present numbers. In addition, in the description of the embodiments of the present application, "a plurality" means two or more (including two), and expressions related to "a plurality" similar thereto are also understood, for example, "a plurality of groups", "a plurality of times", and the like, unless specifically defined otherwise.

In the description of the embodiments of the present application, spatially relative expressions such as "central," "longitudinal," "lateral," "length," "width," "thickness," "up," "down," "front," "back," "left," "right," "vertical," "horizontal," "vertical," "top," "bottom," "inner," "outer," "clockwise," "counterclockwise," "axial," "radial," "circumferential," and the like are used, and the indicated orientations or positional relationships are based on the orientations or positional relationships shown in the specific embodiments or drawings and are only for convenience of describing the specific embodiments of the present application or for the convenience of the reader, and do not indicate or imply that the device or component in question must have a specific position, a specific orientation, or be constructed or operated in a specific orientation and therefore should not be construed as limiting the embodiments of the present application.

Unless specifically stated or limited otherwise, the terms "mounted," "connected," "secured," and "disposed" used in the description of the embodiments of the present application are to be construed broadly. For example, the connection can be a fixed connection, a detachable connection, or an integrated arrangement; it can be a mechanical connection, an electrical connection, or a communication connection; they may be directly connected or indirectly connected through an intermediate; which may be communication within two elements or an interaction of two elements. Specific meanings of the above terms in the embodiments of the present application can be understood by those skilled in the art to which the present application pertains in accordance with specific situations.

Referring to fig. 1 to 4, a liquid removing apparatus 01 of the present embodiment includes: remove fluid reservoir 1 and violently locate except that defroster 2 in the fluid reservoir 1, it is that the cross-section is circular shape tank structure to remove fluid reservoir 1, it removes fluid reservoir air intake 11 and removes fluid reservoir air outlet 12 to be provided with on the lateral wall of fluid reservoir 1, the bottom of removing fluid reservoir 1 is provided with the liquid outlet, it sets up respectively in the upper and lower of defroster 2 to remove fluid reservoir air outlet 12 and remove fluid reservoir air intake 11, it has the intake stack to remove fluid reservoir air intake 11 tangential connection for the wind energy that gets into through removing fluid reservoir air intake 11 can be rotatory along removing fluid reservoir 1 inner wall.

The demister 2(demister/mist eliminator) mainly comprises fixing devices such as a wave-shaped blade, a plate, a clamping strip and the like, and is used for removing mist foam (mist droplets) entrained in gas.

The defroster 2 is violently established and is meant that defroster 2 transversely places in removing fluid reservoir 1, and defroster 2 is fixed mutually with the inner wall of removing fluid reservoir 1, and specific fixed mode can be provided with step or a plurality of protruding structure on removing the lateral wall of fluid reservoir 1, and defroster 2 places in the step structure top, perhaps defroster 2 places in a plurality of protruding structure on. More preferably, the shape of the demister 2 is adapted to the side wall of the liquid-removing tank 1, that is, the gas flowing from the lower part of the liquid-removing tank 1 to the upper part of the liquid-removing tank 1 is demisted by the demister 2.

The tangential connection of the air inlet pipe at the air inlet 11 of the liquid removing tank means that at least one side wall of the air inlet pipe is tangential to the side wall of the liquid removing tank 1, so that the organic waste gas entering the liquid removing tank 1 from the air inlet pipe can do centrifugal motion along the inner wall of the liquid removing tank 1.

Specifically, the air inlet pipe has two sets of side plates which are oppositely arranged, namely a left side plate 131, a right side plate 132, an upper side plate 133 and a lower side plate 134, the left side plate 131 and the right side plate 132 are oppositely arranged, the upper side plate 133 and the lower side plate 134 are oppositely arranged, and the left side plate 131 is tangent to the inner wall of the liquid removing tank 1. Preferably, the right side plate 132 is disposed at an equal distance from the left side plate 131, and the upper side plate 133 and the lower side plate 134 have the same shape and size.

A liquid removal apparatus comprising: remove the fluid reservoir and violently locate the defroster in removing the fluid reservoir, it is that the cross-section is circular shape tank structure to remove the fluid reservoir, it removes the fluid reservoir air intake and removes the fluid reservoir air outlet to be provided with on the lateral wall of fluid reservoir, the bottom that removes the fluid reservoir is provided with the liquid outlet, it sets up respectively in the upper and lower below of defroster to remove the fluid reservoir air outlet and remove the fluid reservoir air intake, it is connected with the air-supply line to remove fluid reservoir air intake department tangential for the wind that gets into through removing the fluid reservoir air intake can be rotatory along removing the fluid reservoir inner wall. Organic waste gas gets into except that during fluid reservoir 1 through except that fluid reservoir air intake 11, because organic waste gas tangential gets into except that fluid reservoir 1, organic waste gas can form the whirlwind in removing fluid reservoir 1, under the centrifugal force effect, the steam in the waste gas is got rid of on the jar wall of removing fluid reservoir 1, leaves along the jar wall again, and through the liquid outlet discharge, waste gas then leaves from except that fluid reservoir air outlet 12 after the defogger 2 defogging in removing fluid reservoir 1. This remove liquid equipment 01 not only can effectively get rid of the steam in the organic waste gas, and still have simple structure, advantage that the cost is with low costs.

In some preferred embodiments, a conical hopper 3 is further disposed in the liquid removal tank 1, the conical hopper 3 is disposed below the demister 2, openings are disposed at both upper and lower ends of the conical hopper 3, one end of the conical hopper 3 with a larger opening faces upward, and one end of the conical hopper 3 with a smaller opening faces downward.

Concrete awl is fought 3 and is fought 3 structures including conical upward awl and cylindrical lower awl, and upward awl is fought the lower extreme of 3 structures and has been seted up the through-hole, and the lower awl is fought 3 structures and all sets up the through-hole from top to bottom, and upward awl is fought the lower extreme of 3 structures and is fought the upper end looks adaptation connection of 3 structures with lower awl, and is concrete, upward awl is fought 3 structures and is fought 3 structures down and fix through the welded mode, perhaps upward awl is fought 3 structures and is fought 3 structures as an organic whole structure with lower awl.

Preferably, the size of the upper opening of the conical hopper 3 is matched with the size of the demister 2, that is, the organic waste gas entering the liquid removal tank 1 from the liquid removal tank air inlet 11 passes through the lower opening of the conical hopper 3, upwards passes through the demister 2 for demisting, and then leaves from the liquid removal tank air outlet 12.

The beneficial effect lies in, can prevent that after organic waste gas gets into except that fluid reservoir 1, the part waste gas that is close to defroster 2 is not enough centrifugation just directly through defroster 2. Set up the awl and fight 3 backs, organic waste gas tangential entering removes fluid reservoir 1 because the lateral wall that the awl was fought 3 shelters from, and organic waste gas is along removing fluid reservoir 1 centrifugal motion, and the great steam of quality is by centrifugation to the periphery of air current, along with the continuous increase of tolerance, is close to removing fluid reservoir 1 central part, the less organic waste gas of steam just can follow the lower extreme opening upward movement that the awl was fought 3, leaves from removing fluid reservoir air outlet 12 after the defogger 2 defogging again.

In certain preferred embodiments, the cone 3 is connected below the demister 2. Its beneficial effect lies in, organic waste gas gets into defroster 2 behind awl fill 3, and can not get into defroster 2 from the gap that awl fill 3 and defroster 2 for the tangential gets into defroster 2 of reentrant defroster 2 after can abundant centrifugation of organic waste gas that removes fluid reservoir 1, can effectively prolong defroster 2's life, also is favorable to improving the steam of organic waste gas and gets rid of efficiency.

In certain preferred embodiments, the bottom of the liquid removal tank 1 is of a tapered configuration. Namely, the height of the center of the bottom of the liquid removing tank 1 is lower than the height of the edge of the bottom of the liquid removing tank 1. The beneficial effects are that, after organic waste gas is at the centrifugation in the fluid removal tank 1, steam in the organic waste gas is got rid of on the jar wall of fluid removal tank 1, flows to the bottom of fluid removal tank 1 through the jar body of fluid removal tank 1, and the discharge of liquid can be accelerated to the toper bottom.

In certain preferred embodiments, the liquid outlet is arranged at the center of the bottom of the liquid removal tank 1.

In certain preferred embodiments, the mist eliminator 2 is a wire mesh mist eliminator 2. The wire mesh demister 2 is generally made of metal wires with the diameter of 0.10mm to 0.28mm or engineering plastics (PP, PTFE, FEP, PVDF and the like) by weaving a wire mesh in a special warp and weft mode, and then the woven wire mesh is pressed into corrugations with a certain angle. The corrugated silk screen is manufactured into various specifications and sizes. The wire mesh demister 2 has the advantages of simple structure, light weight, large porosity, small pressure drop, large contact surface area and high defoaming efficiency, and is convenient to install, operate and maintain and long in service life. And the method can separate the fog in the gas, improve the operation condition, optimize the process index, reduce the corrosion of equipment, prolong the service life of the equipment, improve the treatment capacity, recover valuable substances, protect the environment and reduce the air pollution.

In certain preferred embodiments, an outlet pipe 14 is connected to the outlet. The liquid outlet can discharge the water vapor to be discharged in the liquid removing tank into a designated container or a designated position through the liquid outlet pipe 14.

In some preferred embodiments, a plurality of pillars 15 are further disposed below the liquid removal tank, and specifically, the pillars 15 are made of angle steel, steel material, iron columns or other materials and are used for supporting and fixing the liquid removal tank 1. The support column 15 can be fixed at the bottom of the liquid removing tank 1 by welding or can be detachably connected at the bottom of the liquid removing tank 1 by a connecting piece. The length of each strut may be set to the same length.

Referring to fig. 5, the inventor further provides a split condensing apparatus, which includes a split condenser 8 and a liquid removing device 01, where the liquid removing device 01 is the liquid removing device 01 in any of the above technical solutions, and the liquid removing device 01 is connected to an air outlet of the split condenser 8.

Shunt condenser 8 includes air-supply line 4, goes out tuber pipe 5, first pipeline 6, second pipeline 7 and condenser 8, air-supply line 4 is linked together through first pipeline 6 and second pipeline 7 and play tuber pipe 5 respectively, condenser 8 sets up on first pipeline 6, it connects in the air outlet of a tuber pipe 5 to remove liquid equipment 01. The first pipeline 6 and the second pipeline 7 are both provided with a manual butterfly valve 9, the manual butterfly valve 9 on the first pipeline 6 is arranged in front of the condenser 8, the air quantity of waste gas entering the condenser 8 can be adjusted by adjusting the opening of the manual butterfly valve 9, the waste gas after condensation treatment is mixed with the waste gas which is not subjected to waste gas treatment and passes through an air outlet pipe to generate a large amount of water vapor, the waste gas enters the liquid removing device 01, the organic waste gas tangentially enters the liquid removing tank 1 from an air inlet 11 of the liquid removing tank, and due to the centrifugal force, the moisture in the waste gas is thrown onto the wall of the liquid removing tank 1 to flow down and is discharged through a liquid discharge pipe; then the waste gas passes through the lower extreme opening of awl fill 3 and upwards passes through silk screen mist eliminator 2 and further gets rid of the water liquid of waste gas. Through the two-stage liquid removal, the moisture in the waste gas is removed cleanly, and the waste gas enters the rear end through the air outlet 12 of the liquid removal tank.

The manual butterfly valve has the following advantages: the valve is convenient and quick to open and close, saves labor, has small fluid resistance and can be operated frequently. The valve has the advantages of simple structure, small overall dimension, short structural length, small volume and light weight, and is suitable for large-caliber valves. Less liquid is accumulated at the mouth of the pipeline. At low pressures, good sealing can be achieved. In other embodiments, other types of valves, gate valves, ball valves, etc. may be disposed on the first and second pipelines.

Finally, it should be noted that, although the above embodiments have been described in the text and drawings of the present application, the scope of the patent protection of the present application is not limited thereby. All technical solutions generated by replacing or modifying the equivalent structure or the equivalent flow described in the text and the drawings of the present application and directly or indirectly implementing the technical solutions of the above embodiments in other related technical fields and the like based on the substantial idea of the present application are included in the scope of the patent protection of the present application.

Claims

1. A fluid removal apparatus, comprising: the liquid removing tank is of a tank body structure with a circular cross section, a liquid removing tank air inlet and a liquid removing tank air outlet are formed in the side wall of the liquid removing tank, a liquid outlet is formed in the bottom of the liquid removing tank, the liquid removing tank air outlet and the liquid removing tank air inlet are formed in the upper portion and the lower portion of the demister respectively, an air inlet pipe is tangentially connected to the liquid removing tank air inlet, and accordingly air entering through the liquid removing tank air inlet can rotate along the inner wall of the liquid removing tank.

2. The liquid removal apparatus of claim 1, wherein: still be provided with the awl fill in the fluid removal tank, the awl is fought and is set up in the below of defroster, the upper and lower both ends that the awl was fought all are provided with the opening, the great opening one end that the awl was fought sets up, and the less opening one end that the awl was fought sets up down.

3. The liquid removal apparatus of claim 2, wherein: the cone hopper is connected below the demister.

4. The liquid removal apparatus of claim 1, wherein: the bottom of the liquid removal tank is of a conical structure.

5. The liquid removal apparatus of claim 1 or 4, wherein: the liquid outlet is arranged in the center of the bottom of the liquid removing tank.

6. The liquid removal apparatus of claim 1, wherein: the demister is a wire mesh demister.

7. The liquid removal apparatus of claim 1, wherein: and a liquid outlet pipe is connected at the liquid outlet.

8. A reposition of redundant personnel condensing equipment which characterized in that: the device comprises a shunting condenser and liquid removing equipment, wherein the liquid removing equipment is the liquid removing equipment in any one of the claims, and the liquid removing equipment is connected to an air outlet of the shunting condenser.