CN210751920U

CN210751920U - Condensing device

Info

Publication number: CN210751920U
Application number: CN201921469750.8U
Authority: CN
Inventors: 金禹东; 丁天赠; 尤志权
Original assignee: Jiangyin Rongxin Plasticizing Co ltd
Current assignee: Jiangyin Rongxin Plasticizing Co ltd
Priority date: 2019-09-05
Filing date: 2019-09-05
Publication date: 2020-06-16
Anticipated expiration: 2029-09-05

Abstract

The utility model relates to a condensing unit, comprising a tower body, be equipped with condenser pipe and baffle in the tower body, the baffle is located the top of condenser pipe and uses the central line of tower body to crisscross the setting as the center, the below of baffle is equipped with the barb, outside the tower body was stretched out at the both ends of condenser pipe, the tower body bottom is equipped with the condensate export, and the lower part is equipped with the tail gas entry, and the top is equipped with the tail gas export, the tail gas entry is located the below of condenser pipe, the tower body is equipped with outward and presss from both sides the cover, it is equipped with and presss from both sides. The utility model discloses guaranteed the increase of waste gas circulation route, prolonged the condensation time for the possibility increase that waste gas condenses effectively promotes the recovery of tail gas, and the mode of condensation can be retrieved wherein most useful material, can the energy recovery, is an effective purifier of energy-conservation but environmental protection again.

Description

Condensing device

Technical Field

The utility model relates to a waste gas treatment equipment technical field, concretely relates to condensing equipment.

Background

The reaction kettle is a comprehensive reaction vessel, is often applied to different fields such as petroleum, chemical engineering, rubber, pesticides, dyes, medicines, foods and the like, and can complete preset reaction steps with higher automation degree for feeding, reaction and discharging in different technological processes. The reaction steps are usually carried out at high temperature and high pressure, and the high temperature and high pressure in the reaction kettle must be released after one process flow is finished, so that waste gas is generated, which is often called as reaction kettle emptying waste gas. Many enterprises discharge the tail gas only by simply adsorbing the tail gas through the adsorption tower, so that the recovery and the utilization of harmful components in the tail gas are not high, and the temperature of the tail gas is not reduced; some enterprises have carried out condensation preliminary treatment before the adsorption tower adsorbs, but condenser simple structure, it is lower to harmful ingredient's condensation efficiency, and tail gas treatment is not thorough, is difficult to reach emission standard.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to overcome the aforesaid not enough, provide a condensing equipment, the comdenstion water gets into the clamp cover and the condenser pipe of condensing tower simultaneously, condenses the tail gas that gets into in the condensing tower, and the condenser pipe is the heliciform, is equipped with the baffle in the top of condenser pipe, the baffle is equipped with the barb, and baffle and spiral helicine condenser pipe have stopped gaseous direct tail gas entry to the possibility of tail gas export, have guaranteed the increase of waste gas circulation route, have prolonged the condensation time for the possibility that waste gas condenses increases, effectively promotes the recovery of tail gas, and wherein most useful material can be retrieved to the mode of condensation, can retrieve the energy, is an effective purifier of energy-conservation and environmental protection again.

The purpose of the utility model is realized like this:

the utility model provides a condensing equipment, includes the tower body, be equipped with condenser pipe and baffle in the tower body, the baffle is located the top of condenser pipe and uses the central line of tower body to crisscross the setting as the center, the below of baffle is equipped with the barb, outside the tower body was stretched out at the both ends of condenser pipe, the tower body bottom is equipped with the condensate export, and the lower part is equipped with the tail gas entry, and the top is equipped with the tail gas export, the tail gas entry is located the below of condenser pipe, the tower body is equipped with outward and presss from both sides the cover, it is equipped with and presss.

Preferably, the condenser pipe is spiral, and a condenser pipe water inlet and a condenser pipe water outlet of the condenser pipe are located at the bottom of the condenser pipe and are located on the same horizontal plane.

Preferably, the condenser pipe is formed by serially connecting an even number of spiral single pipes, each spiral single pipe is located at the same height, the distance from the center line of each spiral single pipe to the center line of the tower body 1 is equal, and all spiral single pipes share one condenser pipe water inlet and one condenser pipe water outlet.

The utility model has the advantages that:

the utility model discloses the comdenstion water gets into the clamp cover and the condenser pipe of condensing tower simultaneously, condenses the tail gas that gets into in the condensing tower, and the condenser pipe is the heliciform, is equipped with the baffle in the top of condenser pipe, the baffle is equipped with the barb, and baffle and spiral helicine condenser pipe have stopped gaseous possibility of directly entering into the tail gas export from the tail gas, have guaranteed the increase of waste gas circulation route, have prolonged the condensation time for the possibility that waste gas condenses increases, effectively promotes the recovery of tail gas, and the mode of condensation can be retrieved wherein most useful material, can retrieve the energy, is an effective purifier of energy-conservation and environmental protection.

Drawings

Fig. 1 is a schematic structural diagram of the present invention.

Fig. 2 is a front view of the condensation duct.

Wherein: a tower body 1; a condensate outlet 1.1; a tail gas inlet 1.2; a tail gas outlet 1.3; a jacket 2; a jacket water inlet 2.1; a jacket water outlet 2.2; a condenser tube 3; a water inlet of the condensation pipe is 3.1; a water outlet of the condensation pipe is 3.2; 3.3, spiral single tube; a baffle 4; barb 4.1.

Detailed Description

Referring to fig. 1 and 2, the utility model relates to a condensing device, which comprises a tower body 1, a condensing pipe 3 and a baffle 4 are arranged in the tower body 1, the baffle plates 4 are positioned above the condensing pipe 3 and are staggered by taking the central line of the tower body 1 as the center, the barbs 4.1 are arranged below the baffle 4, the barbs 4.1 incline downwards to play a good role in blocking, so that the time for the tail gas to reach the tail gas outlet is prolonged, the condensation effect is prolonged, the two ends of the condenser pipe 3 extend out of the tower body 1, the bottom of the tower body 1 is provided with a condensate outlet 1.1, the lower part is provided with a tail gas inlet 1.2, the top is provided with a tail gas outlet 1.3, the tail gas inlet 1.2 is positioned below the condensing pipe 3, a jacket 2 is arranged outside the tower body 1, the jacket 2 is provided with a jacket water inlet 2.1 and a jacket water outlet 2.2, the jacket water outlet 2.2 is positioned at the upper part of the jacket 2, and the jacket water inlet 2.1 is positioned at the lower part of the jacket 2.

Condenser pipe 3 is the heliciform, condenser pipe water inlet 3.1 and condenser pipe delivery port 3.2 of condenser pipe 3 are located the bottom of condenser pipe 3, and are in on the same horizontal plane. And the water inlet 3.1 and the water outlet 3.2 of the condensation pipe are positioned at two sides of the tower body.

The condenser pipe 3 is formed by connecting an even number of spiral single pipes 3.3 in series, each spiral single pipe 3.3 is positioned at the same height, the distance from the center line of each spiral single pipe 3.3 to the center line of the tower body 1 is equal, and all the spiral single pipes 3.3 share one condenser pipe water inlet 3.1 and one condenser pipe water outlet 3.2.

The working principle is as follows: jacket water inlet 2.1 and condenser pipe water inlet 3.1 insert the cooling water simultaneously, tail gas that comes out from reation kettle gets into tail gas entry 1.2, through the dual condensation of jacket 6 and condenser pipe 7, the buffering of baffle 8 blocks, the condensation is effectual, the possibility increase that gets waste gas and condense, effectively promote the recovery of tail gas, can retrieve wherein most useful material, the useful material of recovery is discharged from condensate export 1.1 and is retrieved, noncondensable gas gets into next process from tail gas export 1.3.

In addition to the above embodiments, the present invention also includes other embodiments, and all technical solutions formed by equivalent transformation or equivalent replacement should fall within the protection scope of the claims of the present invention.

Claims

1. A condensing unit, characterized by: including tower body (1), be equipped with condenser pipe (3) and baffle (4) in tower body (1), baffle (4) are located the top of condenser pipe (3) and use the central line of tower body (1) to set up for the center is crisscross, the below of baffle (4) is equipped with barb (4.1), outside tower body (1) was stretched out at the both ends of condenser pipe (3), tower body (1) bottom was equipped with condensate export (1.1), and the lower part is equipped with tail gas entry (1.2), and the top is equipped with tail gas export (1.3), tail gas entry (1.2) are located the below of condenser pipe (3), tower body (1) is equipped with outward and presss from both sides cover (2), it is equipped with and presss from both sides cover water inlet (2.1) and presss from both sides cover delivery port (2.2) to press.

2. A condensing unit according to claim 1, characterized in that: condenser pipe (3) are the heliciform, condenser pipe water inlet (3.1) and condenser pipe delivery port (3.2) of condenser pipe (3) are located the bottom of condenser pipe (3), and are in on the same horizontal plane.

3. A condensing unit according to claim 1 or 2, characterized in that: the condenser pipe (3) is formed by connecting an even number of spiral single pipes (3.3) in series, each spiral single pipe (3.3) is positioned at the same height, the distance from the center line of each spiral single pipe (3.3) to the center line of the tower body (1) is equal, and all spiral single pipes (3.3) share one condenser pipe water inlet (3.1) and one condenser pipe water outlet (3.2).