Material concentration and evaporation separator system

Abstract

The utility model belongs to the technical field of evaporation separators, and provides a material concentration evaporation separator system which comprises a heating mechanism, a separation mechanism and a condensation mechanism, the heating mechanism is connected with the separation mechanism, and a separator is connected between the separation mechanism and the condensation mechanism; the separation mechanism comprises a first separation tank and a second separation tank, the first separation tank is arranged at the top of the second separation tank and communicated with the first separation tank, an inlet of the separator is connected with the first separation tank, and an outlet of the separator is connected with the condensation mechanism. By additionally arranging the separator, the first separation tank, the first U-shaped pipe and the second U-shaped pipe, the system can effectively separate materials from steam, reduce the loss of the materials, and improve the product yield and the recovery rate of the materials. According to the system, sufficient separation of materials is ensured through multiple times of gas-liquid separation in the first separation tank, the second separation tank and the separator, the loss of the materials is reduced, the production efficiency is improved, the consumption of energy and resources is reduced, and the overall economic benefit is improved.

Description

TECHNICAL FIELD

[0001] The utility model belongs to evaporative separator technical field, concretely relates to a material concentration evaporative separator system. BACKGROUND

[0002] The secondary steam port of the common concentration evaporative separator is rarely equipped with a secondary steam liquid separation and recovery system, and even if the secondary steam liquid separation and recovery system is installed, the effect is not obvious, and the secondary steam carrying material interception rate can only reach below 40%. The original equipment mainly has the following shortcomings:

[0003] (1) The secondary steam containing a large number of liquid droplets is not fully separated, directly enters the condenser, and causes material running;

[0004] (2) Even if the secondary steam recovery system is installed, the effect is not very ideal, and a lot of material liquid still directly enters the condenser with the secondary steam, causing material running, affecting product yield, increasing product cost, and seriously affecting product economic benefits;

[0005] Therefore, the present application provides a material concentration evaporative separator system to solve the above technical problems. CONTENT OF THE UTILITY MODEL

[0006] The utility model aims at overcoming the shortcomings of the prior art, providing a material concentration evaporative separator system, thereby improving product yield, reducing product cost, and improving production efficiency.

[0007] The utility model aims at overcoming the shortcomings of the prior art, providing a material concentration evaporative separator system, thereby improving product yield, reducing product cost, and improving production efficiency.

[0008] The utility model provides a material concentration evaporative separator system, including heating mechanism, separation mechanism and condensing mechanism, heating mechanism is connected with separation mechanism, separation mechanism and condensing mechanism are connected with the separator between, separation mechanism includes first separation tank and second separation tank, just first separation tank sets up at the top of second separation tank, and it is linked with second separation tank, the import of separator is connected with first separation tank, and the export is connected with condensing mechanism.

[0009] Further, the first separation tank includes a tank body connected to the top of the second separation tank, and a first separation pipe and a second separation pipe are sequentially and spacedly arranged in the tank body from the inside to the outside, the first separation pipe and the second separation pipe are connected in communication, and three channels in communication are formed in the tank body.

[0010] Further, the bottom of the first separation pipe is in communication with the top of the second separation tank, and the top of the second separation pipe is connected to the inner top of the tank body, and the secondary steam separated by the second separation tank enters the first separation pipe, the second separation pipe and the tank body in sequence.

[0011] Further, the first separation tube comprises a first tube body in communication with the top of the second separation tank, and a first spiral blade is arranged on the outer periphery of the first tube body.

[0012] Further, the second separation tube comprises a second tube body connected with the top of the tank body, and a second spiral blade is arranged on the outer periphery of the second tube body.

[0013] Further, the side wall of the tank body is provided with a steam outlet pipe, the outlet of the steam outlet pipe is connected with the inlet of the separator, and the outlet of the separator is connected with the inlet of the condensing mechanism.

[0014] Further, the tank body and the second separation tank are communicated through a first U-shaped pipe.

[0015] Further, the separator and the second separation tank are communicated through a second U-shaped pipe.

[0016] Further, the bottom of the second U-shaped pipe is provided with a liquid outlet, and a valve is arranged on the liquid outlet.

[0017] Compared with the prior art, the technical scheme provided by the utility model has the following beneficial effects:

[0018] (1) The utility model discloses a material concentration evaporation separator system, which is characterized in that a separator is arranged between the separation mechanism and the condensing mechanism, and a first separation tank is arranged at the top of the separation mechanism, so that the system can effectively separate the material and the steam, reduce the loss of the material and improve the product yield.

[0019] (2) The utility model discloses a material concentration evaporation separator system, which is characterized in that a first U-shaped pipe is arranged between the tank body and the second separation tank, and a second U-shaped pipe is arranged between the separator and the second separation tank, so that the recovery rate of the material is improved, the loss of the material is reduced, and the interception rate of the secondary steam carrying the material reaches more than 98%, thereby reducing the problem of material running directly into the condenser with the secondary steam.

[0020] (3) The system is simple to operate, has low failure rate, long maintenance period and improved overall economic benefit. BRIEF DESCRIPTION OF DRAWINGS

[0021] The drawings incorporated into the specification and forming part of the specification, together with the specification, serve to explain the principle of the utility model.

[0022] In order to more clearly illustrate the technical solutions of the embodiments of the present application or the prior art, the following will briefly introduce the drawings needed to be used in the embodiments or prior art description, and obviously, for those skilled in the art, other drawings can also be obtained without creative labor under the premise of these drawings.

[0023] Fig. 1 The structure diagram of the material concentration evaporation separator system of the present application is shown in the figure.

[0024] Fig. 2 The structure diagram of the heating mechanism-first separation tank of the present application is shown in the figure.

[0025] Among them:

[0026] 1 is a heating mechanism;

[0027] 2 is a separation mechanism; 21 is a first separation tank; 22 is a second separation tank;

[0028] 21 is a first separation tank; 211 is a first separation pipe; 212 is a second separation pipe; 213 is a tank body;

[0029] 3 is a condensing mechanism;

[0030] 4 is a separator;

[0031] 5 is a first U-shaped pipe;

[0032] 6 is a second U-shaped pipe. DETAILED DESCRIPTION

[0033] Hereinafter, the exemplary embodiments will be described in detail with reference to the accompanying drawings. In the following description, the same numbers are assigned to the same components, and a repeated description will be omitted. The embodiments described in the following exemplary embodiments do not represent all the embodiments consistent with the present application. Rather, they are merely examples of apparatuses consistent with some aspects of the present application as detailed in the appended claims.

[0034] In order to make those skilled in the art better understand the technical solutions of the present application, the present application will be further described in detail below in combination with the drawings and embodiments.

[0035] Referring to Figs. 1-2The utility model provides a kind of material concentration evaporative separator system, including heating mechanism 1, separation mechanism 2 and condensing mechanism 3, the heating mechanism 1 is connected with the separation mechanism 2, and the separation mechanism 2 and condensing mechanism 3 are connected with separator 4;The separation mechanism 2 includes first separation tank 21 and second separation tank 22, and the first separation tank 21 is arranged at the top of second separation tank 22, and is communicated with second separation tank 21, the inlet of the separator 4 is connected with first separation tank 21, and the outlet is connected with condensing mechanism 3.

[0036] Specifically, in the embodiment, the heating mechanism 1 and condensing mechanism 3 are both devices in the prior art, and the related structure is disclosed in Chinese Patent No. CN214075076U, which will not be repeated here. The separator 4 can use a baffle separator to separate the secondary steam entering the separation mechanism 2 again.

[0037] Further, the first separation tank 21 includes a tank body 213 connected to the top of the second separation tank 22, and a first separation pipe 211 and a second separation pipe 212 are sequentially and spacedly arranged inside the tank body 213 from inside to outside, and the first separation pipe 211 and the second separation pipe 212 are communicated to form three channels in the tank body 213.

[0038] Further, the bottom of the first separation pipe 211 is communicated with the top of the second separation tank 22, and the top of the second separation pipe 212 is connected to the inner top of the tank body 213. The secondary steam separated by the second separation tank 22 enters the first separation pipe 211, the second separation pipe 212 and the tank body 213 sequentially.

[0039] Further, the first separation pipe 211 includes a first pipe body communicated with the top of the second separation tank 22, and a first spiral blade is arranged on the outer periphery of the first pipe body.

[0040] Further, the second separation pipe 212 includes a second pipe body connected to the top of the tank body 213, and a second spiral blade is arranged on the outer periphery of the second pipe body.

[0041] Specifically, in the embodiment, the material-carrying liquid enters the three channels at high speed, and when entering the channel between the first separation pipe 211 and the second separation pipe 212, the liquid moves upward along the first spiral blade to contact the high-speed entering secondary steam again, and the liquid vaporizes again under high temperature conditions to separate gas and liquid. When the remaining liquid enters the channel between the second separation pipe 212 and the tank body 213, the above process is repeated to separate gas and liquid again.

[0042] Further, the side wall of the tank body 213 is provided with a steam outlet pipe, the outlet of the steam outlet pipe is connected with the inlet of the separator 4, the outlet of the separator 4 is connected with the inlet of the condensing mechanism 3.

[0043] Further, the tank body 213 and the second separation tank 22 are communicated through the first U-shaped pipe 5.

[0044] Further, the separator 4 and the second separation tank 22 are communicated through the second U-shaped pipe 6.

[0045] Further, the bottom of the second U-shaped pipe 6 is provided with a liquid outlet, and the liquid outlet is provided with a valve.

[0046] Specifically, in the embodiment, the bottom of the first U-shaped pipe 5 and the second U-shaped pipe 6 is provided with a liquid seal due to the liquid separation, the liquid seal prevents the backflow of the gas, and the liquid after the gas-liquid separation can be recycled through the first U-shaped pipe 5 and the second U-shaped pipe 6. When the system stops running, the valve connected with the liquid outlet at the bottom of the second U-shaped pipe 6 is used to discharge the impurities and residual liquid accumulated in the pipe.

[0047] The above only is the specific implementation manner of the present application, and enables the person skilled in the art to understand or realize the present application. Various modifications to these embodiments will be apparent to those skilled in the art, and the general principles defined herein can be implemented in other embodiments without departing from the spirit or scope of the present application.

[0048] It should be understood that the present application is not limited to the above described and that various modifications and changes can be made without departing from the scope thereof. The scope of the present application is limited only by the claims that follow.

Claims

1. A material concentration evaporation separator system, characterized in that, It includes a heating mechanism (1), a separation mechanism (2) and a condensation mechanism (3), wherein the heating mechanism (1) is connected to the separation mechanism (2), and a separator (4) is connected between the separation mechanism (2) and the condensation mechanism (3); The separation mechanism (2) includes a first separation tank (21) and a second separation tank (22), and the first separation tank (21) is located on top of the second separation tank (22) and communicates with the second separation tank (22). The inlet of the separator (4) is connected to the first separation tank (21), and the outlet is connected to the condensation mechanism (3).

2. The material concentration evaporation separator system according to claim 1, characterized in that, The first separation tank (21) includes a tank body (213) connected to the top of the second separation tank (22). The tank body (213) is provided with a first separation pipe (211) and a second separation pipe (212) arranged sequentially from the inside to the outside. The first separation pipe (211) and the second separation pipe (212) are connected to each other, forming three interconnected channels inside the tank body (213).

3. The material concentration evaporation separator system according to claim 2, characterized in that, The bottom of the first separation pipe (211) is connected to the top of the second separation tank (22), and the top of the second separation pipe (212) is connected to the inner top of the tank body (213). The secondary steam separated by the second separation tank (22) enters the first separation pipe (211), the second separation pipe (212) and the tank body (213) in sequence.

4. The material concentration evaporation separator system according to claim 2, characterized in that, The first separation tube (211) includes a first tube body that communicates with the top of the second separation tank (22), and a first spiral blade is provided on the outer periphery of the first tube body.

5. The material concentration evaporation separator system according to claim 2, characterized in that, The second separation tube (212) includes a second tube body connected to the top of the tank body (213), and a second spiral blade is provided on the outer periphery of the second tube body.

6. The material concentration evaporation separator system according to claim 2, characterized in that, The side wall of the tank (213) is provided with a steam outlet pipe, the outlet of which is connected to the inlet of the separator (4), and the outlet of the separator (4) is connected to the inlet of the condensing mechanism (3).

7. The material concentration evaporation separator system according to claim 2, characterized in that, The tank (213) and the second separation tank (22) are connected by a first U-shaped pipe (5).

8. The material concentration evaporation separator system according to claim 1, characterized in that, The separator (4) and the second separation tank (22) are connected by a second U-shaped pipe (6).

9. The material concentration evaporation separator system according to claim 8, characterized in that, The bottom of the second U-shaped tube (6) is provided with a liquid outlet, and a valve is provided on the liquid outlet.

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