CN112156489B

CN112156489B - MVR evaporator and MVR evaporation system

Info

Publication number: CN112156489B
Application number: CN202011068301.XA
Authority: CN
Inventors: 陈悦
Original assignee: Shenzhen Bluestone Environmental Protection Technology Co ltd
Current assignee: Shenzhen Bluestone Environmental Protection Technology Co ltd
Priority date: 2017-09-26
Filing date: 2017-09-26
Publication date: 2022-08-12
Anticipated expiration: 2037-09-26
Also published as: CN107469370B; CN112156489A; CN107469370A

Abstract

The embodiment of the invention discloses an MVR evaporator, which comprises a shell (1) and a plurality of heat exchange tubes (2) vertically arranged in the shell (1), wherein the bottom surface (11) of the shell (1) is inclined, so that the heat exchange tubes (2) on the bottom surface (11) have various lengths, and a liquid outlet (13) is formed in a side wall (12) of the shell (1) connected with the lowest part of the bottom surface (11). The MVR evaporator in the technical scheme can reduce the risk of mixing distilled water and polluting substances, and is beneficial to improving the quality of the final outlet water of the MVR evaporation system; in addition, the MVR evaporator has a larger heat exchange area, and the heat exchange efficiency of the MVR evaporator is improved.

Description

MVR evaporator and MVR evaporation system

Technical Field

The application relates to MVR evaporation equipment field especially relates to an MVR evaporimeter. In addition, the application also relates to an MVR evaporation system.

Background

The MVR (Mechanical Vapor Recompression) evaporation technology has been widely used in the industries of chemical industry, pharmaceutical industry, food, beverage, environmental protection, etc. due to its outstanding energy-saving property. In the MVR evaporation system, the MVR evaporator is a core device.

The MVR evaporator uses low temperature and low pressure steaming technology and clean energy (i.e., electrical energy) to generate steam, which separates the moisture in the medium. Specifically, the liquid to be treated is in the tube pass of the evaporator, and under certain temperature and pressure, water reaches the boiling point and is vaporized, and the liquid is evaporated from the tube pass of the MVR evaporator to form low-quality steam. Low-quality steam is recompressed through the vapor compressor, the temperature and the pressure are improved, the high-quality saturated steam is changed, the saturated steam enters the shell pass of the MVR evaporator, heat exchange is carried out through the heat exchange tube and liquid in the tube pass, and heat required by liquid evaporation in the tube pass is maintained. The circulation provides heat required by the evaporated liquid in the tube pass, and reduces the requirement on external energy. Meanwhile, the water vapor in the shell pass is condensed into distilled water after heat exchange, so that the separation of water and other substances in the liquid to be treated is realized.

When the MVR evaporator is used for treating a liquid with complex components, such as industrial wastewater, the distilled water condensed and discharged from the shell pass may be mixed with polluting substances, which affects the quality of the final effluent water, and thus, a problem to be solved by those skilled in the art is urgently needed.

Disclosure of Invention

In order to solve the technical problem, the application provides a new MVR evaporator to reduce the risk that distilled water and polluting substances mix, help promoting the quality of MVR evaporation system final water.

Specifically, the first aspect provides an MVR evaporimeter, including casing and a plurality of vertical setting in heat exchange tube in the casing, the bottom surface slope of casing makes a plurality of on the bottom surface the heat exchange tube has multiple length, with the bottom of bottom surface is connected it has the liquid outlet to open on the lateral wall of casing.

With reference to the first aspect, in a first possible implementation manner of the first aspect, the heat exchange tube includes a central tube disposed in the center of the shell, and short and long tubes disposed on the periphery of the central tube, and a tube diameter of the central tube is greater than a tube diameter of the short and long tubes.

With reference to the first aspect and the foregoing possible implementation manners, in a second possible implementation manner of the first aspect, the bottom surface is a plane that is obliquely arranged.

With reference to the first aspect and the foregoing possible implementation manners, in a third possible implementation manner of the first aspect, the bottom surface is a curved surface that is obliquely arranged.

With reference to the first aspect and the foregoing possible implementation manners, in a fourth possible implementation manner of the first aspect, the liquid discharge device further includes an expanding pipe connected to the liquid discharge port, a pipe diameter of one end of the expanding pipe is smaller than a pipe diameter of the other end, and the end with the smaller pipe diameter is connected to the liquid discharge port.

With reference to the fourth implementation manner of the first aspect, in a fifth possible implementation manner of the first aspect, a first baffle is fixedly connected to the inner top of the divergent pipe, and a gap is formed between the bottom end of the first baffle and the bottom of the divergent pipe.

With reference to the fifth implementation manner of the first aspect, in a sixth possible implementation manner of the first aspect, a second baffle is further fixedly connected to the top of the inside of the divergent tube, a gap is formed between the bottom end of the second baffle and the bottom of the divergent tube, and porous filler is filled in the divergent tube between the first baffle and the second baffle.

With reference to the fourth or fifth implementation manner of the first aspect, in a seventh possible implementation manner of the first aspect, the pipe diameter of the divergent pipe gradually increases from one end to the other end.

With reference to the fourth or fifth implementation manner of the first aspect, in an eighth possible implementation manner of the first aspect, the divergent pipe includes at least one straight pipe section and at least one inclined pipe section, the straight pipe section is connected to the inclined pipe section at intervals, and a caliber of one end of the inclined pipe section is the same as a caliber of the straight pipe section connected to the inclined pipe section.

In a second aspect, an MVR evaporation system is provided, comprising any one of the MVR evaporators of the first aspect, a vapor-liquid separator, a vapor compressor, a condensate separator, and a vent line; the gas-liquid separator is arranged above the MVR evaporator and is communicated with the tube pass of the MVR evaporator; the air inlet of the steam compressor is communicated with the gas-liquid separator, and the air outlet of the steam compressor is communicated with the shell pass of the MVR evaporator; the condensate separator is communicated with a liquid outlet of the MVR evaporator; the exhaust pipeline is communicated with the shell pass of the MVR evaporator.

In the MVR evaporator in the scheme of the application, the gravity of condensed liquid is utilized to form natural and stable flow, and distilled water and condensed polluting substances are prevented from being stirred and mixed in the flowing process; in the second aspect, condensed liquid in the shell pass is removed at the first time without remaining in the shell pass, so that the situation that polluting substances are continuously accumulated on the surface of distilled water is reduced, and more polluting gases are discharged through a gas discharge pipeline; in the third aspect, relatively more polluting substances are condensed at the longer heat exchange tube, and the position of the polluting substances away from the liquid outlet is closer, so that the polluting substances can be discharged out of the shell side through the liquid outlet as soon as possible, and the retention time of the polluting substances in the shell side is reduced. The three aspects of effects are mutually cooperated, so that the risk of mixing distilled water and polluting substances is reduced, the condensation of polluting gas and polluting small droplets is reduced, and the quality of the final outlet water of the MVR evaporation system is improved. In addition, because no condensed liquid occupies the heat exchange surface of the heat exchange tube in the shell pass, the MVR evaporator is enabled to have a larger practical heat exchange area, and the heat exchange efficiency of the MVR evaporator is improved.

Drawings

In order to more clearly explain the technical solution of the present application, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious to those skilled in the art that other drawings can be obtained according to the drawings without any creative effort.

FIG. 1 is a schematic view of a first embodiment of an MVR evaporator according to the present application;

FIG. 2 is a schematic view of a portion of a first embodiment of an MVR evaporator according to the present application;

FIG. 3 is a schematic diagram of a second embodiment of the MVR evaporator of the present application;

FIG. 4 is a schematic view of a portion of a second embodiment of an MVR evaporator according to the present application;

FIG. 5 is a schematic view of a portion of a third embodiment of an MVR evaporator according to the present application;

FIG. 6 is a schematic view of a portion of a third embodiment of an MVR evaporator according to the present application;

FIG. 7 is a schematic view of a first embodiment of the diverging tube and associated apparatus of the MVR evaporator of the present application;

FIG. 8 is a schematic view of a second embodiment of the diverging tube and associated apparatus of the MVR evaporator of the present application;

FIG. 9 is a schematic view of a third embodiment of the diverging tube and associated apparatus of the MVR evaporator of the present application;

fig. 10 is a schematic structural diagram of one embodiment of the MVR evaporation system of the present application.

Description of reference numerals: a housing 1; a bottom surface 11; a side wall 12; a liquid outlet 13; an axis 14; a heat exchange tube 2; a central tube 21; a long and short pipe 22; a long tube 221; a short tube 222; shell pass 3; a tube pass 4; a divergent tube 5; an end 51 of the divergent tube; the opposite end 52 of the divergent tube; the first shutter 53; a second shutter 54; a porous filler 55; a gap 56; a straight tube 57; an inclined tube 58; a liquid inlet cavity 6; a liquid inlet 61; a gas-liquid separator 7; a vapor compressor 8; an intake pipe 81; a condensate separator 9; a filter packing 91; distilled water 92; a contaminating substance 93; an exhaust line 10.

Detailed Description

The following examples are given for the detailed implementation and specific operation of the present invention, but the scope of the present invention is not limited to the following examples.

In the description of the present invention and embodiments, it is to be understood that the terms "first", "second", and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implying any number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature.

In the description of the present invention and embodiments, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", and the like, indicate orientations and positional relationships based on the orientations and positional relationships shown in the drawings, are only for convenience in describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention.

The inventors have analyzed that liquids with complex compositions, such as industrial wastewater, often contain oils, solvents, or other volatile residues. In the processing of such liquids using MVR evaporation processes, volatile solvents and contaminants, in addition to water, are vaporized in the tube side of the MVR evaporator. At the same time, droplets and bubbles of oils and contaminants are also entrained in the water vapor due to the vigorous boiling in the tube side. These solvents, gases or droplets of contaminants, along with water vapor, exit the tube side and return to the shell side of the MVR evaporator. As the gas exotherms in the tube pass, the volatile solvent and contaminant gases condense on the surface of the distilled water or re-dissolve in the distilled water; meanwhile, oil and contaminant droplets are easy to accumulate on the surface of the distilled water. Thus, both distilled water and contaminating substances are present in the condensate in the shell side. When the condensate is retained in the shell side for a long time, the polluting substances are mixed with the distilled water again to form a mixture which is difficult to separate, so that the distilled water discharged from the shell side is mixed with the polluting substances, and the quality of the final effluent is further influenced.

To this end, referring to fig. 1 and 2, in a first embodiment of the present application, there is provided an MVR evaporator, which includes a casing 1 and a plurality of heat exchange tubes 2 vertically disposed in the casing 1, wherein a bottom surface 11 of the casing 1 is inclined so that the plurality of heat exchange tubes 2 on the bottom surface 11 have various lengths, and a liquid outlet 13 is formed on a side wall 12 of the casing 1 connected to the lowest portion of the bottom surface 11.

In the present application, a plurality means two or more, and a plurality means two or more.

When the MVR evaporator in the above embodiment is used, please refer to fig. 9, a liquid inlet cavity 6 may be further disposed below the bottom surface 11 of the housing 1, a liquid inlet 61 is disposed at the bottom of the liquid inlet cavity 6, the liquid inlet cavity 6 is communicated with the tube pass 4 of the MVR evaporator, and the liquid to be treated enters the tube pass 4 through the liquid inlet 61 and is heated for evaporation and separation. When the MVR evaporator of the embodiment is used, the gas-liquid separator 7 can be further arranged above the shell 1, the gas-liquid separator 7 is respectively communicated with the tube pass 4 and the external vapor compressor 8, and the vapor compressor 8 is communicated with the shell pass 3 of the MVR evaporator through the air inlet pipeline 81. The gas-liquid separator 7 and the MVR evaporator may be assembled into a whole or may be disposed independently of the MVR evaporator, which is not limited in this application. In addition, when in use, the side wall 12 of the shell 1 may be provided with an exhaust pipeline 10, and the exhaust pipeline 10 is communicated with the shell side 3 and used for exhausting gas which is not condensed in the shell side 3. Preferably, the exhaust pipeline 10 and the air inlet pipeline 81 are respectively arranged on two opposite sides of the side wall 12 of the shell 1, so that the high-quality steam entering the shell side 3 from the air inlet pipeline 81 and the heat exchange pipe 2 are discharged from the exhaust pipeline 10 after sufficient heat exchange, and enter the subsequent processing step of the gas.

The bottom surface of a shell of a common MVR evaporator is a horizontally arranged plane, all the heat exchange tubes are the same in length, and a liquid outlet is formed in the side wall. In the MVR evaporator of the embodiment of the present application, please refer to fig. 1 and 2, the bottom surface 11 of the housing 1 is inclined, so that the lengths of the heat exchange tubes 2 at different heights on the bottom surface 11 are different, such as the long tube 221 and the short tube 222 in fig. 2. In the embodiment of the present application, the long pipe and the short pipe are not absolute, but are relative concepts, and among the two heat exchange pipes 2 of different lengths, the longer one is called the long pipe and the shorter one is called the short pipe. The liquid outlet 13 is located on the side wall 12 of the housing 1 connected to the lowest portion of the bottom surface 11, that is, the bottom surface 11 of the housing 1 has the same height as that of the liquid outlet 13 as the lowest portion of the bottom surface 11, and the heat exchange tube 2 closest to the liquid outlet 13 has the longest length.

During operation, liquid to be treated is heated and evaporated in the tube pass 4, volatile solvent gas, pollutant gas and other pollutant gases, and oil droplets, pollutant droplets and other pollutant droplets are mixed in water vapor, most droplets and foams in steam generated by evaporation in the tube pass 4 are removed through the gas-liquid separator 7, and then the steam is compressed by the steam compressor to form high-quality steam which enters the shell pass 3. The high-quality steam is exothermically condensed in the shell pass 3 into a condensed liquid comprising distilled water and polluting substances, forms a natural and smooth flow on the bottom surface 11, and is discharged from the liquid outlet 13.

The bottom surface is the condensation liquid that the horizontally evaporimeter generally needs wait after certain volume is accumulated to the shell side, takes out in the shell side from the evaporimeter through the pump, consequently can not discharge condensation liquid the very first time, also can cause violent stirring to condensation liquid simultaneously for distilled water and pollutant in the condensation liquid mix, are unfavorable for subsequent further separation. With the MVR evaporator in this embodiment, on the first hand, the bottom surface 11 of the shell 1 is inclined, so that the condensed liquid in the shell side 3 forms a natural and smooth flow, and is discharged from the liquid outlet 13, thereby preventing the distilled water and the polluting substances from being stirred and mixed in the flowing process. In the second aspect, since the condensed liquid is discharged from the shell pass 3 at the first time, the condensed liquid cannot be remained in the shell pass 3, and the continuous condensation and aggregation of the polluting gas and the polluting small liquid drops on the water surface of the distilled water are reduced, so that more polluting gas is discharged through the exhaust pipeline, the condensation quantity of the polluting gas is reduced, and the risk of mixing the distilled water and the pollutants is reduced. In the third aspect, since the lengths of the plurality of heat exchange tubes 2 are different, the heat exchange area of the longer heat exchange tube 2 is larger than that of the shorter heat exchange tube 2, so that the pollutant gas and droplets entrained in the water vapor are relatively more condensed and accumulated at the longer heat exchange tube 2 to form the pollutant in a liquid state. The longer heat exchange tube 2 is closer to the liquid outlet 13, so that the condensed polluting substances can more quickly leave the shell pass 3 of the MVR evaporator through the liquid outlet 13, thereby shortening the retention time of the polluting substances in the shell pass 3 of the MVR evaporator and further reducing the risk of mixing distilled water and pollutants. The three aspects of the effects are mutually cooperated, so that the risk of mixing distilled water and pollutant substances is reduced, the condensation of pollutant gas and pollutant droplets is reduced, and the quality of the final outlet water of the MVR evaporation system is improved.

In addition, distilled water and pollutant do not remain in MVR evaporator shell pass 3 and occupy the heat exchange surface of heat exchange tube, also make the practical heat transfer area in the MVR evaporator bigger, improved the heat exchange efficiency of MVR evaporator.

In this application, the passageway in the heat exchange tube is the tube side of MVR evaporimeter, and the outside circulation space of heat exchange tube is the shell side of MVR evaporimeter in the casing.

Alternatively, referring to fig. 1 and 2, the bottom surface 11 of the shell 1 may be a plane that is obliquely arranged, and in this case, the heights of the junctions of the bottoms of the plurality of heat exchange tubes 2 and the bottom surface 11 of the shell 1 may be different. The heat exchange tubes 2 at the same height have the same length, and the heat exchange tubes 2 having lower heights have longer lengths. Preferably, the inclination angle α of the plane is 3 to 20 degrees. An excessively large tilting angle would cause the condensed liquid to flow too fast towards the liquid outlet 13, increasing the likelihood of the two mixing in the flow. And if the angle of inclination is set too small, the liquid may not be able to flow effectively. When the included angle between the bottom surface 11 of the shell 1 and the horizontal plane is 3-20 degrees, the condensed liquid can naturally and smoothly flow on the bottom surface 11, so that the distilled water and the polluted substances can be prevented from being mixed in the flowing process, the condensed liquid can be quickly discharged from the shell pass 3 of the MVR evaporator, and the continuous condensation and aggregation of the polluted gas and the polluted small liquid drops on the surface of the distilled water are reduced.

Alternatively, the bottom surface 11 of the housing 1 may also be a curved surface that is obliquely arranged, please refer to fig. 5, the curved surface may be a curved surface that is convex from bottom to top. Similarly to the case of the flat surface, in this case, there may be a height difference between the positions where the bottoms of the plurality of heat exchange tubes 2 are connected to the bottom surface 11 of the shell 1. The heat exchange tubes 2 at the same height have the same length, and the heat exchange tubes 2 having lower heights have longer lengths. Different from the above, when the bottom surface 11 of the housing 1 is a curved surface, the distilled water and the contaminating material flow around the curved convex surface, a portion of the distilled water and the contaminating material near the liquid outlet 13 can still be discharged from the shell side 3 quickly and smoothly, and another portion of the distilled water and the contaminating material flow around the curved convex surface to a position far away from the liquid outlet 13 and then gradually flow back to the liquid outlet 13 from a position lower than the curved surface. Compared with the common MVR evaporator structure, the MVR evaporator can still reduce the continuous accumulation of the polluting substances on the surface of the distilled water to a certain extent, and reduce the retention time of the polluting substances in the shell pass 3, thereby reducing the mixing risk of the distilled water and the polluting substances.

In addition, please refer to fig. 6, the curved surface may be a concave curved surface from top to bottom, the concave curved surface is inclined as the bottom surface 11 when in use, the height of the concave curved surface is gradually reduced from one side to the other side, and the liquid outlet 13 is still disposed at the lowest height, so that the situation that part of the distilled water stays in the concave curved surface and cannot flow out is avoided, and the distilled water and the polluting substances can still flow into the liquid outlet 13 smoothly to a certain extent. Such an MVR evaporator also can reduce the continuous accumulation of contaminating materials on the surface of the distilled water to some extent, and reduce the residence time of the contaminating materials in shell pass 3, thereby reducing the risk of mixing of the distilled water and the contaminating materials.

Referring to fig. 3 and 4, in a second embodiment, an MVR evaporator is provided, which comprises a shell 1 and a plurality of heat exchange tubes 2 vertically arranged in the shell 1, wherein a bottom surface 11 of the shell 1 is inclined, so that the plurality of heat exchange tubes 2 on the bottom surface 11 have various lengths, and a liquid outlet 13 is formed on a side wall 12 of the shell 1 connected with the lowest part of the bottom surface 11; the heat exchange tube 2 comprises a central tube 21 arranged in the center of the shell 1 and long and short tubes 22 arranged on the periphery of the central tube 21, and the diameter of the central tube 21 is larger than that of the long and short tubes 22.

The center of the housing 1 is a relative position, and a position closer to the radial distance of the axis 14 of the housing 1 relative to a position farther from the radial distance of the axis 14 of the housing 1 is understood as a position at the center of the housing 1.

Compare with the MVR evaporimeter of the flat bottom that all heat exchange tube 2 pipe diameters are the same, under the same condition of total heat transfer area, the MVR evaporimeter in this embodiment, because the pipe diameter of central authorities pipe 21 is bigger, consequently the heat transfer area of its central authorities pipe 21 and the heat transfer area of surrounding long and short pipe 22 than is littleer, it is bigger to lead to the gasification degree and the density difference of liquid in the heat exchange tube 2, the heat flow circulation that forms is also more violent, and then cooperates with the slope bottom surface, has further improved the heat exchange efficiency of MVR evaporimeter. And, because the liquid flow speed in the tube pass 4 is higher, the heat exchange tube 2 in the embodiment is less prone to scaling.

In fig. 2, 4, 5 and 6, only a part of the heat exchange tubes are schematically shown to avoid excessive clutter.

Optionally, referring to fig. 7 to 9, the MVR evaporator further includes an expanding tube 5 connected to the liquid outlet 13, wherein a diameter of one end 51 of the expanding tube 5 is smaller than a diameter of the other end 52, and the end 51 with the smaller diameter is connected to the liquid outlet 13. Alternatively, the top of the divergent tube 5 may be horizontal, while the bottom gradually decreases in height.

In use, the other end 52 of the divergent conduit 5 is connected to a condensate separator. Through the structure of the gradually expanding pipe 5, the distilled water and the polluting substances flowing out of the liquid outlet 13 of the MVR evaporator can continuously keep natural and smooth flow under the action of gravity and enter the condensate separator for separation, so that the disturbance caused by quick flow is avoided, and the distilled water and the polluting substances are mixed.

Specifically, referring to fig. 8, the divergent pipe 5 may be a slant pipe with a pipe diameter gradually increasing from one end 51 to the other end 52.

Referring to fig. 7 and 9, the divergent pipe 5 may further include at least one straight pipe 57 and at least one inclined pipe 58, the straight pipe 57 is connected to the inclined pipe 58 at an interval, and the caliber of one end of the inclined pipe 58 is the same as the caliber of the straight pipe 57 connected adjacent to the inclined pipe. In contrast, the height of the bottom of the straight tube 57 or the inclined tube 58 near the liquid outlet 13 is not lower than the height of the bottom of the straight tube 57 or the inclined tube 58 far from the liquid outlet 13, so that the distilled water and the contaminating substances flowing out of the liquid outlet 13 can flow by gravity. The divergent pipe 5 with the straight pipe 57 and the inclined pipe 58 connected at intervals can reduce the flow rate of the distilled water and the polluting substances after leaving the MVR evaporator shell pass 3, so that the distilled water and the polluting substances can flow more stably and gently without too high flow rate, the distilled water and the polluting substances are further prevented from being mixed in the continuous acceleration flow process, and the quality of the final effluent is improved.

The inclined pipe in the embodiment of the application refers to a pipeline with the pipe diameter gradually increasing or decreasing.

Optionally, referring to fig. 8 and fig. 9, the first baffle 53 may be fixedly connected to the top of the divergent pipe 5, and a gap 56 is formed between the bottom of the first baffle 53 and the bottom of the divergent pipe 5. A second baffle 54 may be further fixed to the top of the divergent tube 5, a gap 56 is provided between the bottom end of the second baffle 54 and the bottom of the divergent tube 5, and a porous filler 55 is filled in the divergent tube 5 between the first baffle 53 and the second baffle 54. The size of the gap 56 between the first baffle 53 and the second baffle 54 and the bottom of the divergent pipe 5 can be adjusted according to practical situations, which is not limited in this application.

There will also be uncondensed gases in the MVR evaporator shell side 3, which will be mostly vented from the vent line, but a small portion will enter the divergent pipe 5 through the exit port 13 and into the condensate separator. On the one hand, the gases stir distilled water and pollutant substances which are originally in a natural and smooth flowing state, and on the other hand, volatile gases and fine oil drops in the gases directly enter a condensate separator to be condensed and aggregated, so that distilled water and pollutant substances to be further separated in the condensate separator are continuously polluted.

In the present embodiment, since the bottom end of the first baffle 53 is higher than the bottom of the divergent pipe 5, a gap 56 exists between the bottom end of the first baffle 53 and the bottom of the divergent pipe 5. Because the MVR evaporator is used, the distilled water and the polluting substances can be continuously and smoothly discharged without being retained in the shell pass 3, and therefore, the flow rate of the distilled water and the polluting substances is not large, and the distilled water and the polluting substances can be continuously and smoothly discharged into the condensate separator through the gap 56. Volatile gases and oil droplets in the gas in the shell side 3 are blocked to a certain extent by the first baffle 53, reducing the gas entering the condensate separator through the divergent pipe 5, thereby reducing the risk of contamination of the liquid in the condensate separator by volatile gases and oil droplets in the gas.

Further, through setting up two baffles to pack porous filler 55 in the divergent pipe 5 between the baffle, make tiny liquid drop further by porous filler 55 catch in the gas, and then prevent better that tiny liquid drop from getting into in the condensate separator, make the rivers through divergent pipe 5 more even gentle simultaneously.

In a third embodiment of the present application, please refer to fig. 10, further providing an MVR evaporation system, which includes any one of the aforementioned MVR evaporators, a gas-liquid separator 7, a vapor compressor 8, a condensate separator 9, and an exhaust pipeline 10; the gas-liquid separator 7 is arranged above the MVR evaporator and is communicated with the tube pass 4 of the MVR evaporator; an air inlet of the vapor compressor 8 is communicated with the gas-liquid separator 7, and an air outlet is communicated with the shell pass 3 of the MVR evaporator; the condensate separator 9 is communicated with a liquid outlet 13 of the MVR evaporator; the exhaust line 10 is in communication with the shell side 3 of the MVR evaporator. Preferably, the air inlet pipeline 81 and the exhaust pipeline which are communicated with the air outlet of the vapor compressor 8 and the shell pass 3 of the MVR evaporator are respectively arranged on two opposite sides of the side wall 12 of the shell 1. The condensate separator 9 is used for separating distilled water from polluting substances, purifying the distilled water and improving the effluent quality of the MVR evaporation system. The bottom of the condensate separator 9 may also be filled with a filter packing 91 to allow further filtration of the distilled water as it leaves the condensate separator.

This MVR evaporation system's heat exchange efficiency is higher, and final play water quality is better simultaneously. Since the MVR evaporation system includes any one of the MVR evaporators, the MVR evaporation system also has the beneficial effects of the MVR evaporator in the foregoing embodiments, and details are not repeated herein.

The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.

Claims

1. An MVR evaporator is characterized by comprising a shell (1) and a plurality of heat exchange tubes (2) vertically arranged in the shell (1), wherein the bottom surface (11) of the shell (1) is inclined, so that the heat exchange tubes (2) on the bottom surface (11) have various lengths, a liquid outlet (13) is formed in a side wall (12) of the shell (1) connected with the lowest part of the bottom surface (11), the bottom surface (11) is an inclined plane, and the inclination angle alpha of the plane is 3-20 degrees; the MVR evaporator also comprises an expanding pipe (5) connected with the liquid outlet (13), the pipe diameter of one end (51) of the expanding pipe is smaller than that of the other end (52), and the end (51) with the smaller pipe diameter is connected with the liquid outlet (13); the top in the divergent pipe (5) is fixedly connected with a first baffle (53), and a gap (56) is arranged between the bottom end of the first baffle (53) and the bottom of the divergent pipe (5).

2. The MVR evaporator according to claim 1, wherein the heat exchange tubes (2) comprise a central tube (21) arranged in the center of the housing (1) and short and long tubes (22) arranged at the periphery of the central tube (21), and the diameter of the central tube (21) is larger than that of the short and long tubes (22).

3. The MVR evaporator according to claim 1 or 2, characterized in that the bottom surface (11) is a plane that is obliquely arranged.

4. The MVR evaporator according to claim 1 or 2, characterized in that the bottom surface (11) is a curved surface which is obliquely arranged.

5. The MVR evaporator according to claim 1, wherein a second baffle (54) is further fixed to the top of the inside of the divergent tube (5), a gap (56) is formed between the bottom end of the second baffle (54) and the bottom of the divergent tube (5), and a porous filler (55) is filled in the divergent tube between the first baffle (53) and the second baffle (54).

6. The MVR evaporator according to claim 1, wherein the diameter of the divergent tube (5) increases gradually from one end (51) to the other end (52).

7. The MVR evaporator according to claim 1, wherein the divergent tube (5) comprises at least one straight tube (57) and at least one inclined tube (58), the straight tube (57) is connected with the inclined tube (58) at intervals, and the caliber of one end of the inclined tube (58) is the same as that of the straight tube (57) connected adjacent to the inclined tube.

8. The MVR evaporator according to claim 1, wherein a vent line (10) is arranged on a side wall (12) of the housing (1), the vent line (10) being in communication with the shell side (3).

9. The MVR evaporator according to claim 8, characterized in that the exhaust duct (10) and the air intake duct (81) are respectively arranged on opposite sides of a side wall (12) of the housing (1).

10. An MVR evaporation system, characterized by comprising an MVR evaporator according to any of claims 1 to 9, a gas-liquid separator (7), a vapor compressor (8), a condensate separator (9) and a vent line (10); the gas-liquid separator (7) is arranged above the MVR evaporator and is communicated with a tube pass (4) of the MVR evaporator; the air inlet of the steam compressor (8) is communicated with the gas-liquid separator (7), and the air outlet is communicated with the shell pass (3) of the MVR evaporator; the condensate separator (9) is communicated with the liquid outlet (13) of the MVR evaporator; the exhaust pipeline (10) is communicated with the shell pass (3) of the MVR evaporator.