Chemical pressure distillation heat exchanger
By designing the inner layer, liquid discharge port, separation cover and separation pipeline in the chemical distillation heat exchanger, the problems of large total contact area of heat exchange and inconvenient movement adjustment are solved, the pressure reduction and heat exchange effect are maintained, and the pressure is allowed to be maintained. Flexible adjustment of the device.
Patent Information
- Application Number
- CN202420421506.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-03-05
- Publication Date
- 2025-02-14
- Estimated Expiration
- 2034-03-05
AI Technical Summary
When the existing chemical distillation heat exchanger enters the tube bundles in the heat exchanger, due to the diverting and transportation method, the total contact area of heat exchange is larger, and the mass of cold flow medium that absorbs heat and vaporizes into gaseous state is also greater. Changing the pressure in the casing cavity affects the strength of the casing and is not convenient for movement and adjustment.
A chemical pressure distillation heat exchanger is designed, including a housing, an intake pipe, an outlet pipe, a support base, a support adjustment assembly and a heat exchange assembly. By setting up an inner layer, liquid discharge port, separation cover and separation pipeline, the condensate liquid can be separated and discharged, the internal pressure is reduced, and the heat exchange effect is maintained. Meanwhile, the support adjustment assembly allows adjustment of the height and angle of the housing.
Through the design of the separation cover and separation pipeline, the internal pressure is reduced, the steam is fully utilized to maintain the heat exchange effect, the device is improved in effect and practicality, and the device is flexible to move and adjust by supporting the design of the adjustment component.
Smart Images
Figure CN222481153U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of chemical distillation, and in particular to a chemical pressure distillation heat exchanger. Background Art
[0002] A heat exchanger is a device that transfers part of the heat of a hot fluid to a cold fluid. It is also called a heat exchanger. According to the heat transfer principle, it can be divided into a partition heat exchanger, a heat storage heat exchanger, a fluid-connected indirect heat exchanger, a direct contact heat exchanger, and a compound heat exchanger. Among them, the partition heat exchanger is the most widely used heat exchanger. In the partition heat exchanger, two fluids with different temperatures flow in a space separated by a wall. Heat is exchanged between the two fluids through heat conduction on the wall and convection of the fluid on the wall surface.
[0003] The shell-and-tube heat exchanger is a type of partition-type heat exchanger. When the heat exchanger is in operation, the hot flow medium directly enters each tube bundle from the liquid inlet and flows out from the liquid outlet after completing the heat exchange. When the hot flow medium enters each tube bundle in the heat exchanger, due to the diversion and transportation method, the total contact area of the heat exchange (that is, the total wall area for heat conduction between the hot flow medium and the cold flow medium) is large, so the amount of cold flow medium that absorbs heat and vaporizes into gas is also large. In the process of filling the cavity of the entire heat exchanger shell, the pressure in the shell cavity is changed, which in turn affects the strength of the shell to a certain extent. It is also inconvenient to move and adjust.
[0004] Therefore, improvements are made to address the above problems. Utility Model Content
[0005] The utility model proposes a chemical distillation heat exchanger, which solves the problem in the related technology that when the hot flow medium enters each tube bundle in the heat exchanger, due to the diversion transportation mode, the total contact area of the heat exchange is large, so the amount of the cold flow medium that absorbs heat and vaporizes into gas is also large, and the pressure in the shell cavity is changed in the process of filling the entire cavity of the heat exchanger shell, thereby causing a certain degree of influence on the strength of the shell, and it is inconvenient to move and adjust.
[0006] The technical solution of the utility model is as follows:
[0007] A housing, an air inlet pipe and an air outlet pipe, wherein the air inlet pipe is installed on the top of the housing, and the air outlet pipe is installed on the bottom of the housing;
[0008] A pair of supporting bases, the supporting bases being fixed at two ends of the bottom of the housing;
[0009] A support adjustment component, wherein the support adjustment component is arranged inside the support base;
[0010] A heat exchange component is arranged inside the shell, and the heat exchange component includes a liquid inlet pipe, which is installed in the side surface of the shell, and the side surface of the shell is provided with a liquid outlet pipe, and one end of the liquid outlet pipe and the liquid inlet pipe are both connected to a cavity shell.
[0011] As a further technical solution, an inner layer is provided inside the outer shell, the inner layer is fixed inside the outer shell, a number of heat exchange tubes are connected between the cavity shells, a number of inner support plates are provided inside the inner layer, a number of drainage ports are opened at the bottom of the inner layer, a separation hood is provided on the inner surface of the air outlet pipe, and a separation pipe is provided on the side surface of the air outlet pipe.
[0012] As a further technical solution, the support adjustment assembly includes a bottom groove, which is opened at the bottom of the support base. A pair of vertical screws are rotatably connected in the bottom groove. A pair of round rods are arranged in the bottom groove, and the round rods and the vertical screws are located in the same straight line position.
[0013] As a further technical solution, the outside of the vertical screw is connected to an internally threaded tube through threaded cooperation, a connecting frame is provided on one side of the internally threaded tube, the connecting frame is connected to the round rod sliding sleeve, the lower end of the internally threaded tube is connected to a cross support frame, the side end surface of the support base is provided with a side groove, and the upper end of the vertical screw is located in the side groove.
[0014] As a further technical solution, a screw block is provided at the upper end of the vertical lead screw, and the screw block is a polygonal structure.
[0015] As a further technical solution, the cross section of the cross brace is a structure that is wide at the top and narrow at the bottom, and both ends of the bottom of the cross brace are arc-shaped structures.
[0016] As a further technical solution, a plurality of the heat exchange tubes are evenly distributed and connected in a staggered lattice shape, and the cross-section of the heat exchange tubes is a polygonal structure.
[0017] As a further technical solution, there are two separation pipes, which are located inside and outside the shell respectively.
[0018] The working principle and beneficial effects of the utility model are:
[0019] The utility model is provided with a heat exchange component, and an inner layer, a drain port, a separation cover and a separation pipe are arranged inside the outer shell. During the steam heat exchange process, a condensation effect will be generated and the internal pressure will increase. By arranging the separation cover and the separation pipe, the liquid generated by the condensation reaction can be separated and discharged, the internal pressure can be reduced, and the steam can be fully utilized to maintain the heat exchange effect, which has good use effect and practicality. BRIEF DESCRIPTION OF THE DRAWINGS
[0020] The utility model is further described in detail below in conjunction with the accompanying drawings and specific implementation methods.
[0021] Figure 1 It is a schematic diagram of the structure of the utility model;
[0022] Figure 2 This is the axonometric drawing of the utility model;
[0023] Figure 3 This is a cross-sectional view of the utility model;
[0024] Figure 4 This is a cross-sectional view from another perspective of the utility model;
[0025] Figure 5 This is another cross-sectional view of the utility model from another perspective;
[0026] Figure 6 For the utility model Figure 3 A partial enlarged view of part A;
[0027] In the figure: 1. outer shell; 2. air inlet pipe; 3. air outlet pipe; 4. support base; 5. heat exchange component; 5-1. liquid inlet pipe; 5-2. liquid outlet pipe; 5-3. cavity shell; 5-4. inner layer; 5-5. heat exchange tube; 5-6. inner support plate; 5-7. drain port; 5-8. separation cover; 5-9. separation pipe; 6. support adjustment component; 6-1. bottom groove; 6-2. vertical screw; 6-3. round rod; 6-4. internal threaded pipe; 6-5. connecting frame; 6-6. cross support frame; 7. side groove; 8. screw block. DETAILED DESCRIPTION
[0028] The following will be combined with the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.
[0029] like Figure 1 to Figure 6 As shown, this embodiment proposes a chemical distillation heat exchanger, comprising
[0030] A housing 1, an air inlet pipe 2 and an air outlet pipe 3, wherein the air inlet pipe 2 is installed at the top of the housing 1 and the air outlet pipe 3 is installed at the bottom of the housing 1;
[0031] A pair of supporting bases 4, the supporting bases 4 are fixed at two ends of the bottom of the housing 1;
[0032] A support adjustment component 6, the support adjustment component 6 is arranged inside the support base 4;
[0033] The heat exchange component 5 is arranged inside the outer shell 1. The heat exchange component 5 includes a liquid inlet pipe 5-1, which is installed on the side surface of the outer shell 1. A liquid outlet pipe 5-2 is arranged on the side surface of the outer shell 1. One end of the liquid outlet pipe 5-2 and the liquid inlet pipe 5-1 are connected to a cavity shell 5-3. An inner layer 5-4 is arranged inside the outer shell 1. The inner layer 5-4 is fixed inside the outer shell 1. A plurality of heat exchange tubes 5-5 are connected between the cavity shells 5-3. A plurality of inner support sheets 5-6 are arranged inside the inner layer 5-4. A plurality of drain ports 5-7 are opened at the bottom of the inner layer 5-4. A separation cover 5-8 is arranged on the inner surface of the outlet pipe 3. A separation pipe 5-9 is arranged on the side surface of the outlet pipe 3.
[0034] In this embodiment, in order to achieve the effect of heat exchange using distilled steam, a heat exchange component 5 is designed, and a liquid inlet pipe 5-1 and a liquid outlet pipe 5-2 are respectively arranged on both sides of the outer shell 1, and are connected to a cavity shell 5-3, and a plurality of heat exchange tubes 5-5 are connected between the cavity shells 5-3 for flowing liquid for heat exchange, an inner layer 5-4 is arranged inside the outer shell 1, and a gap is left between the inner layer 5-4 and the outer shell 1, and a drain port 5-7 is opened at the bottom of the inner layer 5-4, and the drain port 5-7 is used for concentratedly discharging condensed liquid generated by heat exchange downward, a separation hood 5-8 is arranged inside the gas outlet pipe 3, and two diversion pipes are arranged on the side surface of the gas outlet pipe 3 for separating and discharging the condensed liquid from the gas.
[0035] Furthermore, the support adjustment component 6 includes a bottom groove 6-1, which is opened at the bottom of the support base 4. A pair of vertical screws 6-2 are rotatably connected in the bottom groove 6-1. A pair of round rods 6-3 are arranged in the bottom groove 6-1. The round rods 6-3 and the vertical screws 6-2 are located in the same straight line. The outside of the vertical screw 6-2 is connected to an internal threaded tube 6-4 through threaded cooperation. A connecting frame 6-5 is arranged on one side of the internal threaded tube 6-4. The connecting frame 6-5 is connected to the round rod 6-3 in a sliding sleeve. The lower end of the internal threaded tube 6-4 is connected to a cross support frame 6-6. A side groove 7 is opened on the side end surface of the support base 4, and the upper end of the vertical screw 6-2 is located in the side groove 7.
[0036] In this embodiment, in order to achieve the adjustable effect of the overall device, a support adjustment component 6 is designed, and a bottom groove 6-1 is opened at the bottom of the support base 4. A vertical screw 6-2 and a round rod 6-3 are arranged in the bottom groove 6-1. The outside of the vertical screw 6-2 is connected to an internal threaded tube 6-4 through threaded cooperation. A connecting frame 6-5 is arranged on the side end face of the internal threaded tube 6-4. The connecting frame 6-5 is slidably connected to the round rod 6-3. The round rod 6-3 serves as a guide to enable the internal threaded tube 6-4 to move vertically downward. A cross support frame 6-6 is arranged at the bottom of the internal threaded tube 6-4 for supporting it on the ground. The overall height and angle of the shell 1 can be adjusted.
[0037] Furthermore, a screw block 8 is provided at the upper end of the vertical screw 6-2, and the screw block 8 is a polygonal structure.
[0038] In this embodiment, the polygonal screw block 8 makes it easy to use a tool to clamp the screw block 8 to operate and control the rotation of the vertical screw 6-2, making the adjustment more precise.
[0039] Furthermore, the cross section of the cross brace 6-6 is a structure that is wide at the top and narrow at the bottom, and both ends of the bottom of the cross brace 6-6 are arc-shaped structures.
[0040] In this embodiment, the arc-shaped structures on both sides of the bottom of the horizontal support frame 6 - 6 enable the housing 1 to maintain a support effect in contact with the ground by changing the angle when it is supported.
[0041] Furthermore, a plurality of heat exchange tubes 5 - 5 are evenly distributed and connected in a staggered lattice shape, and the cross section of the heat exchange tube 5 - 5 is a polygonal structure.
[0042] In this embodiment, the heat exchange effect of the plurality of heat exchange tubes 5 - 5 is made more uniform through the distribution of the lattice structure.
[0043] Furthermore, there are two separation pipes 5 - 9 , which are located inside and outside the housing 1 , respectively.
[0044] In this embodiment, two separation pipes 5-9 are connected to the inside and outside of the shell 1 respectively, so that all the liquid generated by the condensation reaction is discharged to the outside.
[0045] When heat exchange is required, the air inlet pipe 2 is connected to the steam equipment, and the liquid inlet pipe 5-1 and the liquid outlet pipe 5-2 are all connected to start circulating the liquid. The liquid enters the cavity shell 5-3 on one side through the liquid inlet pipe 5-1, flows through the heat exchange tube 5-5, enters the cavity shell 5-3 on the other side, and is finally discharged through the liquid outlet pipe 5-2. During the process, steam enters through the air inlet pipe 2, flows inside the inner layer 5-4 of the outer shell 1, heats the heat exchange tube 5-5, and is then discharged through the air outlet pipe 3. During the process, heat exchange is completed, and the liquid produced by the condensation effect caused by the temperature difference flows downward through the drain port 5-7 at the bottom of the inner layer 5-4, and is then discharged through the separation pipe 5-9 and the separation cover 5-8.
[0046] The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention should be included in the protection scope of the present invention.
Claims
1. A chemical distillation heat exchanger, characterized in that: include A housing (1), an air inlet pipe (2) and an air outlet pipe (3), wherein the air inlet pipe (2) is installed at the top of the housing (1) and the air outlet pipe (3) is installed at the bottom of the housing (1); A pair of supporting bases (4), wherein the supporting bases (4) are fixed at two ends of the bottom of the housing (1); A support adjustment component (6), wherein the support adjustment component (6) is arranged inside the support base (4); A heat exchange component (5), the heat exchange component (5) being arranged inside the outer shell (1), the heat exchange component (5) comprising a liquid inlet pipe (5-1), the liquid inlet pipe (5-1) being installed inside the side surface of the outer shell (1), the side surface of the outer shell (1) being provided with a liquid outlet pipe (5-2), one end of the liquid outlet pipe (5-2) and the liquid inlet pipe (5-1) being connected to a cavity shell (5-3).
2. A chemical distillation heat exchanger according to claim 1, characterized in that: An inner layer (5-4) is arranged inside the outer shell (1), and the inner layer (5-4) is fixed inside the outer shell (1); a plurality of heat exchange tubes (5-5) are connected between the cavity shells (5-3); a plurality of inner support sheets (5-6) are arranged inside the inner layer (5-4); a plurality of liquid discharge ports (5-7) are opened at the bottom of the inner layer (5-4); a separation cover (5-8) is arranged on the inner surface of the air outlet pipe (3); and a separation pipe (5-9) is arranged on the side surface of the air outlet pipe (3).
3. A chemical pressure distillation heat exchanger according to claim 1, characterized in that: The support adjustment assembly (6) comprises a bottom groove (6-1), wherein the bottom groove (6-1) is opened at the bottom of the support base (4), a pair of vertical lead screws (6-2) are rotatably connected in the bottom groove (6-1), a pair of round rods (6-3) are arranged in the bottom groove (6-1), and the round rods (6-3) and the vertical lead screws (6-2) are located in the same straight line position.
4. A chemical distillation heat exchanger according to claim 3, characterized in that: The outside of the vertical screw (6-2) is connected to an internally threaded tube (6-4) through threaded matching, a connecting frame (6-5) is provided on one side of the internally threaded tube (6-4), the connecting frame (6-5) is connected to the round rod (6-3) in a sliding sleeve manner, the lower end of the internally threaded tube (6-4) is connected to a cross brace (6-6), a side groove (7) is provided on the side end surface of the support base (4), and the upper end of the vertical screw (6-2) is located in the side groove (7).
5. A chemical distillation heat exchanger according to claim 3, characterized in that: A screwing block (8) is arranged at the upper end of the vertical lead screw (6-2), and the screwing block (8) is a polygonal structure.
6. A chemical distillation heat exchanger according to claim 4, characterized in that: The cross section of the cross brace (6-6) is a structure that is wide at the top and narrow at the bottom, and both ends of the bottom of the cross brace (6-6) are arc-shaped structures.
7. A chemical distillation heat exchanger according to claim 2, characterized in that: A plurality of the heat exchange tubes (5-5) are evenly distributed and connected in a staggered lattice pattern, and the cross section of the heat exchange tube (5-5) is a polygonal structure.
8. A chemical distillation heat exchanger according to claim 2, characterized in that: There are two separation pipes (5-9), and the separation pipes (5-9) are located inside and outside the shell (1) respectively.