CN206683445U - A kind of heat exchanger of anti-solid accumulation - Google Patents
A kind of heat exchanger of anti-solid accumulation Download PDFInfo
- Publication number
- CN206683445U CN206683445U CN201720426225.2U CN201720426225U CN206683445U CN 206683445 U CN206683445 U CN 206683445U CN 201720426225 U CN201720426225 U CN 201720426225U CN 206683445 U CN206683445 U CN 206683445U
- Authority
- CN
- China
- Prior art keywords
- perforated plate
- heat exchanger
- tube
- solid accumulation
- box
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of heat exchanger of anti-solid accumulation, belong to technical field of medical equipment, including lower tube box, lower perforated plate, shell-side cylinder, heat exchanger tube, upper perforated plate, upper tube box, it is characterised in that, lower tube box bottom sets discharging opening, and down tube upper box part is connected with lower perforated plate;Bearing and expansion joint are set in shell-side cylinder and opens up cold and hot medium import and export adapter and pore corresponding with heat exchanger tube is equipped with the upper perforated plate and lower perforated plate, heat exchanger tube is welded by intensity and is connected with lower perforated plate and upper perforated plate;Blocking cylinder is provided between upper tube lower box part and upper perforated plate charging aperture is set as transition, upper tube box top.The utility model can solve the problems, such as existing anti-solid accumulation solid accumulation, have simple in construction, ingenious in design, the advantages of cost is low.
Description
Technical field
Solid material drying or cooling device technical field are the utility model is related to, in particular to a kind of anti-material
The heat exchanger of accumulation.
Background technology
The pore bored on the tube sheet of traditional heat exchangers is cylindrical hole, has platform between plane hole and hole on tube sheet, changes
Heat pipe generally stretches out Tube-sheet Welding, and upper and lower end socket typically uses ellipse head, and the heat exchanger is used for solid material drying or cooling
When, on tube sheet can stacking material, skewness, bottom blanking is not smooth, and temperature causes material to change colour or imitation frosted glass compared with Gao Shihui
Situation, influence heat transfer efficiency and product quality.
Utility model content
The purpose of this utility model is to provide a kind of heat exchanger of anti-solid accumulation, the pore upper end processing on upper perforated plate
It is tapered or spherical, ensure that the adjacent three round intersection points of plane are summit on tube sheet, solve the problems, such as the solid accumulation of upper perforated plate.
To realize the utility model purpose, the technical scheme used for:A kind of heat exchanger of anti-solid accumulation, including down tube
Case, lower perforated plate, shell-side cylinder, heat exchanger tube, upper perforated plate, upper tube box, it is characterised in that lower tube box bottom sets discharging opening, down tube
Upper box part is connected with lower perforated plate;Bearing and expansion joint are set in shell-side cylinder and open up cold and hot medium import and export adapter and, it is described
Pore corresponding with heat exchanger tube is equipped with upper perforated plate and lower perforated plate, heat exchanger tube is connected by intensity weldering with lower perforated plate and upper perforated plate
Connect;Blocking cylinder is provided between upper tube lower box part and upper perforated plate charging aperture is set as transition, upper tube box top.
Further, the processing of upper perforated plate pore upper end is tapered or spherical, ensure on tube sheet plane it is adjacent three it is round
Intersection point is peak, eliminates the platform between pore.
Further, upper perforated plate and heat exchanger tube junction rounding off.
Further, it is columnar structured to be that pyramidal structure or taper add for the blocking cylinder.
Further, expansion joint is set in shell-side cylinder.
The beneficial effects of the utility model are, using heat exchanger provided by the utility model, solid material to be effectively ensured
In the smooth of tube side passage flow, be not in the situation of solid accumulation, material is evenly distributed, improve heat transfer effect, protect
Product quality is demonstrate,proved, on the other hand, the connection stress of exchanger tubes and tubesheets is small, improves the service life of equipment.
Brief description of the drawings
Fig. 1 is the structural representation of the heat exchanger of anti-solid accumulation;
Fig. 2 is the partial sectional view of upper perforated plate;
Fig. 3 is the partial sectional view of upper perforated plate(Another welding manner of heat exchanger tube).
Embodiment
The utility model is described in further detail below by specific examples of the implementation and with reference to accompanying drawing.
Fig. 1 shows the heat exchanger of anti-solid accumulation provided by the utility model, including lower tube box 2, lower perforated plate 3, shell side
Cylinder 5, heat exchanger tube 6, upper perforated plate 11, upper tube box 13, the bottom of lower tube box 2 set discharging opening 1, and the top of lower tube box 2 connects with lower perforated plate 3
Connect;Bearing 8 and expansion joint 9 are set in shell-side cylinder 5 and open up cold and hot medium import and export adapter 4 and 10, inside shell-side cylinder 5
Along the length direction of heat exchanger tube 6, deflection plate is set;Heat exchanger tube 6 is welded by intensity and is connected with lower perforated plate 3 and upper perforated plate 11;Upper tube box 13
Bottom sets blocking cylinder 12 close to the position of upper perforated plate 11, and the top of upper tube box 13 sets charging aperture 14.
Fig. 2 and Fig. 3 respectively illustrates two kinds of connected modes, two kinds of different connections between heating tube 6 and upper perforated plate 11
Mode.
The pore upper end of upper perforated plate 11 processes tapered or spherical, the changeover portion 15 between upper perforated plate 11 and heat exchanger tube 6
A smooth transition is formed, ensures that the adjacent three round intersection points 16 of plane are summit on upper perforated plate 11, eliminate pore and pore
Between platform.
The bottom of upper tube box 13 sets blocking cylinder close to the position of upper perforated plate 11(12), blocking cylinder 12 is pyramidal structure or taper
Add columnar structured, half cone-apex angle A of taper is less than the angle of repose of solid material, and the conelet internal diameter of taper is just upper perforated plate 11
Peripheral platform separates outside.
Expansion joint is set in shell-side cylinder 5(9).
The cylinder of lower tube box 2 uses pyramidal structure, and half cone-apex angle D of taper is less than the angle of repose of solid material.
Solid material continuously enters upper tube box 13 from charging aperture 14, enters heat exchanger tube 6 by upper perforated plate 11, then pass through down tube
Case 2 discharges from discharging opening 1;Cold and hot medium enters in shell-side cylinder 5 from cold heat medium inlet 4 simultaneously, is drawn by deflection plate 7
Long flow, heat exchange efficiency is improved, is finally gone out from cold heat media outlet pipe 10, the whole heat exchange of solid material and cold and hot medium
Process is completed inside and outside heat exchanger tube 6, reaches the effect dried or cooled down.Because the upper plane of upper perforated plate 11 does not have platform, backgauge
Cylinder 12 again shelters from the platform of the surrounding of upper perforated plate 11, and solid material can pass through upper perforated plate 11 and enter heat exchanger tube 6, without
It can be deposited on tube sheet, avoid causing solid material the discoloration even phenomenon of imitation frosted glass, ensure that product quality, while lower tube box 2
Design it is tapered, and ensure semi-cone angle C be less than solid material angle of repose, enable dry or cool down after material smoothly go out
Material, does not interfere with the heat exchange of epimere material.On the other hand, it is hot swollen due to heat exchanger tube 6 and shell-side cylinder 5 in heat transfer process
Bulk is inconsistent, and difference portion is compensated by expansion joint 9, and reduce heat exchanger tube 6 and upper perforated plate 11 and the weld of lower perforated plate 3 should
Power, improve the service life of equipment.Drying or cooling for solid material provide a kind of preferable heat transmission equipment.
Preferred embodiment of the present utility model is the foregoing is only, is not limited to the utility model, for this
For the technical staff in field, there can be various modifications and variations in the spirit and principles of the utility model, these are equivalent
Modification or replacement etc., are all contained within the scope of protection of the utility model.
Claims (5)
1. a kind of heat exchanger of anti-solid accumulation, including lower tube box, lower perforated plate, shell-side cylinder, heat exchanger tube, upper perforated plate, upper tube box,
Characterized in that, lower tube box bottom sets discharging opening, down tube upper box part is connected with lower perforated plate;Bearing and swollen is set in shell-side cylinder
It is swollen save and open up the adapter of cold and hot medium import and export and, pore corresponding with heat exchanger tube is equipped with the upper perforated plate and lower perforated plate,
Heat exchanger tube is welded by intensity and is connected with lower perforated plate and upper perforated plate;It was used as between upper tube lower box part and upper perforated plate provided with blocking cylinder
Cross, charging aperture is set at the top of upper tube box.
2. the heat exchanger of anti-solid accumulation according to claim 1, it is characterised in that be processed into cone in upper perforated plate pore upper end
Shape is spherical, ensures that the adjacent three round intersection points of plane are peak on upper perforated plate, eliminate the platform between pore.
3. the heat exchanger of anti-solid accumulation according to claim 1, it is characterised in that upper perforated plate is justified with heat exchanger tube junction
Slip over and cross.
4. the heat exchanger of anti-solid accumulation according to claim 1, it is characterised in that the blocking cylinder be pyramidal structure or
Person's taper adds columnar structured.
5. the heat exchanger of anti-solid accumulation according to claim 1, it is characterised in that expansion joint is set in shell-side cylinder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720426225.2U CN206683445U (en) | 2017-04-21 | 2017-04-21 | A kind of heat exchanger of anti-solid accumulation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720426225.2U CN206683445U (en) | 2017-04-21 | 2017-04-21 | A kind of heat exchanger of anti-solid accumulation |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206683445U true CN206683445U (en) | 2017-11-28 |
Family
ID=60404040
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720426225.2U Active CN206683445U (en) | 2017-04-21 | 2017-04-21 | A kind of heat exchanger of anti-solid accumulation |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206683445U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109323271A (en) * | 2018-12-04 | 2019-02-12 | 深圳市中粤华远科技有限公司 | Porous type water cooling self-adapting seal discharging device and its discharging method |
CN110056848A (en) * | 2018-04-23 | 2019-07-26 | 新能能源有限公司 | High temperature and high pressure flue gas afterheat utilizing system |
-
2017
- 2017-04-21 CN CN201720426225.2U patent/CN206683445U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110056848A (en) * | 2018-04-23 | 2019-07-26 | 新能能源有限公司 | High temperature and high pressure flue gas afterheat utilizing system |
CN110056848B (en) * | 2018-04-23 | 2024-05-03 | 新能能源有限公司 | High-temperature high-pressure flue gas waste heat utilization system |
CN109323271A (en) * | 2018-12-04 | 2019-02-12 | 深圳市中粤华远科技有限公司 | Porous type water cooling self-adapting seal discharging device and its discharging method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105937857A (en) | Shell-and-tube heat exchanger suitable for three-fluid heat exchange | |
CN206683445U (en) | A kind of heat exchanger of anti-solid accumulation | |
CN107362560B (en) | Two-phase countercurrent vertical in-tube falling film evaporator with circumferential tangential feeding | |
CN106440883A (en) | Horizontal type shell-and-tube heat exchanger | |
CN207316970U (en) | A kind of U-shaped heat exchanger | |
CN104006663B (en) | Cooling device for materials after calcination of anthracite or petroleum coke | |
CN103542742B (en) | Can to loose core heat exchanger | |
CN203518710U (en) | Spiral countercurrent flow heat exchange device provided with heat exchange tubes with inward-protruded ribs | |
CN205918707U (en) | Three -dimensional manage -style cold type oil cooler | |
CN210400083U (en) | Heat exchanger with sufficient cooling | |
CN209355735U (en) | A kind of intelligence shell-and-tube energy conservation heat-exchange unit | |
CN207649426U (en) | A kind of heat exchanger | |
CN206073772U (en) | A kind of high-performance heat exchanger | |
CN203744607U (en) | Double-tube-pass dry type evaporator and refrigeration equipment | |
CN207035905U (en) | A kind of macroporous plate convergent-divergent pipe efficient heat exchanger | |
CN206399241U (en) | High-performance solid heat exchanger | |
CN205049016U (en) | Fin -type heat exchanger | |
CN205383913U (en) | Sleeve pipe and adopt this sheathed tube heat exchange device | |
KR101723461B1 (en) | Double-pipe heat exchanger with airflow arrangement of gas and liquid | |
CN104776641A (en) | Double-tube-pass dry-type evaporator and refrigerating equipment | |
CN208059403U (en) | Holding vessel cooling structure | |
CN202177319U (en) | Efficient condenser for rubber production | |
CN209431929U (en) | A kind of liquid-liquid type heat pipe heat exchanger device | |
CN213687995U (en) | Gas cooler with flow divider | |
CN208579663U (en) | A kind of graphite heat exchanger with long service life |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |