CN218410775U - Recovery equipment for reducing volatile organic compound treatment capacity - Google Patents
Recovery equipment for reducing volatile organic compound treatment capacity Download PDFInfo
- Publication number
- CN218410775U CN218410775U CN202222606263.XU CN202222606263U CN218410775U CN 218410775 U CN218410775 U CN 218410775U CN 202222606263 U CN202222606263 U CN 202222606263U CN 218410775 U CN218410775 U CN 218410775U
- Authority
- CN
- China
- Prior art keywords
- tube plate
- shell
- heat exchange
- water
- air
- 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
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model relates to a gaseous condensation technical field, and a reduce volatile organic compounds handling capacity recovery plant is disclosed, including the heat transfer casing, the symmetric connection has upper tube plate and lower tube plate in the heat transfer casing, the inner shell top of upper tube plate and heat transfer casing is connected with the division board jointly, be connected with the air guide subassembly jointly between upper tube plate and the lower tube plate, the shell top intercommunication of heat transfer casing has business turn over gas subassembly, it has a plurality of baffling boards to connect in the staggered connection on the shell wall in the heat transfer casing between upper tube plate and the lower tube plate, the air guide subassembly runs through a plurality of baffling board settings, be connected with cooling water circulation business turn over subassembly on the shell wall of heat transfer casing, the shell bottom intercommunication of heat transfer casing has the water receiving tank, the water receiving tank intussuseption is filled with the overflow pipe that is down "U" type on one side outer wall of water receiving tank the utility model discloses in advance with the moisture in the peculiar smell gas get rid of, the work load of gas treatment equipment has been reduced, the work efficiency of gas treatment equipment has been improved.
Description
Technical Field
The utility model relates to a gaseous condensation technical field especially relates to a reduce volatile organic compounds handling capacity recovery plant.
Background
Plastic processing operations typically include compounding, forming, joining, assembling, mechanical finishing, etc., wherein the forming step is typically accomplished by a plastic extruder. After plastics are molded, peculiar smells with different degrees exist, the peculiar smells belong to organic volatile matters, also called VOC, more organic volatile matters can be emitted from materials with higher temperature in the plastic processing process, the peculiar smell gas consists of the organic volatile matters, air and moisture, at present, the peculiar smell gas is usually directly introduced into corresponding gas treatment equipment for treatment and then discharged, but the gas contains partial moisture, the moisture is also introduced into the gas treatment equipment for treatment, the working load of the gas treatment equipment can be aggravated, and the working efficiency of the gas treatment equipment is influenced.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the above problems in the background art and providing a recovery device for reducing the processing capacity of volatile organic compounds.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a reduce volatile organic compounds throughput recovery plant, includes the heat transfer casing, upper tube plate and lower tube plate of symmetric connection in the heat transfer casing, the inner shell top of upper tube plate and heat transfer casing is connected with the division board jointly, be connected with the air guide subassembly jointly between upper tube plate and the lower tube plate, the shell top intercommunication of heat transfer casing has business turn over gas subassembly, and the staggered connection has a plurality of baffling boards on the shell wall of the heat transfer casing that is located between upper tube plate and the lower tube plate, the air guide subassembly runs through a plurality of baffling boards and sets up, be connected with cooling water circulation business turn over subassembly on the shell wall of heat transfer casing, the shell bottom intercommunication of heat transfer casing has the water receiving tank, the water receiving tank intussuseption is filled with water, run through the intercommunication on one side outer wall of water receiving tank has the overflow pipe that is "U" type, the overflow pipe end portion that is located in the water receiving tank inserts the aquatic, install the valve on the overflow pipe.
Preferably, the air guide assembly comprises a lower air tube group and an upper air tube group, the two ends of the lower air tube group and the upper air tube group are embedded with the upper tube plate, the lower tube plate and the plurality of baffle plates in a penetrating manner, and the lower air tube group and the upper air tube group are symmetrically arranged relative to the partition plate.
Preferably, the gas inlet and outlet assembly comprises a gas inlet pipe and a gas outlet pipe, and the gas inlet pipe and the gas outlet pipe are symmetrically communicated with the top of the heat exchange shell relative to the partition plate.
Preferably, the cooling water circulation inlet and outlet assembly comprises a water inlet pipe and a water outlet pipe, and the water inlet pipe and the water outlet pipe are symmetrically communicated with the shell wall of the heat exchange shell in a crossed mode.
Preferably, a DN150 sight glass is inlaid in the front face of the water receiving box.
Preferably, the inner pipe wall of the air inlet pipe is connected with a support ring, and the upper end of the support ring is provided with a filter screen.
Compared with the prior art, the utility model provides a reduce volatile organic compounds handling capacity recovery plant possesses following beneficial effect:
1. this reduce volatile organic compounds handling capacity recovery plant, the moisture condensation in the peculiar smell gas goes out, and the moisture that the condensation goes out falls into in the water receiving case, gets rid of the peculiar smell gas of moisture and enters into the gas treatment equipment through the outlet duct again and handles, gets rid of the peculiar smell gas moisture in advance, has reduced gas treatment equipment's work load, has improved gas treatment equipment's work efficiency.
2. This reduce volatile organic compounds handling capacity recovery plant for continuously keep vacuum device in the water receiving tank, after the water level surpassed the highest height of overflow pipe, unnecessary water passes through the automatic discharge of overflow pipe in the water receiving tank.
The part that does not relate to in the device all is the same with prior art or can adopt prior art to realize, the utility model discloses get rid of the moisture in the peculiar smell gas in advance, reduced gas treatment equipment's work load, improved gas treatment equipment's work efficiency.
Drawings
FIG. 1 is a schematic view of a recycling apparatus for reducing the processing capacity of volatile organic compounds according to the present invention;
FIG. 2 is a schematic structural view of a recycling apparatus for reducing the processing amount of volatile organic compounds according to the present invention;
fig. 3 is an enlarged view of a portion a in fig. 2.
In the figure: 1. a heat exchange housing; 2. an upper tube sheet; 3. a lower tube plate; 4. a separator plate; 5. a baffle plate; 6. a water receiving tank; 7. an overflow pipe; 8. a lower gas pipe group; 9. an upper gas pipe group; 10. an air inlet pipe; 11. an air outlet pipe; 12. a water inlet pipe; 13. a water outlet pipe; 14. DN150 sight glass; 15. a support ring; 16. and (4) a filter screen.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.
Referring to fig. 1-2, a recovery device for reducing volatile organic compound treatment capacity comprises a heat exchange shell 1, wherein an upper tube plate 2 and a lower tube plate 3 are symmetrically connected in the heat exchange shell 1, a plurality of baffle plates 5 are connected on the inner shell wall of the heat exchange shell 1 between the upper tube plate 2 and the lower tube plate 3 in a staggered manner, and a separation plate 4 is connected on the top of the inner shell of the heat exchange shell 1 and the upper tube plate 2.
The shell wall of the heat exchange shell 1 is connected with a cooling water circulation inlet and outlet assembly, the cooling water circulation inlet and outlet assembly comprises a water inlet pipe 12 and a water outlet pipe 13, the water inlet pipe 12 and the water outlet pipe 13 are symmetrically communicated with the shell wall of the heat exchange shell 1 in a crossed mode, cooling water enters the heat exchange shell 1 through the water inlet pipe 12, and the cooling water is discharged through the water outlet pipe 13 after passing through a channel formed by the baffle plates 5.
Referring to fig. 2-3, an air guide assembly is connected between the upper tube plate 2 and the lower tube plate 3, the air guide assembly penetrates through the plurality of baffle plates 5, the air guide assembly comprises a lower air tube group 8 and an upper air tube group 9, two ends of the lower air tube group 8 and the upper air tube group 9 penetrate through and are embedded with the upper tube plate 2, the lower tube plate 3 and the plurality of baffle plates 5, the lower air tube group 8 and the upper air tube group 9 are symmetrically arranged relative to the isolation plate 4, and odor gas firstly enters the lower air tube group 8 and then enters the upper air tube group 9.
The shell top intercommunication of heat transfer casing 1 has the business turn over gas subassembly, the business turn over gas subassembly includes intake pipe 10 and outlet duct 11, intake pipe 10 and outlet duct 11 are close to 4 symmetry intercommunications of division board at the shell top of heat transfer casing 1, be connected with support ring 15 on the interior pipe wall of intake pipe 10, filter screen 16 is installed to the upper end of support ring 15, filter the impurity in the peculiar smell gas that gets into in the intake pipe 10 through filter screen 16, the shell bottom intercommunication of heat transfer casing 1 has water receiving tank 6, water receiving tank 6 intussuseption is filled with water, the front of water receiving tank 6 is inlayed and is had DN150 sight glass 14.
Referring to fig. 1-2, run through the intercommunication on the outer wall of one side of water receiving tank 6 and have overflow pipe 7 that is "U" type, 7 tip of overflow pipe that are located water receiving tank 6 insert the aquatic, install the valve on overflow pipe 7, when there is not water in the water receiving tank 6, the valve keeps the off-state earlier, when water begins to accumulate the water inlet that overflows overflow pipe 7 in the water receiving tank 6 afterwards, the valve keeps normally open state, make and continuously keep negative pressure device in the water receiving tank 6, after the water level exceeded overflow pipe 7's highest height, unnecessary water passes through overflow pipe 7 automatic discharge in the water receiving tank 6.
The working principle is as follows: cooling water enters the heat exchange shell 1 through a water inlet pipe 12, the cooling water passes through a channel formed by the baffle plates 5 and then is discharged through a water outlet pipe 13, the gas treatment equipment is connected with a gas outlet pipe 11, peculiar smell gas enters the heat exchange shell 1 through a gas inlet pipe 10, then the peculiar smell gas sequentially passes through the lower gas pipe group 8 and the upper gas pipe group 9, the gas circulating in the lower gas pipe group 8 and the upper gas pipe group 9 is condensed through the cooling water, moisture in the peculiar smell gas is condensed out, the condensed moisture falls into the water receiving tank 6, the water level overflows through a water inlet of the overflow pipe 7, so that a negative pressure device is continuously kept in the water receiving tank 6, when the water level exceeds the highest height of the overflow pipe 7, redundant water in the water receiving tank 6 is automatically discharged through the overflow pipe 7, the peculiar smell gas with the moisture removed is treated by entering the gas treatment equipment through the gas outlet pipe 11, the moisture in advance is removed from the peculiar smell gas, the working load of the gas treatment equipment is reduced, and the working efficiency of the gas treatment equipment is improved.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.
Claims (6)
1. A recovery device for reducing the treatment capacity of volatile organic compounds comprises a heat exchange shell and is characterized in that an upper tube plate and a lower tube plate are symmetrically connected in the heat exchange shell, the tops of the upper tube plate and the inner shell of the heat exchange shell are jointly connected with a partition plate, an air guide assembly is jointly connected between the upper tube plate and the lower tube plate, the top of the heat exchange shell is communicated with an air inlet and outlet assembly, a plurality of baffle plates are connected to the inner wall of the heat exchange shell between the upper tube plate and the lower tube plate in a staggered mode, the air guide assembly penetrates through the plurality of baffle plates, a cooling water circulation inlet and outlet assembly is connected to the wall of the shell of the heat exchange shell, a water receiving tank is communicated to the bottom of the heat exchange shell and is filled with water, an inverted U-shaped overflow pipe penetrates through the outer wall of one side of the water receiving tank, the end portion of the overflow pipe in the water receiving tank is inserted into the water, and a valve is installed on the overflow pipe.
2. The recycling apparatus for reducing the processing amount of volatile organic compounds according to claim 1, wherein the air guide assembly comprises a lower air tube set and an upper air tube set, two ends of the lower air tube set and the upper air tube set are inserted through the upper tube plate, the lower tube plate and the plurality of baffle plates, and the lower air tube set and the upper air tube set are symmetrically arranged with respect to the partition plate.
3. The recycling apparatus for reducing the processing amount of volatile organic compounds according to claim 1, wherein the air inlet and outlet assembly comprises an air inlet pipe and an air outlet pipe, and the air inlet pipe and the air outlet pipe are symmetrically communicated with the top of the heat exchange housing with respect to the partition plate.
4. The recovery apparatus according to claim 1, wherein the cooling water circulation inlet and outlet assembly comprises a water inlet pipe and a water outlet pipe, and the water inlet pipe and the water outlet pipe are symmetrically communicated with the shell wall of the heat exchange shell in a crossed manner.
5. The recycling apparatus for reducing the processing amount of volatile organic compounds according to claim 1, wherein a DN150 viewing mirror is embedded in the front surface of the water receiving tank.
6. The recycling apparatus for reducing the processing amount of volatile organic compounds according to claim 3, wherein a support ring is connected to the inner wall of the air inlet pipe, and a filter screen is installed at the upper end of the support ring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222606263.XU CN218410775U (en) | 2022-09-30 | 2022-09-30 | Recovery equipment for reducing volatile organic compound treatment capacity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222606263.XU CN218410775U (en) | 2022-09-30 | 2022-09-30 | Recovery equipment for reducing volatile organic compound treatment capacity |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218410775U true CN218410775U (en) | 2023-01-31 |
Family
ID=84999176
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222606263.XU Active CN218410775U (en) | 2022-09-30 | 2022-09-30 | Recovery equipment for reducing volatile organic compound treatment capacity |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218410775U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118320441A (en) * | 2024-06-13 | 2024-07-12 | 山东顺成化学有限公司 | Evaporation separation device for bromine purification |
| CN118320441B (en) * | 2024-06-13 | 2024-10-25 | 山东顺成化学有限公司 | Evaporation separation device for bromine purification |
-
2022
- 2022-09-30 CN CN202222606263.XU patent/CN218410775U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118320441A (en) * | 2024-06-13 | 2024-07-12 | 山东顺成化学有限公司 | Evaporation separation device for bromine purification |
| CN118320441B (en) * | 2024-06-13 | 2024-10-25 | 山东顺成化学有限公司 | Evaporation separation device for bromine purification |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN218410775U (en) | Recovery equipment for reducing volatile organic compound treatment capacity | |
| CN210495547U (en) | Gas-liquid separator with condensation function | |
| CN209752226U (en) | Falling film evaporation device for nylon production | |
| CN215002997U (en) | Marine steam collecting and cooling device | |
| CN212425762U (en) | Sewage treatment regenerator | |
| CN215062291U (en) | Multi-functional UV photodissociation petticoat pipe is bright wind groove even | |
| CN214354035U (en) | Condensing unit suitable for double screw extruder | |
| CN211635928U (en) | Vacuumizing equipment and garbage treatment equipment with same | |
| CN211357991U (en) | Corrugated paper effluent treatment plant | |
| CN220206412U (en) | Air draft condensing device and cleaning and texturing equipment | |
| CN221486550U (en) | Gas-liquid separator for hydrogen fuel cell engine | |
| CN108692595B (en) | Horizontal multi-source steam waste heat recovery energy-saving device | |
| CN219457675U (en) | Integrated drain and vent for fuel cell hydrogen circulation system | |
| CN220194448U (en) | Annular exhaust water-gas separation device for laboratory | |
| CN218515727U (en) | Multi-stage water-vapor separation respirator for dish washing machine | |
| CN201105167Y (en) | Capasity-enlarging main body continuous capasity-enlarging evaporator | |
| CN218692432U (en) | Photovoltaic silicon chip work groove updraft ventilator | |
| CN214453738U (en) | Self-cooling ventilating cap of asphalt storage tank | |
| CN220959701U (en) | Emptying pipe condensate water collecting device | |
| CN210050789U (en) | Deaerator exhaust steam recovery device | |
| CN219914118U (en) | Waste gas waste heat recovery heat exchange device for rock wool production line | |
| CN214914642U (en) | Separation device for hood-type furnace tail gas treatment | |
| CN217037766U (en) | Electric automatization control device | |
| CN214223804U (en) | Gas separation device in condenser vacuumizing process | |
| CN215099523U (en) | Vacuumizing liquid overflowing barrel |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |