CN115317950A - Resin production device capable of reducing volatile matter emission - Google Patents
Resin production device capable of reducing volatile matter emission Download PDFInfo
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- CN115317950A CN115317950A CN202211066724.7A CN202211066724A CN115317950A CN 115317950 A CN115317950 A CN 115317950A CN 202211066724 A CN202211066724 A CN 202211066724A CN 115317950 A CN115317950 A CN 115317950A
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- resin production
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- volatile matters
- kettle body
- pipe
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- 239000011347 resin Substances 0.000 title claims abstract description 35
- 229920005989 resin Polymers 0.000 title claims abstract description 35
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 31
- 239000007788 liquid Substances 0.000 claims abstract description 29
- 238000009833 condensation Methods 0.000 claims abstract description 24
- 230000005494 condensation Effects 0.000 claims abstract description 23
- 238000009825 accumulation Methods 0.000 claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000002156 mixing Methods 0.000 claims abstract description 10
- 230000005540 biological transmission Effects 0.000 claims description 24
- 238000003860 storage Methods 0.000 claims description 12
- 238000013329 compounding Methods 0.000 claims description 8
- 239000006185 dispersion Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 5
- 238000005507 spraying Methods 0.000 claims description 3
- 239000002994 raw material Substances 0.000 description 14
- 230000000694 effects Effects 0.000 description 9
- 238000004321 preservation Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000017525 heat dissipation Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
- B01D5/0006—Coils or serpentines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
- B01D5/009—Collecting, removing and/or treatment of the condensate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
- B01J4/002—Nozzle-type elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a resin production device capable of reducing emission of volatile matters, which relates to the technical field of resin production devices and comprises a kettle body and a condensation box, wherein cold water circulates in the condensation box, a liquid collecting box I and a liquid collecting box II are installed in the condensation box, a feeding pipe is installed on the liquid collecting box II and communicated with the outlet end of a conveying pump, a cold accumulation component is installed in the condensation box, a rotating shaft is rotatably installed on the kettle body, an air cooling component opposite to the condensation box is connected to the rotating shaft in a driving manner, and a mixing component in the kettle body is connected to the rotating shaft in a driving manner; the conveying pump can convey the volatile matters in the resin production process, the volatile matters flow in the spiral condensing pipe and are condensed by circulating cold water, and the volatile matters are finally circulated into the kettle body for reuse, so that the emission of the volatile matters can be greatly reduced, and the production efficiency of the resin is improved.
Description
Technical Field
The invention relates to the technical field of resin production devices, in particular to a resin production device capable of reducing volatile matter emission.
Background
The resin is generally referred to as an organic polymer which has a softening or melting range after being heated, has a tendency to flow under an external force when softened, is solid, semi-solid or liquid at room temperature, and may be liquid at some time.
Although the patent of China with the publication number of CN 205495019U discloses a device for reducing the emission of volatile matters in the production process of unsaturated resins, the device comprises a reaction kettle, a bent pipe, a condenser and a material guide pipe, wherein the top of the reaction kettle is connected with the condenser through the bent pipe with a heat preservation function, and the bottom of the condenser is connected to the middle part of the reaction kettle through the material guide pipe; however, although the device can realize the circulation of the volatile raw materials in the resin production process, the volatile raw materials cannot be efficiently condensed and refluxed, which is not beneficial to reducing the emission of volatile matters and improving the production efficiency of the resin; to this end, a resin production apparatus that reduces emission of volatile matters is now provided to solve the above-described technical problems.
Disclosure of Invention
The utility model provides a reduce resin apparatus for producing that volatile matter discharged, includes the cauldron body, installs the delivery pump on the cauldron body, the import end and the cauldron body intercommunication of delivery pump still include the condensation box, the circulation flow has cold water in the condensation box, install in the condensation box and gather liquid case I and II, it has a plurality of spiral condenser pipe to gather the intercommunication between liquid case I and the liquid case II, gather the back flow of installing with cauldron body intercommunication on the liquid case I, install the inlet pipe on the liquid case II, inlet pipe and delivery pump outlet end intercommunication, install the cold-storage subassembly in the condensation box, the rotation axis is installed in the cauldron body, and the drive is connected with the air-cooled subassembly relative with the condensation box on the rotation axis, the drive is connected with the compounding subassembly that is in the cauldron is internal on the rotation axis.
As a modified scheme of the invention: the cold accumulation assembly comprises a plurality of pairs of cold accumulation fins which are vertically arranged, the cold accumulation fins extend to the outside of the condensing box, a plurality of dispersing holes which are located in the inside of the condensing box are formed in the cold accumulation fins, and a plurality of strip holes which are located in the outside of the condensing box are formed in the cold accumulation fins.
As a modified scheme of the invention: the air cooling assembly comprises a bevel gear I which is coaxially connected with the driving shaft, a bevel gear II is meshed with the bevel gear I, an axial flow fan is connected to the bevel gear II in a driving mode, the axial flow fan and the condensation box are arranged oppositely, a servo motor is installed on the kettle body, and an output shaft of the servo motor is in transmission connection with the driving shaft through a belt pulley mechanism.
As a modified scheme of the invention: the reflux pipe is kept away from the one end of condensing box and is installed spiral honeycomb duct, and spiral honeycomb duct and the laminating of cauldron external wall, the spiral honeycomb duct is kept away from installing of reflux pipe and is in the internal spray assembly of cauldron.
As a modified scheme of the invention: the cauldron body overcoat is equipped with the heat preservation cover, spiral honeycomb duct is in between the cauldron body and the heat preservation cover.
As a modified scheme of the invention: the spray assembly comprises a collecting ring pipe communicated with the spiral flow guide pipe, and a plurality of spray heads are uniformly arranged at the bottom of the collecting ring pipe.
As a modified scheme of the invention: the compounding subassembly is established at the epaxial transmission sleeve pipe of drive including the cover, the slip inlays on the transmission sleeve pipe and is equipped with transmission card strip, transmission card strip is fixed in the drive shaft, the equidistant a plurality of puddler that is fixed with of transmission sleeve pipe lateral wall.
As a modified scheme of the invention: the compounding subassembly is still including supporting the push pedal, the transmission sleeve pipe passes through the bearing and connects the rotation to be installed on supporting the push pedal, it is fixed with the spring coil to support between push pedal and the cauldron body, it has the rotatory cam of driving motor drive to support the sliding butt of push pedal bottom.
Compared with the prior art, the invention has the beneficial effects that:
1. the conveying pump can convey the volatile matters in the resin production process, the volatile matters flow in the spiral condensing pipe and are subjected to the condensation effect of the circulating cold water, and finally the volatile matters are circulated into the kettle body for reuse, so that the emission of the volatile matters can be greatly reduced, and the production efficiency of the resin is improved.
2. The air cooling assembly arranged in the spiral condenser can effectively perform air cooling heat dissipation effect on the cold accumulation fins, and meanwhile, the cold accumulation fins can fully dissipate heat in the condenser box, so that gaseous volatile matters in the spiral condenser pipe can be promoted to be rapidly condensed, the condensation efficiency of the volatile matters is greatly improved, and the emission of the volatile matters is effectively reduced.
3. In the invention, the air cooling assembly drives the mixing assembly in the air cooling process of the cold accumulation fin, so that the mixing assembly can fully stir the resin production raw materials in the kettle body, the full mixing of the volatilizable raw materials with the rest raw materials after circulation is effectively promoted, and the resin production efficiency is obviously improved.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention at a certain viewing angle;
FIG. 2 is a partial structure view of the present invention from another perspective;
FIG. 3 is a schematic view of the connection structure of the spiral draft tube and the condenser case;
FIG. 4 is a schematic structural view of a compounding assembly of the present disclosure;
FIG. 5 is a schematic view of the air cooling assembly of the present invention;
FIG. 6 is a schematic view of the internal structure of the condenser case according to the present invention;
fig. 7 is a schematic diagram of the position distribution of the spiral condenser tube and the cold accumulation fins of the present invention.
In the figure: 1-kettle body, 2-heat preservation cover, 3-reflux pipe, 4-condensation box, 5-cold accumulation fin, 6-feeding pipe, 7-axial flow fan, 8-delivery pump, 9-servo motor, 11-bevel gear I, 12-bevel gear II, 13-cold water outlet pipe, 14-cold water inlet pipe, 15-collection ring pipe, 16-stirring rod, 17-spiral guide pipe, 18-pushing plate, 19-cam, 20-driving shaft, 21-nozzle, 22-driving sleeve, 23-driving clamping strip, 24-spring ring, 25-driving motor, 26-belt pulley mechanism, 27-liquid collection box I, 28-dispersion hole, 29-spiral condensation pipe, 30-liquid collection box II and 31-strip hole.
Detailed Description
The technical scheme of the patent is further explained in detail by combining the specific embodiments as follows:
example 1
Referring to fig. 1-7, a resin production apparatus for reducing emission of volatile matter, comprising a kettle 1, a delivery pump 8 installed on the kettle 1, an inlet end of the delivery pump 8 communicated with the kettle 1, a condenser tank 4, cold water circulating in the condenser tank 4, a liquid collecting tank I27 and a liquid collecting tank II30 installed in the condenser tank 4, a plurality of spiral condenser pipes 29 communicated between the liquid collecting tank I27 and the liquid collecting tank II30, a return pipe 3 communicated with the kettle 1 installed on the liquid collecting tank I27, an inlet pipe 6 installed on the liquid collecting tank II30, the inlet pipe 6 communicated with an outlet end of the delivery pump 8, volatile raw materials in the kettle 1 that are heated and volatile and then collected to the top of the kettle 1, the delivery pump 8 pumps out the unreacted gaseous raw materials, the volatile matter enters the spiral condenser pipes 29 along the inlet pipe 6, a cold water inlet pipe 14 and a cold water outlet pipe 13 installed on the condenser tank 4, external cold water flows through the cold water inlet pipe 14, the condenser tank 4 and the cold water outlet pipe 13, thereby ensuring that the volatile matter in the condenser tank 4 flows, and the volatile matter in the condenser tank 1 flows along the spiral condenser pipe 29, and the volatile matter that the volatile matter in the liquid condensate pipe 29 flows, and the volatile matter in the liquid condensate tank is effectively reduced, and the volatile matter in the liquid volatile matter that is discharged along the volatile matter in the spiral condenser pipe 29, and the volatile matter that is discharged.
Install the cold-storage subassembly in the condensing box 4, the cauldron body 1 is gone up to rotate and is installed rotation axis 20, and the drive is connected with the forced air cooling subassembly relative with condensing box 4 on the rotation axis 20, and the drive is connected with the compounding subassembly that is in the cauldron body 1 on the rotation axis 20.
Wherein, the cold-storage subassembly includes a plurality of cold-storage fins 5 to the perpendicular setting, and cold-storage fins 5 extend to the 4 outsides of condensing box, has seted up a plurality of dispersion holes 28 that lie in the inside of condensing box 4 on cold-storage fins 5, has seted up a plurality of on the cold-storage fins 5 and has been located the outside strip hole 31 of condensing box 4.
The cold-storage fin 5 that sets up can conduct heat to condensing box 4 for the heat in condensing box 4 gives off, makes condensing box 4 obtain fine promotion to the condensation effect of spiral honeycomb duct 17, and the dispersion hole 28 of setting does benefit to cold water and passes the flow, promotes cold-storage fin 5's abundant contact heat dissipation.
Wherein, the air-cooled subassembly includes bevel gear I11 with drive shaft 20 coaxial coupling, and the meshing is connected with bevel gear II12 on the bevel gear I11, and the drive is connected with axial fan 7 on bevel gear II12, and axial fan 7 sets up with condenser box 4 is relative, installs servo motor 9 on the cauldron body 1, and servo motor 9's output shaft passes through belt pulley mechanism 26 and is connected with drive shaft 20 transmission.
The servo motor 9 that sets up passes through belt pulley mechanism 26 drive shaft 20 and rotates, drive shaft 20 drive bevel gear I11 is rotatory, bevel gear I11 drive bevel gear II12 with its meshing is rotatory, bevel gear II12 drive axial fan 7 is rotatory, the realization is bloied to the part that cold-storage fin 5 is located the condensing box 4, promote the rapid cooling of cold-storage fin 5 and dispel the heat to the heat of condensing box 4, but further promoted the condensation cycle of volatile matter.
Example 2
Referring to fig. 1-7, based on embodiment 1, in addition, a spiral guide pipe 17 is installed at one end of the return pipe 3 away from the condensing box 4, the spiral guide pipe 17 is attached to the outer wall of the kettle body 1, and a spraying assembly located in the kettle body 1 is installed at the position of the spiral guide pipe 17 away from the return pipe 3.
The thing that can volatilize after the condensation flows through spiral honeycomb duct 17 along back flow 3, at the flow in-process, because the heat transfer of the cauldron body 1 to spiral honeycomb duct 17 for the inside volatile substance that can volatilize of back flow 3 realizes fully preheating the effect when backward flow to the cauldron body 1 in, guarantees the abundant reaction after the thing that can volatilize backward flow, has promoted resin processing effect.
In addition, be equipped with heat preservation cover 2 at cauldron body 1 overcoat, spiral honeycomb duct 17 is in the cauldron body 1 and keeps warm between the cover 2, and the heat preservation cover 2 that sets up plays the heat preservation effect to spiral honeycomb duct 17, reduces the heat and gives off, but promotes volatile substance's preheating effect.
The spray assembly of this device includes the collection ring pipe 15 with spiral honeycomb duct 17 intercommunication, collects ring pipe 15 bottom and evenly installs a plurality of shower nozzle 21, but collects the liquid volatile substance after the condensation through collecting ring pipe 15 realization, but liquid volatile substance from shower nozzle 21 dispersion blowout afterwards, but realizes volatile substance and other raw materials intensive mixing, has promoted the high-efficient production of resin.
Wherein, the compounding subassembly of this device establishes the drive shaft 20 on transmission sleeve pipe 22 including the cover, it inlays and is equipped with transmission card strip 23 to slide on the transmission sleeve pipe 22, transmission card strip 23 is fixed on drive shaft 20, transmission sleeve pipe 22 lateral wall equidistant is fixed with a plurality of puddler 16, the compounding subassembly is still including propping the push pedal 18, transmission sleeve pipe 22 is connected through the bearing and is rotated and install on propping push pedal 18, it is fixed with spring coil 24 to support between push pedal 18 and the cauldron body 1, it has the rotatory cam 19 of drive motor 25 drive to support the slip butt in push pedal 18 bottom.
When rotation axis 20 was rotatory, the transmission card strip 23 on the rotation axis 20 drive transmission sleeve pipe 22 rotatory, and a plurality of puddlers 16 on the transmission sleeve pipe 22 rotated the stirring effect that realizes raw materials in the cauldron body 1 this moment, guaranteed the intensive dispersion and the mixture of raw materials, promoted resin production efficiency.
During the period, the driving motor 25 is started to drive the cam 19 to rotate, the cam 19 pushes against the pushing plate 18, under the elastic action of the spring ring 24, the pushing plate 18 is pushed to drive the transmission sleeve 22 to vertically reciprocate, namely, the stirring rod 16 can vertically reciprocate, so that raw materials at different vertical positions are fully stirred and mixed, and the resin production efficiency is greatly improved.
In summary, the conveying pump 8 provided in the invention can convey the volatile matter in the resin production process, the volatile matter spirally flows in the spiral condensing pipe 29 and is condensed by the circulating cold water, and finally the volatile matter is circulated to the kettle body 1 for reuse, so that the emission of the volatile matter can be greatly reduced, and the resin production efficiency can be improved. The air cooling assembly arranged in the invention can effectively perform air cooling heat dissipation effect on the cold accumulation fins 5, and meanwhile, the cold accumulation fins 5 can fully dissipate heat in the condensing box 4, so that gaseous volatile matters in the spiral condensing pipe 29 can be promoted to be rapidly condensed, the condensing efficiency of the volatile matters is greatly improved, and the emission of the volatile matters is effectively reduced. In the invention, the air cooling component drives the mixing component in the process of air cooling the cold accumulation fins 5, so that the mixing component can fully stir the resin production raw materials in the kettle body 1, the full mixing of the volatile raw materials with the rest raw materials after circulation is effectively promoted, and the resin production efficiency is obviously improved.
It should be noted that, although the present specification describes embodiments, each embodiment does not include only a single technical solution, and such description of the specification is only for clarity, and those skilled in the art should take the specification as a whole, and the technical solutions in the embodiments may be appropriately combined to form other embodiments understood by those skilled in the art, and the above embodiments only express the preferred embodiments of the technical solutions, and the description thereof is more specific and detailed, but not construed as limiting the scope of the claims of the technical solutions. It should be noted that, for those skilled in the art, various changes, modifications and substitutions can be made without departing from the spirit of the present invention, and these changes and substitutions belong to the protection scope of the present invention. The protection scope of this technical solution patent should be subject to the appended claims.
Claims (8)
1. The utility model provides a resin apparatus for producing that reduction volatilizable thing discharged, includes the cauldron body (1), installs delivery pump (8) on the cauldron body (1), the entrance point and the cauldron body (1) intercommunication of delivery pump (8), its characterized in that still includes condensate box (4), circulation has cold water in condensate box (4), install in condensate box (4) and gather liquid case I (27) and gather liquid case II (30), gather liquid case I (27) and gather between liquid case II (30) the intercommunication have a plurality of spiral condenser pipe (29), gather and install back flow (3) with cauldron body (1) intercommunication on liquid case I (27), install inlet pipe (6) on gathering liquid case II (30), inlet pipe (6) and delivery pump (8) exit end intercommunication, install the cold-storage subassembly in condensate box (4), the cauldron body (1) is gone up to rotate and is installed rotation axis (20), and the drive is connected with the forced air cooling subassembly relative with condensate box (4) on rotation axis (20), the drive is connected with the compounding subassembly in the cauldron body (1).
2. The resin production device for reducing the emission of volatile matters according to claim 1, wherein the cold accumulation assembly comprises a plurality of pairs of cold accumulation fins (5) which are vertically arranged, the cold accumulation fins (5) extend to the outside of the condensation box (4), a plurality of dispersion holes (28) which are positioned inside the condensation box (4) are formed in the cold accumulation fins (5), and a plurality of strip holes (31) which are positioned outside the condensation box (4) are formed in the cold accumulation fins (5).
3. The resin production device capable of reducing emission of volatile matters according to claim 1, wherein the air cooling assembly comprises a bevel gear I (11) coaxially connected with the driving shaft (20), the bevel gear I (11) is engaged with a bevel gear II (12), the bevel gear II (12) is in driving connection with an axial fan (7), the axial fan (7) is arranged opposite to the condensation tank (4), the kettle body (1) is provided with a servo motor (9), and an output shaft of the servo motor (9) is in driving connection with the driving shaft (20) through a belt pulley mechanism (26).
4. The resin production device for reducing emission of volatile matters according to claim 1, wherein a spiral guide pipe (17) is installed at one end of the return pipe (3) far away from the condensation box (4), the spiral guide pipe (17) is attached to the outer wall of the kettle body (1), and the spiral guide pipe (17) is far away from the return pipe (3) and is provided with a spraying assembly in the kettle body (1).
5. The resin production device capable of reducing emission of volatile matters according to claim 4, wherein the kettle body (1) is externally sleeved with a heat-insulating cover (2), and the spiral flow guide pipe (17) is positioned between the kettle body (1) and the heat-insulating cover (2).
6. A resin production apparatus with reduced emission of volatile substances according to claim 4, wherein said spraying assembly comprises a collecting loop (15) communicating with a spiral duct (17), and a plurality of spray nozzles (21) are uniformly installed on the bottom of said collecting loop (15).
7. The resin production device for reducing emission of volatile matters according to claim 1, wherein the mixing component comprises a transmission sleeve (22) sleeved on the driving shaft (20), a transmission clamping strip (23) is embedded on the transmission sleeve (22) in a sliding manner, the transmission clamping strip (23) is fixed on the driving shaft (20), and a plurality of stirring rods (16) are fixed on the side wall of the transmission sleeve (22) at equal intervals.
8. The resin production device for reducing emission of volatile matters according to claim 7, wherein the mixing assembly further comprises a pushing plate (18), the transmission sleeve (22) is rotatably mounted on the pushing plate (18) through a bearing connection, a spring ring (24) is fixed between the pushing plate (18) and the kettle body (1), and a cam (19) driven to rotate by a driving motor (25) is connected to the bottom of the pushing plate (18) in a sliding and abutting mode.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211066724.7A CN115317950A (en) | 2022-09-01 | 2022-09-01 | Resin production device capable of reducing volatile matter emission |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211066724.7A CN115317950A (en) | 2022-09-01 | 2022-09-01 | Resin production device capable of reducing volatile matter emission |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN115317950A true CN115317950A (en) | 2022-11-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202211066724.7A Pending CN115317950A (en) | 2022-09-01 | 2022-09-01 | Resin production device capable of reducing volatile matter emission |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115317950A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN206369389U (en) * | 2016-12-13 | 2017-08-01 | 浙江汇明节能科技有限公司 | A kind of ice cold-storage storage tank based on heat transfer technology of heat pipe |
| CN211988581U (en) * | 2019-12-04 | 2020-11-24 | 博立尔化工（扬州）有限公司 | Resin reaction kettle |
-
2022
- 2022-09-01 CN CN202211066724.7A patent/CN115317950A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN206369389U (en) * | 2016-12-13 | 2017-08-01 | 浙江汇明节能科技有限公司 | A kind of ice cold-storage storage tank based on heat transfer technology of heat pipe |
| CN211988581U (en) * | 2019-12-04 | 2020-11-24 | 博立尔化工（扬州）有限公司 | Resin reaction kettle |
Non-Patent Citations (1)
| Title |
|---|
| 吴业正等: "制冷与低温技术原理", 高等教育出版社, pages: 323 - 324 * |
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