CN203231621U - Energy-saving type material drying device - Google Patents
Energy-saving type material drying device Download PDFInfo
- Publication number
- CN203231621U CN203231621U CN201320171175XU CN201320171175U CN203231621U CN 203231621 U CN203231621 U CN 203231621U CN 201320171175X U CN201320171175X U CN 201320171175XU CN 201320171175 U CN201320171175 U CN 201320171175U CN 203231621 U CN203231621 U CN 203231621U
- Authority
- CN
- China
- Prior art keywords
- pipe
- water collecting
- energy
- drying device
- container
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses an energy-saving type material drying device. The energy-saving type material drying device comprises a main dryer, a cyclone separator and an induced draft fan, wherein the main dryer, the cyclone separator and the induced draft fan are sequentially connected through pipes. The lower portion of the main dryer is connected with a hot air pipe and a feeding port, a steam heater is arranged on the hot air pipe, a condensed water collecting pipe is arranged on the steam heater, and a container is arranged on an outer wall of the main dryer and connected with the condensed water collecting pipe through a pipe device. Heat in condensed water of the steam heater can be effectively utilized, energy is saved, and efficiency of the drying device is improved.
Description
Technical field
The utility model relates to a kind of chemical production equipment, relates in particular to the material drying device in a kind of production of chlorinated polyethylene process.
Background technology
In the production process of chliorinated polyvinyl chloride, pneumatic conveying drying is to adopt at present more dry technology, this dry technology is to use hot-air directly to contact with the material that is dried, the convection heat transfer' heat-transfer by convection mass transfer, and make the material that is dried be suspended in the fluid equably, thereby the two-phase contact area is big, strengthened the heat and mass transfer process, this mode need be used a large amount of hot-airs, required hot-air mostly obtains by steam heater, also produced a large amount of condensed waters in the steam heater with air heat the time, the temperature of this condensed water is basically all greater than 85 degree, and these condensed waters were unemployed in the past, and year in year out, this has just caused the waste of a large amount of energy.
The utility model content
At the above-mentioned deficiency of existing in prior technology, technical problem to be solved in the utility model provides a kind of energy-saving material drying device, and it can effectively utilize the heat in the steam heater condensed water, energy savings, the efficient of raising drying device.
In order to solve the problems of the technologies described above, a kind of energy-saving material drying device of the present utility model, comprise the main drier, cyclone separator, the air-introduced machine that lead to successively by pipeline, leading in main drier bottom has warm-air pipe and charging aperture, warm-air pipe is provided with steam heater, and described steam heater is provided with the condensed water collecting pipe; Described main drier outer wall is provided with container, and this container and described condensed water collecting pipe lead to by piping installation.
In said structure, because described steam heater is provided with the condensed water collecting pipe, the condensed water with higher temperature that produces in the steam heater course of work just can collect; Again because described main drier outer wall is provided with container, this container and described condensed water collecting pipe lead to by piping installation, the collected high-temperature condensation water of condensed water collecting pipe just can be passed in the container on the main drier outer wall by piping installation like this, because collected condensed water itself has the above temperature of 85 degree, after it arrives in the container on the main drier outer wall, just can heat to the material in the main drier by main drier outer wall, and can intercept temperature higher in the main drier to external diffusion, make waste heat obtain effective utilization, save the energy, also improved the efficient of dry materials simultaneously.
A kind of preferred embodiment of the present utility model, described main drier is pneumatic conveyer dryer.Owing to adopt pneumatic conveyer dryer as main drier; and pneumatic conveyer dryer is to utilize swiftly flowing thermal current that wet fine grained or granular material are suspended in wherein, carries out drying in the air current flow process, has the heat transfer coefficient height; characteristics such as heat transfer area is big, and drying time is short.So drying effect is comparatively desirable concerning the haloflex product of fine particulate, can obtain drying effect preferably.
Another kind of preferred embodiment of the present utility model, described container is the jacket water tank around main drier outer wall.This embodiment structure is simple relatively, and the condensation hot water that utilizes can heat main drier around the outer wall of main drier.
Further preferred embodiment of the present utility model, described container is the helix water pipe structure around main drier outer wall.Adopt this structure that condensation heat water is heated along the helix water pipe around main drier outer wall, heating is evenly distributed, and effect is better.
Another preferred embodiment of the utility model, described piping installation is by hot water collecting box, heat-exchanger pump and lead at the water inlet pipe of described container bottom and the outlet pipe that leads on described container top and constitute, described hot water collecting box and condensed water collecting pipe lead to, described water inlet pipe leads to by heat-exchanger pump and hot water collecting box, and described outlet pipe and hot water collecting box lead to.Adopt this mode, can guarantee that condensation hot water effectively collects and utilize heat-exchanger pump to be transported in the needed container, the hot water that still has uniform temperature that the container outlet pipe can also be come out is collected the use of remaining valid in the hot water collecting box.
The another further preferred embodiment of the utility model, described container, hot water collecting box, water inlet pipe, outlet pipe are coated with heat-insulation layer.Adopt this mode, can prevent the loss of heat better, reach further energy-saving effect.
Description of drawings
Below in conjunction with the drawings and specific embodiments a kind of energy-saving material drying device of the utility model is described in further detail.
Fig. 1 is the structural representation of an embodiment of a kind of energy-saving material drying device of the utility model
Among the figure: 1-piping installation, 101-outlet pipe, 102-heat-exchanger pump, 103-hot water collecting box, 104-water inlet pipe, 2-condensed water collecting pipe, 3-container, 4-steam heater, 5-warm-air pipe, 6-master's drier, 7-charging aperture, 8-cyclone separator, 9-air-introduced machine.
The specific embodiment
Main drier 6 is pneumatic conveyer dryer in a kind of energy-saving material drying device shown in Figure 1, it leads to cyclone separator 8, air-introduced machine 9 from top successively by conveyance conduit, the outer wall at main drier middle part is provided with container 3, this container 3 is the jacket water tank around main drier 6 outer walls, bottom at main drier 6, lead to warm-air pipe 5 and charging aperture 7 are arranged, warm-air pipe 5 is provided with steam heater 4, described steam heater 4 is provided with condensed water collecting pipe 2, and this condensed water collecting pipe 2 leads to by piping installation 1 and container 3; Described piping installation 1 is by hot water collecting box 103, heat-exchanger pump 102 and lead at the water inlet pipe 104 of described container 3 bottoms and the outlet pipe 101 that leads on described container 3 tops and constitute, described hot water collecting box 103 leads to condensed water collecting pipe 2, described water inlet pipe 104 leads to by heat-exchanger pump 102 and hot water collecting box, and described outlet pipe 101 leads to hot water collecting box 103.Described container 3, hot water collecting box 103, water inlet pipe 104, outlet pipe 101 are coated with the heat-insulation layer (not shown).
In the course of work; enter and enter in the main drier 6 after the warm-air pipe 5 interior air with certain pressure heat by steam heater 4; and under the effect of Venturi effect, the raw material to be dried in the charging aperture 7 is delivered in the main drier 6; in main drier 6; the swiftly flowing thermal current that enters in the warm-air pipe makes wet fine grained or powdery haloflex therein material suspended; the haloflex material is able to form maximum effective contact area with thermal current; in the air current flow process, carry out drying; obtaining dry material top from main drier 6 under the effect of air-flow enters in the cyclone separator 8 along pipeline; cyclone separator 8 utilizes the air-flow power of air-introduced machine 9 that raw material is separated with air draught; the product of the drying that separation obtains is concentrated to the bottom of cyclone separator 8 and from discharging opening output, air-flow is then derived by air-introduced machine 9.The entire product dry run circulates continuously like this and carries out.
The temperature that produces in steam heater 4 courses of work reaches the condensation hot water of 85 degree in condensed water collecting pipe 2 is collected hot water collecting box 103, by heat-exchanger pump 102 with the hot water in the hot water collecting box 103 in water inlet pipe 104 is transported to container 3, in order to the outer wall through main drier 6 material in the main drier 6 is heated simultaneously, and can intercept temperature higher in the main drier 6 to external diffusion, make waste heat obtain effective utilization, save the energy, also improved the efficient of dry materials simultaneously.The flow of hot water that enters container 3 is crossed container 3 backs and is flow in the hot water collecting box 103 utilization of can remaining valid from outlet pipe 101.
Above-mentionedly only enumerated a kind of preferred embodiment of the present utility model, but the utility model is not limited thereto, can also does many improvement and conversion.Main drier 6 as described also can adopt the drier of other type, can container 3 be set at its outer wall equally, forms the energy-conservation utilization to the high temperature condensation hot water of steam heater 4; Described container 3 can also be the helix water pipe structure around main drier 6 outer walls, and hot water is flow through along the pipeline of this helix water pipe, can reach the UTILIZATION OF VESIDUAL HEAT IN effect equally.Therefore, as long as in improvement and the conversion under the situation of the utility model basic principle, done, all should be considered as falling in the protection domain of the present utility model.
Claims (6)
1. energy-saving material drying device, comprise the main drier (6), cyclone separator (8), the air-introduced machine (9) that lead to successively by pipeline, lead to warm-air pipe is arranged (5) and charging aperture (7) in main drier (6) bottom, warm-air pipe (5) is provided with steam heater (4), it is characterized in that: described steam heater (4) is provided with condensed water collecting pipe (2); Described main drier (6) outer wall is provided with container (3), and this container (3) leads to by piping installation (1) with described condensed water collecting pipe (2).
2. a kind of energy-saving material drying device according to claim 1, it is characterized in that: described main drier (6) is pneumatic conveyer dryer.
3. a kind of energy-saving material drying device according to claim 1 and 2 is characterized in that: described container (3) is the jacket water tank around main drier (6) outer wall.
4. a kind of energy-saving material drying device according to claim 1 and 2 is characterized in that: described container (3) is the helix water pipe structure around main drier (6) outer wall.
5. a kind of energy-saving material drying device according to claim 1 and 2, it is characterized in that: described piping installation (1) is by hot water collecting box (103), heat-exchanger pump (102) and lead at the water inlet pipe (104) of described container (3) bottom and the outlet pipe (101) that leads on described container (3) top and constitute, described hot water collecting box (103) leads to condensed water collecting pipe (2), described water inlet pipe (104) leads to by heat-exchanger pump (102) and hot water collecting box (103), and described outlet pipe (101) leads to hot water collecting box (103).
6. a kind of energy-saving material drying device according to claim 1 and 2, it is characterized in that: described container (3), hot water collecting box (103), water inlet pipe (104), outlet pipe (101) are coated with heat-insulation layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320171175XU CN203231621U (en) | 2013-04-09 | 2013-04-09 | Energy-saving type material drying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320171175XU CN203231621U (en) | 2013-04-09 | 2013-04-09 | Energy-saving type material drying device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN203231621U true CN203231621U (en) | 2013-10-09 |
Family
ID=49287744
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201320171175XU Expired - Fee Related CN203231621U (en) | 2013-04-09 | 2013-04-09 | Energy-saving type material drying device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN203231621U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105581220A (en) * | 2016-02-20 | 2016-05-18 | 诸城市鑫正达机械有限公司 | Continuous powder damp and hot sterilization equipment |
CN106671216A (en) * | 2016-11-30 | 2017-05-17 | 聊城德晟木业有限公司 | Preparation method for novel low-density, low-cost and high-strength shaving board |
-
2013
- 2013-04-09 CN CN201320171175XU patent/CN203231621U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105581220A (en) * | 2016-02-20 | 2016-05-18 | 诸城市鑫正达机械有限公司 | Continuous powder damp and hot sterilization equipment |
CN106671216A (en) * | 2016-11-30 | 2017-05-17 | 聊城德晟木业有限公司 | Preparation method for novel low-density, low-cost and high-strength shaving board |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203848526U (en) | Novel solar drying system | |
CN103471358A (en) | Drying machine | |
CN105466196A (en) | Double-effect vacuum tube bundle drying system | |
CN203642636U (en) | Powder two-stage drying system | |
CN203231621U (en) | Energy-saving type material drying device | |
CN102901330A (en) | Solar dryer | |
CN207635731U (en) | A kind of mold baking room | |
CN201731738U (en) | Heat recoverer for damp hot discharge air and heat recovery system | |
CN211650768U (en) | System for utilize solar energy heating air supply desicator dry sand material | |
CN205482260U (en) | Economic benefits and social benefits vacuum tube bank drying system | |
CN202543265U (en) | Heat recovery device for heat treatment quenching furnace | |
CN208327790U (en) | A kind of low temperature belt-type drying machine waste heat dehumidification device | |
CN102889763A (en) | Drying equipment | |
CN104126660B (en) | A kind of round-the-clock fluidized bed process crop dryer | |
CN203908259U (en) | Solar power drying device | |
CN202902784U (en) | Drying device | |
CN206385016U (en) | A kind of sludge at low temperature highly effective drying equipment | |
CN204421580U (en) | A kind of food drying process reclaims hot water heat energy and hot water re-use device | |
CN203969080U (en) | Energy-saving fluidized bed process cereal continuous drier | |
CN109915907B (en) | Intelligent control solar heat collector | |
CN203704607U (en) | Steam temperature-controlled drying device | |
CN203719346U (en) | Mesh belt dryer | |
CN203785287U (en) | Solar thermal collector hot air drying device | |
CN206930138U (en) | Air laser heating automatic temp controller in production is dried in one kind polymerization | |
CN205313352U (en) | Fluidized bed sludge drying apparatus |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131009 Termination date: 20190409 |