CN201740358U - Drying tower system - Google Patents
Drying tower system Download PDFInfo
- Publication number
- CN201740358U CN201740358U CN2010202748090U CN201020274809U CN201740358U CN 201740358 U CN201740358 U CN 201740358U CN 2010202748090 U CN2010202748090 U CN 2010202748090U CN 201020274809 U CN201020274809 U CN 201020274809U CN 201740358 U CN201740358 U CN 201740358U
- Authority
- CN
- China
- Prior art keywords
- drying tower
- tower body
- warm
- heat exchanger
- air pipe
- 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
- 238000001035 drying Methods 0.000 title claims abstract description 28
- 239000002699 waste material Substances 0.000 claims description 11
- 230000008676 import Effects 0.000 claims description 4
- 238000003466 welding Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 description 8
- 235000011837 pasties Nutrition 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a drying tower system which comprises a tower body (11), a feeding pipeline (4) and heat exchangers (8), wherein the upper end of the tower body (11) of the drying tower is connected with the feeding pipeline (4), and a warm-air pipe (7) is mounted at the top of the tower body (11). The drying tower system is characterized in that a jacket (1) is arranged outside the feeding pipeline (4) of the drying tower, and a plurality of groups of heat exchangers (8) are connected onto the warm-air pipe (7) mounted at the top of the tower body (11). The utility model has the advantages of fully utilizing the residual heat, saving the energy, and greatly improving the economic benefit.
Description
Technical field
The utility model belongs to chemical machinery field, is specifically related to a kind of drying tower system.
Background technology
Drying tower is that the material of realizing relative back flow of gas motion with the gravity effect is carried out dry equipment.At present, the higher industrial waste gas of temperature that drying tower equipment is discharged is all directly drained, and does not expect and can utilize that in addition, heat exchanger outlet temperature is 100 ℃ in the drying tower equipment, and so the gas of high temperature is directly drained, serious waste the energy.
Summary of the invention
The purpose of this utility model provides a kind of energy-saving and cost-reducing drying tower system.
The purpose of this utility model realizes by following measure:
A kind of drying tower system, comprise tower body, feed pipeline, warm-air pipe and heat exchanger, the upper end of drying tower tower body connects the feed pipeline, warm-air pipe is installed at the top of tower body, it is characterized in that being provided with chuck in the outside of the feed pipeline of drying tower, be installed on the warm-air pipe at tower body top and connect multi-group heat exchanger, preferably connect two groups of heat exchangers.Connect with welding manner between the multi-group heat exchanger.One end of above-mentioned chuck is provided with the waste vapour import, and the other end is provided with the waste vapour outlet.
The beneficial effects of the utility model compared with the prior art: the utility model is by the transformation to the feed pipeline, waste vapour is entered the effect of playing insulation, heating up behind the pipeline, can the pasty material of needs drying be preheated, make pasty material be warmed up to 70 ℃, single energy of at least 30% of just in the dry materials process, can saving from original 20 ℃.
In addition, with warm-air pipe that dry tower body top is connected on increase at least one group of heat exchanger again on original heat exchanger, make cold air shift to an earlier date preheating, heat exchanger exit place temperature is finally reduced to 50 ℃, make the waste heat of drying tower equipment heat exchanger fully obtain utilizing, both saved the energy, and improved economic benefit of enterprises again, annual increase benefit can be up to 30%.
Description of drawings
Fig. 1 is a drying tower feeding pipeline schematic diagram.
Fig. 2 is the drying tower system schematic.
Fig. 3 is the heat exchanger schematic diagram.
Among the figure, 1 is chuck, and 2 is the waste vapour import, and 3 are the waste vapour outlet, and 4 is the feed pipeline, and 5 is material inlet, and 6 is material outlet, and 7 is warm-air pipe, and 8 is heat exchanger, and 9 is air intake, and 10 is venthole, and 11 is tower body, and 12 is inlet of cold air, and 13 is hot air outlet.
The specific embodiment
A kind of drying tower system, comprise tower body 11, feed pipeline 4 and heat exchanger 8, the upper end of drying tower tower body 11 connects feed pipeline 4, warm-air pipe 7 is installed at the top of tower body 11, be provided with chuck 1 in the outside of feed pipeline 4, the warm-air pipe 7 that is installed on tower body 11 tops is provided with multi-group heat exchanger 8, preferably is provided with two groups of heat exchangers 8.Connect with welding manner between the multi-group heat exchanger 8.One end of described chuck is provided with waste vapour import 2, and the other end is provided with waste vapour outlet 3.
When producing, the utility model is by entering the effect of playing insulation, intensification behind the pipeline to the transformation of feed pipeline to waste vapour, and the pasty material of needs drying is preheated, and makes pasty material be warmed up to 70 ℃ from original 20 ℃.
In addition, with warm-air pipe that dry tower body top is connected on increase at least one group of heat exchanger again on the former heat exchanger, make cold air shift to an earlier date preheating, heat exchanger exit place temperature is finally reduced to 50 ℃, makes the waste heat of drying tower equipment heat exchanger fully obtain utilizing.
Claims (4)
1. drying tower system, comprise tower body (11), feed pipeline (4), warm-air pipe (7) and heat exchanger (8), the upper end of drying tower tower body (11) connects feed pipeline (4), warm-air pipe (7) is installed at the top of tower body (11), it is characterized in that being provided with chuck (1) in the outside of the feed pipeline (4) of drying tower, the warm-air pipe (7) that is installed on tower body (11) top is gone up and is connected multi-group heat exchanger (8).
2. drying tower according to claim 1 system is characterized in that an end of described chuck (1) is provided with waste vapour import (2), and the other end is provided with waste vapour outlet (3).
3. drying tower according to claim 1 system, the warm-air pipe (7) that it is characterized in that being installed on tower body (11) top is gone up and is connected two groups of heat exchangers (8).
4. drying tower according to claim 1 system is characterized in that connecting with welding manner between the described multi-group heat exchanger (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202748090U CN201740358U (en) | 2010-07-29 | 2010-07-29 | Drying tower system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202748090U CN201740358U (en) | 2010-07-29 | 2010-07-29 | Drying tower system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201740358U true CN201740358U (en) | 2011-02-09 |
Family
ID=43555633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202748090U Expired - Fee Related CN201740358U (en) | 2010-07-29 | 2010-07-29 | Drying tower system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201740358U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102338555A (en) * | 2010-07-29 | 2012-02-01 | 江苏沃尔得化工有限公司 | Drying tower system |
| CN106885463A (en) * | 2017-04-06 | 2017-06-23 | 胡玉娴 | Drying tower system |
-
2010
- 2010-07-29 CN CN2010202748090U patent/CN201740358U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102338555A (en) * | 2010-07-29 | 2012-02-01 | 江苏沃尔得化工有限公司 | Drying tower system |
| CN106885463A (en) * | 2017-04-06 | 2017-06-23 | 胡玉娴 | Drying tower system |
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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 |
Granted publication date: 20110209 Termination date: 20140729 |
|
| EXPY | Termination of patent right or utility model |