CN201784079U - Air heating device for drying ACR resin - Google Patents
Air heating device for drying ACR resin Download PDFInfo
- Publication number
- CN201784079U CN201784079U CN2010205127453U CN201020512745U CN201784079U CN 201784079 U CN201784079 U CN 201784079U CN 2010205127453 U CN2010205127453 U CN 2010205127453U CN 201020512745 U CN201020512745 U CN 201020512745U CN 201784079 U CN201784079 U CN 201784079U
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- inlet pipe
- heat exchanger
- drying
- heat
- heating device
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Abstract
An air heating device for drying ACR resin comprises a spray tower, and is characterized by further comprising a heat conducting oil furnace and a heat exchanger. An oil inlet pipe and an oil return pipe are arranged between the heat conducting oil furnace and a heat exchanger, a cold air inlet pipe is connected to the heat exchanger, and the spray tower is connected with the heat exchange via an air inlet pipe. The air heating device for drying ACR resin adopts heat conducting oil to heat up cool air to 170 DEG C at one step, thereby reducing cost and energy consumption, shortening processing link and reducing complex degree of equipment.
Description
Technical field
The utility model relates to a kind of air heating apparatus, the air heating apparatus that uses in particularly a kind of ACR product drying process.
Background technology
In the ACR production operation, the emulsion that contains the ACR resin that need will synthesize, drying becomes ACR resin-oatmeal powder finished product, the present ACR drying process of my company adopts the spray tower drying process, spray-drying has continuous operation, moisture is adjustable, advantages such as labor strength is low, but spray-drying needs a large amount of hot-airs that use 170 degrees centigrade, keeps normal drying operation, adopts commercial Steam Heating cold air at present usually, obtain 170 degrees centigrade hot-air again with electrically heated mode, the cost height, power consumption is high, the equipment complexity.
The utility model content
According to above deficiency of the prior art, the technical problems to be solved in the utility model is: a kind of above-mentioned defective that solved is provided, can one time heats cold air to 170 degree centigrade, cost and energy consumption have been reduced, shorten technology chain length, reduced the ACR resin drying air heating apparatus of equipment complexity.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of ACR resin drying air heating apparatus, comprise spray tower, it is characterized in that: also comprise heat-conducting oil furnace and heat exchanger, be provided with oil inlet pipe and oil return pipe between heat-conducting oil furnace and the heat exchanger, be connected with the cold air inlet pipe on the heat exchanger, spray tower is connected by air inlet pipe with heat exchanger.
During use, cold air enters heat exchanger by the cold air inlet pipe, deep fat in the heat-conducting oil furnace enters in the heat exchanger by oil inlet pipe, heats cold air to 170 degree centigrade, hot-air after the heating enters into drying tower by air inlet pipe, and cooled cold oil is recycled in the heat-conducting oil furnace through oil return pipe and reheats in the heat exchanger.
The beneficial effect that the utility model had is: the ACR resin drying by heats cold air to 170 of conduction oil degree centigrade, has reduced cost and energy consumption with air heating apparatus, has shortened technology chain length, has reduced the equipment complexity.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Among the figure: 1, spray tower; 2, heat-conducting oil furnace; 3, heat exchanger; 4, oil inlet pipe; 5, oil return pipe; 6, cold air inlet pipe; 7, air inlet pipe.
The specific embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is described further:
As shown in Figure 1, be provided with oil inlet pipe 4 and oil return pipe 5 between heat-conducting oil furnace 2 and the heat exchanger 3, be connected with cold air inlet pipe 6 on the heat exchanger 3, spray tower 1 is connected by air inlet pipe 7 with heat exchanger 3.
During use, cold air enters heat exchanger 3 by cold air inlet pipe 6, deep fat in the heat-conducting oil furnace 2 enters in the heat exchanger 3 by oil inlet pipe 4, heats cold air to 170 degree centigrade, hot-air after the heating enters into drying tower 1 by air inlet pipe 7, and cooled cold oil is recycled in the heat-conducting oil furnace 2 through oil return pipe 5 and reheats in the heat exchanger 3.
Claims (1)
1. ACR resin drying air heating apparatus, comprise spray tower (1), it is characterized in that: also comprise heat-conducting oil furnace (2) and heat exchanger (3), be provided with oil inlet pipe (4) and oil return pipe (5) between heat-conducting oil furnace (2) and the heat exchanger (3), be connected with cold air inlet pipe (6) on the heat exchanger (3), spray tower (1) is connected by air inlet pipe (7) with heat exchanger (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205127453U CN201784079U (en) | 2010-08-30 | 2010-08-30 | Air heating device for drying ACR resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205127453U CN201784079U (en) | 2010-08-30 | 2010-08-30 | Air heating device for drying ACR resin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201784079U true CN201784079U (en) | 2011-04-06 |
Family
ID=43816056
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205127453U Expired - Fee Related CN201784079U (en) | 2010-08-30 | 2010-08-30 | Air heating device for drying ACR resin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201784079U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104279757A (en) * | 2014-09-26 | 2015-01-14 | 河南鑫企实业有限公司 | Waste heat utilization system for biomass heat-transfer oil furnace |
-
2010
- 2010-08-30 CN CN2010205127453U patent/CN201784079U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104279757A (en) * | 2014-09-26 | 2015-01-14 | 河南鑫企实业有限公司 | Waste heat utilization system for biomass heat-transfer oil furnace |
| CN104279757B (en) * | 2014-09-26 | 2017-08-08 | 河南鑫企实业有限公司 | Biomass heat-conduction oil oven afterheat utilizing 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: 20110406 Termination date: 20140830 |
|
| EXPY | Termination of patent right or utility model |