CN203540475U - Double-layered slurry atomization device for production of detergent powder - Google Patents
Double-layered slurry atomization device for production of detergent powder Download PDFInfo
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- CN203540475U CN203540475U CN201320567090.3U CN201320567090U CN203540475U CN 203540475 U CN203540475 U CN 203540475U CN 201320567090 U CN201320567090 U CN 201320567090U CN 203540475 U CN203540475 U CN 203540475U
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Abstract
The utility model discloses a double-layered slurry atomization device for the production of detergent powder. The device comprises high-pressure ring pipes connected with a slurry supply pipe, a low-pressure ring pipe, slurry atomization spray guns, a spray gun valve and a steam cleaning pipe, wherein the high-pressure ring pipes are sequentially connected with a main slurry supply pipe; the slurry atomization spray guns are sequentially connected with the high-pressure ring pipes; and the steam cleaning pipe is connected with the slurry atomization spray guns via the spray gun valve. The atomization and cleaning of an upper spray gun and a lower spray gun are finished on a same operation platform. By adopting the double-layered slurry atomization device, the detergent powder particles after being atomized and dried are screened via an eight-mesh sieve, and the number of the particles with particle size being smaller than eight meshes is greater than 98%; the powder yield can be increased by more than 20%; and the energy consumption can be reduced by more than 10%.
Description
Technical field
The utility model relates to a kind of washing powder slip atomising device, belongs to washing powder production technical field, particularly relate to a kind of washing powder dust produce double-deck slurry atomization device.
Background technology
For improving washing powder production efficiency, reduce the energy consumption of the production process of dusting, since the end of the nineties in last century, in newly-built washing powder production line, spray tower adopts double-deck gun design substantially.Basic mentality of designing is: the distance of setting up on spray tower between two-layer operating platform, two-layer operating platform is 4 meters of left and right, the distance of lower floor's operating platform at the bottom of apart from tower is more than 20 meters, a set of high pressure slip endless tube is installed in every layer operation platform and also on endless tube separately, the devices such as atomizing lance is installed.Compared with initial individual layer dusting device, double-deck dusting device is under same tower diameter and essentially identical corollary equipment condition, and the productive rate that dusts can improve more than 20%, can consume energy and reduce more than 10%.
Part washing powder factory is the production efficiency that improves existing spray tower, and spray tower is transformed: increase one deck operating platform, more a set of high pressure endless tube and spray gun be installed.Because increase operating platform newly on original spray tower, improvement project amount is larger again, and Meteorological is higher.
Summary of the invention
For existing spray tower of past, carry out double-deck spray gun improvement expenses high, the problem that quantities is large, the purpose of this utility model is to provide a kind of new washing powder double-deck slurry atomization device of producing that dusts, can and increase under the condition of new slip high pressure endless tube at not newly-increased operating platform, increase again one deck slurry atomization spray gun, the effective atomization quantity that significantly promotes according to demand washing powder slip, High-efficient Production goes out uniform particles, the high-quality washing powder product of stable performance.
In order to achieve the above object, the utility model adopts following technical scheme:
A kind of washing powder is produced with double-deck slurry atomization device, comprises the high pressure endless tube, low pressure endless tube, slurry atomization spray gun, spray gun valve, the steam clean pipe that are connected with slip feeding pipeline; Described slip high pressure endless tube connects slip bulk supply pipe successively; Described steam clean pipe is connected with slurry atomization spray gun by spray gun valve; Described slurry atomization spray gun comprises the upper strata spray gun and the lower floor's spray gun that connect successively slip high compression ring pipe.
As preferably, the length that is shorter in length than lower floor's spray gun of described upper strata spray gun, and upper strata spray gun and lower floor's spray gun are arranged on respectively on same set of high pressure slip endless tube.
As preferably, described upper strata spray gun and lower floor's spray gun are on same operating platform.
As preferably, described upper strata spray gun and the installing space of lower floor's spray gun in spray tower are greater than 2.5 meters.
Owing to having adopted above technical scheme, the beneficial effect the utlity model has is:
By adopting double-deck slurry atomization spray gun (double-deck spray gun adopts length rifle collocation form to use), upper strata spray gun adopts short spray gun, lower floor's spray gun adopts long spray gun, expand the spacing (distance in spray tower of double-deck spray gun is more than 2.5 meters) between spray gun, improving spray gun can the actual quantity of utilizing, effectively increased slurry atomization area, in the case of not increasing new operating platform and new high pressure slip endless tube, improve according to demand effective atomization quantity of slip, with the heat utilization efficiency that improves slurry atomization, with low-carbon environment-friendly technique High-efficient Production, go out uniform particles, the high-quality washing powder product of stable performance.
In addition, the washing powder granularity after the atomization drying that employing the utility model device carries out is divided by 8 mesh sieves, and granularity is less than 8 object powdered granule quantity and is greater than 98%.The productive rate that dusts can improve more than 20%, can consume energy and reduce more than 10%.
Accompanying drawing explanation
Fig. 1 is the mounting means schematic diagram of double-deck spray gun on spray tower.
Fig. 2 is the scheme of installation that uses the slip pipeline, jet chimney and the valve that are associated with double-deck spray gun.
Fig. 3 a is that the utility model washing powder is produced the overall structure schematic diagram with double-deck high pressure slurry atomization device; Fig. 3 b is the plan structure figure of Fig. 3 a.
In figure:
1: upper strata spray gun; 2: spray gun valve; 3: slurry valve; 4: slip high pressure endless tube; 5: lower floor's spray gun; 6: pressure-relief valve; 7: steam valve; 8: steam clean pipe; 9: low pressure slip pipe; 10: spray tower wall; 11: operating platform.
The specific embodiment
Refer to shown in Fig. 1 and 2, the utility model washing powder is produced with double-deck slurry atomization device, and its structure comprises: the slip high pressure endless tube, slip low pressure endless tube, slurry atomization spray gun, spray gun valve, the steam clean pipe that are connected with slip feeding pipeline.This slip high pressure endless tube 4 connects slip bulk supply pipe successively; This slurry atomization spray gun connects slip high compression ring pipe 4 successively; This steam clean pipe is connected with slurry atomization spray gun by valve.
This slurry atomization spray gun comprises: the upper strata spray gun 1 and the lower floor's spray gun 5 that are connected with this slip high pressure endless tube 4.This upper strata spray gun 1 is connected with high pressure slip endless tube 4 with slurry valve 3 by spray gun valve 2 with lower floor spray gun 5.This steam clean pipe 8 is connected with lower floor spray gun 5 by steam valve 7 and upper strata spray gun 1.
Refer to shown in Fig. 3 a and Fig. 3 b the length that is shorter in length than lower floor's spray gun 5 of this upper strata spray gun 1.The distribution condition of this bilayer slurry atomization spray gun is: compared with individual layer spray gun, the spray gun quantity on every layer is less than the quantity of individual layer spray gun.But two-layer spray gun quantity sum, is greater than the quantity of individual layer spray gun.The installing space of this bilayer spray gun is greater than individual layer spray gun installing space more than 50%.
Based on said modules and structure, washing powder of the present utility model is produced as follows by the course of work and the principle of double-deck slurry atomization device:
By spray gun valve 2 by the short spray gun of upper strata spray gun 1() and the long spray gun of the spray gun 5(of lower floor) install, close pressure-relief valve 6 and open slurry valve 3, from the slip of high pressure slip pipe 4, through upper and lower layer spray gun, carry out atomization.Spacing between upper and lower layer spray gun is greater than 2.5 meters, has guaranteed that effective atomization of slip and less atomization intersect.Slurry atomization process atomizing pressure remains on 40Kg left and right.
During stopping production, close slurry valve 3, open pressure-relief valve 6, after removal overbottom pressure, open steam valve 7, use steam flush upper strata spray gun 1 and lower floor's spray gun 5 from steam pipe 8.
The atomization of all upper stratas spray gun 1 and lower floor's spray gun 5 and cleaning operation all complete on same operating platform above.Washing powder granularity after the atomization drying being undertaken by this invention is divided by 8 mesh sieves, and granularity is greater than 98%.The productive rate that dusts can improve more than 20%, can consume energy and reduce more than 10%.
The above, it is only preferred embodiment of the present utility model, not the utility model is done to any pro forma restriction, therefore every, do not depart from technical solutions of the utility model content, any simple modification, equivalent variations and the modification above embodiment done according to technical spirit of the present utility model, all still belong in the scope of technical solutions of the utility model.
Claims (4)
1. washing powder is produced with a double-deck slurry atomization device, it is characterized in that it comprises: the slip high pressure endless tube, slip low pressure endless tube, slurry atomization spray gun, spray gun valve, the steam clean pipe that are connected with slip feeding pipeline; Described slip high pressure endless tube connects slip bulk supply pipe successively; Described steam clean pipe is connected with slurry atomization spray gun by spray gun valve; Described slurry atomization spray gun comprises the upper strata spray gun and the lower floor's spray gun that connect successively slip high compression ring pipe.
Washing powder according to claim 1 produce for double-deck slurry atomization device, it is characterized in that: the length that is shorter in length than lower floor's spray gun of described upper strata spray gun, and upper strata spray gun and lower floor's spray gun are arranged on respectively on same set of high pressure slip endless tube.
3. washing powder according to claim 1 is produced with double-deck slurry atomization device, it is characterized in that: described upper strata spray gun and lower floor's spray gun are on same operating platform.
4. washing powder according to claim 1 is produced with double-deck slurry atomization device, it is characterized in that: described upper strata spray gun and the installing space of lower floor's spray gun in spray tower are greater than 2.5 meters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320567090.3U CN203540475U (en) | 2013-09-12 | 2013-09-12 | Double-layered slurry atomization device for production of detergent powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320567090.3U CN203540475U (en) | 2013-09-12 | 2013-09-12 | Double-layered slurry atomization device for production of detergent powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203540475U true CN203540475U (en) | 2014-04-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320567090.3U Expired - Lifetime CN203540475U (en) | 2013-09-12 | 2013-09-12 | Double-layered slurry atomization device for production of detergent powder |
Country Status (1)
| Country | Link |
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| CN (1) | CN203540475U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104472971A (en) * | 2014-11-30 | 2015-04-01 | 重庆市天星寨粉葛食品有限公司 | Powder cooking and feeding device |
| CN112619550A (en) * | 2020-11-17 | 2021-04-09 | 湖南天欣科技股份有限公司 | Method for increasing yield of ceramic tile spray drying tower |
-
2013
- 2013-09-12 CN CN201320567090.3U patent/CN203540475U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104472971A (en) * | 2014-11-30 | 2015-04-01 | 重庆市天星寨粉葛食品有限公司 | Powder cooking and feeding device |
| CN112619550A (en) * | 2020-11-17 | 2021-04-09 | 湖南天欣科技股份有限公司 | Method for increasing yield of ceramic tile spray drying tower |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140416 |