CN202808657U - Starch pulp conditioning apparatus - Google Patents
Starch pulp conditioning apparatus Download PDFInfo
- Publication number
- CN202808657U CN202808657U CN 201220353581 CN201220353581U CN202808657U CN 202808657 U CN202808657 U CN 202808657U CN 201220353581 CN201220353581 CN 201220353581 CN 201220353581 U CN201220353581 U CN 201220353581U CN 202808657 U CN202808657 U CN 202808657U
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- steam
- gelatinization
- heating tube
- starch
- gelatinization device
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Abstract
The utility model discloses a starch pulp conditioning apparatus, comprising a gelatinization device and a pulp conditioning barrel, wherein the gelatinization device is located in the pulp conditioning barrel; the pulp conditioning barrel comprises a stirrer and a feeding hole; the gelatinization device comprises a barrel, a pulp outlet, a channel hole, a steam heating pipe and a steam nozzle; the steam heating pipe is located in the barrel and the bottom of the steam heating pipe is connected with the bottom of the barrel; the pulp outlet is located at the top of the barrel; the through hole is located at the bottom of the barrel; and the steam nozzle is located at the bottom of the steam heating pipe. In this way, the starch pulp conditioning apparatus disclosed by the utility model is capable of accurately controlling the temperature and the steam flow so that the process of directly heating the starch emulsion for quick gelatinization is realized; the pulp conditioning process is simple and convenient in operation; the steam energy source is saved; and effective and accurate control of the viscosity of the semi-gelatinized pulp can be realized and the quality of the semi-gelatinized pulp can be improved.
Description
Technical field
The utility model relates to textile industry Sizing Technology field, particularly relates to a kind of starch size mixing equipment.
Background technology
Before the woven warp sizing, the starch process must be sized mixing after the gelatinization, the slurries that make starch have certain viscosity and clinging power could satisfy the requirement of warp sizing.In order to make slurries meet the requirement of sizing technique, starch will could use through physical or chemical treatment in advance, because different warp thread kinds and fabric specification require corresponding concentration of slurry and viscosity, then to the different viscosity requirement of starch proposition.
Appearance from half gelatinization starching new technology, creatively reverse starch and must pass through the situation that modification could be used for warp sizing, only need use ative starch just to can be used for starching, this greatly saved size mixing with the starching process in the time and the energy that consume, really realized low-carbon (LC), the environmental protection, efficient of warp sizing technique.The used equipment of half gelatinization starching new technology modulation slurries mainly adopts mixing vessels in the tradition, can't accurately control size mixing temperature and steam flow, and the operator is not easy to grasp, and is difficult to obtain the slurries of needs.
The utility model content
The technical problem that the utility model mainly solves provides the starch size mixing equipment of the accurate regulating and controlling temperature of a kind of energy and steam flow.
For solving the problems of the technologies described above, the technical scheme that the utility model adopts is: a kind of starch size mixing equipment is provided, comprise gelatinization device and mixing vessels, described gelatinization device is arranged in described mixing vessels, described mixing vessels comprises agitator and charging opening, described gelatinization device comprises staving, the slurries outlet, access opening, steam heating tube and vapor-nozzle, described steam heating tube is arranged in described staving, described steam heating tube bottom is connected with described staving bottom, described slurries outlet is positioned at described staving top, described access opening is positioned at described staving bottom, and described vapor-nozzle is positioned at described steam heating tube bottom.
In preferred embodiment of the utility model, described gelatinization device also comprises pressurized air decorporation system, described pressurized air decorporation system comprises pressurized air valve, compressed air pipe and compressed-air atomizer, described compressed air pipe wraps up described steam heating tube, described compressed-air atomizer is positioned on the described compressed air pipe, and described compressed-air atomizer is between compressed air inlet and described gelatinization device.
In preferred embodiment of the utility model, described gelatinization device also comprises the anti-spilling safety cover, and described anti-spilling safety cover is positioned at described slurries outlet top.
In preferred embodiment of the utility model, described steam heating tube top comprises flow director.
In preferred embodiment of the utility model, described gelatinization device is near the bucket wall of described mixing vessels.
In preferred embodiment of the utility model, described starch size mixing equipment also comprises the first steam valve and the second steam valve, described the first steam valve is between steam-in and described mixing vessels, described the second steam valve is between described steam-in and described gelatinization device, and described the first steam valve is in described the second steam valve front.
The beneficial effects of the utility model are: starch size mixing equipment of the present utility model, energy is regulating and controlling temperature and steam flow accurately, the technique of the rapid gelatinization of starch emulsion direct heating is achieved, the process operation of sizing mixing is simple and convenient, saved steam energy, the viscosity that can realize half gelatinization slurries is carried out effectively, accurate control, modulates as required required half gelatinization slurries amount, further improves half gelatinization slurries quality.
Description of drawings
Fig. 1 is the sectional view of the utility model starch size mixing equipment one preferred embodiment;
Fig. 2 is the structural representation of the gelatinization device of the size mixing equipment of starch shown in Fig. 1;
The mark of each parts is as follows in the accompanying drawing: 1, gelatinization device, 2, mixing vessels, 3, agitator, 4, charging opening, 5, staving, 6, the gelatinization district, 7, slurries outlet, 8, access opening, 9, steam heating tube, 10, vapor-nozzle, the 11, first steam valve, 12, flow director, 13, anti-spilling safety cover, 14, the pressurized air valve, 15, compressed air pipe, 16, compressed-air atomizer, the 17, second steam valve.
Embodiment
Below in conjunction with accompanying drawing preferred embodiment of the present utility model is described in detail, thereby so that advantage of the present utility model and feature can be easier to be it will be appreciated by those skilled in the art that protection domain of the present utility model is made more explicit defining.
See also Fig. 1 and Fig. 2, the utility model provides a kind of starch size mixing equipment, comprise gelatinization device 1 and mixing vessels 2, in the situation that does not affect stirring described gelatinization device 1 be arranged in described mixing vessels 2 various pieces all can, for example described gelatinization device 1 can be installed on described mixing vessels 2 the bucket wall near.Described mixing vessels 2 comprises agitator 3 and charging opening 4.Described gelatinization device 1 comprises staving 5, slurries outlet 7, access opening 8, steam heating tube 9 and vapor-nozzle 10, described steam heating tube 9 is arranged in described staving 5, described steam heating tube 9 bottoms are connected with described staving 5 bottoms, described slurries outlet 7 is positioned at described staving 5 tops, described access opening 8 is positioned at described staving 5 bottoms, vapor-nozzle 10 is positioned at described steam heating tube 9 bottoms, and described steam heating tube 9 tops can comprise flow director 12, the flow of control steam.
Described gelatinization device 1 also comprises pressurized air decorporation system, described pressurized air decorporation system comprises pressurized air valve 14, compressed air pipe 15 and compressed-air atomizer 16, the described steam heating tube 9 of described compressed air pipe 15 parcels, described compressed-air atomizer 16 is positioned on the described compressed air pipe 15, described compressed-air atomizer 16 is between compressed air inlet and described gelatinization device 1, when concentration of slurry is very high, half gelatinization slurries resistance in described gelatinization device 1 is very large, open described pressurized air decorporation system and can prevent to block, guarantee the normal operation of described gelatinization device 1.
Described gelatinization device 1 also comprises anti-spilling safety cover 13, and described anti-spilling safety cover 13 is positioned at described slurries and exports 7 tops, and described anti-spilling safety cover 13 prevents that the starch emulsion in the described mixing vessels 2 from stopping up described slurries outlet 7, also can prevent described half gelatinization slurries ejection.
Described starch size mixing equipment also comprises the first steam valve 11 and the second steam valve 17, described the first steam valve 11 is between steam-in and described mixing vessels 2, described the second steam valve 17 is between described steam-in and described gelatinization device 1, and described the first steam valve 11 is in described the second steam valve 17 fronts
The principle of work of described gelatinization device 1 is: because of the temperature of the described gelatinization device 1 interior slurries temperature apparently higher than described seasoning bucket 2 interior starch emulsions, the two temperature head, steam from described vapor-nozzle 10 upwards the factors such as ejection and pressure difference starch emulsion is entered from described access opening 8, force the slurries of the gelatinization in the described gelatinization district 6 to overflow from the slurries outlet, reached starch emulsion successively by the purpose of gelatinization.
The starch size mixing equipment that the utility model discloses, energy is regulating and controlling temperature and steam flow accurately, the technique of the rapid gelatinization of starch emulsion direct heating is achieved, and the process operation of sizing mixing is simple and convenient, has saved steam energy, the viscosity that can realize half gelatinization slurries is carried out effectively, accurate control, modulate as required required half gelatinization slurries amount, further improve half gelatinization slurries quality, reduce production costs, enhance productivity, realize the target of save energy, low-carbon environment-friendly.
The above only is embodiment of the present utility model; be not so limit claim of the present utility model; every equivalent structure or equivalent flow process conversion that utilizes the utility model specification sheets and accompanying drawing content to do; or directly or indirectly be used in other relevant technical fields, all in like manner be included in the scope of patent protection of the present utility model.
Claims (6)
1. starch size mixing equipment, it is characterized in that, comprise gelatinization device and mixing vessels, described gelatinization device is arranged in described mixing vessels, described mixing vessels comprises agitator and charging opening, described gelatinization device comprises staving, slurries outlet, access opening, steam heating tube and vapor-nozzle, described steam heating tube is arranged in described staving, described steam heating tube bottom is connected with described staving bottom, described slurries outlet is positioned at described staving top, described access opening is positioned at described staving bottom, and described vapor-nozzle is positioned at described steam heating tube bottom.
2. starch size mixing equipment according to claim 1, it is characterized in that, described gelatinization device also comprises pressurized air decorporation system, described pressurized air decorporation system comprises pressurized air valve, compressed air pipe and compressed-air atomizer, described compressed air pipe wraps up described steam heating tube, described compressed-air atomizer is positioned on the described compressed air pipe, and described compressed-air atomizer is between compressed air inlet and described gelatinization device.
3. starch size mixing equipment according to claim 1 is characterized in that, described gelatinization device also comprises the anti-spilling safety cover, and described anti-spilling safety cover is positioned at described slurries outlet top.
4. starch size mixing equipment according to claim 1 is characterized in that, described steam heating tube top comprises flow director.
5. starch size mixing equipment according to claim 1 is characterized in that, described gelatinization device is near the bucket wall of described mixing vessels.
6. starch size mixing equipment according to claim 1, it is characterized in that, described starch size mixing equipment also comprises the first steam valve and the second steam valve, described the first steam valve is between steam-in and described mixing vessels, described the second steam valve is between described steam-in and described gelatinization device, and described the first steam valve is in described the second steam valve front.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220353581 CN202808657U (en) | 2012-07-20 | 2012-07-20 | Starch pulp conditioning apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220353581 CN202808657U (en) | 2012-07-20 | 2012-07-20 | Starch pulp conditioning apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202808657U true CN202808657U (en) | 2013-03-20 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220353581 Expired - Lifetime CN202808657U (en) | 2012-07-20 | 2012-07-20 | Starch pulp conditioning apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202808657U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111040666A (en) * | 2019-12-31 | 2020-04-21 | 贵州佳德赛新材料有限公司 | Preparation method of plasticized gelatinized starch-based adhesive |
| CN115197333A (en) * | 2022-08-17 | 2022-10-18 | 新昌新和成维生素有限公司 | Starch pasting device and method |
-
2012
- 2012-07-20 CN CN 201220353581 patent/CN202808657U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111040666A (en) * | 2019-12-31 | 2020-04-21 | 贵州佳德赛新材料有限公司 | Preparation method of plasticized gelatinized starch-based adhesive |
| CN115197333A (en) * | 2022-08-17 | 2022-10-18 | 新昌新和成维生素有限公司 | Starch pasting device and method |
| CN115197333B (en) * | 2022-08-17 | 2023-09-01 | 新昌新和成维生素有限公司 | Gelatinization device and gelatinization method for starch |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130320 |
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| CX01 | Expiry of patent term |