CN205241878U - Novel add direct spinning production system of mill base stoste - Google Patents
Novel add direct spinning production system of mill base stoste Download PDFInfo
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- CN205241878U CN205241878U CN201520874031.XU CN201520874031U CN205241878U CN 205241878 U CN205241878 U CN 205241878U CN 201520874031 U CN201520874031 U CN 201520874031U CN 205241878 U CN205241878 U CN 205241878U
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- spinning
- mill base
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- measuring pump
- base stoste
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Abstract
The utility model relates to a novel add direct spinning production system of mill base stoste, it includes polymerization device, booster pump, fuse -element cooler and the spinning box that sets up in pairs, spinning box I is in proper order with measuring pump I, spinning subassembly I, spinning cooler I, the system of oiling I, network ware I, draft setting device I, main network ware I, winding formation device I, inspection grading plant I and packing plant I link to each other in advance, spinning box II in proper order with measuring pump II, spinning subassembly II, spinning cooler II, the system of oiling II, in advance network ware II, draft setting device II, main network ware II, winding formation device II, inspection grading plant II and packing plant II link to each other, be equipped with mill base stoste addition system between the spinning box that sets up in pairs and fuse -element cooler, mill base stoste addition system includes mill base stoste agitator tank and measuring pump III. The utility model discloses the energy consumption is low, and it is effectual to dye, efficient and zero release.
Description
Technical field
The utility model relates to a kind of spinning production system, is specifically related to a kind of spinning production system of adding mill base.
Background technology
Since 21st century, China's polyester industrial development rapidly. Within 2000, polyester fiber output is 5,100,000 tons, within 2009, having reached 2,200 ten thousand tons, and has reached especially 2,510 ten thousand tons in 2010. In 10 years, increased by 2,000 ten thousand tons, average annual growth rate exceedes 15%. Its range of application also expands rapidly, relates to the national economy various aspects such as clothing, decoration, household textiles, fabrics for industrial use, Industrial Engineering. Update demonstration, more than 80% chemical fibre product needs printing and dyeing, and the annual sewage producing of printing and dyeing reaches 5,000,000,000 tons. As textile material, also there is following shortcoming in polyester fiber: dyeability is poor, color fastness is low, weatherability is poor etc. simultaneously. What existing conventional fibre dyeing adopted is to be made into cloth dyeing after polyester is spun into fiber again, requires dyestuff or pigment and polyester to have certain affinity and adhesion, and dyeing course belongs to chemical change. Conventional polyester dyeing is generally to carry out under HTHP, by destarch, add the multiple working procedures such as dyeing and complete, has the problems such as energy consumption is large, efficiency is low, dye rear fiber color fastness and weatherability is poor, dyeing cost is high, seriously polluted.
Summary of the invention
Goal of the invention: the purpose of this utility model is in order to overcome deficiency of the prior art, provides a kind of energy consumption low, and Color is good, the fused mass directly spinning production system of the novel interpolation mill base stoste of efficiency height and zero-emission.
Technical scheme: in order to solve the problems of the technologies described above, the fused mass directly spinning production system of a kind of novel interpolation mill base stoste described in the utility model, it comprises polymerizing reactor, booster pump, melt cooler and the spinning manifold arranging in pairs, the spinning manifold arranging is in pairs divided into spinning manifold I and spinning manifold II, described spinning manifold I successively with measuring pump I, filament spinning component I, spinning cooler I, oil feeding system I, pre-Network device I, drafting-shaping device I, master network device I, coiling and molding device I, inspection grading plant I is connected with packing device I, described spinning manifold II successively with measuring pump II, filament spinning component II, spinning cooler II, oil feeding system II, pre-Network device II, drafting-shaping device II, master network device II, coiling and molding device II, inspection grading plant II is connected with packing device II, between the spinning manifold arranging in pairs and melt cooler, is provided with mill base stoste add-on system, and described mill base stoste add-on system comprises mill base stoste agitator tank and measuring pump III.
Be provided with the former liquid container of mill base in described mill base stoste agitator tank front portion.
In described measuring pump III, be respectively equipped with measurement controller and pressure controller, on the pipeline between described measuring pump III and spinning manifold, be provided with temperature controller.
Described spinning manifold I is connected with melt cooler respectively with spinning manifold II.
The spinning manifold arranging in pairs can arrange four groups or three groups, single spinning manifold rear portion in every group is all connected with packing device with a set of measuring pump independently, filament spinning component, spinning cooler, oil feeding system, pre-Network device, drafting-shaping device, master network device, coiling and molding device, inspection grading plant, and two spinning manifold front portions in every group are all connected with melt cooler respectively.
The utility model is in multiple spinning manifolds or certain branch line production system, to add mill base stoste to produce colored fiber.
Beneficial effect: the utility model compared with prior art, its remarkable advantage is: the utility model is in melt Conveying pipeline, by melt and mill base physical mixed, colouring agent is dispersed in melt, before so just having saved, dye pre-treatment, the high energy consumption maximum discharge operations such as high-temperature pressure dyeing, realize low energy consumption, zero-emission, in melt Conveying pipeline, add mill base stoste adding set, act on follow-up whole spinning system, overall throughput is large, native system Color is good, production efficiency is high, the many casings of realistic colored fiber in enormous quantities (or single production line) Flexible Production is adjusted instructions for use.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further described.
As shown in Figure 1, the fused mass directly spinning production system of a kind of novel interpolation mill base stoste described in the utility model, it comprises polymerizing reactor 1, booster pump 2, melt cooler 3 and the spinning manifold arranging in pairs, the spinning manifold arranging is in pairs divided into spinning manifold I 4 and spinning manifold II 5, described spinning manifold I 4 successively with measuring pump I 6, filament spinning component I 7, spinning cooler I 8, oil feeding system I 9, pre-Network device I 10, drafting-shaping device I 11, master network device I 12, coiling and molding device I 13, inspection grading plant I 14 is connected with packing device I 15, described spinning manifold II 5 successively with measuring pump II 16, filament spinning component II 17, spinning cooler II 18, oil feeding system II 19, pre-Network device II 20, drafting-shaping device II 21, master network device II 22, coiling and molding device II 23, inspection grading plant II 24 is connected with packing device II 25, between the spinning manifold arranging in pairs and melt cooler 3, is provided with mill base stoste add-on system, and described mill base stoste add-on system comprises mill base stoste agitator tank 26 and measuring pump III 27, be provided with the former liquid container 28 of mill base in described mill base stoste agitator tank 26 front portions, in described measuring pump III 27, be respectively equipped with measurement controller 29 and pressure controller 30, on the pipeline between described measuring pump III 27 and spinning manifold, be provided with temperature controller 31, described spinning manifold I 4 is connected with melt cooler 3 respectively with spinning manifold II 5. the utility model is in melt Conveying pipeline, by melt and mill base physical mixed, colouring agent is dispersed in melt, before so just having saved, dye the high energy consumption such as pre-treatment, high-temperature pressure dyeing maximum discharge operation, realize low energy consumption, zero-emission, in melt Conveying pipeline, add mill base stoste adding set, act on follow-up whole spinning system, overall throughput is large, native system Color is good, production efficiency is high, and the many casings of realistic colored fiber in enormous quantities (or single production line) Flexible Production is adjusted instructions for use.
The utility model provides a kind of thinking and method; method and the approach of this technical scheme of specific implementation are a lot; the above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art, not departing under the prerequisite of the utility model principle, can also make some improvements and modifications; these improvements and modifications also should be considered as protection domain of the present utility model, in the present embodiment not clear and definite each part all available prior art realized.
Claims (4)
1. a fused mass directly spinning production system for novel interpolation mill base stoste, is characterized in that: it comprises polymerizing reactor (1), booster pump (2), melt cooler (3) and the spinning manifold arranging in pairs, the spinning manifold arranging is in pairs divided into spinning manifold I (4) and spinning manifold II (5), described spinning manifold I (4) successively with measuring pump I (6), filament spinning component I (7), spinning cooler I (8), oil feeding system I (9), pre-Network device I (10), drafting-shaping device I (11), master network device I (12), coiling and molding device I (13), inspection grading plant I (14) be connected with packing device I (15), described spinning manifold II (5) successively with measuring pump II (16), filament spinning component II (17), spinning cooler II (18), oil feeding system II (19), pre-Network device II (20), drafting-shaping device II (21), master network device II (22), coiling and molding device II (23), inspection grading plant II (24) is connected with packing device II (25), between the spinning manifold arranging in pairs and melt cooler (3), be provided with mill base stoste add-on system, described mill base stoste add-on system comprises mill base stoste agitator tank (26) and measuring pump III (27).
2. the fused mass directly spinning production system of novel interpolation mill base stoste according to claim 1, is characterized in that: be provided with the former liquid container of mill base (28) in described mill base stoste agitator tank (26) front portion.
3. the fused mass directly spinning production system of novel interpolation mill base stoste according to claim 1, it is characterized in that: in described measuring pump III (27), be respectively equipped with measurement controller (29) and pressure controller (30), on the pipeline between described measuring pump III (27) and spinning manifold, be provided with temperature controller (31).
4. the fused mass directly spinning production system of novel interpolation mill base stoste according to claim 1, is characterized in that: described spinning manifold I (4) is connected with melt cooler (3) respectively with spinning manifold II (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520874031.XU CN205241878U (en) | 2015-11-05 | 2015-11-05 | Novel add direct spinning production system of mill base stoste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520874031.XU CN205241878U (en) | 2015-11-05 | 2015-11-05 | Novel add direct spinning production system of mill base stoste |
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| Publication Number | Publication Date |
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| CN205241878U true CN205241878U (en) | 2016-05-18 |
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| CN201520874031.XU Active CN205241878U (en) | 2015-11-05 | 2015-11-05 | Novel add direct spinning production system of mill base stoste |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106676659A (en) * | 2015-11-05 | 2017-05-17 | 无锡索力得科技发展有限公司 | Novel straight-spinning production system for melt added with color paste stock solution |
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2015
- 2015-11-05 CN CN201520874031.XU patent/CN205241878U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106676659A (en) * | 2015-11-05 | 2017-05-17 | 无锡索力得科技发展有限公司 | Novel straight-spinning production system for melt added with color paste stock solution |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190416 Address after: 214253 New Town Industrial Park, Yixing City, Wuxi City, Jiangsu Province Patentee after: Jiangsu Huaya Chemical Fiber Co.,Ltd. Address before: 214253 No. 1 Huaya Road, Industrial Park, Xinxin Town, Yixing, Wuxi City, Jiangsu Province Patentee before: WUXI SUOLIDE TECHNOLOGY DEVELOPMENT CO., LTD. |
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| TR01 | Transfer of patent right |