CN205223429U - Divide warm area multichannel online heat treatment device - Google Patents

Divide warm area multichannel online heat treatment device Download PDF

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Publication number
CN205223429U
CN205223429U CN201521091448.5U CN201521091448U CN205223429U CN 205223429 U CN205223429 U CN 205223429U CN 201521091448 U CN201521091448 U CN 201521091448U CN 205223429 U CN205223429 U CN 205223429U
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China
Prior art keywords
multichannel
drying tunnel
warm area
heater
directive wheel
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CN201521091448.5U
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Chinese (zh)
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韩和平
石和平
杨开丛
张鸥
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Sichuan Huiteng Technology Co Ltd
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Sichuan Huiteng Technology Co Ltd
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  • Treatment Of Fiber Materials (AREA)

Abstract

The utility model belongs to the technical field of special fiber and specifically relates to divide warm area multichannel online heat treatment device. The device includes filament delivery unit (1), first leading wheel (2), tension sheave (3), multichannel drying tunnel heater (4), second leading wheel (6), third leading wheel (7) and a receipts silk unit (8), filament delivery unit (1) loop through first leading wheel (2) and tension sheave (3) and be connected with multichannel drying tunnel heater (4), set up warm area (5) at multichannel drying tunnel heater (4), the rear end of multichannel drying tunnel heater (4) loops through second leading wheel (6) and third leading wheel (7) and receives silk units (8) and is connected. The utility model discloses a method that multistage warm area gradient changes in the multichannel drying tunnel heater makes fibre " core ", " table " layer porosity reduce, but adopt multichannel drying tunnel simultaneous processing multiple fibre, efficiency is higher, can obtain the steady quality, intensity, the fibre that elastic modulus is higher.

Description

Divide warm area multichannel burning optimization on line device
Technical field
The utility model relates to a kind of annealing device of aramid IIII fiber, belongs to special fibre technical field, is specially a point warm area multichannel burning optimization on line device.
Background technology
Wet spinning is one of main spinning process of chemical fibre, and aramid IIII fiber textile technology both domestic and external improves in conventional wet spinning, defines the manufacturing system of a set of comparatively perfect.
General wet spinning primarily of solidifying, spray washing, cold and hot baking, rolling, to oil/starching and a few procedure composition of heat treatment.
Prior heat treatment device divides two kinds: intermittent vacuum heat treatment and the heat treatment of single drying tunnel continous mode.Intermittent vacuum heat treatment is that the silk cylinder of spinning process rolling is put into multistation heat treatment still, and under vacuum condition, heat up, nitrogen is filled in cooling, drives still and obtains finished silk cylinder.The method has the large advantage for the treatment of capacity, but does not stretch to fiber due to during this device heat treatment, and molecularly oriented declines, and product mechanical performance reduces.The heat treatment of single drying tunnel continous mode is at some tension, in nitrogen protection, tow passes through heater continuously at a certain temperature, the method is suitable for the lower tenacity fibers of heat setting temperature below 300 DEG C, and aramid IIII fiber belongs to high-module high-strength special fibre, setting temperature is at 450 DEG C, therefore before and after sizing, the temperature difference is larger, " core " when the quick dehydration of fiber causes height-oriented, " table " layer produces hole, fibre machinery performance is not ideal, fibre strength is 4.5GPa, in addition, single drying tunnel continous mode heat treatment process amount is little, be difficult to meet large-scale industrial production.
Summary of the invention
The utility model is just for above technical problem, a kind of point of warm area multichannel burning optimization on line device is provided, adopting this device can overcome material makes fiber dry out fast in drawing-off weightlessness because being subject to excessive alternating hot and cold, " core ", " table " layer when causing height-oriented produces hole, the problem that fibre machinery performance is undesirable, can also overcome the shortcoming that single drying tunnel continous mode heat treatment process amount is little.
Concrete technical scheme of the present utility model is as follows:
Divide warm area multichannel burning optimization on line device, this device comprises thread supplying machine group, the first directive wheel, straining pulley, multichannel drying tunnel heater, the second directive wheel, the 3rd directive wheel and receipts silk unit, described thread supplying machine group is connected with multichannel drying tunnel heater with straining pulley by the first directive wheel successively, arrange warm area at multichannel drying tunnel heater, the rear end of multichannel drying tunnel heater is connected with receipts silk unit with the 3rd directive wheel by the second directive wheel successively.
Described warm area arranges 9, and the temperature of these 9 warm areas is respectively 250 DEG C-300 DEG C-350 DEG C-400 DEG C-450 DEG C-400 DEG C-350 DEG C-300 DEG C-250 DEG C.
A kind of point warm area multichannel burning optimization on line device that adopts carries out a point warm area multichannel burning optimization on line method, and the method comprises the following steps:
S1, heats up multichannel drying tunnel heater and reaches technological temperature;
S2, is filled with nitrogen in multichannel drying tunnel heater;
S3, puts web-like raw tow into thread supplying machine group;
S4, raw tow is released from thread supplying machine group, successively by the first directive wheel, straining pulley, multichannel drying tunnel heater, the second directive wheel, the 3rd directive wheel and receipts silk unit;
S5, receives silk unit by finished product tow last volume.
The temperature of described multichannel drying tunnel heater is multistage warm area graded, is divided into 9 warm areas according to heating-up temperature, successively by 250 DEG C-300 DEG C-350 DEG C-400 DEG C-450 DEG C-400 DEG C-350 DEG C-300 DEG C-250 DEG C during heat treatment of fiber.
24 parallel equally distributed passages are set in described multichannel drying tunnel heater and run through whole heater.
Owing to have employed this devices and methods therefor, make raw tow in heat treatment process, straining pulley is by tow tension signal feedback to spin bank, and spin bank controls spinning motor spinning speed, thus reaches heat treatment of fiber process identical tension raising molecularly oriented.Raw tow in the heater successively by each warm area, gradual intensification and cooling in each warm area.Being filled with nitrogen in warm area, protecting tow when being heated, not oxidation by air.
Good effect of the present utility model is embodied in:
(1), by adopting the method for multistage warm area graded in multichannel drying tunnel heater, fiber " core ", " table " layer porosity are reduced;
(2), adopt multichannel drying tunnel to process multi beam tow simultaneously, increase heat treatment process amount.
(3), can process multiple fibre, efficiency is higher simultaneously, can obtain steady quality, the fiber that intensity, elastic modelling quantity are higher.
Accompanying drawing explanation
Fig. 1 is the structural representation of point warm area multichannel burning optimization on line device in the utility model.
Wherein, 1---thread supplying machine group, 2---the first directive wheel, 3---straining pulley, 4---multichannel drying tunnel heater, 5---warm area, 6---the second directive wheel, 7---the 3rd directive wheel, 8---receipts silk unit.
Detailed description of the invention
Clearly understand to make goal of the invention of the present utility model, technical scheme and advantage, below in conjunction with detailed description of the invention, the utility model is described in further detail, but this should be interpreted as that the scope of the above-mentioned theme of the utility model is only limitted to following embodiment.
Embodiment 1:
Divide warm area multichannel burning optimization on line device, this device comprises thread supplying machine group, the first directive wheel, straining pulley, multichannel drying tunnel heater, the second directive wheel, the 3rd directive wheel and receipts silk unit, described thread supplying machine group is connected with multichannel drying tunnel heater with straining pulley by the first directive wheel successively, arrange warm area at multichannel drying tunnel heater, the rear end of multichannel drying tunnel heater is connected with receipts silk unit with the 3rd directive wheel by the second directive wheel successively.
Described warm area arranges 9, and the temperature of these 9 warm areas is respectively 250 DEG C-300 DEG C-350 DEG C-400 DEG C-450 DEG C-400 DEG C-350 DEG C-300 DEG C-250 DEG C.
A kind of point warm area multichannel burning optimization on line device that adopts carries out a point warm area multichannel burning optimization on line method, and the method comprises the following steps:
S1, heats up multichannel drying tunnel heater and reaches technological temperature;
S2, is filled with nitrogen in multichannel drying tunnel heater;
S3, puts web-like raw tow into thread supplying machine group;
S4, raw tow is released from thread supplying machine group, successively by the first directive wheel, straining pulley, multichannel drying tunnel heater, the second directive wheel, the 3rd directive wheel and receipts silk unit;
S5, receives silk unit by finished product tow last volume.
The temperature of described multichannel drying tunnel heater is multistage warm area graded, is divided into 9 warm areas according to heating-up temperature, successively by 250 DEG C-300 DEG C-350 DEG C-400 DEG C-450 DEG C-400 DEG C-350 DEG C-300 DEG C-250 DEG C during heat treatment of fiber.
24 parallel equally distributed passages are set in described multichannel drying tunnel heater and run through whole heater.
Owing to have employed this devices and methods therefor, make raw tow in heat treatment process, straining pulley is by tow tension signal feedback to spin bank, and spin bank controls spinning motor spinning speed, thus reaches heat treatment of fiber process identical tension raising molecularly oriented.Raw tow in the heater successively by each warm area, gradual intensification and cooling in each warm area.Being filled with nitrogen in warm area, protecting tow when being heated, not oxidation by air.
Above embodiment only for illustration of the utility model, and is not limitation of the utility model, and the those of ordinary skill of relevant technical field, when not departing from spirit and scope of the present utility model, can also make various change and modification.Therefore all equivalent technical schemes also belong to category of the present utility model.

Claims (3)

1. point warm area multichannel burning optimization on line device, it is characterized in that: this device comprises thread supplying machine group (1), first directive wheel (2), straining pulley (3), multichannel drying tunnel heater (4), second directive wheel (6), 3rd directive wheel (7) and receipts silk unit (8), described thread supplying machine group (1) is connected with multichannel drying tunnel heater (4) with straining pulley (3) by the first directive wheel (2) successively, at multichannel drying tunnel heater (4), warm area (5) is set, the rear end of multichannel drying tunnel heater (4) is connected with receipts silk unit (8) with the 3rd directive wheel (7) by the second directive wheel (6) successively.
2. according to claim 1 point of warm area multichannel burning optimization on line device, is characterized in that: described warm area (5) is 9 warm areas.
3. according to claim 1 point of warm area multichannel burning optimization on line device, is characterized in that: arrange 24 parallel equally distributed passages in described multichannel drying tunnel heater (4) and run through whole heater.
CN201521091448.5U 2015-12-25 2015-12-25 Divide warm area multichannel online heat treatment device Active CN205223429U (en)

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Application Number Priority Date Filing Date Title
CN201521091448.5U CN205223429U (en) 2015-12-25 2015-12-25 Divide warm area multichannel online heat treatment device

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106591973A (en) * 2016-11-22 2017-04-26 殷石 Method for preparing high-strength synthetic fibers by using two-stage high-temperature sectional drafting
CN106637447A (en) * 2016-11-22 2017-05-10 殷石 Method for preparing high-strength synthetic fibers via multi-pass high-temperature segment-based drafting
CN106702508A (en) * 2016-11-22 2017-05-24 殷石 Method for preparing high strength synthetic fibers by sectional drafting at high temperature
CN109778328A (en) * 2018-12-19 2019-05-21 四川辉腾科技股份有限公司 A kind of aramid IIII fiber continous way air blast annealing device and technique
CN111519264A (en) * 2020-04-24 2020-08-11 江苏奥神新材料股份有限公司 Fiber heating system
CN111636107A (en) * 2020-05-29 2020-09-08 中鸿纳米纤维技术丹阳有限公司 Polyglycolic acid liquid crystal nascent fiber heat treatment device and method
CN115198384A (en) * 2022-07-19 2022-10-18 安徽弋尚纺织科技有限公司 Drying and shaping equipment for processing flame-retardant elastic fibers

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106591973A (en) * 2016-11-22 2017-04-26 殷石 Method for preparing high-strength synthetic fibers by using two-stage high-temperature sectional drafting
CN106637447A (en) * 2016-11-22 2017-05-10 殷石 Method for preparing high-strength synthetic fibers via multi-pass high-temperature segment-based drafting
CN106702508A (en) * 2016-11-22 2017-05-24 殷石 Method for preparing high strength synthetic fibers by sectional drafting at high temperature
CN106637447B (en) * 2016-11-22 2020-02-04 殷石 Method for preparing high-strength synthetic fiber through multi-channel high-temperature sectional drafting
CN106591973B (en) * 2016-11-22 2020-02-07 殷石 Method for preparing high-strength synthetic fiber by two-stage high-temperature sectional drafting
CN106702508B (en) * 2016-11-22 2020-02-07 殷石 Method for preparing high-strength synthetic fiber by one-step high-temperature sectional drafting
CN109778328A (en) * 2018-12-19 2019-05-21 四川辉腾科技股份有限公司 A kind of aramid IIII fiber continous way air blast annealing device and technique
CN111519264A (en) * 2020-04-24 2020-08-11 江苏奥神新材料股份有限公司 Fiber heating system
CN111636107A (en) * 2020-05-29 2020-09-08 中鸿纳米纤维技术丹阳有限公司 Polyglycolic acid liquid crystal nascent fiber heat treatment device and method
CN111636107B (en) * 2020-05-29 2022-04-15 中鸿纳米纤维技术丹阳有限公司 Polyglycolic acid liquid crystal nascent fiber heat treatment device and method
CN115198384A (en) * 2022-07-19 2022-10-18 安徽弋尚纺织科技有限公司 Drying and shaping equipment for processing flame-retardant elastic fibers
CN115198384B (en) * 2022-07-19 2024-02-09 安徽弋尚纺织科技有限公司 Drying and shaping equipment for processing flame-retardant elastic fibers

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Multi-channel online heat treatment device in different temperature zones

Effective date of registration: 20220901

Granted publication date: 20160511

Pledgee: Sichuan Fushun Rural Commercial Bank Co.,Ltd.

Pledgor: SICHUAN HUITENG TECHNOLOGY Co.,Ltd.

Registration number: Y2022980014202

PE01 Entry into force of the registration of the contract for pledge of patent right