CN100379904C - Preparation method of low damping internal circular blow multipore spinning fiber - Google Patents

Preparation method of low damping internal circular blow multipore spinning fiber Download PDF

Info

Publication number
CN100379904C
CN100379904C CNB2004100526901A CN200410052690A CN100379904C CN 100379904 C CN100379904 C CN 100379904C CN B2004100526901 A CNB2004100526901 A CN B2004100526901A CN 200410052690 A CN200410052690 A CN 200410052690A CN 100379904 C CN100379904 C CN 100379904C
Authority
CN
China
Prior art keywords
blowing
rectification tube
air
rectification
low damping
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CNB2004100526901A
Other languages
Chinese (zh)
Other versions
CN1718875A (en
Inventor
来可华
杨洪平
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Pacific Second Textile Machine Chemical Fiber Complete Equipment Co ltd
Original Assignee
Shanghai Taipingyang Textile Machinery Complement Equipment Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shanghai Taipingyang Textile Machinery Complement Equipment Co Ltd filed Critical Shanghai Taipingyang Textile Machinery Complement Equipment Co Ltd
Priority to CNB2004100526901A priority Critical patent/CN100379904C/en
Publication of CN1718875A publication Critical patent/CN1718875A/en
Application granted granted Critical
Publication of CN100379904C publication Critical patent/CN100379904C/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Artificial Filaments (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

The present invention belongs to a terylene production method, particularly to a method for preparing inner ring blown terylene staple fibers with low damping. An inner ring blown technology has the characteristic of low damping of the air pressure of a cooling-air main air pipe passing through a rectifying cylinder of an air blowing head besides adopting other procedures in the prior art, namely that the goals of reduction of the equipment for devices of air conditioning systems, reduction of actual installation capacity of air conditioning units and reduction of the self cold energy consumption of air conditioning systems can be realized by using the inner ring blown cooling air blowing process for production. The actual installation capacity of air conditioning units is 55.7(kW), and the consumption of refrigerated water is 50(*10<4>kCal).

Description

Preparation method of low damping inner loop porously fibrous
Technical field
The invention belongs to the terylene production technology, be in particular a kind of Preparation method of low damping inner loop porously fibrous.
Background technology
The wearability of polyster fibre is good, applied range, and its Volume and Growth speed is all far above other chemical fibre kinds.Cutting down the consumption of energy is one of approach that improves product competitiveness, and the energy consumption of air-conditioning system accounts for fiber manufacturing cost about more than 1/3rd in the polyester staple fiber production.For the tow process for cooling in the spinning technique, require to possess characteristics such as the attaching capacity cold energy energy consumption few, air-conditioning system self of reduced investment, air-conditioning unit is low.
In the current domestic and international polyester staple fiber tow process for cooling, interior ring blow moulding (adopting circular spinnerets, cooling air outwards to be blown by the center) is divided into the form of high damping and two kinds of blowings of superelevation damping:
(1) polyester staple fiber tow process for cooling has ring blow moulding in the high damping, ring blow moulding in the superelevation damping.Between 4000pa.s~5000pa.s, a blowing rectification tube is micropore sintered metal cylinder to the ring blow moulding to the cooling air air main blast of molten polyester cooling curing in the high damping.This rectification tube complex manufacturing technology of drying, in 1~2 year service life, one-time investment quite high (be equivalent to the technology of the present invention 100 times) need purge with high pressure air during cleaning.
(2) between 6000pa.s~10000pa.s, a blowing rectification tube adds porous metals rectification tube for high molecular foam material to the interior ring of employing superelevation damping blow moulding to the cooling air air main blast of molten polyester cooling curing.This complex manufacturing technology of drying, high molecular foam material are the imported material of a kind of " with promptly abandon ", and in service life short (10~20 days), cost of investment height (be equivalent to the technology of the present invention 10 times) need add clear water with cleaning agent during cleaning.
Summary of the invention
Purpose of the present invention is exactly to provide a kind of Preparation method of low damping inner loop porously fibrous for the above-mentioned defective that solves prior art.
Purpose of the present invention can be achieved through the following technical solutions:
A kind of Preparation method of low damping inner loop porously fibrous, its polyester fondant with inherent viscosity 0.63~0.65 is that raw material carries out in the fiber manufacture process, other steps in adopting prior art, interior ring blow moulding also has the cooling air air main blast≤2500pa.s through a blowing rectification tube, a blowing rectification tube adds porous metals rectification tube for woven wire, spinnerets hole count 〉=3701~4620, blowing wind speed 0.8~2m/s, blowing rectification tube inlet pressure 1500~1800pa.s, 1200pa.s falls in rectification pressure, the feature of Blowing drum blast 200~350pa.s.
The structure and the material of a described blowing rectification tube are: the woven wire material is a stainless steel, wire twine footpath 0.05~1mm, several 30~70 orders of wire net mesh; Porous metals rectification tube material is a stainless steel, plate thickness 1~3mm, and perforate aperture 1~3mm, percent opening 10~30%, open-cellular form is for evenly distributing from top to bottom; Length 400~the 700mm of rectification tube.
The blowing manufacture craft that the present invention adopts is simple, adopts common clear water to clean and adds common compressed air purging, and service life, one-time investment was low more than 2 years, and the simple expense of service procedure is low.
The invention has the advantages that: (1) low resistance process route, air-conditioning system can be selected fan with low voltage for use, has reduced the voltage withstand class of airduct, and the equipment investment of whole system is reduced; (2) the unit attaching capacity of air-conditioning draught fan reduces, and air-conditioning technology chilled water amount reduces, and the material consumption energy consumption greatly reduces; (3) the production equipment requirement is low, and the product-specific investments cost reduces, and increases economic efficiency.Ring blows the porous polyester staple fibre and has product top grade rate height in the low resistance that makes with this method, quality such as maintain the leading position among the colleague at home, and also production run is stable.
Purpose of the present invention, advantage and characteristics will illustrate by the non-limitative illustration of following preferential enforcement and explain that these embodiment only provide as an example with reference to accompanying drawing.
Description of drawings
Fig. 1 is a process flow diagram of the present invention.
The specific embodiment
As shown in Figure 1, the present invention is that raw material carries out in the fiber manufacture process with the polyester fondant of inherent viscosity 0.63~0.65, other steps in adopting prior art, the cooling air air main blast≤2500pa.s of interior ring blow moulding, the blowing head adds porous metals rectification tube, spinnerets hole count 〉=3701~4620 for woven wire, blowing wind speed 0.8~2m/s, blowing rectification tube inlet pressure 1500~1800pa.s, 1200pa.s falls in rectification pressure, Blowing drum blast 200~350pa.s.
The structure and the material of the blowing rectification tube that the present invention adopts are: the woven wire material is a stainless steel, wire twine footpath 0.05~1mm, several 30~70 orders of wire net mesh; Porous metals rectification tube material is a stainless steel, plate thickness 1~3mm, and perforate aperture 1~3mm, percent opening 10~30%, open-cellular form is for evenly distributing from top to bottom; Length 400~the 700mm of rectification tube.
Adopt the present invention to carry out the spinning of 1.33dtex (spinnerets hole count 3780), 1.56dtex (spinnerets hole count 3780), three kinds of polyester staple fiber kinds of 1.56dtex (spinnerets hole count 4250), all obtained good effect, the interior ring of low resistance blows the porous polyester staple fibre and has product top grade rate height, the quality that maintains the leading position etc. among the colleague at home, production run is stable.
Embodiment one:
With inherent viscosity is that 0.63~0.65 polyester fondant is that raw material carries out in 1.33dtex (spinnerets hole count 3780) the fiber production process, other steps in adopting prior art, the cooling air air main blast≤2500pa.s of interior ring blow moulding, the blowing head adds porous metals rectification tube for woven wire, blowing wind speed 1~2m/s, a blowing rectification tube inlet pressure 1500pa.s, 1200pa.s falls in rectification pressure, Blowing drum blast 200~300pa.s.The properties of product that make are good, and the physical index of gained silk sees Table 1.
Embodiment two:
With inherent viscosity is that 0.63~0.65 polyester fondant is that raw material carries out in 1.56dtex (spinnerets hole count 3780) the fiber production process, other steps in adopting prior art, the cooling air air main blast≤2500pa.s of interior ring blow moulding, the blowing head adds porous metals rectification tube for woven wire, blowing wind speed 1~2m/s, a blowing rectification tube inlet pressure 1600pa.s, 1200pa.s falls in rectification pressure, Blowing drum blast 200~300pa.s.The properties of product that make are good, and the physical index of gained silk sees Table 1.
Embodiment three:
With inherent viscosity is that 0.63~0.65 polyester fondant is that raw material carries out in 1.56dtex (spinnerets hole count 4250) the fiber production process, other steps in adopting prior art, the cooling air air main blast≤2500pa.s of interior ring blow moulding, the blowing head adds porous metals rectification tube for woven wire, blowing wind speed 1~2m/s, a blowing rectification tube inlet pressure 1600pa.s, 1200pa.s falls in rectification pressure, Blowing drum blast 300~350pa.s.The properties of product that make are good, and the physical index of gained silk sees Table 1.Spin the contrast of precursor performance indications before the made polyester staple fiber of table 1 the present invention and prior art *
Sample Line density dtex Line density irregularity cv% Fracture strength Cn.dtex Fracture strength cv% Extension at break degree % Extension at break irregularity % Overall target
Contrast sample one 4.74 7.80 1.70 7.60 368.60 10.40 Excellent
Contrast sample two 5.35 7.20 1.65 7.90 306.00 7.80 Excellent
Embodiment one 4.78 6.70 1.78 7.50 376.00 7.90 Excellent
Embodiment two 5.33 6.50 1.68 7.79 308.60 7.31 Excellent
Embodiment three 5.30 6.80 1.72 7.00 320.00 8.80 Excellent
*Spin precursor before 1.33dtex (the spinnerets hole count 3780) polyester staple fiber of contrast sample one for the production of Shanghai terylene enterprise.
*Spin precursor before 1.56dtex (the spinnerets hole count 2800) polyester staple fiber of contrast sample two for the introduction of foreign technology production of Zhejiang terylene enterprise.
The present invention adds porous metals rectification tube by the blowing head for woven wire, and the cooling air air main blast≤2500pa.s of ring blow moulding in adopting realizes that the tow cooling curing is shaped.Under the condition of spinnerets hole count 〉=3780~4430, the polyester staple fiber that is spun into has product top grade rate height, has at home quality and production run stable properties such as maintain the leading position among the colleague.The present invention and process route comparison in the past, obtained following effect:
Adopt the production process that ring blow moulding route carries out the tow cooling in the low resistance, the voltage withstand class of air-conditioning system airduct reduces, and equipment is required to reduce, and the material consumption energy consumption is required to reduce, and helps reducing investment, reduces product cost.It is good to spin the precursor quality before the ring blow moulding is produced in the low resistance, product top grade rate height, and product quality maintains the leading position in going together at home.Production technology of the present invention and corollary equipment have the function advanced with state generation in polyester staple fiber production equipment field, to save foreign exchange, development of national industry is very useful.

Claims (2)

1. Preparation method of low damping inner loop porously fibrous, it is characterized by: with inherent viscosity is that 0.63~0.65 polyester fondant is that raw material carries out in the fiber manufacture process, other steps in adopting prior art, interior ring blow moulding also has the cooling air air main blast≤2500pa.s through a blowing rectification tube, a blowing rectification tube adds porous metals rectification tube for woven wire, spinnerets hole count 〉=3701~4620, blowing wind speed 0.8~2.0m/s, blowing rectification tube inlet pressure 1500~1800pa.s, 1200pa.s falls in rectification pressure, Blowing drum blast 200~350pa.s.
2. Preparation method of low damping inner loop porously fibrous according to claim 1 is characterized by: the structure and the material of a blowing rectification tube are: the woven wire material is a stainless steel, wire twine footpath 0.05~1mm, several 30~70 orders of wire net mesh; Porous metals rectification tube material is a stainless steel, plate thickness 1~3mm, and perforate aperture 1~3mm, percent opening 10~30%, open-cellular form is for evenly distributing from top to bottom; Length 400~the 700mm of rectification tube.
CNB2004100526901A 2004-07-09 2004-07-09 Preparation method of low damping internal circular blow multipore spinning fiber Expired - Lifetime CN100379904C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2004100526901A CN100379904C (en) 2004-07-09 2004-07-09 Preparation method of low damping internal circular blow multipore spinning fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2004100526901A CN100379904C (en) 2004-07-09 2004-07-09 Preparation method of low damping internal circular blow multipore spinning fiber

Publications (2)

Publication Number Publication Date
CN1718875A CN1718875A (en) 2006-01-11
CN100379904C true CN100379904C (en) 2008-04-09

Family

ID=35930819

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2004100526901A Expired - Lifetime CN100379904C (en) 2004-07-09 2004-07-09 Preparation method of low damping internal circular blow multipore spinning fiber

Country Status (1)

Country Link
CN (1) CN100379904C (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103774254B (en) * 2012-10-19 2016-05-18 河北达瑞化纤机械有限公司 A kind of preparation method of encircling blowing device flow regulating barrels
CN105401234B (en) * 2015-12-29 2019-07-12 重庆市大通茂纺织科技有限公司 A kind of screw extruding method of composite fibre
CN106567147B (en) * 2016-11-15 2018-08-21 东华大学 A kind of low resistance polyamide negative pressure melt spinning manufacturing process
CN106637442B (en) * 2016-11-15 2018-10-23 东华大学 A kind of low resistance polyester negative pressure melt spinning manufacturing process
CN106637434B (en) * 2016-11-15 2019-02-26 东华大学 A kind of low resistance polymer high efficiency melt spinning method

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86209037U (en) * 1986-11-13 1987-10-31 大连合成纤维研究所 Airtight low damping annular air blower
JPH02216213A (en) * 1989-02-14 1990-08-29 Unitika Ltd High-speed spinning of polyester fiber
JPH07118912A (en) * 1993-10-14 1995-05-09 Murata Mach Ltd Device for spinning synthetic filament
US5593705A (en) * 1993-03-05 1997-01-14 Akzo Nobel Nv Apparatus for melt spinning multifilament yarns
CN2418138Y (en) * 1999-09-28 2001-02-07 上海华新纺科技发展公司 High-wind-speed low-damp cyclical blowing device
CN2528783Y (en) * 2002-01-24 2003-01-01 宏大化纤技术装备有限公司 Low-damp center ring blowing device for cooling melting spinning material
CN2549020Y (en) * 2002-06-04 2003-05-07 上海二纺机股份有限公司 Central air blower for melt spinning cooling
CN2567238Y (en) * 2002-09-17 2003-08-20 上海二纺机股份有限公司 Central blowing device for melt filament cooling

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86209037U (en) * 1986-11-13 1987-10-31 大连合成纤维研究所 Airtight low damping annular air blower
JPH02216213A (en) * 1989-02-14 1990-08-29 Unitika Ltd High-speed spinning of polyester fiber
US5593705A (en) * 1993-03-05 1997-01-14 Akzo Nobel Nv Apparatus for melt spinning multifilament yarns
JPH07118912A (en) * 1993-10-14 1995-05-09 Murata Mach Ltd Device for spinning synthetic filament
CN2418138Y (en) * 1999-09-28 2001-02-07 上海华新纺科技发展公司 High-wind-speed low-damp cyclical blowing device
CN2528783Y (en) * 2002-01-24 2003-01-01 宏大化纤技术装备有限公司 Low-damp center ring blowing device for cooling melting spinning material
CN2549020Y (en) * 2002-06-04 2003-05-07 上海二纺机股份有限公司 Central air blower for melt spinning cooling
CN2567238Y (en) * 2002-09-17 2003-08-20 上海二纺机股份有限公司 Central blowing device for melt filament cooling

Also Published As

Publication number Publication date
CN1718875A (en) 2006-01-11

Similar Documents

Publication Publication Date Title
CN101487144B (en) Spinning equipment for producing porous fine denier polyester POY
CN100379904C (en) Preparation method of low damping internal circular blow multipore spinning fiber
CN1328419C (en) Steam distribution ring for spinning machines
CN201390809Y (en) Spinning equipment used for producing porous fine denier POY (polyester pre-oriented yarn) yarn
CN201276611Y (en) External ring blowing cooling apparatus for polyester filament yarn
CN102586906A (en) Production method of circular-blow multi-end bright profiled polyester filament yarns more than 3dpf (denier per filament)
CN117488419B (en) Preparation device and preparation method of low-pore Gao Yun micro polyester fiber
CN103866405A (en) High-orifice-density profiled filaments and preparation method thereof
CN211848217U (en) Terylene short fiber circular blowing cooling device
CN104233486A (en) Production process of porous fine denier nylon 6 pre-orientation fibers
CN103307867A (en) Uniform drying process of chemical fiber slices
CN201722447U (en) Melt-spinning polyurethane fiber spinning box
CN111155189B (en) Preparation method of melt-spun profiled polyvinyl alcohol fiber
CN104480557A (en) Chinlon 6 high-strength and fine-denier full-drawn yarns with flattened circular section and preparation method thereof
CN101724928B (en) Second air return system for producing spandex
CN102051695B (en) Melt direct spinning cooling device
CN112760729A (en) Melting spinning ground state cooling device
CN214361871U (en) Distributed melt-blown cold air device
CN202581953U (en) Condenser of outdoor machine and air-conditioner
CN104928771A (en) Production process of 24 cake nylon 6 fully-drawn fibers
CN103981587A (en) Polyamide 6 POY/FDY interlaced yarn and preparation method adopting one-step process
CN2418138Y (en) High-wind-speed low-damp cyclical blowing device
CN208980832U (en) It is a kind of for stablizing the production equipment of fine count fiber spinning
CN201485543U (en) Spinneret
CN2528783Y (en) Low-damp center ring blowing device for cooling melting spinning material

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: Zhejiang Zhink Chemical Fiber Co.,Ltd.

Assignor: Shanghai Pacific Textile Complete Equipment Co.,Ltd.

Contract fulfillment period: 2006.9.18 to 2015.9.17

Contract record no.: 2008330002268

Denomination of invention: Preparation method of low damping internal circular blow multipore spinning fiber

Granted publication date: 20080409

License type: Exclusive license

Record date: 20081124

LIC Patent licence contract for exploitation submitted for record

Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2006.9.18 TO 2015.9.17; CHANGE OF CONTRACT

Name of requester: ZHEJIANG PROVINCE ZHENGKAI FIBER CO., LTD.

Effective date: 20081124

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20180824

Address after: 200070 A, 9 floor, 600 Hengfeng Road, Jingan District, Shanghai.

Patentee after: SHANGHAI PACIFIC SECOND TEXTILE MACHINE CHEMICAL FIBER COMPLETE EQUIPMENT Co.,Ltd.

Address before: 200050 two, building 554, Kai Xuan Road, Shanghai.

Patentee before: Shanghai Pacific Textile Complete Equipment Co.,Ltd.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20080409