CN105297288A - Preparation device for melt-blown non-woven fabric - Google Patents
Preparation device for melt-blown non-woven fabric Download PDFInfo
- Publication number
- CN105297288A CN105297288A CN201510768771.XA CN201510768771A CN105297288A CN 105297288 A CN105297288 A CN 105297288A CN 201510768771 A CN201510768771 A CN 201510768771A CN 105297288 A CN105297288 A CN 105297288A
- Authority
- CN
- China
- Prior art keywords
- spinning
- melt
- nozzle
- woven fabrics
- preparation facilities
- 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.)
- Pending
Links
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 239000004744 fabric Substances 0.000 title abstract description 10
- 239000004750 melt-blown nonwoven Substances 0.000 title abstract description 3
- 239000000835 fiber Substances 0.000 claims abstract description 43
- 238000009987 spinning Methods 0.000 claims abstract description 22
- 239000004745 nonwoven fabric Substances 0.000 claims abstract description 20
- 238000000034 method Methods 0.000 claims abstract description 8
- 239000000155 melt Substances 0.000 claims abstract 5
- 238000005507 spraying Methods 0.000 claims description 16
- 239000000919 ceramic Substances 0.000 claims description 12
- 239000000853 adhesive Substances 0.000 claims description 11
- 230000001070 adhesive effect Effects 0.000 claims description 11
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 238000001125 extrusion Methods 0.000 claims description 3
- 229910052809 inorganic oxide Inorganic materials 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 abstract description 9
- 238000005516 engineering process Methods 0.000 abstract description 6
- 230000003068 static effect Effects 0.000 abstract description 6
- 230000005684 electric field Effects 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 4
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 3
- 230000009977 dual effect Effects 0.000 abstract 2
- 230000005686 electrostatic field Effects 0.000 description 18
- 239000004743 Polypropylene Substances 0.000 description 10
- 229920001155 polypropylene Polymers 0.000 description 10
- 238000007664 blowing Methods 0.000 description 8
- 238000013461 design Methods 0.000 description 8
- 238000009941 weaving Methods 0.000 description 8
- 230000003247 decreasing effect Effects 0.000 description 5
- 238000005421 electrostatic potential Methods 0.000 description 5
- 238000005457 optimization Methods 0.000 description 5
- -1 polypropylene Polymers 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 238000010041 electrostatic spinning Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002121 nanofiber Substances 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Nonwoven Fabrics (AREA)
Abstract
The invention discloses a preparation device for melt-blown non-woven fabric. The preparation device comprises a spinning nozzle used for extruding a melt, an airflow channel used for guiding a high-speed airflow to draw the melt, a high-voltage static generator used for generating high-voltage static to draw the melt and a receiving roller used in cooperation with the spinning nozzle to form the non-woven fabric. The outlet end of the airflow channel is close to an outlet of the spinning nozzle, the spinning nozzle is connected with a positive electrode of the high-voltage static generator, and the receiving roller is grounded. By connecting the high-voltage static generator to the spinning nozzle and grounding the receiving roller, the melt can be subjected to dual drawing in the drawing process; as the polymer melt is subjected to the dual effects of drawing force (airflow force for short) generated by the high-speed high-temperature airflow and drawing force (electric field force for short) generated by a high-voltage static electric field after being extruded out of a spinneret orifice, fibers are thinner and can reach the nanometer scale; meanwhile, the production technology can be applied to large-scale production.
Description
Technical field
The present invention relates to a kind of melt spraying non-woven fabrics preparation facilities.
Background technology
Non-weaving cloth refers to without common operation of spinning cotton and weaving cloth, the sheet-like article be directly made up of fiber.The advantage of non-woven processing is that technological process is short, speed of production is high, product purpose is wide.Melt-blown is a kind of main method preparing not weaving fabric of superfine fiber.It utilizes high-speed and high-temperature air-flow that polymer melt is drawn into superfine fibre.Superfine fibre refers to the fiber of diameter between 1mm to 5mm.Melt-blowing nonwoven is due to fiber fine, thus there is the advantages such as the many and aperture of hole is little, tree root shape channel system can be formed, filter efficiency reaches more than 99.9%, be widely used in the fields such as metallurgy, chemical industry, medicine, machinery, electronics, food, nuclear industry, automobile, also can be used as the advanced filters of the depollution of environment and biologic cleanliness.
A Main Trends of The Development of melt-blown non-woven technology is the further refinement of fiber, or even prepares nanofiber.If fibre diameter can reach nanometer scale, so the strainability of its goods and absorption property will significantly improve, and have good application prospect in the field such as biology, medicine, national defence, electronics.Prior art is badly in need of a kind of melt spraying non-woven fabrics preparation facilities can preparing nanometer scale fiber.
Summary of the invention
The object of the invention is to overcome the defect existed in prior art, a kind of melt spraying non-woven fabrics preparation facilities can preparing nanometer scale fiber is provided.
For achieving the above object, technical scheme of the present invention there is provided a kind of melt spraying non-woven fabrics preparation facilities, comprise for the spinning-nozzle of melt extrusion, to make the gas channel of melt drawn for the high velocity air that leads, obtain for generation of high-pressure electrostatic the HV generator of melt drawn and with spinning-nozzle with the use of and form the reception roller of nonwoven fabric; The port of export of described gas channel is near the outlet of spinning-nozzle; Described spinning-nozzle is connected with the positive electrode of HV generator, described reception roller ground connection.By connecting HV generator and roller ground connection will be received on spinning-nozzle; melt can be made in drawing process to be subject to double tension; polymer melt is from the double action of tensile force (abbreviation electric field force) being subject to tensile force (being called for short air-flow power) that high-speed and high-temperature air-flow produces and high-voltage electrostatic field generation after spinneret orifice is extruded; make fiber more refinement; can reach Nano grade, such production technology can large-scale production simultaneously.
As preferably, described spinning-nozzle and gas channel are all arranged in spinning dies, and described spinning-nozzle insulate with spinning dies and is connected.Such design prevents positive electricity from leaking outside.
As preferably, insulated by ceramic fiber blanket between described spinning-nozzle and spinning dies.Such design realizes insulation preferably, and this melt-blown electrostatic spinning device ceramic fiber blanket used can tolerate the high temperature of 1000 ° of C, and has excellent electrical insulation capability.
As preferably, described spinning-nozzle is bonding by high-temperature-resistant adhesive with between ceramic fiber blanket.This melt-blown electrostatic spinning device high-temperature-resistant adhesive used can tolerate the high temperature of 1000 ° of C.
As preferably, fixed bonding between described ceramic fiber blanket and spinning dies.Such design makes spinning-nozzle fixing-stable.
As preferably, described gas channel inlet end is connected with gas manifold.Such design is the one optimization to scheme.
As preferably, also comprise the screw extruder, heater block and the measuring pump that are arranged on spinning dies preceding working procedure, described measuring pump is communicated with spinning-nozzle by pipeline, and insulating between described pipeline and spinning-nozzle is arranged.Such design is the one optimization to scheme.
As preferably, the air-flow angle of described nozzle is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.Such design is the one optimization to scheme.
As preferably, the voltage of HV generator is 10kv ~ 100kv.Such design is the one optimization to scheme.
As preferably, described high-temperature-resistant adhesive is inorganic oxide copper high-temperature-resistant adhesive.Such design is the one optimization to scheme.
Advantage of the present invention is with beneficial effect: by being connected HV generator and will receiving roller ground connection on spinning-nozzle; melt can be made in drawing process to be subject to double tension; polymer melt is from the double action of tensile force (abbreviation electric field force) being subject to tensile force (being called for short air-flow power) that high-speed and high-temperature air-flow produces and high-voltage electrostatic field generation after spinneret orifice is extruded; make fiber more refinement; can reach Nano grade, such production technology can large-scale production simultaneously.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
In figure: screw extruder-1, measuring pump-2, gas manifold-3, nozzle-4, ceramic fiber blanket-5, HV generator-7, reception roller-8, gas channel-9.
Detailed description of the invention
Below in conjunction with drawings and Examples, the specific embodiment of the present invention is further described.Following examples only for technical scheme of the present invention is clearly described, and can not limit the scope of the invention with this.
As shown in Figure 1, a kind of melt spraying non-woven fabrics preparation facilities, comprise for the spinning-nozzle 4 of melt extrusion, to make the gas channel 9 of melt drawn for the high velocity air that leads, obtain for generation of high-pressure electrostatic the HV generator 7 of melt drawn and with spinning-nozzle 4 with the use of and form the reception roller 8 of nonwoven fabric; The port of export of described gas channel 9 is near the outlet of spinning-nozzle 4; Described spinning-nozzle 4 is connected with the positive electrode of HV generator 7, described reception roller 8 ground connection.
Described spinning-nozzle 4 and gas channel 9 are all arranged in spinning dies, and described spinning-nozzle 4 insulate with spinning dies and is connected.
Insulated by ceramic fiber blanket 5 between described spinning-nozzle 4 and spinning dies.
Described spinning-nozzle 4 is bonding by high-temperature-resistant adhesive with between ceramic fiber blanket 5.
Fixed bonding between described ceramic fiber blanket 5 and spinning dies.
Described gas channel 9 inlet end is connected with gas manifold 3.
Also comprise the screw extruder 1, heater block and the measuring pump 2 that are arranged on spinning dies preceding working procedure, described measuring pump 2 is communicated with spinning-nozzle 4 by pipeline, and insulating between described pipeline and spinning-nozzle 4 is arranged.
The air-flow angle of described nozzle 4 is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.
The voltage of HV generator 7 is 10kv ~ 100kv.
Described high-temperature-resistant adhesive is inorganic oxide copper high-temperature-resistant adhesive.
The embodiment of nanofiber is prepared to further illustrate the beneficial effect of above-mentioned melt-blown electrostatic spinning device below in conjunction with melt-blown electrostatic spinning device of the present invention.
Embodiment 1
Polymer melt (modified polypropene) is extruded from nozzle 4, and high-speed high-temperature gas sprays from gas channel 9, forms high-voltage electrostatic field (electrostatic potential 60kV) between nozzle 4 and reception roller 8.Wherein, the air-flow angle of nozzle 4 is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.Supply raw materials polypropylene, melt flow rate is 800g/10min, and flow is 0.031g/s, and initial temperature is 280 ° of C, and gas initial velocity is 340m/s, and gas initial temperature is 300 ° of C.
Under above-mentioned condition, the diameter mean value of obtained fiber is 451nm, and the fibre diameter mean value not applying the non-weaving cloth prepared by melt-blowing equipment of high-voltage electrostatic field under equal conditions is 1.42mm, applies fibre diameter after behind high-voltage electrostatic field and decreased 68.2% than originally.
Embodiment 2
Polymer melt (modified polypropene) is extruded from nozzle 4, and high-speed high-temperature gas sprays from gas channel 9, forms high-voltage electrostatic field (electrostatic potential 50kV) between nozzle 4 and reception roller 8.Wherein, the air-flow angle of nozzle 4 is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.Supply raw materials polypropylene, melt flow rate is 100g/10min, and flow is 0.008g/s, and initial temperature is 290 ° of C, and gas initial velocity is 480m/s, and gas initial temperature is 330 ° of C.
Under above-mentioned condition, the diameter mean value of obtained fiber is 875nm, and the fibre diameter mean value not applying the non-weaving cloth prepared by melt-blowing equipment of high-voltage electrostatic field under equal conditions is 2.59mm, applies fibre diameter after behind high-voltage electrostatic field and decreased 66.2% than originally.
Embodiment 3
Polymer melt (modified polypropene) is extruded from nozzle 4, and high-speed high-temperature gas sprays from gas channel 9, forms high-voltage electrostatic field (electrostatic potential 40kV) between nozzle 4 and reception roller 8.Wherein, the air-flow angle of nozzle 4 is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.Supply raw materials polypropylene, melt flow rate is 800g/10min, and flow is 0.057g/s, and initial temperature is 280 ° of C, and gas initial velocity is 320m/s, and gas initial temperature is 290 ° of C.
Under above-mentioned condition, the diameter mean value of obtained fiber is 859nm, and the fibre diameter mean value not applying the non-weaving cloth prepared by melt-blowing equipment of high-voltage electrostatic field under equal conditions is 2.51mm, applies fibre diameter after behind high-voltage electrostatic field and decreased 65.8% than originally.
Embodiment 4
Polymer melt (modified polypropene) is extruded from nozzle 4, and high-speed high-temperature gas sprays from gas channel 9, forms high-voltage electrostatic field (electrostatic potential 40kV) between nozzle 4 and reception roller 8.Wherein, the air-flow angle of nozzle 4 is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.Supply raw materials polypropylene, melt flow rate 75g/10min, flow is 0.006g/s, and initial temperature is 310 ° of C, and gas initial velocity is 530m/s, and gas initial temperature is 380 ° of C.
Under above-mentioned condition, the diameter mean value of obtained fiber is 996nm, and the fibre diameter mean value not applying the non-weaving cloth prepared by melt-blowing equipment of high-voltage electrostatic field under equal conditions is 2.78mm, applies fibre diameter after behind high-voltage electrostatic field and decreased 64.2% than originally.
Embodiment 5
Polymer melt (modified polypropene) is extruded from nozzle 4, and high-speed high-temperature gas sprays from gas channel 9, forms high-voltage electrostatic field (electrostatic potential 100kV) between nozzle 4 and reception roller 8.Wherein, the air-flow angle of nozzle 4 is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.Supply raw materials polypropylene, melt flow rate is 1000g/10min, and flow is 0.022g/s, and initial temperature is 290 ° of C, and gas initial velocity is 380m/s, and gas initial temperature is 310 ° of C.
Under above-mentioned condition, the diameter mean value of obtained fiber is 347nm, and the fibre diameter mean value not applying the non-weaving cloth prepared by melt-blowing equipment of high-voltage electrostatic field under equal conditions is 1.16mm, applies fibre diameter after behind high-voltage electrostatic field and decreased 70.1% than originally.
Illustrated by above embodiment, the present invention significantly can reduce the fibre diameter of melt-blowing nonwoven, and the diameter of prepared fiber reduces more than 64% than the diameter of fiber prepared by the melt-blowing equipment not applying electrostatic field, reaches nano-scale dimension.Simultaneously, as long as conventional meltblowing apparatus adheres to ceramic fiber blanket 5 at nozzle 4 external application high-temperature-resistant adhesive, and the positive electrode of nozzle 4 with HV generator 7 is connected, roller 8 ground connection will be received, melt-blown Static Spinning equipment can be repacked into, equipment miscellaneous part need not make any change, is conducive to cost-saving.
The above is only the preferred embodiment of the present invention; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the technology of the present invention principle; can also make some improvements and modifications, these improvements and modifications also should be considered as the protection domain invented.
Claims (10)
1. a melt spraying non-woven fabrics preparation facilities, is characterized in that: comprise for the spinning-nozzle of melt extrusion, to make the gas channel of melt drawn for the high velocity air that leads, obtain for generation of high-pressure electrostatic the HV generator of melt drawn and with spinning-nozzle with the use of and form the reception roller of nonwoven fabric; The port of export of described gas channel is near the outlet of spinning-nozzle; Described spinning-nozzle is connected with the positive electrode of HV generator, described reception roller ground connection.
2. melt spraying non-woven fabrics preparation facilities as claimed in claim 1, it is characterized in that: described spinning-nozzle and gas channel are all arranged in spinning dies, described spinning-nozzle insulate with spinning dies and is connected.
3. melt spraying non-woven fabrics preparation facilities as claimed in claim 2, be is characterized in that: insulated by ceramic fiber blanket between described spinning-nozzle and spinning dies.
4. melt spraying non-woven fabrics preparation facilities as claimed in claim 3, is characterized in that: described spinning-nozzle is bonding by high-temperature-resistant adhesive with between ceramic fiber blanket.
5. melt spraying non-woven fabrics preparation facilities as claimed in claim 4, is characterized in that: fixed bonding between described ceramic fiber blanket and spinning dies.
6. melt spraying non-woven fabrics preparation facilities as claimed in claim 5, is characterized in that: described gas channel inlet end is connected with gas manifold.
7. melt spraying non-woven fabrics preparation facilities as claimed in claim 6, it is characterized in that: also comprise the screw extruder, heater block and the measuring pump that are arranged on spinning dies preceding working procedure, described measuring pump is communicated with spinning-nozzle by pipeline, and insulating between described pipeline and spinning-nozzle is arranged.
8. melt spraying non-woven fabrics preparation facilities as claimed in claim 7, is characterized in that: the air-flow angle of described nozzle is 60 °, and width of rebate is 0.6mm, and head end width is 0.5mm, and orifice diameter is 0.3mm.
9. melt spraying non-woven fabrics preparation facilities as claimed in claim 8, is characterized in that: the voltage of HV generator is 10kv ~ 100kv.
10. melt spraying non-woven fabrics preparation facilities as claimed in claim 9, is characterized in that: described high-temperature-resistant adhesive is inorganic oxide copper high-temperature-resistant adhesive.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510768771.XA CN105297288A (en) | 2015-11-12 | 2015-11-12 | Preparation device for melt-blown non-woven fabric |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510768771.XA CN105297288A (en) | 2015-11-12 | 2015-11-12 | Preparation device for melt-blown non-woven fabric |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105297288A true CN105297288A (en) | 2016-02-03 |
Family
ID=55195069
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510768771.XA Pending CN105297288A (en) | 2015-11-12 | 2015-11-12 | Preparation device for melt-blown non-woven fabric |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105297288A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108265340A (en) * | 2018-03-06 | 2018-07-10 | 杨晓波 | Nano-fiber manufacturing apparatus |
| CN112609248A (en) * | 2020-12-30 | 2021-04-06 | 苏州市吴中喷丝板有限公司 | Electrostatic melt-blown spinning device and method thereof |
| WO2022007181A1 (en) * | 2020-07-06 | 2022-01-13 | 浙江宸唯环保科技股份有限公司 | Melt-blown nonwoven fabric electret adding device and adding method |
| CN114411336A (en) * | 2021-12-30 | 2022-04-29 | 承德石油高等专科学校 | Method and device for producing in-situ electret fiber membrane |
| US11447893B2 (en) | 2017-11-22 | 2022-09-20 | Extrusion Group, LLC | Meltblown die tip assembly and method |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001098453A (en) * | 1999-09-28 | 2001-04-10 | Daiwabo Co Ltd | Electret nonwoven fabric and air filter |
| CN1348514A (en) * | 1999-04-23 | 2002-05-08 | 赖特卜福叶特公司 | Installation for making a nonwoven textile web and method for using such an installation |
| JP2009057655A (en) * | 2007-08-31 | 2009-03-19 | Japan Vilene Co Ltd | Extra fine fiber nonwoven fabric, method for producing the same, and apparatus for producing the same |
| CN101709534A (en) * | 2009-11-17 | 2010-05-19 | 天津工业大学 | Device and method for manufacturing airflow melting electrostatic spinning nano-fiber non-woven fabric |
| CN102839431A (en) * | 2012-09-28 | 2012-12-26 | 北京化工大学 | Device and process for mass production of nanometer fiber by melt electro-spinning method |
| CN103205818A (en) * | 2013-04-28 | 2013-07-17 | 厦门大学 | Air-current-assisted hybrid electrostatic spinning device |
| CN205205412U (en) * | 2015-11-12 | 2016-05-04 | 江阴金港无纺布有限公司 | Polyurethane elastic nonwoven preparation facilities |
-
2015
- 2015-11-12 CN CN201510768771.XA patent/CN105297288A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1348514A (en) * | 1999-04-23 | 2002-05-08 | 赖特卜福叶特公司 | Installation for making a nonwoven textile web and method for using such an installation |
| JP2001098453A (en) * | 1999-09-28 | 2001-04-10 | Daiwabo Co Ltd | Electret nonwoven fabric and air filter |
| JP2009057655A (en) * | 2007-08-31 | 2009-03-19 | Japan Vilene Co Ltd | Extra fine fiber nonwoven fabric, method for producing the same, and apparatus for producing the same |
| CN101709534A (en) * | 2009-11-17 | 2010-05-19 | 天津工业大学 | Device and method for manufacturing airflow melting electrostatic spinning nano-fiber non-woven fabric |
| CN102839431A (en) * | 2012-09-28 | 2012-12-26 | 北京化工大学 | Device and process for mass production of nanometer fiber by melt electro-spinning method |
| CN103205818A (en) * | 2013-04-28 | 2013-07-17 | 厦门大学 | Air-current-assisted hybrid electrostatic spinning device |
| CN205205412U (en) * | 2015-11-12 | 2016-05-04 | 江阴金港无纺布有限公司 | Polyurethane elastic nonwoven preparation facilities |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11447893B2 (en) | 2017-11-22 | 2022-09-20 | Extrusion Group, LLC | Meltblown die tip assembly and method |
| CN108265340A (en) * | 2018-03-06 | 2018-07-10 | 杨晓波 | Nano-fiber manufacturing apparatus |
| WO2022007181A1 (en) * | 2020-07-06 | 2022-01-13 | 浙江宸唯环保科技股份有限公司 | Melt-blown nonwoven fabric electret adding device and adding method |
| CN112609248A (en) * | 2020-12-30 | 2021-04-06 | 苏州市吴中喷丝板有限公司 | Electrostatic melt-blown spinning device and method thereof |
| CN112609248B (en) * | 2020-12-30 | 2022-01-14 | 苏州市吴中喷丝板有限公司 | Electrostatic melt-blown spinning device and method thereof |
| CN114411336A (en) * | 2021-12-30 | 2022-04-29 | 承德石油高等专科学校 | Method and device for producing in-situ electret fiber membrane |
| CN114411336B (en) * | 2021-12-30 | 2023-10-27 | 承德石油高等专科学校 | Method and device for producing in-situ electret fiber membrane |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105297288A (en) | Preparation device for melt-blown non-woven fabric | |
| CN104153119B (en) | Melt-blow non-woven material capable of effectively filtering PM 2.5 particles and preparation method thereof | |
| CN200981905Y (en) | Electric spinning nano fibre beam gas current twister twisting collecting device | |
| He et al. | Nanofiber coated hybrid yarn fabricated by novel electrospinning-airflow twisting method | |
| CN108716023B (en) | A kind of melt-blown die head for nanofiber preparation | |
| CN203333875U (en) | Electrostatic spinning nano-fiber air-jet twisting yarn-forming device | |
| CN103215660B (en) | Electrospun nano-fibers equipment | |
| CN105734724A (en) | Novel method for preparing carbon nanofibers through electrospinning | |
| CN114197062A (en) | Melt differential electrostatic spinning pre-oriented filament continuous preparation device | |
| CN205205412U (en) | Polyurethane elastic nonwoven preparation facilities | |
| CN110629299A (en) | A continuous preparation device and continuous preparation method for nanofiber yarn | |
| CN104480546A (en) | Electrospinning paralleling shaft spinning head with angle correlation and application | |
| CN103572386A (en) | Flat plate pinhole coaxial electrostatic spinning fiber composite spinning jet and spinning method thereof | |
| CN105332068A (en) | Fusion electrostatic spinning equipment | |
| TWM623551U (en) | Improved meltblown nonwoven fabric manufacturing equipment | |
| CN104831426B (en) | Two-stage shear-type drawing-off Static Spinning directly spins a micron yarn feeding device, method and purposes | |
| CN105568400A (en) | Ultrasonic-assisted electrostatic spinning apparatus | |
| CN104831434B (en) | Shear-type-drafting electrostatic-spinning micron-yarn direct-spinning device and method and use thereof | |
| CN203382863U (en) | Melt spinning flocking device | |
| CN102220658A (en) | Conductive polytrimethylene terephthalate (PTT) nanofibers and preparation method | |
| CN103409813A (en) | Melt spinning flocking device | |
| Yang et al. | Electrospun uniform fibres with a special regular hexagon distributed multi-needles system | |
| CN103173878B (en) | Acetate fiber high speed spinning integrated technique | |
| CN210974940U (en) | A needleless roller type electrospinning equipment | |
| CN109402747A (en) | A kind of netted bitubular cylindrical static electric spinning device and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160203 |
|
| RJ01 | Rejection of invention patent application after publication |