Manufacturing apparatus and method of microporous polyolefin resin sheet
A technology of polyolefin resin, manufacturing device, applied in the direction of flat products, applications, coatings, etc., which can solve the problems of contamination, dripping, flake defects, etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0063] A specific sheet manufacturing method in this embodiment is as follows.
[0064] (1) Sheet material
[0065] ·High-density polyethylene (HDPE), viscosity 1000Pa·s. Here, the viscosity is measured by the method of JIS K7117-2 on the condition of a shear rate of 100 / s and a temperature of 200 degreeC.
[0066] ·Liquid paraffin (LP), dynamic viscosity 51cSt (40℃mm 2 / s).
[0067] (2) Feeding
[0068] After the sheet material is dried, it is supplied to an extruder, and after passing through a gear pump and a filter, it is supplied to a sheet forming die. In addition, the temperature of the device before reaching the die was set to 230°C.
[0069] (3) Sheet forming die
[0070] Using a die with a slit width of 300 mm, the resin was discharged at a flow rate of 70 kg / hr.
[0071] It should be noted that the concentration of LP in the resin is 70% by mass, and 49kg / hr is LP. Also, depending on the sheet width and decompression degree, about 0.1% of the resin flow rate...
Embodiment 2
[0080] A specific sheet manufacturing method in this embodiment is as follows.
[0081] (1) Sheet material
[0082] The same material as in Example 1 was used.
[0083] (2) Feeding
[0084] It carried out similarly to Example 1 except having set the temperature of the apparatus before reaching a die to 200 degreeC.
[0085] (3) Sheet forming die
[0086] Using a die with a slit width of 300 mm, the resin was discharged at a flow rate of 250 kg / hr. It should be noted that the concentration of LP in the resin is 70% by mass, and 175kg / hr is LP. Also, as described above, about 0.1% of LP in the resin flow rate volatilized from the sheet, and about 6.0 kg of LP volatilized per day was sucked into the decompression chamber together with the ambient air.
[0087] (4) Cast cooling device
[0088] Except having set the casting speed to 10 m / min, it carried out similarly to Example 1.
[0089] (5) Decompression chamber
[0090] The same decompression chamber as in Example 1 was...
Embodiment 3
[0094] A specific sheet manufacturing method in this embodiment is as follows.
[0095] (1) Sheet material
[0096] The same material as in Example 1 was used.
[0097] (2) Feeding
[0098] It carried out similarly to Example 1 except having set the temperature of the apparatus before reaching a die to 200 degreeC.
[0099] (3) Sheet forming die
[0100] A die with a slit width of 400mm was used. The above-mentioned resin was discharged from the die at a flow rate of 300 kg / hr. It should be noted that the concentration of LP in the resin is 70% by mass, and 210kg / hr is LP. Also, as described above, about 0.1% of LP in the resin flow rate volatilized from the sheet, and about 7.2 kg of LP volatilized per day was sucked into the decompression chamber together with the ambient air.
[0101] (4) Cast cooling device
[0102] Except having set the casting speed to 16 m / min, it carried out similarly to Example 1.
[0103] (5) Decompression chamber
[0104] The same decompres...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


