Extruder screw, extruder, and extrusion method
US-2016332332-A1 · Nov 17, 2016 · US
US2020032003A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020032003-A1 |
| Application number | US-201816493504-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 12, 2018 |
| Priority date | Mar 21, 2017 |
| Publication date | Jan 30, 2020 |
| Grant date | — |
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Provided is a method for producing a shaping material that contains a cyclic olefin polymer and has a low content of a volatile impurity. This method for producing a shaping material is a method which includes passing a raw-material resin in a molten state through an extruder to produce a shaping material, and in which the extruder is equipped with a cylinder, a screw housed within the cylinder, a resin introduction port for introducing the raw-material resin into the cylinder, a resin discharge port for discharging the molten resin from the cylinder, a fluid injection port for injecting carbon dioxide or water into the cylinder between the resin introduction port and the resin discharge port, and a fluid discharge port for removing fluid in the cylinder by suction downstream of the fluid injection port and between the resin introduction port and the resin discharge port.
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1 . A method for producing a shaping material by passing a raw-material resin that contains a cyclic olefin polymer in a molten state through an extruder, the extruder being equipped with a cylinder, a screw housed within the cylinder, a resin introduction port for introducing the raw-material resin into the cylinder, a resin discharge port for discharging the molten resin from the cylinder, a fluid injection port for injecting carbon dioxide or water into the cylinder between the resin introduction port and the resin discharge port, and a fluid discharge port for removing fluid in the cylinder by suction downstream of the fluid injection port and between the resin introduction port and the resin discharge port; the method comprising: injecting 1 to 6 parts by mass of carbon dioxide or water per 100 parts by mass of the raw-material resin into the cylinder from the fluid injection port while transporting the molten raw-material resin within the cylinder to bring carbon dioxide or water into contact with the molten raw-material resin, and discharging fluid in the cylinder from the fluid discharge port, thereby removing a volatile compound in the raw-material resin; and cooling and solidifying the molten resin discharged from the resin discharge port, wherein the rotation number of the screw during extrusion of the molten raw-material resin is 150 rpm or higher, and the oxygen concentration of the gas phase within the cylinder is 5% by volume or less. 2 . The method for producing a shaping material according to claim 1 , wherein a content ratio of a compound that has a boiling point of lower than 200° C. with respect to the whole raw-material resin is 15 to 50 ppm in terms of n-decane when components of the raw-material resin are analyzed by the following dynamic headspace-gas chromatography/mass spectrometry: a sample container composed of a glass tube having an inner diameter of 4 mm, in which 100 mg of the raw-material resin is charged, is connected to a gas collection tube that have been cooled by liquid nitrogen, and then the sample container is heated at 200° C. for 30 minutes in a high-purity helium stream, followed by continuously collecting gas released from the raw-material resin into the gas collection tube; and the collected gas is subjected to thermal desorption-gas chromatography-mass spectrometry using n-decane as an internal standard, and the amount of the gas released from the raw-material resin is calculated in terms of n-decane. 3 . The method for producing a shaping material according to claim 1 , wherein the extruder is a twin-screw extruder. 4 . The method for producing a shaping material according to claim 1 , wherein the temperature of the molten raw-material resin in the cylinder is 290° C. to 330° C. 5 . The method for producing a shaping material according to claim 1 , wherein the pressure at the fluid discharge port is 500 to 3,000 kPa. 6 . The method for producing a shaping material according to claim 1 , wherein the content ratio of a compound that has a boiling point of lower than 200° C. with respect to the whole shaping material is 3 ppm or less in terms of n-decane when components of the shaping material are analyzed by the following dynamic headspace-gas chromatography/mass spectrometry: a sample container composed of a glass tube having an inner diameter of 4 mm, in which 100 mg of the shaping material is charged, is connected to a gas collection tube that have been cooled by liquid nitrogen, and then the sample container is heated at 200° C. for 30 minutes in a high-purity helium stream, followed by continuously collecting gas released from the shaping material into the gas collection tube; and the collected gas is subjected to thermal desorption-gas chromatography-mass spectrometry using n-decane as an internal standard, and the amount of the gas released from the shaping material is calculated in terms of n-decane.
with screw or helix · CPC title
Liquid charges · CPC title
Screws (B29B7/482 takes precedence) · CPC title
Venting, degassing or removing evaporated components in devices with rotary stirrers · CPC title
Characterised by the use of homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic ring system; Derivatives of such polymers · CPC title
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