Water stable fibers and articles comprising starch, and methods of making the same
a technology of thermoplastic starch and water stable fibers, which is applied in the direction of monocomponent polyamide artificial filaments, monocomponent polyester artificial filaments, blow-molded articles, etc., can solve the problems of large disruption of the stable supply of petroleum-based polymers used in making synthetic fibers, small defects, and inability to meet the current, and achieves the effect of improving the stability of the supply of petroleum-based polymers
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example 1
[0091]This example demonstrates melt mixing and one-shot spinning of water stable fibers. The following materials are mixed in a Haake Rheocord 90 melt mixer, Thermo Electron Corporation, Newington, N.H.:
30 g Ethylex™ 2015 hydroxyethylated starch (Tate& Lyle, Decatur, Ill.)
12.5 g Glycerol (Aldrich Chemicals, St. Louis, Mo.)
7.5 g Stearic Acid (Aldrich Chemicals, St. Louis, Mo.)
7.5 g Adipic Acid (Aldrich Chemicals, St. Louis, Mo.)
[0092]The starch and the glycerol are mixed for about 3 minutes at about 60 rpm at a temperature of about 160° C. The balance of components is added and mixed for an additional 7 minutes at about 60 rpm. The contents are removed and allowed to cool to room temperature. The mixture is then chopped using a knife into pieces approximately 50 mm in diameter.
[0093]After 24 hours, the pieces are placed into a piston / cylinder one shot spinning system, Alex James, Inc. of Greer, S.C. The extruder barrel is preheated to 160° C. The spinneret capillary is 0.016″ diamet...
example 3
[0098]This example demonstrates melt mixing and one-shot spinning of water stable starch fibers of various compositions. The following materials are mixed in the described Haake Rheocord 90 melt mixer in a manner as described in Example 1 and melt blended. Approximately 50 g of each composition is made.
Adipic AcidEthylex ™GlycerolLauric Acid(Aldrich2015 starch(Aldrich(AldrichChemicals,Material,(Tate& Lyle,Chemicals, St.Chemicals, St.St.wt %Decatur, IL)Louis, MO)Louis, MO)Louis, MO)Sample 1602512.52.5Sample 26025105Sample 360257.57.5
[0099]After 24 hours, the materials are spun into fibers using the described piston / cylinder one shot spinning system. The extruder barrel is preheated to 160° C. The spinneret capillary is 0.016″ diameter and has an L / D of 3. Fibers are extruded by activating the piston at an extrusion rate of approximately 0.8 g / minute. Approximately 40 g of fibers of each composition are collected.
[0100]Approximately 20 g of each composition of fibers are dried in a co...
example 4
[0101]This example demonstrates additional blending and spinning of fibers with water stability. The following materials are used:
3500 g Ethylex™ 2015 (Tate& Lyle, Decatur, Ill.)
[0102]1095 g Glycerol (Aldrich Chemicals, St. Louis, Mo.)
438 g Adipic acid (Solutia Chemicals, St. Louis, Mo.)
438 g Stearic acid (Aldrich Chemicals, St. Louis, Mo.)
50 g Magnesium stearate (Aldrich Chemicals, St. Louis, Mo.)
[0103]The starch, adipic acid, stearic acid and magnesium stearate (employed as a process aid) are dry mixed in a Henschel Raw Material Mixer (Green Bay, Wis.) for 4 minutes at 1000 rpm. The mixture is then fed into a B&P Process System Twin Screw Extrusion Compounding System (Saginaw, Mich.) with 40 mm co-rotating screws. Glycerol is fed through a liquid feed port at a rate that maintains the desired composition stated above. The screw speed is set at 90 rpm with the thermal profile as shown below:
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