Apparatus and methods for manufacturing biodegradable, compostable, drink straws from polyhydroxyalkanoate material
Apparatus and methods for manufacturing compostable, biodegradable drink straws from polyhydroxyalkanoate (PHA) material are disclosed herein. Such apparatus may include a hopper that contains raw PHA material, an extruder that receives the raw PHA material from the hopper and produces extruded PHA material, one or more waters baths that cool the extruded PHA material, a puller that pulls a tubular stream of PHA material through the system, and a cutter that is configured to cut the stream of PHA material into finished straws. The finished straws may be soil- and marine-biodegradable, as well as home- and industrial-compostable.
1. A process for manufacturing a drink straw, the drink straw having an outer diameter and a wall thickness, the process comprising:
providing raw polyhydroxyalkanoate (PHA) material from a hopper to an extruder, wherein the extruder is configured to receive the raw PHA material from the hopper and to produce molten PHA material;
providing the molten PHA material from the extruder to an extruder die, wherein the extruder die is configured to receive the molten PHA material from the extruder and to produce a stream of extruded PHA material that has a tubular shape; and
providing the stream of extruded PHA material directly from the extruder die to a pre-sizing water bath that is configured to receive the stream of extruded PHA material directly from the extruder die and to provide the stream of extruded PHA material to a second water bath via a bore defined by a sizing tube;
wherein the sizing tube extends a distance into the second water bath and is configured to control the outer diameter and wall thickness of the straw, and
wherein the pre-sizing water bath is a non-vacuum container having an open top.
2. The process of claim 1 , wherein the raw PHA material is made of a material comprising at least 50% PHA.
3. The process of claim 1 , wherein the stream of extruded PHA material has an outer diameter, and the sizing tube has an inner diameter that is larger than the outer diameter of the stream of PHA material.
4. The process of claim 3 , wherein the sizing tube has an inner diameter that is about 40% larger than the outer diameter of the stream of extruded PHA material.
5. The process of claim 1 , wherein the sizing tube defines a plurality of holes extending through an outer surface thereof.
6. The process of claim 1 , wherein the pre-sizing water bath has a length within a range of about four to five inches in a direction along which the stream of extruded PHA material is being provided from the extruder die to the sizing tube.
7. The process of claim 1 , wherein the pre-sizing water bath has a length of at least four inches in a direction along which the stream of extruded PHA material is being provided from the extruder die to the sizing tube.
8. The process of claim 1 , wherein the pre-sizing water bath contains water that is at a temperature of greater than 125° F.
9. The process of claim 1 , wherein the pre-sizing water bath contains water that is at a temperature that is within a range of 125° F. to 150° F.
10. The process of claim 1 , wherein the pre-sizing water bath contains water that is at a temperature that is within a range of 60° F. to 135° F.
11. The process of claim 10 , wherein the extruded PHA material is extruded from an end of the extruder having a temperature within a range of 340° F. to 390° F.
12. The process of claim 1 , wherein the pre-sizing water bath contains water that is at a temperature that is at least 200° F. cooler than the temperature of the extruded PHA material that is received by the pre-sizing water bath.
13. The process of claim 12 , wherein the temperature of the water contained by the pre-sizing water bath is within a range of 60° F. to 135° F.
14. The process of claim 13 , wherein the difference between the temperature of the water contained by the pre-sizing water bath and the temperature of the extruded PHA material received by the pre-sizing water bath shocks the extruded PHA material into beginning a crystallization process.
15. The process of claim 1 , wherein the extruded PHA material is at a first temperature, the pre-sizing water bath contains water that is at a second temperature, and the difference between the first temperature and second the temperature shocks the extruded PHA material into beginning a crystallization process.
16. The process of claim 1 , wherein the raw PHA material is made of a material comprising at least 80% PHA.
17. A process for manufacturing a drink straw, the straw having an outer diameter and a wall thickness, the process comprising:
providing raw polyhydroxyalkanoate (PHA) material from a hopper to an extruder, wherein the extruder is configured to receive the raw PHA material from the hopper and to produce molten PHA material;
providing the molten PHA material from the extruder to an extruder die, wherein the extruder die is configured to receive the molten PHA material from the extruder and to produce a stream of extruded PHA material that has a tubular shape; and
providing the stream of extruded PHA material directly from the extruder die to a pre-sizing water bath that is located downstream of the extruder die, wherein the pre-sizing water bath is configured to receive the stream of extruded PHA material directly from the extruder die and to provide the stream of extruded PHA material to a second water bath via a bore defined by a sizing tube;
wherein the sizing tube is located downstream of the pre-sizing water bath, and is configured to receive the extruded PHA material from the pre-sizing water bath and to control the outer diameter and wall thickness of the straw, and
wherein the pre-sizing water bath is a non-vacuum container having an open top.
18. The process of claim 17 , wherein the raw PHA material is made of a material comprising at least 50% PHA.