Systems and methods for producing superabsorbent polymers
Provided herein are systems, and methods of using such systems, for producing superabsorbent polymers from ethylene oxide and carbon monoxide. The production systems have various unit operations, including, for example, a (β-propiolactone production system configured to produce (β-propiolactone from ethylene oxide and carbon monoxide and a superabsorbent polymer production system configured to produce superabsorbent polymers from (β-propio lactone and/or acrylic acid.
1. A production system for superabsorbent polymers from ethylene oxide and carbon monoxide, comprising:
a β-propiolactone production system, comprising:
a first reactor comprising:
at least one inlet to receive carbon monoxide, ethylene oxide, carbonylation catalyst, and solvent; and
at least one outlet for a first β-propiolactone stream comprising β-propiolactone, solvent, and carbonylation catalyst;
a carbonylation catalyst recycling system configured to separate at least a portion of the carbonylation catalyst from the first β-propiolactone stream to produce a second β-propiolactone stream; and
a superabsorbent polymer production system, comprising:
a second reactor comprising:
at least one inlet to receive the second β-propiolactone stream, a crosslinking agent, and a sodium-containing component; and
at least one outlet for a superabsorbent polymer stream comprising superabsorbent polymer.
2. The production system of claim 1 , wherein the second reactor comprises at least one selected from the group of a distillation reactor, a loop reactor, or a continuous stirred-tank reactor.
3. The production system of claim 1 , wherein the at least one inlet of the second reactor is further configured to receive a chelating agent.
4. The production system of any of claim 1 , wherein the at least one inlet of the second reactor is further configured to receive a gelling agent.
5. The production system of any of claim 1 , wherein the sodium-containing component comprises sodium hydroxide, sodium acrylate, or sodium methacrylate, or any combinations thereof.
6. The production system of any of claim 1 , further comprising a β-propiolactone purification system between the carbonylation catalyst recycling system and the superabsorbent polymer production system configured to separate at least a portion of the solvent from the second β-propiolactone stream to produce a third β-propiolactone stream which is received by the at least one inlet of the second reactor instead of the second β-propiolactone stream.
7. A production system for superabsorbent polymers, comprising:
a distillation reactor comprising:
at least one inlet to receive β-propiolactone, a crosslinking agent, and a sodium-containing component; and
at least one outlet for a superabsorbent polymer stream comprising superabsorbent polymer.
8. The production system of claim 7 , wherein the at least one inlet of the distillation reactor is further configured to receive a chelating agent.
9. The production system of claim 7 , wherein the at least one inlet of the distillation reactor is further configured to receive a gelling agent.
10. The production system of any of claim 7 , wherein the sodium-containing component comprises sodium hydroxide, sodium acrylate, or sodium methacrylate, or any combinations thereof.
11. The production system of any of claim 7 , wherein the β-propiolactone comprises solvent.
12. The production system of any of claim 7 , wherein the β-propiolactone and the sodium-containing component are combined prior to entering the distillation reactor.
13. The production system of any of claim 7 , wherein the crosslinking agent and the sodium-containing component are combined prior to entering the distillation reactor.
14. The production system of any of claim 7 , wherein the distillation reactor further comprises a catalytic material.
15. The production system of any of claim 7 , wherein the distillation reactor comprises a separate inlet to receive the β-propiolactone, the crosslinking agent, and the sodium-containing component.
16. A production system for superabsorbent polymers, comprising:
a distillation reactor, comprising:
at least one inlet to receive acrylic acid, a crosslinking agent, and a sodium-containing component; and
at least one outlet for a superabsorbent polymer stream comprising superabsorbent polymer,
wherein the sodium-containing component comprises sodium hydroxide, sodium acrylate, or sodium methacrylate, or any combinations thereof.
17. The production system of claim 16 , wherein the acrylic acid and the sodium-containing component are combined prior to entering the distillation reactor.
18. The production system of claim 16 , wherein the crosslinking agent and the sodium-containing component are combined prior to entering the distillation reactor.
19. The production system of claim 16 , wherein the at least one inlet of the distillation reactor is further configured to receive a catalytic material.
20. The production system of claim 16 , wherein the distillation reactor comprises a separate inlet to receive the acrylic acid, the crosslinking agent, and the sodium-containing component.
21. A production system for superabsorbent polymers, comprising:
a loop reactor comprising:
at least one inlet to receive β-propiolactone, a crosslinking agent, and a sodium-containing component; and
at least one outlet for a superabsorbent polymer stream comprising superabsorbent polymer.
22. The production system of claim 21 , wherein the at least one inlet of the loop reactor is further configured to receive a chelating agent.
23. The production system of claim 21 , wherein the at least one inlet of the loop reactor is further configured to receive a gelling agent.
24. The production system of claim 21 , wherein the sodium-containing component comprises sodium hydroxide, sodium acrylate, or sodium methacrylate, or any combinations thereof.
25. The production system of claim 21 , wherein the β-propiolactone comprises solvent.
26. The production system of claim 21 , wherein the β-propiolactone and the sodium-containing component are combined prior to entering the loop reactor.
27. The production system of claim 21 , wherein the crosslinking agent and the sodium-containing component are combined prior to entering the loop reactor.
28. The production system of claim 21 , wherein the at least one inlet of the loop reactor is further configured to receive a catalytic material.
29. The production system of claim 21 , wherein the at least one inlet of the loop reactor is further configured to receive a diluent.
30. The production system of claim 21 , wherein the loop reactor comprises a separate inlet to receive the β-propiolactone, the crosslinking agent, and the sodium□ containing component.
31. A production system for superabsorbent polymers, comprising:
a loop reactor comprising:
at least one inlet to receive acrylic acid, a crosslinking agent, and a sodium-containing component; and
at least one outlet for a superabsorbent polymer stream comprising superabsorbent polymer,
wherein the sodium-containing component comprises sodium hydroxide, sodium acrylate, or sodium methacrylate, or any combinations thereof.
32. The production system of claim 31 , wherein the acrylic acid and the sodium-containing component are combined prior to entering the loop reactor.
33. The production system of claim 31 , wherein the crosslinking agent and the sodium-containing component are combined prior to entering the loop reactor.
34. The production system of claim 31 , wherein the at least one inlet of the loop reactor is further configured to receive a catalytic material.
35. The production system of claim 31 , wherein the at least one inlet of the loop reactor is further configured to receive a diluent.
36. The production system of claim 31 , wherein the distillation reactor comprises a separate inlet to receive the acrylic acid, the crosslinking agent, and the sodium-containing component.
37. A production system for superabsorbent polymers from ethylene oxide and carbon monoxide, comprising:
a β-propiolactone production system, comprising:
a first reactor comprising:
at least one inlet to receive carbon monoxide, ethylene oxide, carbonylation catalyst, and solvent; and
at least one outlet for a first β-propiolactone stream comprising β-propiolactone, solvent, and carbonylation catalyst;
a carbonylation catalyst recycling system configured to separate at least a portion of the carbonylation catalyst from the first β-propiolactone stream to produce a second β-propiolactone stream;
an acrylic acid production system, comprising:
at least one inlet to receive the second β-propiolactone stream; and
at least one outlet for an acrylic acid stream comprising acrylic acid; and
a superabsorbent polymer production system, comprising:
a second reactor comprising:
at least one inlet to receive the acrylic acid stream, a crosslinking agent, and a sodium-containing component; and
at least one outlet for a superabsorbent polymer stream comprising superabsorbent polymer.
38. The production system of claim 37 , wherein the second reactor comprises at least one selected from the group of a distillation reactor, a loop reactor, or a continuous stirred-tank reactor.
39. The production system of claim 37 , wherein the at least one inlet of the second reactor is further configured to receive a chelating agent.
40. The production system of claim 37 , wherein the at least one inlet of the second reactor is further configured to receive a gelling agent.
41. The production system of claim 37 , wherein the sodium-containing component comprises sodium hydroxide, sodium acrylate, or sodium methacrylate, or any combinations thereof.
42. The production system of claim 41 , wherein the sodium-containing component comprises sodium hydroxide.
43. The production system of claim 42 , wherein the sodium-containing component further comprises water.
44. The production system of claim 37 , further comprising a β-propiolactone purification system between the carbonylation catalyst recycling system and the acrylic acid production system configured to separate at least a portion of the solvent from the second β-propiolactone stream to produce a third β-propiolactone stream which is received by the at least one inlet of the acrylic acid production system instead of the second β-propiolactone stream.
45. The production system of claim 37 , wherein the superabsorbent polymer stream further comprises solvent.
46. The production system of claim 45 , further comprising a superabsorbent polymer purification system configured to separate at least a portion of the solvent from the superabsorbent polymer stream to produce a second superabsorbent polymer stream.
47. The production system of claim 37 , wherein the superabsorbent polymer stream further comprises water.
48. The production system of claim 47 , further comprising a superabsorbent polymer purification system configured to separate at least a portion of the solvent and water from the superabsorbent polymer stream to produce a second superabsorbent polymer stream.