IP Library Granted Patent US 7,205,376
Granted Patent B2
US 7,205,376 · App. 10/897,732 · Granted Apr 17, 2007

Processes for the production of cumene, polyetherimides, and polycarbonates

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Quick Facts
Patent No.
US 7,205,376
App. No.
10/897,732
Granted
Apr 17, 2007
Kind
B2
Abstract

A method for the manufacture of polycarbonate by combining methane and inlet water to produce methanol, converting the methanol to propylene, gasoline aromatics, and gasoline olefins, converting the propylene and gasoline olefins to hydrogen, first benzene, and toluene, reacting the first benzene with propylene to form cumene, reacting the cumene with oxygen to form cumene hydroperoxide, cleaving the cumene hydroperoxide to produce acetone and phenol, reacting the phenol, additional phenol, and acetone to produce a dihydric aromatic compound, and reacting the dihydric aromatic compound with a carbonate precursor to form polycarbonate.

Claims (39)

1. A method for the manufacture of polycarbonate, comprising:

combining methane and inlet water to produce methanol;

converting the methanol to propylene, gasoline aromatics, and gasoline olefins;

converting the propylene and gasoline olefins to hydrogen, first benzene, and toluene;

reacting the first benzene with propylene to form cumene;

reacting the cumene with oxygen to form cumene hydroperoxide;

cleaving the cumene hydroperoxide to produce acetone and phenol;

reacting the phenol and acetone to produce a dihydric aromatic compound; and

reacting the dihydric aromatic compound with a carbonate precursor to form polycarbonate.

2. The method of claim 1 , further comprising reacting the toluene, the gasoline aromatics, and hydrogen to produce additional benzene; and reacting the additional benzene with propylene to form cumene.

3. The method of claim 1 , further comprising combining outlet water from the production of the methanol with the inlet water.

4. The method of claim 1 , comprising reacting the dihydric aromatic compound with a carbonate precursor in an interfacial polymerization reaction.

5. The method of claim 1 , wherein the carbonate precursor comprises a diaryl carbonate ester.

6. The method of claim 1 , wherein the carbonate precursor comprises a carbonyl halide.

7. The method of claim 6 , wherein the carbonyl halide is carbonyl chloride.

8. The method of claim 1 , comprising combining natural gas and inlet water to produce methanol.

9. The method of claim 1 , wherein the dihydric aromatic compound comprises bisphenol-A.

10. A method for the manufacture of polyetherimide, comprising:

combining methane and water to produce methanol;

converting the methanol to propylene, gasoline aromatics, and gasoline olefins;

converting the propylene and gasoline olefins to hydrogen, first benzene, and toluene;

reacting the first benzene with propylene to form cumene;

reacting the cumene with oxygen to form cumene hydroperoxide;

cleaving the cumene hydroperoxide to produce acetone and phenol;

reacting the phenol and acetone to produce a dihydric aromatic compound;reacting the dihydric aromatic compound with a base to form a dihydric aromatic salt; and

reacting the dihydric aromatic salt with a material to form the polyetherimide.

11. The method of claim 10 , wherein reacting the dihydric aromatic salt with the material to form the polyetherimide further comprises reacting the dihydric aromatic salt with a nitro substituted phenyl dinitrile to form a bis(ether anhydride); and

reacting the bis(ether anhydride) with a diamino compound to form polyetherimide.

12. The method of claim 10 , wherein the material comprises a bis(halophthalimide).

13. The method of claim 10 , further comprising reacting the toluene, the gasoline aromatics, and hydrogen to produce additional benzene; and reacting the additional benzene with propylene to form cumene.

14. The method of claim 10 , further comprising combining outlet water from the production of the methanol with the inlet water.

15. The method of claim 10 , wherein the dihydric aromatic compound comprises bisphenol-A.

16. A method for the manufacture of cumene, comprising:

combining methane and inlet water to produce methanol;

converting the methanol to propylene, gasoline aromatics, and gasoline olefins;

converting the propylene and gasoline olefins to hydrogen, first benzene, and toluene; and

reacting the first benzene with propylene to form cumene.

17. The method of claim 16 , further comprising reacting the toluene, the gasoline aromatics, and hydrogen to produce additional benzene; and combining the additional benzene with the first benzene.

18. The method of claim 16 , further comprising combining outlet water from the production of the methanol with the inlet water.

Assignments (3)
CHANGE OF NAME Recorded Jun 6, 2016
From: SABIC INNOVATIVE PLASTICS IP B.V.
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 038883/0791 →
RELEASE OF SECURITY INTEREST Recorded Mar 17, 2014
From: CITIBANK, N.A.
To: SABIC INNOVATIVE PLASTICS IP B.V.
Reel/Frame 032459/0798 →
SECURITY AGREEMENT Recorded Aug 18, 2008
From: SABIC INNOVATIVE PLASTICS IP B.V.
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 021423/0001 →