IP Library Patent Application 11332741
Patent Application
App. No. 11/332,741

Manufacture of cellulose esters: recycle of caustic and/or acid from pre-treatment of pulp

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Quick Facts
Patent No.
US None
App. No.
11/332,741
Abstract

A process for the manufacture of cellulose esters is described. The process includes the steps of: pre-treating pulp for the removal of impurities with either caustic or acid or both, esterifying the pre-treated pulp, and recycling the caustic or acid or both from the pre-treating step.

Claims (52)

1 . In a process for the manufacture of cellulose esters wherein the process comprising the steps of pre-treating pulp for the removal of impurities with either caustic or acid or both and esterifying the pretreated pulp, the improvement comprising the steps of:

recycling the caustic or acid or both from a stream from the pre-treating step.

2 . The process of claim 1 wherein recycling caustic further comprising:

filtering the caustic stream from the pre-treating step; and

recovering caustic to form a filter concentrate.

3 . The process of claim 1 wherein recycling further comprises the steps of:

filtering impurities from the caustic stream from the pre-treating step, and

forming a filtrate for return to the pre-treating of pulp and a concentrate.

4 . The process of claim 3 wherein filtering comprises the step of:

nano-filtering impurities from the caustic stream.

5 . The process of claim 3 wherein filtering comprises the steps of:

pre-filtering particles having a predetermined size from the caustic stream,

nano-filtering impurities from the pre-filtered caustic stream, and

returning the filtrate from the nano-filtering to pre-treating the pulp.

6 . The process of claim 5 wherein the predetermined size being selected from the group consisting of a particle size of >5 microns.

7 . The process of claim 3 further comprising the step of:

precipitating impurities from the concentrate with a precipitating agent and forming precipitated impurities and a mixture of precipitating agent and caustic.

8 . The process of claim 7 wherein the precipitating agent being selected from the group consisting of alcohol, ketone, and mixtures thereof.

9 . The process of claim 8 wherein the alcohol being selected from the group consisting of alcohols containing 1 to 4 carbons.

10 . The process of claim 8 wherein the ketone being acetone.

11 . The process of claim 7 further comprising the step of:

separating precipitated impurities from the mixture of precipitating agent and caustic.

12 . The process of claim 7 further comprising the step of:

separating the precipitating agent from the mixture of precipitating agent and caustic and forming a precipitating agent stream and a caustic stream.

13 . The process of claim 12 wherein separating being distilling.

14 . The process of claim 12 further comprising the step of:.

removing impurities from the caustic stream prior to returning the caustic to the pre-treating of the pulp.

15 . The process of claim 14 wherein removing being selected from the group consisting of extracting and adsorbing.

16 . The process of claim 1 wherein recycling further comprising the steps of:

distilling the acid from the pre-treating step.

17 . The process of claim 1 wherein recycling further comprising the steps of:

filtering the acid from the pre-treating step and forming a filtrate stream and a concentrate stream;

separating acid from the filtrate stream; and

separating acid from the concentrate stream.

18 . The process of claim 1 wherein recycling further comprises the steps of:

filtering impurities from the acid stream from the pre-treating step, and

forming a filtrate and a concentrate.

19 . The process of claim 18 wherein filtering comprises the step of:

nano-filtering impurities from the acid stream.

20 . The process of claim 18 wherein filtering comprises the steps of:

pre-filtering particles having a predetermined size from the acid stream, and

nano-filtering impurities from the pre-filtered acid.

21 . The process of claim 20 wherein the predetermined size being selected from the group consisting of a particle size of >5 microns.

22 . The process of claim 18 wherein recycling further comprises extracting acid from the filtrate.

23 . The process of claim 22 wherein extracting further comprising contacting the acid stream with a solvent.

24 . The process of claim 23 wherein the solvent being selected from the group consisting of benzene, diethyl ether, diisobutyl ketone, ethyl acetate, methyl amyl ketone, methyl ethyl ketone, methyl t-butyl ether (MTBE), C-6 hydrocarbons, isopropyl acetate, isobutyl acetate, isopropyl ether, and mixtures thereof.

25 . The process of claim 23 further comprising separating acid from an acid/solvent stream.

26 . The process of claim 18 wherein recycling further comprises extracting acid from the concentrate.

27 . The process of claim 26 wherein extracting further comprising contacting the acid stream with a solvent.

28 . The process of claim 27 wherein the solvent being selected from the group consisting of hexane, pentane, heptane, and mixtures thereof.

29 . The process of claim 16 further comprising the step of removing any residual impurities.

30 . The process of claim 29 wherein said impurities being organic solvent extractives.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 3, 2008
From: CELANESE ACETATE LLC
To: DEUTSCHE BANK AG, NEW YORK BRANCH, AS COLLATERAL AGENT
Reel/Frame 020753/0559 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 27, 2006
From: WANG, LINFU; STOGNER, HENRY P.; FALLON, DENIS G.; KIZER, LAWTON E.; TONEY, CHARLES E.; BATSON, BILLY C.
To: CELANESE ACETATE, LLC
Reel/Frame 017729/0522 →