IP Library Granted Patent US 8,829,212
Granted Patent B2
US 8,829,212 · App. 13/127,508 · Granted Sep 9, 2014

Method of separating solid salt from epoxy resin solutions

Inventors: Shuji Maeda (Lake Jackson, TX); Ryosuke Tamai (Suginam-Ku, JP); Takashi Ikeda (Handa, JP); Joseph Weber (Himmelpforten, DE)
Assignee: Dow Global Technologies LLC
C08G59/00C07D303/04C07D301/23
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Quick Facts
Patent No.
US 8,829,212
App. No.
13/127,508
Granted
Sep 9, 2014
Kind
B2
Abstract

Use a centrifuge, especially a peeler centrifuge, that has a coarse salt particle layer deposited on its screen to effect recovery of an epoxy resin, especially a liquid epoxy resin, from a product slurry, which epoxy resin has a lower residual salt content than an epoxy resin recovered without use of the coarse salt particle layer.

Claims (10)

1. An improved method for producing a liquid epoxy resin, which method comprises a) reacting, with water removal, a polyhydric phenol, an epihalohydrin and an alkali metal hydroxide or alkaline earth metal hydroxide, to yield a product slurry that comprises liquid epoxy resin, epihalohydrin, and a precipitated, solid alkali metal halide salt or a precipitated, solid alkaline earth metal halide salt, and b) separating the precipitated alkali metal halide salt or alkaline earth metal salt from the product slurry, wherein the improvement comprises effecting separation of the alkali metal salt or alkaline earth metal salt from the product slurry a) using a filtering basket centrifuge that has an internal slurry feed, a centrifuge basket, and an integral screen, the screen being used with or without at least one of an optional filter cloth or other porous barrier, which screen and optional filter cloth or other porous barrier retains solid material but allows liquid to pass through, said screen being disposed on an outer surface of the centrifuge basket and b) disposing a layer of coarse salt particles having an average particle size within a range of from 100 micrometers to 2000 micrometers on an inner surface of the centrifuge, said coarse salt particles lying atop an inner surface of the screen, or when at least one of the optional filter cloth or other porous barrier is used in conjunction with the screen, atop an inner surface of said optional filter cloth and/or other porous barrier, the coarse salt particles having an average particle size that exceeds that of the precipitated alkali metal salt or alkaline earth metal salt particles contained in the product slurry, whereby the precipitated alkali metal salt or precipitated alkaline earth metal salt forms a layer on a slurry feed side of the layer of coarse salt particles.

2. The method of claim 1 , wherein the layer of coarse salt particles has a thickness within a range of from 10 millimeters to 150 millimeters.

3. The method of claim 1 , further comprising a step of removing at least a portion of the precipitated alkali metal halide salt or alkaline earth metal halide salt layer.

4. The method of claim 3 , wherein the step of removing at least a portion of the precipitated salt layer also removes at least an outer surface portion of the layer of coarse salt particles.

5. The method of claim 4 , wherein the step of removing at least a surface portion of the layer of coarse salt particles results in a reduction of coarse salt layer thickness of at least 0.1 millimeter.

6. The method of claim 3 , wherein the step of removing at least a portion of the precipitated salt layer has two sub-steps, sub-step a) which effects removal of substantially all of the precipitated salt layer from an outer surface of said layer of coarse salt particles and sequential sub-step b) which effects removal of at least the surface portion of the layer of coarse salt particles, said surface portion containing plugging amounts of organic contaminants that reduce rates of liquid filtration through the layer of coarse salt particles.

7. The method of claim 1 , wherein separating the precipitated alkali metal halide salt or alkaline earth metal salt from the product slurry occurs as a batch process that comprises at least one sequential series of substeps, said substeps being a) filling a receiving portion of a centrifuge with an amount of the product slurry, the amount being less than that which overfills the receiving portion of the centrifuge, b) allowing a portion of liquids contained in the reaction mixture to drain through the layer of coarse salt particles, and c) operating the centrifuge at a speed sufficient to substantially effect separation of the amount of the reaction product mixture into a resin mixture component that substantially passes through the layer of coarse salt particles and the layer of precipitated alkali metal halide salt or alkaline earth metal halide salt.

8. The method of claim 1 , wherein the particles of the coarse salt layer have a gross chemical composition substantially identical to that of salt particles contained in the product slurry.

9. A method for preparing a filter basket centrifuge for use in the improved method for producing an epoxy resin of claim 1 , which method for preparing the centrifuge comprises establishing a layer of coarse salt particles, which layer has a slurry feed side and a filtrate side and disposing said layer such that the slurry feed side of the layer first contacts product slurry from a source of said product slurry and the filtrate side is spaced apart from said product slurry source.

10. The method of claim 9 , which method comprises substeps a) introducing an aliquot of the coarse salt particles into the centrifuge, and b) forming the aliquot into a layer with a substantially uniform thickness.

Assignments (7)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 11, 2015
From: DOW GLOBAL TECHNOLOGIES LLC
To: BLUE CUBE IP LLC
Reel/Frame 035887/0193 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2014
From: WEBER, JOSEPH
To: DOW DEUTSCHLAND GMBH & CO. OHG
Reel/Frame 033422/0393 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2014
From: DOW DEUTSCHLAND GMBH & CO. OHG
To: THE DOW CHEMICAL COMPANY
Reel/Frame 033422/0520 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2014
From: TAMAI, RYOSUKE; IKEDA, TAKASHI
To: DOW CHEMICAL JAPAN LIMITED
Reel/Frame 033422/0589 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2014
From: DOW CHEMICAL JAPAN LIMITED
To: THE DOW CHEMICAL COMPANY
Reel/Frame 033422/0662 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2014
From: THE DOW CHEMICAL COMPANY
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 033422/0759 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 30, 2014
From: MAEDA, SHUJI
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 033422/0863 →
Continuity (2)
Provisional Application 61138695 · Dec 18, 2008
Related Publication 20110263881A1 · Oct 27, 2011