IP Library Granted Patent US 10,369,491
Granted Patent B2
US 10,369,491 · App. 13/884,623 · Granted Aug 6, 2019

Method for recovering transition metal tetrahalide and hydrocarbons from a waste stream

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Quick Facts
Patent No.
US 10,369,491
App. No.
13/884,623
Granted
Aug 6, 2019
Kind
B2
Abstract

The present invention provides a process for recovering transition metal tetrahalides from a waste stream coming from a catalyst manufacturing process by (a) establishing a mixed stream comprising transition metal tetrahalide and transition metal alkoxyhalides; (b) forming a falling liquid film from the mixed stream of step (a) at a temperature of from 25 to 85° C. and an absolute pressure of from 0.05 to 0.6 bar; and (c) establishing from the film of step (b) a first vapor stream containing from 90 to 100% of recoverable components and a second liquid stream containing about 10 to 80% of titanium haloalkoxides.

Claims (23)

1. A process for recovering TiCl 4 from a process stream comprising the steps of:

(a) establishing a mixed stream comprising TiCl 4 and a transition metal haloalkoxide by

(a-1) contacting a solid olefin polymerization catalyst component with a wash liquid thereby producing a mixture comprising the solid catalyst component and a liquid component,

wherein the wash liquid is selected from a group consisting of n-pentane, isopentane, n-hexane, 2-methylpentane, 3-methylpentane, cyclohexane, n-heptane, 2-methylhexane, 3-methylhexane, 2-ethylpentane, n-octane, 2-methylheptane, 3-methylheptane, 4-methylheptane, 3-ethylhexane, benzene, toluene, and their mixtures, and

wherein the liquid component comprises the wash liquid, TiCl 4 , and the transition metal haloalkoxide;

(a-2) dividing the mixture of step (a-1) into a product fraction comprising a majority of the solid catalyst component and a liquid fraction comprising the liquid component;

(a-3) recovering the liquid fraction; and

(a-4) establishing said mixed stream from said liquid fraction;

(b) forming a falling liquid film from the mixed stream of step (a) at a temperature of from 50 to 80° C. and an absolute pressure of from 0.1 to 0.6 bar; and

(c) establishing from the film of step (b):

an amount of a distillate, the distillate containing from 90 to 100% by weight of recoverable components, the recoverable components comprising TiCl 4 and the wash liquid, and

an amount of a residue, the residue containing about 20 to 80% by weight of the transition metal haloalkoxide,

wherein the ratio of the amount of residue to the amount of distillate (R/D) is from 0.05 to 0.35.

2. The process according to claim 1 , wherein said distillate contains less than 1% by weight of the transition metal haloalkoxide.

3. The process according to claim 1 , wherein the transition metal haloalkoxide comprises a group 4 or group 5 transition metal.

4. The process according to claim 3 , wherein said group 4 or group 5 transition metal is titanium.

5. The process according to claim 1 , wherein the transition metal haloalkoxide is a transition metal chloroalkoxide.

6. The process according to claim 1 , wherein the process further comprises the steps of:

(d) condensing the distillate into a condensate, and directing the condensate into a distillation step;

(e) withdrawing a first light stream from said distillation step, wherein the first light stream comprises at least 80% by weight of the wash liquid; and

(f) withdrawing a first bottom stream from said distillation step, wherein the first bottom stream comprises at least 80% by weight of TiCl 4 .

7. The process according to claim 6 , wherein the first light stream contains at least 90% by weight of the wash liquid.

8. The process according to claim 6 , wherein the first bottom stream contains at least 95% by weight of TiCl 4 .

Assignments (2)
CHANGE OF ADDRESS Recorded Feb 23, 2022
From: BOREALIS AG
To: BOREALIS AG
Reel/Frame 059219/0949 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 9, 2013
From: LYLYKANGAS, MIKKO; RASANEN, JUKKA; NYFORS, KLAUS; MALINEN, PEKKA
To: BOREALIS AG
Reel/Frame 030758/0007 →
Cited By (3)
US 12,377,365 US 12,508,518 US 12,623,161