Removing volatile compounds from polymer granules by vapour distillation

Patent metadata

Field	Value
Publication number	US-9550132-B2
Application number	US-201214240826-A
Country	US
Kind code	B2
Filing date	Nov 12, 2012
Priority date	Nov 14, 2011
Publication date	Jan 24, 2017
Grant date	Jan 24, 2017

Abstract

The present invention relates to a process for treating polyolefin granules in a treatment vessel comprising the steps of: —Providing a bed of granules in liquid in said treatment vessel —Withdrawing a first stream of liquid from said treatment vessel, wherein said first stream of liquid contains hydrocarboneous compounds —introducing a first stream of vapor into said treatment vessel —Withdrawing a second stream of vapor from said treatment vessel wherein said second stream of vapor contains volatile hydrocarboneous compounds —Recovering the granules from said treatment vessel wherein said first stream of vapor has a temperature from Tb to Tb+10° C., wherein Tb is the boiling point of the liquid at the applied pressure, and said first stream of vapor produces an upwards rising vapor stream in said treatment vessel, the superficial vapor velocity of which is no more than 0.2 m/s, and a plant suitable for conducting said process.

First claim

The invention claimed is:

1. A process for treating polyolefin granules in a treatment vessel comprising the steps of:
providing a bed of granules in liquid in said treatment vessel
withdrawing a first stream of liquid from said treatment vessel, wherein said first stream of liquid contains hydrocarboneous compounds
introducing a first stream of vapour into said treatment vessel
withdrawing a second stream of vapour from said treatment vessel wherein said second stream of vapour contains volatile hydrocarboneous compounds
recovering the granules from said treatment vessel
wherein said first stream of vapour has a temperature from Tb to Tb+10° C., wherein Tb is the boiling point of the liquid at the applied pressure, and said first stream of vapour produces an upwards rising vapour stream in said treatment vessel, the superficial vapour velocity of which is no more than 0.2 m/s.

2. The process according to claim 1 , wherein the polyolefin granules contain hydrocarbons selected from C 1 to C 30 hydrocarbons as impurity and wherein at least a part of said hydrocarbons are removed from said granules in said treatment vessel.

3. The process according to claim 1 , wherein the vapour is selected from water vapour, methanol vapour, ethanol vapour, propanol vapour, isopropanol vapour, butanol vapour and mixtures thereof.

4. The process according to claim 1 , wherein the polyolefin granules are selected from a polyolefin material based on C 2 , C 3 and C 4 to C 8 monomers.

5. The process according to claim 1 , wherein a portion of said first stream of vapour condensates upon contact with said bed of granules.

6. The process according to claim 1 , wherein the bed of granules is contacted with the vapour for 15 minutes to 12 hours.

7. The process according to claim 1 , wherein the polyolefin granules withdrawn from the treatment tank are dried before storage and packaging.

8. The process according to claim 1 , wherein the second stream of vapour withdrawn from the treatment tank is condensed to a third stream of liquid and separated from an off-gas that contains volatile hydrocarboneous compounds.

9. The process according to claim 8 , wherein the third stream of liquid is reintroduced into the treatment vessel.

10. The process according to claim 1 , wherein the polyolefin granules are pelletized and combined with liquid prior to introduction into the treatment vessel.

11. The process according to claim 10 , wherein a part of the liquid is removed from the granules prior to introduction into the treatment vessel and stored in a liquid tank.

12. The process according to claim 1 , wherein the granules and the first stream of liquid are withdrawn from the treatment vessel together, separated and the granules are reintroduced into the treatment vessel.

13. The process according to claim 1 , wherein The process further comprises the step of
evaporating a part of said first stream of liquid to produce the first stream of vapour and a second stream of liquid,
and the step of
introducing a first stream of vapour into said treatment vessel
is the step of
reintroducing said first stream of vapour into said treatment vessel.

14. A plant for removing volatile components from polyolefin granules comprising
(a) a treatment tank or a group of treatment tanks ( 1 ) for degassing the polyolefin granules;
(b) a boiler or a group of boilers ( 6 ) for producing vapour;
(c) a conduit or a group of conduits ( 12 ) for introducing pellet slurry into the upper part of the treatment tank or to the group of treatment tanks ( 1 );
(d) a conduit or a group of conduits ( 20 ) for transporting the vapour from the boiler or the group of boilers ( 6 ) to the lower part of the treatment tank or group of treatment tanks ( 1 );
(e) a conduit or a group of conduits ( 14 ) for withdrawing the granules from the lower part of the treatment tank or of each of the group of treatment tanks ( 1 );
(f) a conduit or a group of conduits ( 21 ) for withdrawing vapour from the upper part of the treatment tank or of each of the group of treatment tanks ( 1 ); and
(g) a conduit or a group of conduits ( 16 ) for withdrawing liquid from the lower part of the treatment tank or of each of the group of treatment tanks ( 1 ).

15. The plant according to claim 14 , further comprising
(h) a conduit or a group of conduits ( 18 ) for transporting a part of the liquid withdrawn from the treatment tank or of each of the group of treatment tanks ( 1 ) to the boiler ( 6 ).

16. The plant according to claim 14 , wherein the treatment tank or group of treatment tanks comprises one or more distillation stages ( 2 ) at the lower part and, optionally, the upper part of the treatment tank or group of treatment tanks ( 1 ).

17. A method for removal of volatile components from polyolefin granules, wherein vapour is provided, which has a temperature from Tb to Tb+10° C., wherein Tb is the boiling point of the liquid at the applied pressure, and the vapour is contacted with the polyolefin granules at a superficial vapour velocity of lower than 0.2 m/s.

18. The process of claim 1 , wherein said first stream of vapour is introduced into said treatment vessel at a flow rate of from 10 kg/h to 20 kg/h.

Assignees

• Borealis Ag

Inventors

• Bergstra Michiel
• Hagane Kai
• Jarzombek Manfred
• Arellano Pablo Ivan Aguayo

Classifications

• B29B2009/168

  Removing undesirable residual components, e.g. solvents, unreacted monomers; Degassing · CPC title

• B29B9/16

  Auxiliary treatment of granules · CPC title

• B29K2023/12

  PP, i.e. polypropylene · CPC title

• B01D3/02 Primary

  in boilers or stills · CPC title

• C08L23/00

  Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers · CPC title