Degassing method, degassing device and use of screw elements
AssigneeLANXESS Deutschland GmbH
InventorsJoerg Kirchhoff, Thomas Koenig, Michael Bierdel
Life of this patent
Estimating the term…
Abstract
The present invention relates to a process for devolatilising polymer-containing media such as, in particular, polymer melts, polymer solutions and dispersions and also devolatilisation apparatuses for carrying out the abovementioned process.
Claims35
Devolatilisation apparatus comprising at least one extruder which has:
- a barrel and n barrel holes Bn having the associated hole diameters Dn where n is an integer, preferably an integer from 1 to 16, particularly preferably from 1 to 12, very particularly preferably from 2 to 8 and even more preferably 2, and the barrel holes in the case of n being greater than 1 preferably pass through opposite one another and are likewise preferably arranged parallel to one another,
- one or more screws Wn which can be driven so as to rotate and are in each case arranged concentrically in one of the barrel holes Bn, have an axis of rotation An and are equipped with treatment elements whose cross-sectional profile in the circumferential direction has
- m relative maxima Rmmax n in respect of the radial dimension of the cross-sectional profile to the axis of rotation An of the screw Wn, where m is an integer from 1 to 8, preferably from 1 to 4, particularly preferably 1, 2 or 3, very particularly preferably 1 or 2 and even more preferably 2,
- a maximum value Rmax n in respect of the radial dimension of the cross-sectional profile to the axis of rotation An of the screw Wn, where Rmax n fulfils:
- Rmax n<=(Dn/2)
- at least one feed zone,
- one or more devolatilisation zones comprising in each case at least one devolatilisation opening which is suitable for discharge of volatile constituents from a polymer-containing medium from the extruder,
- at least one discharge zone,
- where the extruder has screw elements SE having a pitch t as treatment elements, which are configured so that at least two of the following three conditions are met:
- S1) the cross-sectional profile has at least one relative maximum Rmmax n based on the radial dimension of the profile curve, for which:
- 0.420 Dn<Rmmax n<0.490 Dn, preferably 0.430 Dn>=Rmmax n<0.485 Dn, particularly preferably 0.440 Dn<Rmmax n<0.482 Dn and particularly preferably 0.450 Dn<Rmmax n<0.480 Dn,
- S2) 1.38 Dn<t<5.00 Dn, preferably 1.60 Dn<t<3.00 Dn, particularly preferably 1.80 Dn<t<2.50 Dn and very particularly preferably 1.90 Dn<t<2.40 Dn,
- S3) the cross-sectional profile of the respective screw element has no tangential angle β greater than 30°, preferably greater than 25°, particularly preferably 22°, very particularly preferably 15° and very particularly preferably 10°, on the active flanks located at the front in the direction of rotation in the range of the radial dimension from 0.95 Rmax to Rmax, preferably from 0.90 Rmax to Rmax, particularly preferably from 0.80 Rmax to Rmax, very particularly preferably from 0.50 Rmax to Rmax and even more preferably in the entire range from 0 to Rmax, where the tangential angle β is defined as
- the smaller of the two angles formed on drawing the tangents at any point on the cross-sectional profile of the treatment element at which the cross-sectional profile cannot be continually differentiated
- and is 0° at any point on the cross-sectional profile of the treatment element at which the cross-sectional profile can always be differentiated.
Process for removing volatile compounds from a polymer-containing medium (PM) which contains at least one polymer and at least one volatile compound, which process comprises at least the following steps:
- a) provision of a devolatilisation apparatus according to any of claims 1 to 27,
- b) introduction of the polymer-containing medium (PM) into the devolatilisation apparatus which is operated so that volatile compounds are given off from the polymer-containing medium (PM) through the devolatilisation openings of the devolatilisation unit and the polymer-containing medium (PM) is in this way depleted in volatile compounds and the polymer is isolated as product P from the polymer-containing medium on discharge from the devolatilisation apparatus and the product P then has a lower proportion of volatile compounds than the polymer-containing medium (PM) introduced into the devolatilisation apparatus and preferably has a total concentration of volatile compounds of less than 1% by weight, preferably less than 0.5% by weight, based on the mass of the polymer.
Use of screw elements having a pitch t which are configured so that at least two of the three following conditions are satisfied:
- S1) the cross-sectional profile has at least one relative maximum Rmmax n based on the radial dimension of the profile curve, for which:
- 0.420 Dn<Rmmax n<0.490 Dn, preferably 0.430 Dn>=Rmmax n<0.485 Dn, particularly preferably 0.440 Dn<Rmmax n<0.482 Dn and particularly preferably 0.450 Dn<Rmmax n<0.480 Dn,
- S2) 1.38 Dn<t<5.00 Dn, preferably 1.60 Dn<t<3.00 Dn, particularly preferably 1.80 Dn<t<2.50 Dn and very particularly preferably 1.90 Dn<t<2.40 Dn,
- S3) the cross-sectional profile of the respective screw element has no tangential angle β greater than 30°, preferably greater than 25°, particularly preferably 22°, very particularly preferably 15° and very particularly preferably 10°, on the active flanks located at the front in the direction of rotation in the range of the radial dimension from 0.95 Rmax to Rmax, preferably from 0.90 Rmax to Rmax, particularly preferably from 0.80 Rmax to Rmax, very particularly preferably from 0.50 Rmax to Rmax and even more preferably in the entire range from 0 to Rmax, where the tangential angle β is defined as
- the smaller of the two angles formed on drawing the tangents at any point on the cross-sectional profile of the treatment element at which the cross-sectional profile cannot be continually differentiated
- and is 0° at any point on the cross-sectional profile of the treatment element at which the cross-sectional profile can always be differentiated,
- in an extruder.
Dependencies are inferred from the claim text.