Process for preparing a polyolefin composition

Abstract

A process for continuously preparing a polyolefin composition made from or containing a polyolefin and carbon black in an extruder device. The process includes the steps of supplying polyolefin in form of a polyolefin powder and carbon black to a mixing device; alternatively, (a) measuring the flow rate of the polyolefin powder supplied to the mixing device or (b) measuring the flow rate of the polyolefin pellets prepared in the extruder device; adjusting the flow rate of the carbon black to the mixing device in response to the measured flow rate of the polyolefin powder or adjusting the flow rate of the polyolefin powder to the mixing device in response to the measured flow rate of the polyolefin pellets; melting and homogenizing the mixture within the extruder device; and pelletizing the polyolefin composition into the polyolefin pellets.

1 . A process for continuously preparing polyolefin pellets of a polyolefin composition in an extruder comprising:
 (i) supplying a polyolefin in form of a polyolefin powder at a flow rate to a mixing device;   (ii)
 (a) measuring the flow rate of the polyolefin powder supplied to the mixing device or 
 (b) measuring a flow rate of the polyolefin pellets prepared in the extruder device; 
   (iii) supplying carbon black at a flow rate to the mixing device;   (iv) optionally supplying one or more further additives at a flow rate to the mixing device;   (v)
 (a) when measuring the flow rate of the polyolefin powder supplied to the mixing device, adjusting the flow rates of the carbon black and any optional additives in response to the measured flow rate of the polyolefin powder or, 
 (b) when measuring the flow rate of the polyolefin pellets prepared in the extruder device, adjusting the flow rate of the polyolefin powder to the mixing device in response to the measured flow rate of the polyolefin pellets and either
 (1) keeping the flow rates of the carbon black and any optional additives constant or 
 (2) adjusting the flow rates of the carbon black and any optional additives, 
 in response to the measured flow rate of the polyolefin pellets; 
 
   (vi) mixing the polyolefin powder, the carbon black and any optional additives to form a powder mixture,   (vii) transferring the powder mixture obtained in step (vi) from the mixing device into the extruder device;   (viii) heating the powder mixture to form a melt and homogenizing the melt within the extruder device to form a polyolefin composition in a molten state; and   (ix) pelletizing the molten polyolefin composition, thereby yielding the polyolefin pellets at a flow rate.   
     
     
         2 . The process of  claim 1 , wherein the flow rate of the polyolefin powder is measured. 
     
     
         3 . The process of  claim 1 , wherein the flow rate of the polyolefin pellets prepared in the extruder device is measured. 
     
     
         4 . The process of  claim 1 , wherein the flow rate of the polyolefin powder or the flow rate of the polyolefin pellets is measured by a solids flow meter. 
     
     
         5 . The process of  claim 1 , wherein the mixing device is a paddle mixer having two horizontally orientated counter-rotating shafts. 
     
     
         6 . The process of  claim 1 , wherein the carbon black is supplied to the mixing device from a carbon black storage vessel in a process comprising
 (iiia) transferring the carbon black from the storage vessel through a first carbon black discharge valve to a carbon black feeding vessel;   (iiib) subsequently transferring the carbon black from the carbon black feeding vessel through a second carbon black discharge valve by gravity to a dosing device; and   (iiic) subsequently transferring the carbon black from the dosing device to the mixing device.   
     
     
         7 . The process of  claim 6 , wherein the first carbon black discharge valve and the second carbon black discharge valve are pinch valves. 
     
     
         8 . The process of  claim 6 , wherein the carbon black feeding vessel is equipped with an agitator. 
     
     
         9 . The process of  claim 6 , wherein the dosing device is equipped with a dosing device hopper and the dosing device hopper is equipped with an agitator. 
     
     
         10 . The process of  claim 6 , wherein in transferring step (iiia), the carbon black passes a conveying chute after having passed the first carbon black discharge valve. 
     
     
         11 . The process of  claim 6 , wherein transferring step (iiia) is carried out intermittently, the carbon black feeding vessel is on a scale, and transferring step (iiib) is controlled by measuring changes in the weight of the carbon black feeding vessel. 
     
     
         12 . The process of  claim 1 , wherein the polyolefin is a polyethylene. 
     
     
         13 . The process of  claim 1 , wherein the polyolefin powder is a powder of a bimodal or multimodal polyolefin. 
     
     
         14 . The process of  claim 12 , wherein the polyethylene is a high density polyethylene having a density determined according to ISO 1183 at 23° C. from about 0.945 to about 0.965 g/cm 3 . 
     
     
         15 . The process of  claim 1 , further comprising the steps of:
 (x) supplying a second amount of polyolefin pellets to the extruder device; and   (xi) adjusting the flow rate of the second amount of polyolefin pellets fed to the extruder device in response to the measured flow rate of the polyolefin powder or in response to the measured flow rate of the resulting polyolefin pellets.   
     
     
         16 . A process for continuously preparing a polyolefin composition comprising polyolefin and carbon black in an extruder device, the process comprising the steps
 (i) supplying polyolefin in form of a polyolefin powder to a mixing device;   (ii) measuring the flow rate of the polyolefin powder supplied to the mixing device or measuring a flow rate of the polyolefin pellets prepared in the extruder device;   (iiia) transferring carbon black from a storage vessel through a first carbon black discharge valve to a carbon black feeding vessel;   (iiib) subsequently transferring the carbon black from the carbon black feeding vessel through a second carbon black discharge valve by gravity to a dosing device; and   (iiic) subsequently transferring the carbon black from the dosing device to the mixing device.   (iv) optionally supplying one or more further additives to the mixing device;   (v) when measuring the flow rate of the polyolefin powder supplied to the mixing device, adjusting the flow rates of the carbon black and the optionally supplied one or more further additives to the mixing device in response to the measured flow rate of the polyolefin powder or, when measuring the flow rate of the polyolefin pellets prepared in the extruder device, adjusting the flow rate of the polyolefin powder to the mixing device in response to the measured flow rate of the polyolefin pellets and either keeping the flow rates of the carbon black and the optionally supplied one or more further additives supplied to the mixing device constant or also adjusting the flow rates of the carbon black and the optionally supplied one or more further additives supplied to the mixing device in response to the measured flow rate of the polyolefin pellets;   (vi) mixing the polyolefin powder, the carbon black and the optionally supplied one or more further additives to form a powder mixture,   (vii) transferring the powder mixture obtained in step (vi) from the mixing device into the extruder device;   (viii) heating the powder mixture to form a melt and homogenizing the melt within the extruder device to form a polyolefin composition in liquid state; and   (ix) pelletizing the polyolefin composition.   
     
     
         17 . The process of  claim 16 , wherein, in transferring step (iiia), the carbon black passes a conveying chute after having passed the first carbon black discharge valve. 
     
     
         18 . The process of  claim 16 , wherein transferring step (iiia) is carried out intermittently, the carbon black feeding vessel is situated on a scale and transferring step (iiib) is controlled by measuring differences in the weight of the carbon black feeding vessel. 
     
     
         19 . The process of  claim 16 , wherein the polyolefin is a polyethylene. 
     
     
         20 . A process for continuously preparing a polyolefin composition comprising polyolefin and carbon black in an extruder device, the process comprising the steps
 (i) supplying polyolefin in form of a polyolefin powder to a mixing device;   (ii) measuring the flow rate of the polyolefin powder supplied to the mixing device or measuring a flow rate of the polyolefin pellets prepared in the extruder device;   (iii) supplying carbon black to the mixing device;   (iv) optionally supplying one or more further additives to the mixing device;   (v) when measuring the flow rate of the polyolefin powder supplied to the mixing device, adjusting the flow rates of the carbon black and the optionally supplied one or more further additives to the mixing device in response to the measured flow rate of the polyolefin powder or, when measuring the flow rate of the polyolefin pellets prepared in the extruder device, adjusting the flow rate of the polyolefin powder to the mixing device in response to the measured flow rate of the polyolefin pellets and either keeping the flow rates of the carbon black and the optionally supplied one or more further additives supplied to the mixing device constant or also adjusting the flow rates of the carbon black and the optionally supplied one or more further additives supplied to the mixing device in response to the measured flow rate of the polyolefin pellets;   (vi) mixing the polyolefin powder, the carbon black and the optionally supplied one or more further additives to form a powder mixture,   (vii) transferring the powder mixture obtained in step (vi) from the mixing device into the extruder device;   (viii) heating the powder mixture to form a melt and homogenizing the melt within the extruder device to form a polyolefin composition in liquid state;   (ix) pelletizing the polyolefin composition;   (x) supplying polyolefin pellets to the extruder device; and   (xi) adjusting the flow rate of the polymer pellets fed to extruder device in response to the measured flow rate of the polyolefin powder or in response to the measured flow rate of the polyolefin pellets.