search.noResults

search.searching

dataCollection.invalidEmail
note.createNoteMessage

search.noResults

search.searching

orderForm.title

orderForm.productCode
orderForm.description
orderForm.quantity
orderForm.itemPrice
orderForm.price
orderForm.totalPrice
orderForm.deliveryDetails.billingAddress
orderForm.deliveryDetails.deliveryAddress
orderForm.noItems
MACHINERY | ALTERNATIVE COMPOUNDERS


Right: B&P Littleford’s TriVolution system is said to offer good dispersive and distributive mixing


improve the venting and material feeding function and reduce energy consumption and space requirements. “Most importantly, it can produce a better dispersion and mixing and provide stability and precision extrusion,” he says.


Below: Farrel Pomini’s US Process Laboratory and Customer Demonstration Center at Ansonia


Working in triplicate KMD Plastifizierungstechnik, which changed its name from Keimei a few months ago, offers a triple-screw extruder. “Our current interest is in polyolefin production, material reaction and most importantly, material property modification and nanomaterial production,” says Project Manager Kevin Duan. He says the company has obtained “excellent” results in degassing, thanks to the much greater gas exchange area than available from twin-screw extruders. He says the “kneading frequency” (degassing frequency) is triple that of twin-screw extruders with three starts with the same cross section. However, Duan claims the triple-screw extruder is as convenient to use as a twin-screw. “You can change material as quickly, you can replace a screw as easily, and the screw adjustment is as conveni- ent,” he says. B&P Littleford’s TriVolution Compounder is something of a hybrid, being essentially a kneader with three screws. The company says it “offers excellent dispersive and distributive mixing without damaging critical ingredients by its innovative mixing mechanism. Its controlled shear with enhanced material exposure is also well adapted for devolatilisation and reactive processing.”


Minimising shear Farrel Pomini’s Continuous Mixing Technology (FCM) is said to offer several standard equipment features that address key concerns when process- ing flame retardant materials including ATH, MDH


and brominated based formulations. The FCM utilises two non-intermeshing, counter rotating rotors, which apply controlled levels of shear to the polymer. The company says this makes it an ideal technology for shear and temperature-sensitive materials. Among these are flame-retardant compounds. The FCM is based on a mixer with high free


volume. This enhances the quantity of flame-retard- ant filler materials that can be incorporated into the polymer matrix. Quantities of 75-80% have been routinely processed, a company representative says. When processing ATH, for example, Farrel


Pomini has found that by using a hard surface chamber liner and a combination of rotor styles, which it classifies as #15 and #7, it has been able to increase production rates by as much as 30% compared to a twin-screw machine but at process temperatures below 190°C. In addition, in the same study, melt temperature was found to be further decreased when rotor cooling was activated. In another scenario processing MDH, use of a


PTFE orifice resulted in a 15% lower melt tempera- ture. And in a separate study processing LLDPE & MDH (60%), and using the rotor styles #15 and #7 in combination with and a hard surface chamber liner, it proved possible to achieve a 30% increase in productivity with only a 17 °C process tempera- ture rise, the company says.


CLICK ON THE LINKS FOR MORE INFORMATION: � www.busscorp.com � www.x-compound.chwww.gneuss.com � www.entex.dewww.technovel.co.jpwww.keimei.dewww.bplittleford.com � www.farrel-pomini.com


90 COMPOUNDING WORLD | October 2019 www.compoundingworld.com


PHOTO: FARREL POMINI


PHOTO: B&P LITTLEFORD


Page 1  |  Page 2  |  Page 3  |  Page 4  |  Page 5  |  Page 6  |  Page 7  |  Page 8  |  Page 9  |  Page 10  |  Page 11  |  Page 12  |  Page 13  |  Page 14  |  Page 15  |  Page 16  |  Page 17  |  Page 18  |  Page 19  |  Page 20  |  Page 21  |  Page 22  |  Page 23  |  Page 24  |  Page 25  |  Page 26  |  Page 27  |  Page 28  |  Page 29  |  Page 30  |  Page 31  |  Page 32  |  Page 33  |  Page 34  |  Page 35  |  Page 36  |  Page 37  |  Page 38  |  Page 39  |  Page 40  |  Page 41  |  Page 42  |  Page 43  |  Page 44  |  Page 45  |  Page 46  |  Page 47  |  Page 48  |  Page 49  |  Page 50  |  Page 51  |  Page 52  |  Page 53  |  Page 54  |  Page 55  |  Page 56  |  Page 57  |  Page 58  |  Page 59  |  Page 60  |  Page 61  |  Page 62  |  Page 63  |  Page 64  |  Page 65  |  Page 66  |  Page 67  |  Page 68  |  Page 69  |  Page 70  |  Page 71  |  Page 72  |  Page 73  |  Page 74  |  Page 75  |  Page 76  |  Page 77  |  Page 78  |  Page 79  |  Page 80  |  Page 81  |  Page 82  |  Page 83  |  Page 84  |  Page 85  |  Page 86  |  Page 87  |  Page 88  |  Page 89  |  Page 90  |  Page 91  |  Page 92  |  Page 93  |  Page 94  |  Page 95  |  Page 96  |  Page 97  |  Page 98  |  Page 99  |  Page 100  |  Page 101  |  Page 102  |  Page 103  |  Page 104