Method of designing and manufacturing a distributor bar for applying a viscous foamable liquid mixture onto a laminator
AssigneeHuntsman International LLC
InventorMark Joseph Brennan
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AssigneeHuntsman International LLC
InventorMark Joseph Brennan
Estimating the term…
Method of designing and manufacturing a distributor bar for use in a production line comprising a mixing head for providing a viscous foamable liquid mixture, a laminator with a predefined speed of at least 20 m/min, the distributor bar having a central inlet fluidly connected to a number of outlets via a main channel. The method comprises: choosing (3001) a geometry for the distributor bar and defining a set of geometrical parameters; assigning (3002) values to said parameters; creating (3003) a virtual model; simulating (3005) flow in said model by performing a Computational Fluid Dynamics simulation (CFD), taking into account (3004) a non-Newtonian shear thinning model; e) evaluating the simulated flow; building (2007) a physical distributor bar. A distributor bar, a production line, and a computer program product.
A method (3000) of designing and manufacturing a distributor bar (210, 230, 240, 250, 260, 280, 290, 300) having a central inlet (2) for receiving a predefined viscous foamable liquid mixture at a predefined flow rate (Qtotal), and having a predefined even number (Nholes) of outlets (p1-p12) fluidly connected to said inlet via a main channel (5), the number of outlets being spaced apart equidistantly over a predefined length (Lbar),
A distributor bar (210, 230, 240, 250, 260, 280, 290, 300) having a central inlet (2) for receiving a predefined viscous foamable liquid mixture at a predefined flow rate (Qtotal), and having a predefined even number (Nholes) of outlets (p1-p12) fluidly connected to said inlet via a main channel (5), the number of outlets being spaced apart equidistantly over a predefined length (Lbar), characterized in that the distributor bar has a geometry such that, when a ratio of the predefined flow rate (Qtotal) entering the central inlet and the predefined length (Lbar) is at least 1.00×10−4 m2/s, the mixture will leave each of the outlets (p1-p12) with an average velocity which is constant for each of the outlets within a predefined tolerance margin of at most +/−5%.
Dependencies are inferred from the claim text.