Water curtain nozzle
US-2024366980-A1 · Nov 7, 2024 · US
US10328450B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10328450-B2 |
| Application number | US-201515509004-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 24, 2015 |
| Priority date | Sep 11, 2014 |
| Publication date | Jun 25, 2019 |
| Grant date | Jun 25, 2019 |
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Official abstract text for this publication.
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.
Opening claim text (preview).
The invention claimed is: 1. A production line comprising: one or more mixing heads adapted for receiving raw foam materials and producing a viscous foamable liquid mixture; a laminator having a predefined width and being adapted for running at a line speed of at least 15 m/min; a distributor bar having (i) a central inlet fluidly connected to said one or more mixing heads for receiving said viscous foamable liquid mixture at a predefined flow rate and (ii) a predefined even number of cylindrical outlets fluidly connected to said central inlet via a main channel for depositing said viscous foamable liquid mixture on said laminator, the cylindrical outlets spaced over a predefined length and the main channel having an inner diameter that linearly decreases from a first diameter D 1 at its center to a second diameter αD 1 at each outer end where α is a constant value in a range of 0.5 to 0.95, wherein the viscous foamable liquid mixture is deposited from cylindrical outlets positioned at each outer end of the main channel directly downward with respect to a direction perpendicular to the laminator and wherein when a ratio of the predefined flow rate entering the central inlet and the predefined length is at least 1.00×10 −4 m 2 /s the viscous foamable liquid mixture will leave each of the cylindrical outlets with an average velocity which is constant for each of the cylindrical outlets within a predefined tolerance margin of at most+/−5%. 2. The production line of claim 1 , wherein the laminator is adapted for running at a line speed of at least 20 m/min. 3. The production line of claim 1 , wherein the laminator is adapted for running at a line speed of at least 25 m/min. 4. The production line of claim 1 , wherein the laminator is adapted for running at a line speed of at least 40 m/min. 5. The production line of claim 1 , wherein the cylindrical outlets have a constant inner diameter. 6. The production line of claim 1 , wherein a is a constant value in a range of 0.75 to 0.8. 7. The production line of claim 1 , wherein the predefined tolerance margin is at most+/−3%.
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