Device and Method for Scaling Reduction in a Dead Water Zone of a Fluid Conduit
20170138540 · 2017-05-18
Assignee
Inventors
Cpc classification
F16L55/24
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F17D1/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F16L55/02736
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F17D1/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A scale-dampening or scale-inhibiting device is at a radial restriction in a pipeline. A helical flow guide is arranged in a pipeline portion upstream of the restriction. The flow guide projects radially inwards from a pipe wall and has a longitudinal direction slanted relative to the center axis of the pipeline. A method is for dampening or inhibiting scaling in a dead zone of a fluid flow downstream of a restriction in a pipeline.
Claims
1. A scale-dampening or scale-inhibiting device at a radial restriction in a pipeline wherein at least one helical flow guide is arranged in a pipeline portion upstream of the restriction, the at least one helical flow guide projecting radially inwards from a pipe wall and having a longitudinal direction slanted relative to the center axis of the pipeline.
2. The scale-dampening or scale-inhibiting device according to claim 1, wherein the at least one helical flow guide forms a wall that provides two separate flow paths in the pipeline portion.
3. The scale-dampening or scale-inhibiting device according to claim 1, wherein the smallest diameter of the at least one helical flow guide is, maximally, equal to the diameter of the radial restriction.
4. The scale-dampening or scale-inhibiting device according to claim 1, wherein the pitch of the at least one flow guide decreases in the direction of the restriction.
5. A method of dampening or inhibiting scaling in a dead zone of a fluid flow downstream of a restriction in a pipeline, the fluid flow exhibiting an axial flow velocity wherein the method comprises: via at least one helical flow guide, providing a peripheral flow velocity at least on a lee side of the restriction.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] In what follows, an example of a preferred embodiment is described, which is visualized in the accompanying drawings, in which:
[0017]
[0018]
[0019]
DETAILED DESCRIPTION OF THE DRAWINGS
[0020] In the drawings, the reference numeral 1 indicates a pipeline including a restriction 12 in a flow path 13 for a fluid flow 3. On a lee side 121 of the restriction 12, that is to say downstream of the restriction 12, a dead zone 31 is brought about in the fluid flow, that is to say a zone in which a flow rate V.sub.T is approximately zero according to the prior art (see
[0021] In a first embodiment of the invention (see
[0022] In a second embodiment of the invention (see
[0023] When a fluid flow 3 is provided in the pipeline 1, the flow guide(s) 2, 2 bring(s) about a peripheral velocity component V.sub.P in the flow 3. This leads to a far higher resulting flow rate V.sub.T being provided on the lee side 121 of the restriction 12 than on the lee side 121 of a restriction 12 where the pipeline 1 is not provided with one or more flow guides 2, 2, see
[0024] The peripheral flow velocity V.sub.P on the lee side 121 of the restriction 12 is affected by, among other things, the flow rate of the fluid 3 at the entrance to the pipeline portion 1a, which is provided with one or more flow guides 2, 2, the distance between the flow guide(s) 2, 2 and the lee side 121 of the restriction 12, the difference between the internal diameters of the restriction 12 and the flow guide(s) 2, 2, the pitch P of the flow guide(s) 2, 2, especially the pitch P at the downstream end of the flow guide(s) 2, 2, and the viscosity of the fluid 3.
[0025] The flow rates indicated in the figures are examples of how the flow guide(s) 2, 2 give(s) a positive effect on the flow rate downstream of the restriction 12. The flow rate that is necessary to prevent scaling is obtained from trials and experience with well fluids of different chemical compositions, and the design of the flow guide(s) 2, 2, for example the pitch P, is selected on the basis of what radial flow velocity component R.sub.R is desirably to be achieved at a specific fluid flow.