4.16. Merger

../_images/image582.png

Fig. 4.16.1 Schematic wanda component merger

type label

description

active

2-merger

Three-node junction which merges 2 separate branch flows into a combined flow.

Cross section can be circular or rectangular.

no

The merger differs from the Y-junctions (Section 4.40) because there is no straight main flow. The area of the three legs may be different.

Instead of negative flow the Merger component acts as a Splitter component (Section 4.27).

4.16.1. Mathematical model

4.16.1.1. Positive flow definition

The positive flow definition and the numbers of the connect points is important to understand the results in the property window. Notice that the connect point numbering of the Merger differs from that of the Splitter (Section 4.27).

For the Merger-junction the positive flow definition and connect point numbers are defined in the figure below.

../_images/image583.png

Fig. 4.16.2 Merger-junction positive flow direction and connection points.

4.16.1.2. Flow regimes

The Merger supports only the positive merging flow and for negative flow the splitting variant. The other flow regimes are not supported and for these circumstances the local losses are ignored, that means the Merger becomes frictionless.

In the table below the different flow regimes are explained with a scheme with corresponding actual flow arrows.

Table 1: definition of different flow regimes

Merging flow (Positive flow)

../_images/image584.png

Splitting flow (Negative flow)

../_images/image585.png

Not supported flow regimes

../_images/image586.png

Not supported flow regimes

../_images/image587.png

4.16.1.3. Equations

The head loss over a 3-node component depends on the distribution of the discharges and the area of the connected legs. The Merger supports only the user specified resistance coefficient Xi (ξ) depending on discharge ratio’s for a fixed area ratio.

The head loss in 3-node components is a function of the combined flow in the combined leg. Including the continuity equation (no production or loss of mass in the component) the general set of the three equations of the Y-junction is:

(4.16.1)f1=Q1+Q2Q3=0

Where:

Q i = total discharge in leg i

[m3/s]

Hi = energy head in connect point i

[m]

Ai = pipe area leg i (leg with total flow)

[m2]

ξij = loss coefficient between point i and j

[-]

The subscripts (1), (2) and (3) correspond to the different legs.

For negative splitting flow the formulas of the Splitter component (Section 4.27) will be used with Q1 taken into account instead of Q3.

For the not supported flow regimes the head loss equation becomes H1-H3 = 0 and H2-H3 = 0

4.16.2. Merger properties

The input and output properties for both types are specified below.

Input properties

Description

input

unit

range

default

Remarks

Cross section

Circular

Rectangular

Circular

Diameter combined leg

Real

[mm]

If Cross section = Circular

Diameter merge branch 1

Real

[mm]

If Cross section = Circular

Diameter merge branch 2

Real

[mm]

If Cross section = Circular

Width combined leg

Real

[mm]

If Cross section = Rectangular

Height combined leg

Real

[mm]

If Cross section = Rectangular

Width merge branch 1

Real

[mm]

If Cross section = Rectangular

Height merge branch 1

Real

[mm]

If Cross section = Rectangular

Width merge branch 2

Real

[mm]

If Cross section = Rectangular

Height merge branch 2

Real

[mm]

If Cross section = Rectangular

Xi method

Formula

Table

If Xi method = Formula, the following input should be defined:

Description

input

unit

range

default

Remarks

Angle

15

30

45

De definition of the angle is shown in Fig. 4.16.3.

../_images/merger1248.png

Fig. 4.16.3 Definition of the angle

If Xi method = Table, the following input should be defined:

Description

input

unit

range

default

Remarks

Xi tables valid for

Splitting

Merging

Both

Xi splitting branch 1

Table

12)

if Xi tables = Splitting or Both

Xi splitting branch 2

Table

13)

if Xi tables = Splitting or Both

Xi merging branch 1

Table

21)

if Xi tables = Merging or Both

Xi merging branch 2

Table

31)

if Xi tables = Merging or Both

Example of Xi table (valid for Area ratio = 0.5); Merging branch 1 (ξ13)

Discharge ratio

Xi

[-]

[-]

0.0

0.90

0.2

0.12

0.4

0.39

0.6

0.92

0.8

1.48

1.0

2.08

Component specific output properties

Loss coefficient branch 1 [-]

The ξ13 for positive flow and ξ31 for negative flow

Loss coefficient branch 2 [-]

The ξ23 for positive flow and ξ32 for negative flow

Head loss branch 1 [m]

The ΔH13 for positive flow and ΔH31 for negative flow

Head loss branch 2 [m]

The ΔH23 for positive flow and ΔH32 for negative flow

Component messages

Message

Type

Explanation

Merging flow

Info

image114

Splitting flow

Info

image115

Not supported flow regime

Info

image116 orimage117