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Moisture Separator (MA)

Remove water vapor and water droplets from moist air flow

Since R2024b

  • Moisture Separator (MA) block

Libraries:
Simscape / Foundation Library / Moist Air / Elements

Description

The Moisture Separator (MA) block removes a specified fraction of water vapor and water droplets from the flow through the block in a moist air network. The block assumes that method that removes the moisture is mechanical, and that the temperature change of the flow is negligible across the ports.

If the Nominal density parameter, ρnom, is greater than zero, then the pressure drop is

pApB=K1m˙Am˙A2+(flamm˙nom)2RTinpin

where:

  • A is the mass flow rate at port A.

  • nom is the value of the Nominal mass flow rate parameter.

  • flam is the fraction of the nominal mixture mass flow rate for the laminar flow transition.

  • pin is the inlet pressure, pA or pB, depending on flow direction.

  • Tin is the inlet temperature, TA or TB, depending on flow direction.

  • R is the specific gas constant.

The proportionality constant, K1, is

K1=Δpnomρnomm˙nom2

where ρnom is the value of the Nominal density parameter and Δpnom is the value of the Nominal pressure drop parameter.

If the Nominal density parameter is zero, then the pressure drop is

pApB=K2m˙Am˙A2+(flamm˙nom)2

where the proportionality constant, K1, is

K2=Δpnomm˙nom2

Because the block assumes the flow resistance is adiabatic, the mixture specific total enthalpies are equal,

hA+12(m˙ARTASpA)2=hB+12(m˙BRTBSpB)2

where:

  • hA and hB are the specific enthalpies at ports A and B, respectively.

  • S is the value of the Cross-sectional area at ports A and B parameter.

Mass and Energy Balance

The mass balance equations for the moist air, water vapor, trace gas, and water droplets are

m˙A+m˙Bm˙w,removed=0m˙wA+m˙wBm˙w,removed=0m˙gA+m˙gB=0m˙dA+m˙dBm˙d,removed=0

where:

  • wA and wB are the water vapor mass flow rates at ports A and B, respectively.

  • gA and gB are the trace gas mass flow rates at ports A and B, respectively.

  • dA and dB are the water droplets mass flow rates at ports A and B, respectively.

The water vapor removal rate is

m˙w,removed=θwm˙MA,inxw,in,

where:

  • θw is the value of the Fraction of water vapor removed parameter.

  • MA,in is the moist air mass flow rate of the inflow port, which can be either port A or B.

  • xw,in is the water vapor mass fraction at the inflow port, which can be either port A or B.

The water droplet removal rate is

m˙d,removed=θdm˙MA,inrd,in,

where:

  • θd is the value of the Fraction of water droplets removed parameter.

  • rd,in is the mass ratio of water droplets to moist air at the inflow port, which can be either port A or B.

The energy balance equation is

ΦA+ΦBΦremoved=0,

where ΦA and ΦB are the energy flow rates through ports A and B, respectively.

Φremoved is the energy flow rate from the removed water vapor and water droplets. This term does not represent heat or work and only includes the specific enthalpy contributions from the removed the water vapor and water droplets,

Φremoved=m˙w,removedhw,in+m˙d,removedhd,in,

where hw,in and hd,in are the water vapor and water droplet specific enthalpies at the inflow port.

Assumptions and Limitations

The block does not model any physics or thermodynamic effects related to removing water vapor and water droplets.

Ports

Output

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Physical signal that outputs the rate of water vapor removed, in kg/s.

Physical signal that outputs the rate of water droplets removed, in kg/s.

Conserving

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Moist air conserving port associated with the inlet or outlet of the moisture separator. This block has no intrinsic directionality.

Moist air conserving port associated with the inlet or outlet of the moisture separator. This block has no intrinsic directionality.

Parameters

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Fraction of water vapor removed from the moist air flow through the block.

Option to condense the removed water vapor to liquid. When you select this check box, the block converts water vapor to liquid before removing it, which means that the latent heat of the water vapor remains in the flow. In this case, the temperature change across the block may be more significant.

Fraction of water droplets removed from the moist air flow through the block.

Pressure drop from the inlet to outlet at nominal operating conditions. The block uses the nominal parameters to calculate the constant of proportionality between the pressure drop and the mass flow rate.

Mass flow rate of the air mixture through the block at nominal operating conditions. The block uses the nominal parameters to calculate the constant of proportionality between the pressure drop and the mass flow rate.

Mass density of the moist air mixture inside the flow resistance at nominal operating conditions. The block uses the nominal parameters to calculate the constant of proportionality between the pressure drop and the mass flow rate. Set this parameter to zero to ignore the dependence of the pressure drop on the air mixture density.

Flow area at the ports of the separator. The block assumes that the ports are identical in size.

Ratio of the threshold mass flow rate to the nominal mass flow rate of the air mixture. The block uses this parameter to set the threshold for the linearization of the pressure drop.

Extended Capabilities

C/C++ Code Generation
Generate C and C++ code using Simulink® Coder™.

Version History

Introduced in R2024b