| Welcome | Navigation | Approach | TEST-Code |
| (The Open Process daemons build upon the state and closed-process daemons. Visit States pages first.) |
| States | Closed Process | Closed Steady | Open Steady |
| Closed Cycle | Open Cycles | States-II | |
| HVAC | Combustion | Equilibrium | Gas Dynamics |
| (Each section above is divided into two sub-sections - Manual and Applications.) | |
| Applications | |
|
|
(This page is yet to be completed.)
Daemons>Open Process> Applications |
|
An open process
is a process executed
by an open system.
Charging and discharging
An open process
In a uniform flow process, The desired unknown may be one of the state or process variables. |
a. Open Process:
The chapter on Closed Process
defines a process
. Such a process, where the system evolves from an initial or begin-state,
b-state
, to a final or finish-state, f-state
, can also be executed by an open system. In addition to exchanging
heat
and work
, the system also exchanges mass
with its surroundings.
For instance, when a propane cylinder is charged, or steam escapes a pressure cooker, a clear b-state and a f-state serve as the process anchors signaling a process . In addition, depending on the problem, an inlet or an exit port, identified by the i-state or the e-state characterizes the mass transfer for the open system. As the state of the fluid in the cylinder changes, so does the inlet or exit states. A simplifying assumption, called the uniform flow process , treats the states at the inlet and exit as invariant during the process, which is quite reasonable for many practical problems. For instance, the state of propane in the supply line may not be affected during the charging of a cylinder as long as the supply comes from a large reservoir. When water boils inside a pressure cooker, the steam exiting through the valve is saturated vapor and its state does not change, as the pressure inside remains constant, until the last drop of liquid vaporizes. The open process daemons appear under the branch Daemons. Systems. Open. Process on the TEST-Map. In an Open Process problem, partial information is given about the i- , e- , b- and f-States and the process variables . The task is to find the unknown variables using the balance equations and property relations for the given working fluid. |
|
| Fig. 1 Image of the Analysis panel of an Open Process daemon. |
|
The Open Process variables are same as the closed process variables.
|
b. The Open Process Variables:
There are three kinds of variables
that appear in the balance equations for an open process (see Fig. 1):
(a) The state variables from the i-
, e-
, b-
and f-states
. These include the system property
m (=rho*Vol or rho*A*Vel*t), extrinsic
property j
and thermodynamic property s
. (b) The boundary temperature T_B
(in most situations, it is the ambient temperature); (c) The total heat
transfer, Q
(Qdot_O*t), into the system, the total work,
W (=Wdot*t), delivered by the system
through all means (mostly electrical or shaft) other than flow, and
S_gen
(=Sdot_gen*t), the total entropy generation within the control volume during
the process.
While m
, j
and s
at the i-
, e-
, b-
and f-States
, and T_B
(see Fig. 1) are all State properties, the variables
m_i, m_e, Q, W and
S_gen depend on the particular process
the open system executes in taking the system from the
b-State to the
f-State . These variables,
m_i, m_e, Q, W and
S_gen , are the fingerprints of the open
process and are called the open process
variables . The balance equations
of Fig. 1 provide a bridge between the difficult-to-measure
device variables and the easy-to-evaluate
state properties of the anchor states,
b-state,
f-state,
i-state and
e-state. |
|
Load the b- and f-, and i- or e-states, enter the device variables,
and click the Super-Calculate button to update all variables.
The solution Approach. |
c. The Analysis Panel:
The Analysis Panel for an Open Process daemon is shown in Fig.
1 after the Analysis tab is clicked.
The global control panel remains unaffected. On the local control panel, there are four state selectors for the i- and e-states , and the b- and f-states . The default state of a port, State-Null , is equivalent to leaving a port plugged, i.e., no flow. For a charging problem leave the e-state plugged, while for a discharge problem have the i-state plugged. The device is identified by a letter (just like a State is identified by a number), Device-A being the default device. The boundary temperature
T_B is given a default value of 25 deg-C,
which can be overridden if necessary. For adiabatic devices, the value
of T_B is inconsequential as can be inferred from the balance equations
of Fig. 2. d. Solution Procedure: The solution procedure that is emphasized in example after example in the Archive, Slide Show and the Applications page is simple. (a) Evaluate the anchor states, the b- and f-states and the i- or e-state as best as possible. (b) On the Analysis panel, choose a device name (Device-A, for instance), and select from the calculated states the anchor states. (c) Enter the known device variables (for instance Q=0 for an adiabatic device). (d) Press the Enter key (or the Calculate button) and Super-Calculate to update all variables. A detailed report, a spreadsheet friendly table of properties and a few lines of what is called the TEST-Codes are produced on the I/O panel. The TEST-Codes can be saved for later use. In a later session, the solution can be regenerated by pasting the TEST-Codes on the I/O panel and clicking the Load and Super-Calculate button. In the Archive you will find a library of TEST-Codes for many practical problems involving open processes.. |
|
Change any variable, Calculate and Super-Calculate.
|
e. Parametric Studies:
Once an open process has been set up, it is quite simple to evaluate
the effect of changing one or more variables on the problem. Simply change
the variable of interest, be it a state or process variable,
Calculate and
Super-Calculate. All variables in each
panel are updated.
You will find a number of open process examples on the Applications page, Slide Show and the Archive . Try them all! |
| (Each section above is divided into two sub-sections - Manual and Applications.) | |
| Applications | |
| Copyright 1998-2003: Subrata Bhattacharjee |