Libs/Technological apparatuses

English • ‎mRussian • ‎Українська

Name	Version	License	Source	Languages	Author	Description
Library of models of the technological apparatuses	2.0	GPLv2	OscadaLibs.db (SQL, GZip) > DAQ.JavaLikeCalc.techApp	en, uk, ru	Roman Savochenko Maxim Lysenko (2007,2010), Ksenia Yashina (2007)	Library of models of the technological apparatuses for creating complex simulators of the technological processes of block-schemes of the module DAQ.BlockCalc. Founded: October 2005 Sponsored by: DIYA Ltd Initially created: in the old Wiki Used by: the simulator AGLKS and Boiler

The library is created to provide models of devices of the technological processes. The library is not static, but based on the module JavaLikeCalc, allowing to create calculations on the Java-like language. The functions' names and its parameters are available in languages: English, Ukrainian and mRussian.

To address the library functions you can use the static call address DAQ.JavaLikeCalc.lib_techApp.{Func}() or dynamic SYS.DAQ.JavaLikeCalc["lib_techApp"]["{Func}"].call(), SYS.DAQ.JavaLikeCalc["lib_techApp"].{Func}()". Where {Func} — function identifier in the library.

For connection the library to a project of the OpenSCADA station you can obtain the database file as:

supplied with a ready and proper package of the Linux distribution like to "openscada-libdb-main", "openscada-LibDB.Main";
directly taken for most actual one from the subversion repository and converted to the DB SQLite file in way:

wget http://oscada.org/svn/trunk/OpenSCADA/data/LibsDB/OscadaLibs.sql
sqlite3 -init OscadaLibs.sql OscadaLibs.db .exit

downloaded for the one attached here.

This obtained file next you can place into the project directory of the station and create the database object for the DB module "SQLite", registering the database file in the configuration.

1 Conception

The basis of the model of each apparatus is the calculation of the input flow and output pressure, based on the input pressure and output flow. In general, models of the technological devices are described by difference equations for discrete machines.

Basing on the functions of this library you can easily and quickly build models of technological processes in the module BlockCalc, combining the blocks in accordance with the technological scheme. Example of combination of several devices of the technological scheme is shown in Figure 1.

Fig.1. An example of the block scheme of the technological process.

The basis of any model of the technological device are two basic formulas, that is the formula of flow and pressure. The canonical formula for flow of the environment for the intersection of the pipe or passageway of the narrowing has the form (1).

(1)

Where:

F — mass flow (ton/hour).

S — section (m2).

Qr — real density of the environment (kg/m3).

∆P — pressure difference (at).

The actual density is calculated by the formula (2).

(2)

Where:

Q0 — density of the environment under the normal conditions (kg/m3).

Kpr — coefficient of the compressibility of the environment (0,001 — liquid; 0,95 — gas).

Pi — input pressure (at).

Each pipe makes the dynamic resistance to the flow, associated with the friction of the pipe walls and that depends on the flow speed. The dynamic resistance of the pipe is represented by (3). The total flow of the environment, taking into account the dynamic resistance is calculated by the formula (4).

(3)

Where:

∆P — pressure difference (at), the resistance of the pipe walls to flow of the environment.

Kr — coefficient of friction of the pipe walls.

D — diameter of the pipeline (m).

l — pipeline length (m).

v — flow speed in the pipeline (m3/hour).

(4)

The equation (1) describes the laminar flow of the environment up to the critical speeds. In the case of exceeding the critical flow speed, the calculation is made by the formula (5). A universal formula for calculating the flow at all speeds will have the view (6).

(5)

Where:

Pi — pressure at the pipe beginning.

(6)

Where:

Po — pressure at the pipe ending.

In the dynamical systems the change of the flow at the pipe ending does not change instantaneously, but lags behind the time travel of the environment part from the pipe beginning to its ending. The time depends on the length of the pipe and speed of the environment in the pipe. Delay of the flow changing at the pipe ending can be described by the formula (7). The resulting formula for calculating of the the flow in the pipe, taking into account the above features, is written in the view (8).

(7)

Where:

Fo — flow at the pipe ending.

t — time.

v — speed of the flow = F/(Qr*S).

(8)

The environment pressure in the volume is usually calculated identically for all cases, by the formula (9).

(9)

2 Structure of the library

The library contains about two dozen of models of the often needed devices of the technological processes and the additional elements. The functions' names and their parameters are available in three languages: English, Ukrainian and mRussian.

2.1 Lag (lag)

Lag model. Can be used for lag imitation of the sensor variables.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
out	Output	Real	Return	false	0
in	Input	Real	Input	false	0
t_lg	Lag time, seconds	Real	Input	false	10
f_frq	Calculation frequency, Hz	Real	Input	true	100

Program

out -= (out-in)/(t_lg*f_frq);

2.2 Noise: 2 harmonic + rand (noise)

Noise model. Contains three parts:

first harmonic part;
second harmonic part;
noise based on generator of the randomize numbers.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
out	Output	Real	Return	false	0
off	Main offset	Real	Input	false	1
a_g1	Amplitude of the harmonic 1	Real	Input	false	10
per_g1	Period of the harmonic part 1, seconds	Real	Input	false	10
a_g2	Amplitude of the harmonic 2	Real	Input	false	5
per_g2	Period of the harmonic part 2, seconds	Real	Input	false	0.1
a_rnd	Amplitude of the random numbers	Real	Input	false	1
f_frq	Calculation frequency, Hz	Real	Input	true	100
tmp_g1	Counter of the harmonic 1	Real	Input	true	0
tmp_g2	Counter of the harmonic 2	Real	Input	true	0

Program

tmp_g1 = (tmp_g1 > 6.28) ? 0 : tmp_g1+6.28/(per_g1*f_frq);
tmp_g2 = (tmp_g2 > 6.28) ? 0 : tmp_g2+6.28/(per_g2*f_frq);
out = off + a_g1*sin(tmp_g1) + a_g2*sin(tmp_g2) + a_rnd*(rand(2)-1);

2.3 Ball crane (ballCrane)

Model of the ball crane. Includes for the going and estrangement time.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
pos	Position, %	Real	Output	false	0
com	Command	Boolean	Input	false	0
st_open	State "Opened"	Boolean	Output	false	0
st_close	State "Closed"	Boolean	Output	false	1
t_full	Going time, seconds	Real	Input	false	5
t_up	Estrangement time, seconds	Real	Input	false	0.5
f_frq	Calculation frequency, Hz	Real	Input	true	100
tmp_up	Estrangement counter	Real	Input	true	0
lst_com	Last command	Boolean	Input	true	0

Program

if(!(st_close && !com) && !(st_open && com)) {
  tmp_up = (pos > 0 && pos < 100) ? 0 : (tmp_up>0&&lst_com==com)?tmp_up-1/f_frq:t_up;
  pos += (tmp_up > 0) ? 0 : (100*(com?1:-1))/(t_full*f_frq);
  pos = (pos > 100) ? 100 : (pos<0)?0:pos;
  st_open = (pos >= 100) ? true : false;
  st_close = (pos <= 0) ? true : false;
  lst_com = com;
}

2.4 Separator (separator)

Separator model with two phases, liquid and gas.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Si	Input cutset, m2	Real	Input	false	0.2
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
So	Output cutset, m2	Real	Input	false	0.2
lo	Output length, m	Real	Input	false	10
Fo_lq	Output liquid flow, ton/h	Real	Input	false	0
Po_lq	Output liquid pressure, at	Real	Output	false	1
Llq	Liquid level, %	Real	Output	false	0
PercLq	% liquid	Real	Input	false	0.01
Vap	Device capacity, m3	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Qlq	Liquid density, kg/m3	Real	Input	false	1000
f_frq	Calculation frequency, Hz	Real	Input	true	200

Program

Flq = max(0, Fi*PercLq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi, Pi, 293, Si, Fo+Flq, Po, 293, So, lo, Q0, 0.95, 0.01, f_frq);
Llq = max(0, min(100,Llq+0.27*(Flq-Fo_lq)/(Vap*Qlq*f_frq)));
Po_lq = Po + Llq*Vap/Qlq;

2.5 Valve (valve)

Valve model, include:

two valves in the one;
super-critical speed;
temperature changing at the throttling;
work in one direction, back valve;
speed control of the position changing;
nonlinearity of the intersection from the position.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Ti	Input temperature, K	Real	Input	false	273
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
To	Output temperature, K	Real	Output	false	273
So	Output pipe cutset, m2	Real	Input	false	0.2
lo	Output pipe length, m	Real	Input	false	10
S_v1	Valve 1 cutset, m2	Real	Input	false	0.1
l_v1	Valve 1 position, %	Real	Input	false	0
t_v1	Valve 1 opening time, seconds	Real	Input	false	10
S_v2	Valve 2 cutset, m2	Real	Input	false	0.05
l_v2	Valve 2 position, %	Real	Input	false	0
t_v2	Valve 2 opening time, seconds	Real	Input	false	5
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kln	Coefficient of the linearity	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
Ct	Heat capacity of the environment	Real	Input	false	20
Riz	Heat resistance of the isolation	Real	Input	false	20
noBack	Back valve	Boolean	Input	false	0
Fwind	Air speed	Real	Input	false	1
Twind	Air temperature, K	Real	Input	false	273
f_frq	Calculation frequency, Hz	Real	Input	true	200
tmp_l1	Lag of the position 1	Real	Output	true	0
tmp_l2	Lag of the position 2	Real	Output	true	0

Program

Qr = Q0+Q0*Kpr*(Pi-1);
tmp_l1 += (abs(l_kl1-tmp_l1) > 5) ? 100*sign(l_kl1-tmp_l1)/(t_kl1*f_frq) : (l_kl1-tmp_l1)/(t_kl1*f_frq);
tmp_l2 += (abs(l_kl2-tmp_l2) > 5) ? 100*sign(l_kl2-tmp_l2)/(t_kl2*f_frq) : (l_kl2-tmp_l2)/(t_kl2*f_frq);
Sr = (S_kl1*pow(tmp_l1,Kln)+S_kl2*pow(tmp_l2,Kln))/pow(100,Kln);

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi, Pi, Ti, Sr, EVAL_REAL, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);
if(noBack) Fi = max(0, Fi);
Po = max(0, min(100,Po+0.27*(Fi-Fo)/(Q0*Kpr*So*lo*f_frq)));

To = max(0, min(2e3,To+(abs(Fi)*(Ti*pow(Po/Pi,0.02)-To)+(Fwind+1)*(Twind-To)/Riz)/(Ct*So*lo*Qr*f_frq)));

2.6 Lag: clean (lagClean)

Model of clean(transportable) lag. Realizes by incorporating several links of a simple delay. Appointed for lags into long pipes.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
out	Output	Real	Return	false	0
in	Input	Real	Input	false	0
t_lg	Lag time, seconds	Real	Input	false	10
f_frq	Calculation frequency, Hz	Real	Input	true	100
cl1	Link 1	Real	Input	true	0
cl2	Link 2	Real	Input	true	0
cl3	Link 3	Real	Input	true	0

Program

cl1 -= (cl1-in)/(t_lg*f_frq/4);
cl2 -= (cl2-cl1)/(t_lg*f_frq/4);
cl3 -= (cl3-cl2)/(t_lg*f_frq/4);
out -= (out-cl3)/(t_lg*f_frq/4);

2.7 Boiler: barrel (boilerBarrel)

The model of the boiler's barrel.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi1	Input water flow, ton/h	Real	Output	false	22
Pi1	Input water pressure, at	Real	Input	false	43
Ti1	Input water temperature, K	Real	Input	false	523
Si1	Input water pipes cutset, m2	Real	Input	false	0.6
Fi2	Input smoke gas flow, ton/h	Real	Output	false
Pi2	Input smoke gas pressure, at	Real	Input	false	1.3
Ti2	Input smoke gas temperature, K	Real	Input	false	1700
Si2	Input smoke gas pipes cutset, m2	Real	Input	false	10
Vi1	Barrel volume, m3	Real	Input	false	3
Lo	Barrel level, %	Real	Output	false	10
S	Heating surface, m2	Real	Input	false	15
k	Heat transfer coefficient	Real	Input	false	0.8
Fo	Output steam flow, ton/h	Real	Input	false	20
Po1	Output steam pressure, at	Real	Output	false	41.68
To1	Output steam temperature, K	Real	Output	false	10
So1	Output steam pipe cutset, m2	Real	Input	false	0.5
lo1	Output steam pipe length, m	Real	Input	false	5
Fo2	Output smoke gas flow, ton/h	Real	Input	false	180
Po2	Output smoke gas pressure, at	Real	Output	false	1
To2	Output smoke gas temperature, K	Real	Input	false	0
Fstm	Inner barrel steam flow, ton/h	Real	Output	false	0
Tv	Inner water temperature, K	Real	Output	false	0
f_frq	Calculation frequency, Hz	Real	Input	false	200

Program

// Water
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi1, Pi1, 293, Si1, EVAL_REAL, Po1, 293, So1, lo1, 1e3, 0.001, 0.01, f_frq);
Fi1 = max(0, Fi1);

// Steam
Lo = max(0, min(100,Lo+(Fi1-Fstm)*100/(Vi1*1000*f_frq)));
To1 = (100*pow(Po1,0.241)+5) + 273;

if(Tv < To1) {
  Tv += (k*S*(Ti2-Tv)-Fi1*0.00418*(Tv-Ti1))/f_frq;
  Fstm = 0;
}
if(Tv >= To1) {
  Tv = To1;
  Lambda = 2750-0.00418*(Tv-273);
  Fstm = (5*S*Fi2*(Ti2-Tv)-Fi1*0.00418*(Tv-Ti1))/(Po1*Lambda);
}

To2 = Ti2-Tv/k;
Po1 = max(0, min(100,Po1+0.27*(Fstm-Fo)/(1.2*0.98*((1-Lo/100)*Vi1+So1*lo1)*f_frq)));

// Smoke gas
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi2, Pi2, 293, Si2, Fo2, Po2, 293, Si2, 30, 1.2, 0.98, 0.01, f_frq);

2.8 Boiler: burner (boilerBurner)

The fire-chamber model of the boiler unit, which operates on three types of fuel, initially is: blast-furnace, coke and natural gases.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi1	Input blast furnace gas flow, ton/h	Real	Output	false
Pi1	Input blast furnace gas pressure, at	Real	Input	false
Ti1	Input blast furnace gas temperature, K	Real	Input	false	40
Si1	Input blast furnace gas pipe cutset, m2	Real	Input	false
Fi2	Input natural gas flow, ton/h	Real	Output	false
Pi2	Input natural gas pressure, at	Real	Input	false
Ti2	Input natural gas temperature, K	Real	Input	false	20
Si2	Input natural gas pipe cutset, m2	Real	Input	false
Fi3	Input coke oven gas flow, ton/h	Real	Output	false
Pi3	Input coke oven gas pressure, at	Real	Input	false
Ti3	Input coke oven gas temperature, K	Real	Input	false	0
Si3	Input coke oven gas pipe cutset, m2	Real	Input	false
Fi4	Input air flow, ton/h	Real	Output	false
Pi4	Input air pressure, at	Real	Input	false
Ti4	Input air temperature, K	Real	Input	false	20
Si4	Input air pipe cutset, m2	Real	Input	false
Fo	Output smoke gas flow, ton/h	Real	Input	false
Po	Output smoke gas pressure, at	Real	Output	false
To	Output smoke gas temperature, K	Real	Output	false
So	Output smoke gas pipe cutset, m2	Real	Input	false	90
lo	Output smoke gas pipe length, m	Real	Input	false
V	Burner volume, m3	Real	Input	false	830
CO	Percentage of CO in the flue stack gases, %	Real	Output	false
O2	Percentage of O2 in the flue stack gases, %	Real	Output	false
f_frq	Calculation frequency, Hz	Real	Input	false	200

Program

using DAQ.JavaLikeCalc.lib_techApp;
pipeBase(Fi1, Pi1, Ti1, Si1, EVAL_REAL, Po, 293, So, lo, 1.2, 0.95, 0.01, f_frq); Fi1 = max(0, Fi1);
pipeBase(Fi2, Pi2, Ti2, Si2, EVAL_REAL, Po, 293, So, lo, 0.7, 0.95, 0.01, f_frq); Fi2 = max(0, Fi2);
pipeBase(Fi3, Pi3, Ti3, Si3, EVAL_REAL, Po, 293, So, lo, 1.33, 0.95, 0.01, f_frq); Fi3 = max(0, Fi3);
pipeBase(Fi4, Pi4, Ti4, Si4, EVAL_REAL, Po, 293, So, lo, 1.293, 0.95, 0.01, f_frq); Fi4 = max(0, Fi4);

Neobhod_vzd = Fi1 + 10*Fi2 + 4*Fi3;
F_DG = Fi1 + Fi2 + Fi3 + Fi4;
O2 = max(0, min(100,(Fi4-Neobhod_vzd)*100/F_DG));
CO = min(100, (O2<1) ? (1.2*abs(O2)) : 0);
koef = min(1, Fi4/Neobhod_vzd);
Q = koef*(8050*Fi2+3900*Fi3+930*Fi1);
delta_t = Q/(F_DG*1.047);
To = max(0, min(2000,(delta_t+(Ti4-273)+(Ti3-273)*(Fi3/Fi1)+(Ti2-273)*(Fi2/Fi1)+(Ti1-273)*(Fi1/Fi4))+273));

Po = max(0, min(10,Po+0.27*(F_DG-Fo)/(1.2*0.95*(So*lo+V)*f_frq)));

2.9 Network: load (net)

Loading with constant pressure on the network. Contains a parameter for connection the noise.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	10
Pi	Input pressure, at	Real	Input	false	1
Po	Output pressure setpoint, at	Real	Input	false	1
So	Output pipe cutset, m2	Real	Input	false	0.1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
Noise	Input flow's noise	Real	Input	false	1
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
f_frq	Calculation frequency, Hz	Real	Input	true	200

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi, Pi, 293, So, EVAL_REAL, Po, 293, So, 10, Q0, Kpr, 0.01, f_frq);

2.10 Source: pressure (src_press)

Source of the constant pressure. Contains a parameter for connection the noise.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Pi	Input pressure setpoint, at	Real	Input	false	10
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
So	Output pipe cutset, m2	Real	Input	false	0.1
lo	Output pipe length, m	Real	Input	false	100
Noise	Input flow's noise	Real	Input	false	1
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
f_frq	Calculation frequency, Hz	Real	Input	true	200
Fit	Input flow, lagged	Real	Output	true	0

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fit, Pi*Noise, 293, So, Fo, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);

2.11 Air cooler (cooler)

Model of the air cooler for gas flow.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Ti	Input temperature, K	Real	Input	false	273
Si	Cooler's pipes cutset, m2	Real	Input	false	0.05
li	Full cooler's pipes length, m	Real	Input	false	10
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
To	Output temperature, K	Real	Output	false	273
So	Output pipe cutset, m2	Real	Input	false	0.2
lo	Output pipe length, m	Real	Input	false	10
Tair	Cooling air temperature, К	Real	Input	false	283
Wc	Cooler performance	Real	Input	false	200
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Ct	Heat capacity of the environment	Real	Input	false	100
Rt	Heat resistance	Real	Input	false	1
f_frq	Calculation frequency, Hz	Real	Input	true	200

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi, Pi, 293, Si, Fo, Po, 293, So, lo, Q0, 0.95, 0.01, f_frq);
Qr = Q0 + Q0*0.95*(Pi-1);
To += (Fi*(Ti-To)+Wc*(Tair-To)/Rt)/(Ct*(Si*li+So*lo)*Qr*f_frq);

2.12 Gas compressor (compressor)

Model of the gas compressor. Implements the surge effect. The surge counts from the dynamic-gas curve, and next there counts the surge margin coefficient.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Ti	Input temperature, K	Real	Input	false	273
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
To	Output temperature, K	Real	Output	false	273
So	Output pipe cutset, m2	Real	Input	false	0.2
lo	Output pipe length, m	Real	Input	false	2
Kmrg	Surge protect margin coefficient	Real	Output	false	0.1
N	Turnovers, 1000 x turn/min	Real	Input	false	0
V	Capacity, m3	Real	Input	false	7
Kpmp	Surge coefficient, surge point	Real	Input	false	0.066
Kslp	Slope coefficient of the surge curve	Real	Input	false	0.08
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
Ct	Heat capacity of the environment	Real	Input	false	100
Riz	Heat resistance of the isolation	Real	Input	false	100
Fwind	Air speed	Real	Input	false	1
Twind	Air temperature, K	Real	Input	false	273
f_frq	Calculation frequency, Hz	Real	Input	true	200
Fit	Input flow, lagged	Real	Output	true	0

Program

Pmax = max(Pi, Po);
Pmin = min(Pi, Po);
Qr = Q0 + Q0*Kpr*(Pi-1);
Qrf = Q0 + Q0*Kpr*(Pmax-1);
Ftmp = (N > 0.1) ? (1-10*(Po-Pi)/(Qr*(pow(N,3)+0.1)*Kpmp)) : 1;
Kmrg = 1-Ftmp;  //The margin coefficient
Fi = V*N*Qr*sign(Ftmp)*pow(abs(Ftmp),Kslp)+
     0.3*(4*So*Qrf/(0.01*lo*1.7724+4*Qrf))*sign(Pi-Po)*pow(Qrf*(Pmax-max(Pmax*0.528,Pmin)),0.5);
Fit -= (Fit-Fi)/max(1,(lo*f_frq)/max(1e-4,abs(Fi/(Qrf*So))));
Po = max(0, min(100,Po+0.27*(Fi-Fo)/(Q0*Kpr*So*lo*f_frq)));

To += (abs(Fi)*(Ti*pow(Po/Pi,0.3)-To)+(Fwind+1)*(Twind-To)/Riz)/(Ct*(V+So*lo)*Qr*f_frq);

2.13 Source: flow (src_flow)

Source of the constant flow. Contains a parameter for connection the noise.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow setpoint, ton/h	Real	Input	false	10
Fo	Output flow, ton/h	Real	Input	false	10
Po	Output pressure, at	Real	Output	false	1
So	Output pipe cutset, m2	Real	Input	false	0.1
lo	Output pipe length, m	Real	Input	false	100
Noise	Input flow's noise	Real	Input	false	1
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
f_frq	Calculation frequency, Hz	Real	Input	true	100

Program

Po = max(0, min(100,Po+0.27*(Noise*Fi-Fo)/(Q0*Kpr*So*lo*f_frq)));

2.14 Pipe-base (pipeBase)

Implementation of the basic foundations of the pipe model:

flow in the pipe, taking into account: the speed, pressure difference, resistance due to friction and the critical flow;
calculation of the pressure;
accounting for the environment density and degree of the compressibility for both gases and liquids.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Ti	Input temperature, K	Real	Input	false	293
Si	Input cutset, m2	Real	Input	false	0.2
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
To	Output temperature, K	Real	Output	false	293
So	Output cutset, m2	Real	Input	false	0.2
lo	Output length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.98
Ktr	Coefficient of friction	Real	Input	false	0.01
f_frq	Calculation frequency, Hz	Real	Input	false	100

Program

Pmax = max(Pi, Po);
Pmin = min(Pi, Po);
Qr = Q0 + Q0*Kpr*(Pmax-1);
Fit = 630*(4*Si*So*Qr/(Ktr*lo*1.7724*Si+4*So*Qr))*sign(Pi-Po)*pow(Qr*(Pmax-max(Pmax*0.528,Pmin)),0.5);
Fi -= (Fi-Fit)/max(1,(lo*f_frq)/max(1,abs(Fit/(Qr*So))));
if(!Fo.isEVal()) Po = max(0, min(100,Po+0.27*(Fi-Fo)/(Q0*Kpr*So*lo*f_frq)));

2.15 Pipe 1->1 (pipe1_1)

Model of the pipe by the scheme "1 -> 1".

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
So	Output cutset, m2	Real	Input	false	0.2
lo	Output length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
f_frq	Calculation frequency, Hz	Real	Input	true	200
Pti	Pti	Real	Output	true	1
Fto	Fto	Real	Output	true	0
Pt1	Pt1	Real	Output	true	1
Ft1	Ft1	Real	Output	true	0

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi, Pi, 293, So, Ft1, Pti, 293, So, 0.33*lo, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Ft1, Pti, 293, So, Fto, Pt1, 293, So, 0.33*lo, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fto, Pt1, 293, So, Fo, Po, 293, So, 0.33*lo, Q0, Kpr, 0.01, f_frq);

2.16 Pipe 2->1 (pipe2_1)

Model of the pipe by the scheme "2 -> 1".

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi1	Input 1 flow, ton/h	Real	Output	false	0
Pi1	Input 1 pressure, at	Real	Input	false	1
Ti1	Input 1 temperature, K	Real	Input	false	273
Si1	Input 1 cutset, m2	Real	Input	false	0.2
Fi2	Input 2 flow, ton/h	Real	Output	false	0
Pi2	Input 2 pressure, at	Real	Input	false	1
Ti2	Input 2 temperature, K	Real	Input	false	273
Si2	Input 2 cutset, m2	Real	Input	false	0.2
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
To	Output temperature, K	Real	Output	false	273
So	Output cutset, m2	Real	Input	false	0.2
lo	Output length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
Ct	Heat capacity of the environment	Real	Input	false	20
Riz	Heat resistance of the isolation	Real	Input	false	20
Fwind	Air speed	Real	Input	false	1
Twind	Air temperature, К	Real	Input	false	273
f_frq	Calculation frequency, Hz	Real	Input	true	100

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi1, Pi1, 293, Si1, EVAL_REAL, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi2, Pi2, 293, Si2, EVAL_REAL, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);
Po = max(0, min(100,Po+0.27*(Fi1+Fi2-Fo)/(Q0*Kpr*So*lo*f_frq)));
To = max(0, To+(Fi1*(Ti1-To)+Fi2*(Ti2-To)+(Fwind+1)*(Twind-To)/Riz)/(Ct*So*lo*Q0*f_frq));

2.17 Pipe 3->1 (pipe3_1)

Model of the pipe by the scheme "3 -> 1".

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi1	Input 1 flow, ton/h	Real	Output	false	0
Pi1	Input 1 pressure, at	Real	Input	false	1
Ti1	Input 1 temperature, K	Real	Input	false	273
Si1	Input 1 cutset, m2	Real	Input	false	0.2
Fi2	Input 2 flow, ton/h	Real	Output	false	0
Pi2	Input 2 pressure, at	Real	Input	false	1
Ti2	Input 2 temperature, K	Real	Input	false	273
Si2	Input 2 cutset, m2	Real	Input	false	0.2
Fi3	Input 3 flow, ton/h	Real	Output	false	0
Pi3	Input 3 pressure, at	Real	Input	false	1
Ti3	Input 3 temperature, K	Real	Input	false	273
Si3	Input 3 cutset, m2	Real	Input	false	0.2
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
To	Output temperature, K	Real	Output	false	273
So	Output cutset, m2	Real	Input	false	0.2
lo	Output length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
Ct	Heat capacity of the environment	Real	Input	false	20
Riz	Heat resistance of the isolation	Real	Input	false	20
Fwind	Air speed	Real	Input	false	1
Twind	Air temperature, К	Real	Input	false	273
f_frq	Calculation frequency, Hz	Real	Input	true	100

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi1, Pi1, 293, Si1, EVAL_REAL, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi2, Pi2, 293, Si2, EVAL_REAL, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi3, Pi3, 293, Si3, EVAL_REAL, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);
Po = max(0, min(100,Po+0.27*(Fi1+Fi2+Fi3-Fo)/(Q0*Kpr*So*lo*f_frq)));
To = max(0, To+(Fi1*(Ti1-To)+Fi2*(Ti2-To)+Fi3*(Ti3-To)+(Fwind+1)*(Twind-To)/Riz)/(Ct*So*lo*Q0*f_frq));

2.18 Pipe 1->2 (pipe1_2)

Model of the pipe by the scheme "1 -> 2".

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Fo1	Output 1 flow, ton/h	Real	Input	false	0
Po1	Output 1 pressure, at	Real	Output	false	1
So1	Output 1 cutset, m2	Real	Input	false	0.2
lo1	Output 1 length, m	Real	Input	false	10
Fo2	Output 2 flow, ton/h	Real	Input	false	0
Po2	Output 2 pressure, at	Real	Output	false	1
So2	Output 2 cutset, m2	Real	Input	false	0.2
lo2	Output 2 length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
f_frq	Calculation frequency, Hz	Real	Input	true	100
F1tmp	Temporary flow 1	Real	Output	true	0
F2tmp	Temporary flow 2	Real	Output	true	0
Pot1	Temporary pressure 1	Real	Output	true	1
Pot2	Temporary pressure 2	Real	Output	true	1

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(F1tmp, Pi, 293, So1, Fo1, Po1, 293, So1, lo1, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(F2tmp, Pi, 293, So2, Fo2, Po2, 293, So2, lo2, Q0, Kpr, 0.01, f_frq);
Fi = F1tmp + F2tmp;

2.19 Pipe 1->3 (pipe1_3)

Model of the pipe by the scheme "1 -> 3".

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Fo1	Output 1 flow, ton/h	Real	Input	false	0
Po1	Output 1 pressure, at	Real	Output	false	1
So1	Output 1 cutset, m2	Real	Input	false	0.2
lo1	Output 1 length, m	Real	Input	false	10
Fo2	Output 2 flow, ton/h	Real	Input	false	0
Po2	Output 2 pressure, at	Real	Output	false	1
So2	Output 2 cutset, m2	Real	Input	false	0.2
lo2	Output 2 length, m	Real	Input	false	10
Fo3	Output 3 flow, ton/h	Real	Input	false	0
Po3	Output 3 pressure, at	Real	Output	false	1
So3	Output 3 cutset, m2	Real	Input	false	0.2
lo3	Output 3 length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
f_frq	Calculation frequency, Hz	Real	Input	true	100
F1tmp	Temporary flow 1	Real	Output	true	0
F2tmp	Temporary flow 2	Real	Output	true	0
F3tmp	Temporary flow 3	Real	Output	true	0
Pot1	Temporary pressure 1	Real	Output	true	1
Pot2	Temporary pressure 2	Real	Output	true	1
Pot3	Temporary pressure 3	Real	Output	true	1

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(F1tmp, Pi, 293, So1, Fo1, Po1, 293, So1, lo1, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(F2tmp, Pi, 293, So2, Fo2, Po2, 293, So2, lo2, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(F3tmp, Pi, 293, So3, Fo3, Po3, 293, So3, lo3, Q0, Kpr, 0.01, f_frq);
Fi = F1tmp + F2tmp + F3tmp;

2.20 Pipe 1->4 (pipe1_4)

Model of the pipe by the scheme "1 -> 4".

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Fo1	Output 1 flow, ton/h	Real	Input	false	0
Po1	Output 1 pressure, at	Real	Output	false	1
So1	Output 1 cutset, m2	Real	Input	false	0.2
lo1	Output 1 length, m	Real	Input	false	10
Fo2	Output 2 flow, ton/h	Real	Input	false	0
Po2	Output 2 pressure, at	Real	Output	false	1
So2	Output 2 cutset, m2	Real	Input	false	0.2
lo2	Output 2 length, m	Real	Input	false	10
Fo3	Output 3 flow, ton/h	Real	Input	false	0
Po3	Output 3 pressure, at	Real	Output	false	1
So3	Output 3 cutset, m2	Real	Input	false	0.2
lo3	Output 3 length, m	Real	Input	false	10
Fo4	Output 4 flow, ton/h	Real	Input	false	0
Po4	Output 4 pressure, at	Real	Output	false	1
So4	Output 4 cutset, m2	Real	Input	false	0.2
lo4	Output 4 length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
f_frq	Calculation frequency, Hz	Real	Input	true	100
F1tmp	Temporary flow 1	Real	Output	true	0
F2tmp	Temporary flow 2	Real	Output	true	0
F3tmp	Temporary flow 3	Real	Output	true	0
F4tmp	Temporary flow 4	Real	Output	true	0
Pot1	Temporary pressure 1	Real	Output	true	1
Pot2	Temporary pressure 2	Real	Output	true	1
Pot3	Temporary pressure 3	Real	Output	true	1
Pot4	Temporary pressure 4	Real	Output	true	1

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(F1tmp, Pi, 293, So1, Fo1, Po1, 293, So1, lo1, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(F2tmp, Pi, 293, So2, Fo2, Po2, 293, So2, lo2, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(F3tmp, Pi, 293, So3, Fo3, Po3, 293, So3, lo3, Q0, Kpr, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(F4tmp, Pi, 293, So4, Fo4, Po4, 293, So4, lo4, Q0, Kpr, 0.01, f_frq);
Fi = F1tmp + F2tmp + F3tmp + F4tmp;

2.21 Valve: processing mechanism (valveMech)

Model of the valve processing mechanism. Includes the going and estrangement time.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
pos	Position, %	Real	Output	false	0
pos_sensor	Position by the sensor, %	Real	Output	false	0
com	Command	Real	Input	false	0
st_open	State "Opened"	Boolean	Output	false	0
st_close	State "Closed"	Boolean	Output	false	1
t_full	Going time, seconds	Real	Input	false	3
t_up	Estrangement time, seconds	Real	Input	false	1
t_sensor	Sensor lag time, seconds	Real	Input	false	1
f_frq	Calculation frequency, Hz	Real	Input	true	100
tmp_up	Estrangement count	Real	Output	false	0
lst_com	Last command	Real	Output	false	0

Program

if((pos >= 99 && com >= 99) || (pos <= 1 && com <= 1)) { 
  tmp_up = t_up;
  if(pos >= 99) { pos = 100; st_open = true; }
  else { pos = 0; st_close = true; }
}
else if(tmp_up > 0) tmp_up -= 1/f_frq;
else {
  st_open = st_close = false;
  lst_com += (com-lst_com)/(0.5*t_full*f_frq);
  pos += (lst_com-pos)/(0.5*t_full*f_frq);
}
pos_sensor += (pos-pos_sensor)/(t_sensor*f_frq);

2.22 Diaphragm (diaphragm)

Diaphragm model.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi	Input flow, ton/h	Real	Output	false	0
Pi	Input pressure, at	Real	Input	false	1
Fo	Output flow, ton/h	Real	Input	false	0
Po	Output pressure, at	Real	Output	false	1
dP	Pressure differential, kPa	Real	Output	false	0
Sdf	Diaphragm cutset, m2	Real	Input	false	0.1
So	Output pipe cutset, m2	Real	Input	false	0.2
lo	Output pipe length, m	Real	Input	false	10
Q0	Norm density of the environment, kg/m3	Real	Input	false	1
Kpr	Coefficient of the compressibility [0...1]	Real	Input	false	0.95
f_frq	Calculation frequency, Hz	Real	Input	true	100

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi, Pi, 293, Sdf, Fo, Po, 293, So, lo, Q0, Kpr, 0.01, f_frq);
dP -= (dP-100*(Pi-Po))/f_frq;

2.23 Heat exchanger (heatExch)

Model of the heat exchanger, calculating the heat exchange of the two streams.

Parameters

Identifier	Parameter	Type	Mode	Hidden	Default
Fi1	Input 1 flow, ton/h	Real	Input	false	20
Pi1	Input 1 pressure, at	Real	Input	false	1
Ti1	Input 1 temperature, K	Real	Input	false	20
Si1	Input 1 cutset, m2	Real	Input	false	1
li1	Input 1 length, m	Real	Input	false	10
Q0i1	Input 1 norm density, kg/m3	Real	Input	false	1
Kpr1	Input 1 coefficient of the compressibility [0...1]	Real	Input	false	0.9
Ci1	Input 1 heat capacity	Real	Input	false	1
Fi2	Input 2 flow, ton/h	Real	Input	false	20
Pi2	Input 2 pressure, at	Real	Input	false	1
Ti2	Input 2 temperature, K	Real	Input	false	40
Si2	Input 2 cutset, m2	Real	Input	false	1
li2	Input 2 length, m	Real	Input	false	10
Q0i2	Input 2 norm density, kg/m3	Real	Input	false	1
Kpr2	Input 2 coefficient of the compressibility [0...1]	Real	Input	false	0.9
Ci2	Input 2 heat capacity	Real	Input	false	1
ki	Heat transfer coefficient	Real	Input	false	0.9
Fo1	Output 1 flow, ton/h	Real	Input	false	0
Po1	Output 1 pressure, at	Real	Output	false	1
To1	Output 1 temperature, K	Real	Output	false	273
So1	Output 1 cutset, m2	Real	Output	false	1
lo1	Output 1 length, m	Real	Output	false	10
Fo2	Output 2 flow, ton/h	Real	Input	false	0
Po2	Output 2 pressure, at	Real	Output	false	1
To2	Output 2 temperature, K	Real	Output	false	273
So2	Output 2 cutset, m2	Real	Output	false	1
lo2	Output 2 length, m	Real	Output	false	10
f_frq	Calculation frequency, Hz	Real	Input	false	200

Program

DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi1, Pi1, Ti1, Si1, Fo1, Po1, 293, So1, lo1, Q0i1, Kpr1, 0.01, f_frq);
DAQ.JavaLikeCalc.lib_techApp.pipeBase(Fi2, Pi2, Ti2, Si2, Fo2, Po2, 293, So2, lo2, Q0i2, Kpr2, 0.01, f_frq);

To1 = max(0, min(1e4,(Fi1*Ti1*Ci1+ki*Fi2*Ti2*Ci2)/(Fi1*Ci1+ki*Fi2*Ci2)));
To2 = max(0, min(1e4,(ki*Fi1*Ti1*Ci1+Fi2*Ti2*Ci2)/(ki*Fi1*Ci1+Fi2*Ci2)));

Libs/Technological apparatuses

Contents

1 Conception

2 Structure of the library

2.1 Lag (lag)

2.2 Noise: 2 harmonic + rand (noise)

2.3 Ball crane (ballCrane)

2.4 Separator (separator)

2.5 Valve (valve)

2.6 Lag: clean (lagClean)

2.7 Boiler: barrel (boilerBarrel)

2.8 Boiler: burner (boilerBurner)

2.9 Network: load (net)

2.10 Source: pressure (src_press)

2.11 Air cooler (cooler)

2.12 Gas compressor (compressor)

2.13 Source: flow (src_flow)

2.14 Pipe-base (pipeBase)

2.15 Pipe 1->1 (pipe1_1)

2.16 Pipe 2->1 (pipe2_1)

2.17 Pipe 3->1 (pipe3_1)

2.18 Pipe 1->2 (pipe1_2)

2.19 Pipe 1->3 (pipe1_3)

2.20 Pipe 1->4 (pipe1_4)

2.21 Valve: processing mechanism (valveMech)

2.22 Diaphragm (diaphragm)

2.23 Heat exchanger (heatExch)