ForK Tutorial ForK Tutorial Exercise 2 Creating new simulation project to estimate explosion hazard Aim: Determination of critical conditions of thermal explosion for a storage tank (drum) containing 80% solution of cumene hydroperoxide in cumene (well stirred assumption) Drum:Cylinder with R=0.2 m, H=0.8 m, V=0.1 m 3 (100 l), S=1.26 m 2 ; void volume V V =0.01 m 3 (10 l), phi=1.01 (contribution of mass heat capacity of the container is small) Product properties: =0.8 g/cm 3. Cp=2 J/g/K, sample mass = 80 kg, initial temperature – 20 o C, phi=1.01 Heat exchange:General mode, U=10 W/ m 2 /K; T env =50 o C Aim: Determination of critical conditions of thermal explosion for a storage tank (drum) containing 80% solution of cumene hydroperoxide in cumene (well stirred assumption) Drum:Cylinder with R=0.2 m, H=0.8 m, V=0.1 m 3 (100 l), S=1.26 m 2 ; void volume V V =0.01 m 3 (10 l), phi=1.01 (contribution of mass heat capacity of the container is small) Product properties: =0.8 g/cm 3. Cp=2 J/g/K, sample mass = 80 kg, initial temperature – 20 o C, phi=1.01 Heat exchange:General mode, U=10 W/ m 2 /K; T env =50 o C Click here to continue Run Scoring
ForK Tutorial ForK Tutorial Exercise 2 Creating new simulation project to estimate explosion hazard Kinetics: Complex reaction with 2 stages in parallel: (1) A B – N-order initiation reaction; stage rate – r 1 (2) A+B 2B – autocatalytic stage; stage rate - r 2 Math model:(1): lnK 01 =20.4; n 11 =2; E 1 =102 kJ/mol; Q 1 =800 J/g (2) lnK 02 =23; n 21 =4; n 22 =3; E 2 =96 kJ/mol; Q 2 =1800 J/g Kinetics: Complex reaction with 2 stages in parallel: (1) A B – N-order initiation reaction; stage rate – r 1 (2) A+B 2B – autocatalytic stage; stage rate - r 2 Math model:(1): lnK 01 =20.4; n 11 =2; E 1 =102 kJ/mol; Q 1 =800 J/g (2) lnK 02 =23; n 21 =4; n 22 =3; E 2 =96 kJ/mol; Q 2 =1800 J/g Click here to continue
ForK Tutorial Select Simulation mode
ForK Tutorial Preliminary adjustment: setting appropriate units
ForK Tutorial
Defining the drum model Step 1. Defining general data Data that are to be assigned: 1. Response to be simulated (heat production) 2. Mass of a reagent and initial T 3. Void volume and pad gas data (in our case Pgo and Tgo are optional) 4. Mass specific heat and phi-factor
ForK Tutorial General data are ready
ForK Tutorial Defining the drum model Step 2. Defining Heat exchange mode Data that are to be assigned: 1. Heat exchange mode - General 2. Неat exchange Surface 3. Неat transfer coefficient 4. Environment temperature (on the “Env. Temperqature” tab) 1.26
ForK Tutorial
ForK Tutorial Defining the drum model Step 3. Defining kinetic model Data that should be assigned: 1. Model structure 2. “Elementary” models for stages 3. Kinetic parameters Creating model of two stages in parallel (the model of full autocatalysis) Stage 1 – of N-order type Stage 2 - Proto
ForK Tutorial Data that should be assigned: 1. Model structure 2. “Elementary” models for stages 3. Kinetic parameters 1. Creating model of two stages in parallel (the model of full autocatalysis) Stage 1 – of N-order type Stage 2 - Proto
ForK Tutorial Data that should be assigned: 1. Model structure 2. “Elementary” models for stages 3. Kinetic parameters 1. Creating model of two stages in parallel (the model of full autocatalysis) Stage 1 – of N-order type Stage 2 - Proto
ForK Tutorial Data that should be assigned: 1. Model structure 2. “Elementary” models for stages 3. Kinetic parameters 1. Creating model of two stages in parallel (the model of full autocatalysis) Stage 1 – of N-order type Stage 2 - Proto
ForK Tutorial Data that should be assigned: 1. Model structure 2. “Elementary” models for stages 3. Kinetic parameters Model created with the kinetic parameters for the second stage defined
ForK Tutorial Data that should be assigned: 1. Model structure 2. “Elementary” models for stages 3. Kinetic parameters Kinetic parameters for the first stage have been defined
ForK Tutorial Evaluating critical parameters of thermal explosion by using the “Effect of controls” option 1. Adjusting time interval for simulation
ForK Tutorial Note that max temperature rise (overheat) at initial environment T=60 C is very small. Next step is to elevate env. temperature
ForK Tutorial At Tenv=75 C overheat becomes much bigger. Continue to elevate Tenv till reaching explosion
ForK Tutorial There is pronounced thermal explosion a t Tenv~77.5 C. More precise value can be obtained by varying Tenv with smaller step
ForK Tutorial Simulation of thermal explosion in the drum
ForK Tutorial
Add simulated responses to be saved within the project
ForK Tutorial
Now the complete project can be saved into a data volume for further use The 2 st Exercise is over. Press [Esc] to close presentation. If you have ForK installed we recommend to repeat this exercise by yourself.