Hysys (Pressure drop calculation in a pipe)

Water is flowing in a 10-m horizontal smooth pipe at 4 m/s and 25°C. The pipe is Schedule 40, 1 in nominal diameter. Water inlet pressure is 2atm. Calculate pressure drop.

Water properties:

Density 1000 kg/m3

Viscosity =0.001 kg/m s.

simulation

 

Crude Oil Simulation 2

>called Water, at 15°C and a mass flow rate of 21600 kg/h cooler 

>Delta P of 50 kPa. temperature of 65°C Temperature 180 C,

 >Pressure 200 kPa and Std Ideal Liq Vol Flow of 175 m3/h

Min Approach = 30°C heater 

 >Delta P 375 kPa To Preflash Temperature 175°C %3D heater 2 

>Delta P 250 kPa Feed Temperature 400°C.

part3

part4

part5

link part1&2

Hysys simulation.Amna Elhelali : Croud Oil Simulation (hysys-program-simulation- amnaelhelali.blogspot.com)

 

Croud Oil Simulation

>called Water, at 15°C and a mass flow rate of 21600 kg/h cooler 

>Delta P of 50 kPa. temperature of 65°C Temperature 180 C,

 >Pressure 200 kPa and Std Ideal Liq Vol Flow of 175 m3/h

Min Approach = 30°C heater 

 >Delta P 375 kPa To Preflash Temperature 175°C %3D heater 2 

>Delta P 250 kPa Feed Temperature 400°C

very important simulation 

part1

part2

link part3&5

Hysys simulation.Amna Elhelali : Crude Oil Simulation 2 (hysys-program-simulation-amnaelhelali.blogspot.com)

 

Absorbed Statement / Hysys

                                                                                                              This lecture introduces the use of Aspen HYSYS

 to model continuous gas adsorption a process in a packed

 column The only unit process in the absorber is the tray section and

 the only streams are the upper steam and the lower liquid products .

                        

PROBLEM STATEMENT

CO2 is absorbed into propylene carbonate

in a packed column. The inlet gas stream

is 20 mol% CO2 and 80 mol% methane

The gas stream flows at a rate of 2 m³/s

and the column operates at 60°C and

60.1 atm. The inlet solvent flow is 2000

kmol/h. Determine the concentration of

CO₂ (mol%) in the exit gas stream, the

column height(m) and the column

diameter(m)

 

Crude Oil Assay >

With the aid of the oil characterization option in Hysys, model a crude oil stream with.

 

following data:

 

The crude oil is the feedstock to a refining process

Fluid package: Peng Robinson 

Standard Density = 29 API_60

? how could use hysys to solve the problem  

If you have Oil Manager checks as part of a HYSYS case, you can easily convert them to the updated HYSYS Petroleum Refining format and use them in cases.

1. In the Properties environment, in the navigation pane, select Petroleum

Assays.

2. On the Home ribbon tab | Oil group, select Convert to Refining Assay.

3. On the Oil to Assay Manager Conversion dialog box, select on of the

following options for the Fluid Package:

> use existing

> use resays default 

see simulation

 

Petroleum Assay

A crude oil assay

   

is the chemical evaluation of crude oil feed   stocks by

 

petroleum testing laboratories. Each crude oil type has unique.

  

molecular and chemical characteristics. no two crude oil types

 

are identical and there are crucial differences in crude oil quality.

 

the results of crude oil ssat testing provide extensive detailed

 

hydrocarbon analysis data for refiners ,oil traders and producers

 

 assay data help refineries determine if a crude oil feedstock is

 

comp a particuular  petroleum refinery or the crude oil could

 

.cause yield   

 

Fluid Package in Hysys

Physical Properties: Fluid Package

.Property Package Selection -      

.Plenty of packages -      

. Each has its specification-       

.Typically, you will know which Package to Apply-       

Recommended → Method Assistant OR → USE HELP BUTTON SERACH: Aspen HYSYS Property Package Selection Assistant

 .Choose the Method Assistant-

.Actually, it pop-ups a Help Site-

.Then, choose either Help button or Method assistant-

 could see mare at simulation  

 

Distillation column design in violin production process

Distillation column design in violin production process

  (isopropyl benzene) is produced by the reaction of propylene 

with benzene

 

 .Cumin production reactions from benzene

C3H6+ C6H6=====> C9H12

:Components

Feed: Benzene (C6H6) Flowrate 102.08 kgmole/h

Propylene (C3H6 - propene) 2.90 kgmole/h

Propane 2.80 kgmole/h

Cumene (C,H12) 91.62 kgmole/h

p-diisopropyl benzene (C12H18, 14-iP-BZ) 2.80 kgmole/h

:Temperature

95 C

:Pressure

 1.75 bar

:Fluid Packagee

PRSV

see the simulation

NGL Fractiontion

Feed part1

Feed Characteristics Pressure (kPa) 5000 Temperature 25 (°C) Molar Flow (kgmol/hr) 2988 Feed Composition Nitrogen 1.49E-02 CO2 2.00E-03 Methane 0.9122 Ethane 4.96E-02 Propane 1.48E-02 i-Butane  2.60E-03 n-butane 2.00E-03 i-pentane 1.00E-03 6.00E-04

 n-pentane 3.00E-04 n-hexane.

SIMULATION DATA

Property Package: Peng-Robinson.

COOLER SPECIFICATIONS

COOLER 100 OUTLET

TEMPERATURE -62 (°C)

 dp (kPa)20

COOLER 101

OUTLET TEMPERATURE(°C)25

dp (kPa) 15

part 2 link

https://hysys-program.blogspot.com/2023/02/ngl-fractionation-2.html 

 

NGL Fractionation 2

Feed part2

Feed Characteristics Pressure (kPa) 5000 Temperature 25 (°C) Molar Flow (kgmol/hr) 2988 Feed Composition Nitrogen 1.49E-02 CO2 2.00E-03 Methane 0.9122 Ethane 4.96E-02 Propane 1.48E-02 i-Butane  2.60E-03 n-butane 2.00E-03 i-pentane 1.00E-03 6.00E-04

 n-pentane 3.00E-04 n-hexane.

DISTILLATION COLUMN SPECS

CONDENSER

FULL REFLUX

5 No of STAGES

COLUMN DUTY 0.001kJ/hr

200 psia (liquid

Reid Vapor Pressure phase)

CONDENSER

PRESSURE

2766 (kPa)

REBOILER

PRESSURE

2800 (kPa)

VALVE SPEC

dp 2165 (kPa)

this simulation part 2 for that is link 

https://hysys-program.blogspot.com/2023/02/ngl-fractiontion.html

 

Crude Oil Pre Heat simulation

 

Problem Statement Cont.

A crude stream at 15°C, 1000 kPa and flowrate of 6x105 kg/hr is

 mixed with a stream of water at 15°C, 1000 kPa and flowrate of

 21600 kg/hr using a Mixer, the outlet from the mixer is then

heated to 65°C through a Heater (Ap=50 kPa),the heater outlet is

 feed to the tube side of a Shell & Tube Heat Exchanger, where it's

 heated using a Shell inlet stream having the same composition as the

 crude feed stream and enters the shell of the heat exchanger at

 180°C, 200 kPa and flowrate of 175m³/hr.

                                                           

The liquid product from the separator is then heated to 400°C inside a Heater (Pressure drop-250 kPa) before entering the Atmospheric Column.

Heat Exchanger Specification:

Use Simple weighted model

- The Shell side outlet Temperature is 95°C

Calculate:

-The vapor fraction of the product stream before

entering the atmospheric column.

Min Approach; This is the minimum temperature difference between

 the hot and the cold stream. The vapor molar flow rate from the 

 Pre-Flash.

The pressure drops for the Tube and Shell sides, will be 35 kPa and 5

 kPa, respectively. The tube outlet from the Heat Exchanger is

then sent to a desalter which is simply modeled as Three Phase

 Separator where desalted water, oil and gas is separated.

The oil stream (light liquid) from the desalter is then heated to 175°C

 through a Heater (Pressure drop=375 kPa) and then sent to a Pre

 flash (Separator) to reduce the light components in the feed.

See the part1 &2 simulation

part1

part2

The petroleum characterization

Introduction

The petroleum characterization method in HYSYS will convert laboratory analyses of condensates, crude oils, petroleum cuts and

coal-tar liquids into a series of discrete hypothetical components

These petroleum hypo components provide the basis for the property package to predict the remaining thermodynamic and

.transport properties necessary for fluid modelling 

Assay

The assay contains all of the petroleum laboratory data, boiling

point curves, light ends, property curves and bulk properties. 

HYSYS uses the supplied Assay data to generate internal TBP, molecular weight, density and viscosity curves, referred to as Working Curves.

Problem Statement 

With the aid of the Oil Characterization option in HYSYS,

.model a crude oil with the following data

• The crude is the feed stock to oil

refining process

- Fluid Package: Peng Robinson

- standard Density = 29 API_60

Assay
 

 

Petroleum characterization

 petroleum characterization method in hysys conversion of laboratory assay analyses of condensate, crude oils, petroleum cuttings and coal-tar liquids into series of discrete hypothetical   components.  These petroleum components provide the basis for a property package to predict the remaining  thermodynamics and transport properties necessary for fluid modeling.

Aspen HYSYS produces a complete set  of physical and critical properties for a petroleum hypo component with minimal information.  However, the more information you can supply  about the fluid, the more accurate these properties will be, and the better 

the Aspen HYSYS  predict the fluid  actual behavior

  See the simulation 

 

CSTR (Adiabatic vs Isothermal)

Workshop

      CSTR (Adiabatic vs Isothermal).

              A chemical reaction is going to be considered:

                  C3H6O + H2O→C3H6O2

                   Propylene Oxide + Water → Propylene glycol

                   Adiabatic operation:

                     - P = 3 bar

                      -V = 1000 L

                       

                     - FEED

                                 P = 3 bar, T = 24°C

                     8.7 C3H60, 300 H2O (kmol/h)

                     - Kinetic Data

                     - K = 9.2E22

                     - Ea= 1.56E8 J/kmol

                   just start see the ex: below learning more for CSTR                             Adiabatic. 

 

what is HYSYS program?

Hysys is chemical process simulation used to mathematically model chemical processes, from  unit operation to full chemical plant  and  refineries  HYSYS is able to perform many of the core calculations of  chemical engineering, including those concerned with mass balance , energy balance,, heat transfer , mass  transfer , and pressure drop . HYSYS is used extensively in industry and academia for steady-state and dynamic simulation, process design, performance modelling.