# data[].attributes.body
Kalsum binti Ismail
55211115361

# data[].attributes.headline
ANOTHER WAY TO DISTINGUISH DIFFERENT REACTOR EQUATIONS

# data[].attributes.subject
ANOTHER WAY TO DISTINGUISH DIFFERENT REACTOR EQUATIONS

# data[].attributes.body
FATIN AQILAH BINTI FAUZI
55211115053
L03

1) Batch Reactor
2) CSTR
3) PFR

# data[].attributes.body
HALIDA BINTI SAAD (55214115363)
L03

# data[].attributes.headline
Noor Khairina Binti Faisal 55211115110 L03-T3

# data[].attributes.subject
Noor Khairina Binti Faisal 55211115110 L03-T3

# data[].attributes.body
Name: Sharifah Nur Jamilah bt Syed Walid
ID no: 55211115357
L03
The overall equation for energy balance is
q

# data[].attributes.headline
First Order Reaction in Isothermal React using Batch Reactor (Liquid Phase)

# data[].attributes.subject
First Order Reaction in Isothermal React using Batch Reactor (Liquid Phase)

# data[].attributes.headline
TITLE: DESIGN EQUATIONS FOR BATCH SYSTEM

# data[].attributes.subject
TITLE: DESIGN EQUATIONS FOR BATCH SYSTEM

# data[].attributes.body
NAME : NUR ARIFFA BINTI SUHAIRI
ID : 55211115356
SECTION : L03-P3

In both liquid and gas system used in batch reactor, the mode of operation is time-varying with a constant volume.

Since there is no inflow and outflow during the batch system, there is also no presence of spatial variations in reaction rate. With such condition, the calculation basis for batch system is related as FA0=FA=0

As shown in the general mole balance below with the condition as mentioned previously, the mole balance will eventually becomes rAV=dNA/dt .

# data[].attributes.attachment_link.title
RATE CONSTANTS AND THE ARRHENIUS EQUATION by NadiaRiyad

# data[].attributes.body
NUR AWANIS BINTI MOHD KHAIRAN
55214115131

# data[].attributes.body
Noraini Saini 55214115102 L03T1

Equation to be used if the question asks for half-life method.
This formula is usually given.

# data[].attributes.headline
NUR DAYANA BINTI MUHAMAD RAFFIN  55220115334

# data[].attributes.subject
NUR DAYANA BINTI MUHAMAD RAFFIN  55220115334

# data[].attributes.body
ABDUL RAHMAN BIN MOHD SAUFIAN
55211115321

# data[].attributes.body
This is the equation for liquid phase.

For Batch Reactor

For Inlet : (A)
CAO is the initial concentration
NAO is the inlet number of moles
V is the reactor volume

For Outlet : (B)
CA is the outlet concentration
NA is the outlet number of moles
V is the reactor volume

For PFR and CSTR

For Inlet : (A)
CAO is the initial concentration
FAO is the inlet molar flow rate
vo is the initial volumetric flow rate

For Outlet : (B)
CA is the outlet concentration
FA is the outlet molar flow rate
v is the outlet volumetric flow rate

Prepared by : Norsuzieanah Halil (55214115354)

# data[].attributes.body
equation for conversion x:
x=Cao - Ca / Cao

# data[].attributes.headline
MUHAMMAD HAFIZ IZUDDIN BIN ZULKIFLI55211115322ENERGY BALANCE FOR ADIABATIC SYSTEM

# data[].attributes.subject
MUHAMMAD HAFIZ IZUDDIN BIN ZULKIFLI55211115322ENERGY BALANCE FOR ADIABATIC SYSTEM

# data[].attributes.body
NUR SYAHIRAH BINTI JAAPAR
55214115028
DIFFERENTIAL METHOD FOR BATCH DATA

ln(-dCA/dt)     =     ln k    +    ∂ ln C_A

# data[].attributes.body
AMEERA NURUL SARAH BINTI AZMAN

55214115287

Energy balance equation: