EQUATIONS IN REACTION ENGINEERING by

EQUATIONS IN REACTION ENGINEERING by https://padlet.com/mohdrazealy/5nwoqi9kzrcx Haii students. I am in the midst of marking your TEST 2. Pheww it such a challenging task. I have figured out the problem that you face during answering any question which is the selection of proper equation according to condition. So as per requirement by UniKL MICET for your final revision before this upcoming final exam in July, it would be nice if every single of you can provide me one equation (with condition) that you have learned throughout this subject. Grab this chance to revise back your knowledge before final exam. Together we react together we success. Salam Aidilfitri. en-us 2017-06-19 01:13:28 UTC 2023-01-28 13:05:43 UTC hello@padlet.com https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176796892 2017-06-19 02:02:37 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176796892 NON-ISOTHERMAL REACTOR DESIGN https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176801073 AMEERA NURUL SARAH BINTI AZMAN

55214115287

Energy balance equation:

]]> 2017-06-19 02:44:37 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176801073 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176859699 2017-06-19 13:18:18 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176859699 DESIGN EQUATION FOR CSTR REACTOR https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176886529 NUR SYAHIRAH BINTI JAAPAR
55214115028
DIFFERENTIAL METHOD FOR BATCH DATA

ln(-dCA/dt) = ln k + ∂ ln C_A ]]> 2017-06-19 16:49:45 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176886529 MUHAMMAD HAFIZ IZUDDIN BIN ZULKIFLI55211115322ENERGY BALANCE FOR ADIABATIC SYSTEM https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176920195 2017-06-20 00:44:58 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176920195 Mohammad Haiqal bin Harun (55214115246) https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176939835 equation for conversion x:
x=Cao - Ca / Cao]]> 2017-06-20 05:54:06 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176939835 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176949242 This is the equation for liquid phase.

For Batch Reactor

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

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

For PFR and CSTR

For Inlet : (A)
C_AO is the initial concentration
F_AO is the inlet molar flow rate
v_o is the initial volumetric flow rate

For Outlet : (B)
C_A is the outlet concentration
F_A is the outlet molar flow rate
v is the outlet volumetric flow rate

Prepared by : Norsuzieanah Halil (55214115354)

]]> 2017-06-20 07:44:49 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176949242 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176954669 2017-06-20 08:42:22 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176954669 abdulrahman_mohdsaufian https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176959247 ABDUL RAHMAN BIN MOHD SAUFIAN
55211115321

]]> 2017-06-20 09:22:49 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/176959247 NUR DAYANA BINTI MUHAMAD RAFFIN 55220115334 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177013536 2017-06-20 17:48:32 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177013536 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177044313 Noraini Saini 55214115102 L03T1

Equation to be used if the question asks for half-life method.
This formula is usually given. ]]> 2017-06-21 01:12:31 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177044313 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177096493 2017-06-21 12:55:13 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177096493 METHODS OF HALF-LIVES https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177158648 NUR AWANIS BINTI MOHD KHAIRAN
55214115131]]> 2017-06-22 02:41:16 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177158648 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177159422 2017-06-22 02:50:01 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177159422 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177206592 2017-06-22 13:37:51 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177206592 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177215320 2017-06-22 14:46:54 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177215320 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177219048 2017-06-22 15:28:02 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177219048 TITLE: DESIGN EQUATIONS FOR BATCH SYSTEM https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177235004 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 F_A0=F_A=0

As shown in the general mole balance below with the condition as mentioned previously, the mole balance will eventually becomes r_AV=dN_A/dt .]]> 2017-06-22 19:00:12 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177235004 First Order Reaction in Isothermal React using Batch Reactor (Liquid Phase) https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177734762 2017-06-29 12:05:47 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177734762 Non-isothermal reactor design sharifahjamilah96 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177768296 Name: Sharifah Nur Jamilah bt Syed Walid
ID no: 55211115357
L03
The overall equation for energy balance is
q]]> 2017-06-29 19:45:18 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177768296 Noor Khairina Binti Faisal 55211115110 L03-T3 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177776874 2017-06-29 22:51:35 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177776874 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177782813 2017-06-30 00:50:10 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177782813 Equations in Reaction Eng halidasaad https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177802551 HALIDA BINTI SAAD (55214115363)
L03]]> 2017-06-30 08:51:54 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177802551 Design equation for each Reactor hajifauzisalleh https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177865917 FATIN AQILAH BINTI FAUZI
55211115053
L03

1) Batch Reactor

2) CSTR

3) PFR

]]> 2017-07-01 17:05:43 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177865917 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177913161 2017-07-03 01:55:48 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177913161 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177990402 2017-07-04 02:12:36 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/177990402 ANOTHER WAY TO DISTINGUISH DIFFERENT REACTOR EQUATIONS https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/178125234 2017-07-05 17:19:12 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/178125234 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/178214012 Kalsum binti Ismail
55211115361]]> 2017-07-06 18:52:35 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/178214012 https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/178255472 2017-07-07 10:26:39 UTC https://padlet.com/mohdrazealy/5nwoqi9kzrcx/wish/178255472