This experiment is about Bernoullis theorem. The objective of this experiment is to
demonstrate the Bernoullis theorem. This experiment use the Bernoullis Theorem
Demonstration Apparatus. The apparatus contains of many part which are venture mete
Mass of stream: 5640
x 1.25 = 7050
Mole flowrate of propane : 0.00
x 1.25 = 0.00
Mole flowrate of propylene: 0.00
x 1.25 = 0.00
Mole flowrate of i-butane:
The company's management is confident that The Company can
achieve its aggressive sales forecasts, generating total sales of
approximately RM (insert amount) and RM (insert amount) in years,
2016 and 2017 respectively. In addition, The Companys
GLYCOL DEHYDRATION PLANT
Figure 1 : Typical Glycol Dehydration Process And Equipment .
The major pieces of component in a glycol dehydration plant are as follows:
Each of these items of process equipment is dis
Change: a singular word that holds so many possibilities yet whether it is
for the better or worse is a whole different story. When we talk about the
economy in this rapid leaping society - the array of influential matters that root
Mining & Quarrying
STATISTIC OF OCCUPATIONAL ACCIDENT BY 3 DIFFERENT SECTORS THAT
LEADS TO DEATH.
(MANUFACTURING, MINING & QUARRYING AND TRANSPORT)
As shown from t
INTRODUCTION TO MALAYSIAN ECONOMIC
Malaysia is a highly open, upper-middle income economy. Malaysia was one of 13
countries identified by the Commission on Growth and Development in its 2008
Growth Report to have recorded average growth of more than 7 per
1. Put component
2. Choose peng-robinson
3. Click simulation - main flowsheet
4. Choose appropriate equipments at model palette
5. Click material, and connect all streams with equipment using red arrow
6. TerhaSILLAH dya
7. Rename the equipments and strea
1. What is the molar flow before entering DC1 and DC2?
1350 kmol/hr for both DC.
2. How to reduce pressure in DC2?
by using valve
3. What is the temperature at the bottom of DC1 and DC2?
154.3C for bottom DC1 and 101.8C for bott