Homework 1
Dikumpulkan pada:
CE-1: 18 Februari 2020
CE-2: 20 Februari 2020
Sebelum Perkuliahan dimulai
1. The following data were obtained at o
70 C for the equilibrium adsorption of n-hexane
on silica gel particles
Partial pressure of C6H14 adsorbed, g
C6H14 in gas, atm moles/(g gel)
0.002 10.5 x 10-5
0.004 16.0 x 10-5
0.008 27.2 x 10-5
0.0113 34.6 x 10-5
0.0156 43.0 x 10-5
0.0206 47.3 x 10-5
a) Determine weather the adsorption process follow molecular or dissociative
adsorption process
b) Determine the constants value by least square
2. A. Peloso et al. [Can. J. Chem. Eng. 57 (1979) 159] investigated the kinetics of the
following reaction over a CuO/Cr2O3/SiO2 catalyst at temperatures of 225 – 285 C:o
𝑃𝐴𝑑 𝑃𝐷𝐻
𝑘 𝑃𝐸𝑡 −
𝐾𝑒
A possible rate law to describe the data is: 𝑟= 2
1 + 𝐾𝐸𝑡 𝑃𝐸𝑡 + 𝐾𝐴𝑑 𝑃𝐴𝑑
Write a reaction mechanism that would give this rate expression.
3. Derive the rate law for below mechanism:
4. Derive the rate law for below mechanism:
5. The dehydration butanol of alumina is carried out over a silica-alumina catalyst at
680 K.
𝑘𝑃𝐵𝑢
The rate law is: −𝑟𝐵𝑢 ′ = 2
1 + 𝐾𝐵𝑢 𝑃𝐵𝑢
With k=0.053 mol/gcat.h.atm and KBu = 0.33 -1
atm .
Pure butanol enters a thin tubed,
packed bed reactor at a molar flow rate of 50 kmol/hr and a pressure of 10 atm.
a. What PBR catalyst weight is necessary to achieve 80% conversion in the
absence of pressure drop?
b. When there is pressure drop, with 𝛼 = 0.0006 kg-1. What catalyst weight is
necessary to achieve 70% conversion?
6. Develop kinetic rate equation based on LHHW dual-site surface reaction for the
dehydrogenation of methylcyclohexane
7.
𝒓𝒆𝒂𝒄𝒕𝒊𝒐𝒏 𝒓𝒂𝒕𝒆
Run PA (atm) PB (atm) PC (atm) 𝒎𝒐𝒍
𝒔. 𝒈 − 𝒄𝒂𝒕
1 1 1 2 0.115
2 1 10 2 1.142
3 10 1 2 0.181
4 1 20 2 2.272
5 1 20 10 0.927
6 20 1 2 0.185
7 0.1 1 2 0.0242
(d)
8.
𝒎𝒐𝒍 𝒕𝒐𝒍𝒖𝒆𝒏𝒆
PH2 (atm) PM (atm) 𝒓′𝑻
𝒔. 𝒌𝒈 − 𝒄𝒂𝒕
1 1 1.21
1.5 1 1.251
0.5 1 1.30
0.5 0.5 1.1
1 0.25 0.92
0.5 0.1 0.64
3 3 1.27
1 4 1.28
3 2 1.26
4 1 1.30
0.5 0.25 0.94
2 0.05 0.41
9.
𝒓𝒆𝒂𝒄𝒕𝒊𝒐𝒏 𝒓𝒂𝒕𝒆
Pcyclohexanol Pcyclohexene Pwater 𝒎𝒐𝒍
Run
(atm) (atm) (atm) 𝒙𝟏𝟎𝟓
𝒔. 𝒅𝒎𝟑
1 1 1 1 3.31
2 5 1 1 1.051
3 10 1 1 0.566
4 2 5 1 1.827
5 2 10 1 1.491
6 3 0 5 1.361
7 3 0 10 1.081
8 1 10 10 0.863
9 0 5 8 0
10 3 3 3 1.372
(c)