The process for large-scale manufacture of paper has been largely unchanged for the last 125 years. The pulp and paper industry today is highly capital intensive, and there is an ongoing drive towards process integration, thereby increasing the efficiency of utilization of available process resources. This paper deals with the Kraft process (see Fig. 1) though the general principles described can be extended to other pulping processes. As shown in Figure 1, five water sinks and four water sources are considered for in-plant water reuse/ recycle. Prior to water reuse/ recycle, the network requires a freshwater flow rate of 36,400 tonne/day and generates 37,186 tonne/day of wastewater (sum of the individual sink and source flow rates in Table 1). The freshwater source that is available for service has an impurity concentration (chloride content) of 4.2 ppm, which is higher than the purest process source W13 (0 ppm). Please refer to first image for the schematic diagram and table of values, then answer this: Task A-1: Determine the minimum fresh water and minimum wastewater targets for the above system using water cascade analysis (WCA). [30%] Task A-2 [ULO2] Based on the results obtained from Task A-1, redraw Figure 1 for this Kraft pulping process (You are required to draw the water network for this Kraft pulping process first). Task A-2: Based on the results obtained from Task A-1, redraw Figure 1 for this Kraft pulping process (You are required to draw the water network for this Kraft pulping process first).   Note: Refer to the 2nd photo for the examples and guides.

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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Section: Chapter Questions
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Answer the two connected questions (Task A-1 and A-2). Provided in the last part are the guides and examples:

The process for large-scale manufacture of paper has been largely unchanged for the last 125 years. The pulp and paper industry today is highly capital intensive, and there is an ongoing drive towards process integration, thereby increasing the efficiency of utilization of available process resources. This paper deals with the Kraft process (see Fig. 1) though the general principles described can be extended to other pulping processes. As shown in Figure 1, five water sinks and four water sources are considered for in-plant water reuse/ recycle. Prior to water reuse/ recycle, the network requires a freshwater flow rate of 36,400 tonne/day and generates 37,186 tonne/day of wastewater (sum of the individual sink and source flow rates in Table 1). The freshwater source that is available for service has an impurity concentration (chloride content) of 4.2 ppm, which is higher than the purest process source W13 (0 ppm).

Please refer to first image for the schematic diagram and table of values, then answer this:

Task A-1: Determine the minimum fresh water and minimum wastewater targets for the above system using water cascade analysis (WCA). [30%] Task A-2 [ULO2] Based on the results obtained from Task A-1, redraw Figure 1 for this Kraft pulping process (You are required to draw the water network for this Kraft pulping process first).

Task A-2: Based on the results obtained from Task A-1, redraw Figure 1 for this Kraft pulping process (You are required to draw the water network for this Kraft pulping process first).

 

Note: Refer to the 2nd photo for the examples and guides.

1
2
Bleach Plant
Grits 35
25
3
Digestor
4
White
Liq Clar
24
Causticizer
23
Slaker
W38
W42
6
38 42
Effluent Treatment
5 Washers Sa 9
Screens
10
26
33
7
8
8b
37
C10₂
Alkali
Stage 39 Extrn. 43
32
Lime
Kiln
271
Washers
Filters
29
40 41
14,520
13,750
6-effect 14
evap
13
(H₂O)
Table 1. Limiting water data for the Kraft pulping process.
Water sinks, SK;
Flowrate, Fskj
(Process MSA)
(tonne/day)
W7
7,000
W18
4,200
W27
2,000
W37
12,000
W41
11,200
Water sources, SR₁
Flowrate, Fsri (tonne/day)
W13
7,971
W8b
945
30
31
34 Dregs
17r
17 b
15
28
22
21
ESP
17
Recovery
Furnace
Recovery Cycle
Fig. 1. Kraft process with bleaching (Sittig, 1977; Jones, 1973).
17 fg
18
Green
Liquor
Green Liq
Clarifier
0
275
20
238
504
16
Concentration, Cskj
(ppm)
110
5.5
38.5
10.12
13.2
19
Concentration, CSRi (ppm)
17a
Transcribed Image Text:1 2 Bleach Plant Grits 35 25 3 Digestor 4 White Liq Clar 24 Causticizer 23 Slaker W38 W42 6 38 42 Effluent Treatment 5 Washers Sa 9 Screens 10 26 33 7 8 8b 37 C10₂ Alkali Stage 39 Extrn. 43 32 Lime Kiln 271 Washers Filters 29 40 41 14,520 13,750 6-effect 14 evap 13 (H₂O) Table 1. Limiting water data for the Kraft pulping process. Water sinks, SK; Flowrate, Fskj (Process MSA) (tonne/day) W7 7,000 W18 4,200 W27 2,000 W37 12,000 W41 11,200 Water sources, SR₁ Flowrate, Fsri (tonne/day) W13 7,971 W8b 945 30 31 34 Dregs 17r 17 b 15 28 22 21 ESP 17 Recovery Furnace Recovery Cycle Fig. 1. Kraft process with bleaching (Sittig, 1977; Jones, 1973). 17 fg 18 Green Liquor Green Liq Clarifier 0 275 20 238 504 16 Concentration, Cskj (ppm) 110 5.5 38.5 10.12 13.2 19 Concentration, CSRi (ppm) 17a
Below is an example of a water cascade analysis table that should be done in Excel. Kindly show the
formula in each cell.
F.. =
sum
k Ck AC EFD, i ΣFs,j ZFD,i+ZFs,j
10
2 10
3 14
4 25
5 34
6 1000
000
Fresh water,
FW
is 0 ppm
Source 4
F is 10 t/h
is 10 ppm
Source 3
F is 40 t/h
is 100 ppm
Source 5
F is 5 t/h
is 100 ppm
Source 2
F is 50 t/h
is 700 ppm
Source 1
F is 20 t/h
10
is 1000 ppm
4
11
9
99996
6
10 t/h
90.6428571 t/h
40 t/h
5t/h
-1.2
50 t/h
-5.8
20 t/h
Water Cascade Table
Cum.
AM
F is 10 t/h
is 0 ppm
0.8
5.0
5.9
1.4
-0.4
10 t/h
SK3
-5.8
5.0
5.9
1.4
Similarly, the figure below shows an example of water network design:
F is 10 t/h
F
FFW
= 0
-0.4
is 0 ppm
-1.2
-6.2 -24.8
4.7
Fww
= 6.1
AM
SK4
-4.0
10 t/h
-13.2
42.3
6099792
-4.0
-28.8 -2.06
0.3
-42.0 -1.68
6099792
FFW
F is 15 t/h
-0.4
ML 150
0.01
is 10 ppm
4.5 t/h
SK5
10 t/h
ML = 100
ML = 50
Fo AM
FFW
=2.06
1.66
-4.14 -16.57
16.57
0.86 9.43
6.76 60.81
Fww
=8.16
0.50 t/h
8159722
F is 80 t/h
ML = 8000
is 100 ppm.
39.5 t/h
ML 3950
Cum.
AM
5 t/h
ML = 500
16.57
30.42857143 t/h
0
9.43
70.24
8159792
SK1
5.071428571 t/h
3550
Transcribed Image Text:Below is an example of a water cascade analysis table that should be done in Excel. Kindly show the formula in each cell. F.. = sum k Ck AC EFD, i ΣFs,j ZFD,i+ZFs,j 10 2 10 3 14 4 25 5 34 6 1000 000 Fresh water, FW is 0 ppm Source 4 F is 10 t/h is 10 ppm Source 3 F is 40 t/h is 100 ppm Source 5 F is 5 t/h is 100 ppm Source 2 F is 50 t/h is 700 ppm Source 1 F is 20 t/h 10 is 1000 ppm 4 11 9 99996 6 10 t/h 90.6428571 t/h 40 t/h 5t/h -1.2 50 t/h -5.8 20 t/h Water Cascade Table Cum. AM F is 10 t/h is 0 ppm 0.8 5.0 5.9 1.4 -0.4 10 t/h SK3 -5.8 5.0 5.9 1.4 Similarly, the figure below shows an example of water network design: F is 10 t/h F FFW = 0 -0.4 is 0 ppm -1.2 -6.2 -24.8 4.7 Fww = 6.1 AM SK4 -4.0 10 t/h -13.2 42.3 6099792 -4.0 -28.8 -2.06 0.3 -42.0 -1.68 6099792 FFW F is 15 t/h -0.4 ML 150 0.01 is 10 ppm 4.5 t/h SK5 10 t/h ML = 100 ML = 50 Fo AM FFW =2.06 1.66 -4.14 -16.57 16.57 0.86 9.43 6.76 60.81 Fww =8.16 0.50 t/h 8159722 F is 80 t/h ML = 8000 is 100 ppm. 39.5 t/h ML 3950 Cum. AM 5 t/h ML = 500 16.57 30.42857143 t/h 0 9.43 70.24 8159792 SK1 5.071428571 t/h 3550
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