(best examples and good practices) on household organic waste ...
(best examples and good practices) on household organic waste ... (best examples and good practices) on household organic waste ...
73 Figure 22.: Andritz drum drying system (Krebs et.al.,2007) A dosing device feeds dewatered sludge to a mixer, where it is mixed into sludge that has already been dried. This produces material which is no longer sticky
74 material,
- Page 33 and 34: 22 4. Finally, methanogenic organis
- Page 35 and 36: 24 If the proper conditions cannot
- Page 37 and 38: 26 Considerations such as the desig
- Page 39 and 40: 28 to the viscosity of the feed, th
- Page 41 and 42: 30 The Netherlands
- Page 43 and 44: 32 Heavy metals in digestate usuall
- Page 45 and 46: 34 3. Large scale biodegradable was
- Page 47 and 48: 36 power and 1,200
- Page 49 and 50: 38 filtration or electrostatic prec
- Page 51 and 52: 40 acceptable range, but reduce the
- Page 53 and 54: 42 Rotary kiln furnaces Rotary kiln
- Page 55 and 56: 44 It has been processed an
- Page 57 and 58: 46 Heavy metals can be grouped into
- Page 59 and 60: 48 choices for a commercial plant w
- Page 61 and 62: 50 Gasification (Figure.19) using o
- Page 63 and 64: 52 AC plasma CO2 plasma arc Microwa
- Page 65 and 66: 54 pulled through an induced draft
- Page 67 and 68: 56 the non-biodegradables a
- Page 69 and 70: 58 3.3.8. Bioreactor land</
- Page 71 and 72: 60 4. Materials Sorting Processes 4
- Page 73 and 74: 62 Plastics Plastics (Fiqure.32) po
- Page 75 and 76: 64 separate containers. There are a
- Page 77 and 78: 66 The sorting of recyclables may b
- Page 79 and 80: 68 4.5. Mechanical and</str
- Page 81 and 82: 70 glass breakage on the tipping fl
- Page 83: 72 within solution under the influe
- Page 87 and 88: 76 changing pole configuration or w
- Page 89 and 90: 78 4.7. Mechanical Biological Treat
- Page 91 and 92: 80 Biological processing compartmen
- Page 93 and 94: 82 equivalence considerations <stro
- Page 95 and 96: 84 5.2. Waste streams considered in
- Page 97 and 98: 86 Figure 27.: Percentage of munici
- Page 99 and 100: 88 6.Italy The Italian strategy Ita
- Page 101 and 102: 90 Italy also set targets for colle
- Page 103 and 104: 92 (Figure 30.). The quality of com
- Page 105 and 106: 94 a controlled environment with wa
- Page 107 and 108: 96 Picture 11.: The Corteolona plan
- Page 109 and 110: 98 The building in the foreground h
- Page 111 and 112: 100 compost their garden waste. The
- Page 113 and 114: 102 The total amount of waste produ
- Page 115 and 116: 104 7. Germany 7.1. Waste managemen
- Page 117 and 118: 106 has been specified only for som
- Page 119 and 120: 108 7.3. Best practices</st
- Page 121 and 122: 110 The installation has different
- Page 123 and 124: 112 The sludge is placed into a lar
- Page 125 and 126: 114 Picture 22.: Air mixing mechani
- Page 127 and 128: 116 Finally the dried sludge is bee
- Page 129 and 130: 118 process treats the wastes as co
- Page 131 and 132: 120 consumption is about 0.7 x106 k
- Page 133 and 134: 122 Picture 30.: The heat exchanger
74<br />
material, <str<strong>on</strong>g>and</str<strong>on</strong>g> the gravitati<strong>on</strong>al force within a c<strong>on</strong>fined volume. In the<br />
interacti<strong>on</strong>, the drag force <str<strong>on</strong>g>and</str<strong>on</strong>g> the gravitati<strong>on</strong>al force are exerted in different<br />
directi<strong>on</strong>s up<strong>on</strong> the particles. The result is that <strong>waste</strong> particles that have a large<br />
drag to- weight ratio are suspended in the air stream, whereas comp<strong>on</strong>ents that<br />
have a small ratio tend to settle out of the air stream. The suspended fracti<strong>on</strong><br />
c<strong>on</strong>venti<strong>on</strong>ally is referred to as the “air-classified light fracti<strong>on</strong>” <str<strong>on</strong>g>and</str<strong>on</strong>g> the settled<br />
fracti<strong>on</strong> is termed “air classified heavy fracti<strong>on</strong>”. The c<strong>on</strong>fined volume in which<br />
the separati<strong>on</strong> takes place is called an “air classifier”. (Tchobanoglous <str<strong>on</strong>g>and</str<strong>on</strong>g> Kreith,<br />
2002)<br />
In air classificati<strong>on</strong> of shredded mixed MSW, the paper <str<strong>on</strong>g>and</str<strong>on</strong>g> plastic materials<br />
tend to be c<strong>on</strong>centrated in the light fracti<strong>on</strong>, <str<strong>on</strong>g>and</str<strong>on</strong>g> metals <str<strong>on</strong>g>and</str<strong>on</strong>g> glass are the<br />
principal comp<strong>on</strong>ents of the heavy fracti<strong>on</strong>.<br />
Since the density of a material (e.g., paper) is not the <strong>on</strong>ly characteristic of a<br />
particle that affects the air classificati<strong>on</strong> process, fine glass particles, by virtue<br />
of their high drag-to-weight ratio, may appear in the light fracti<strong>on</strong>. On the<br />
other h<str<strong>on</strong>g>and</str<strong>on</strong>g>, flat, unshredded milk cart<strong>on</strong>s or wet cardboard may appear in the<br />
heavy fracti<strong>on</strong>. Moisture affects the separati<strong>on</strong> of the various comp<strong>on</strong>ents, as a<br />
result of its influence <strong>on</strong> the density of a material. The influence can be<br />
particularly pr<strong>on</strong>ounced in the case of paper where its density can approach<br />
that of typically denser comp<strong>on</strong>ents, such as food <strong>waste</strong> that normally would<br />
report to the heavy fracti<strong>on</strong>. Air classifiers may be <strong>on</strong>e of a number of designs.<br />
All three require dust collecti<strong>on</strong>, blower, separator, <str<strong>on</strong>g>and</str<strong>on</strong>g> c<strong>on</strong>trol facilities.<br />
(Wastesum.,2010)<br />
The velocity of the air stream required to lift a particle in a vertical column<br />
(e.g., a vertical air classifier) must exceed a minimum value, termed the floating<br />
(or terminal) velocity. The floating velocity is a functi<strong>on</strong> of a number of<br />
parameters. The influence of the parameters <strong>on</strong> the floating velocity is<br />
illustrated in (Table 6.) for a variety of <strong>waste</strong> comp<strong>on</strong>ents. (Tchobanoglous <str<strong>on</strong>g>and</str<strong>on</strong>g><br />
Kreith, 2002)