Sizing of the Biogas Plant - Revision history

Ranisha at 06:41, 7 July 2015

2015-07-07T06:41:24Z

Wiki Gardener at 14:51, 6 July 2015

2015-07-06T14:51:24Z

Ranisha at 11:27, 8 April 2015

2015-04-08T11:27:57Z

Ranisha: /* Further Information */

2015-04-08T11:26:22Z

Further Information

Ranisha at 14:05, 9 July 2014

2014-07-09T14:05:53Z

Frank Helbig: /* Further Information */

2014-01-25T18:18:40Z

Further Information

Frank Helbig: /* Overview */

2014-01-25T15:43:39Z

Overview

Wiki Gardener at 18:10, 21 November 2013

2013-11-21T18:10:32Z

Wiki Gardener at 18:09, 21 November 2013

2013-11-21T18:09:57Z

Show changes

Frank Helbig at 08:22, 7 August 2012

2012-08-07T08:22:37Z

@@ Line 1: / Line 1: @@
 [[Portal:Biogas|►Back to Biogas Portal]]
 == Overview ==
@@ Line 16: / Line 14: @@
 Compared to other gases, biogas needs less air for combustion. Therefore, conventional gas appliances need larger gas jets when they are used for biogas combustion. About 5.7 liters of air are required for the complete combustion of one liter of biogas, while for butane 30.9 liters and for propane 23.8 liters are required.
 == Sizing the Digester ==
@@ Line 24: / Line 21: @@
 <br/>
-'''[[File:]] ''' [ m<sup>3</sup> = m<sup>3</sup>/day × number of days ]<br/><br/>
+'''<math>V_\text{d}= S_\text{d}*R_\text{T}</math> ''' [ m<sup>3</sup> = m<sup>3</sup>/day × number of days ]<br/><br/>
 The retention time, in turn, is determined by the chosen/given digesting temperature. For an unheated biogas plant, the temperature prevailing in the digester can be assumed as 1-2 Kelvin above the soil temperature. Seasonal variation must be given due consideration, however, i.e. the digester must be sized for the least favorable season of the year. For a plant of simple design, the retention time should amount to at least 40 days. Practical experience shows that retention times of 60-80 days, or even 100 days or more, are no rarity when there is a shortage of substrate. On the other hand, extra-long retention times can increase the gas yield by as much as 40%.
@@ Line 42: / Line 39: @@
 The amount of biogas generated each day '''G''' [m<sup>3</sup> gas/d], is calculated on the basis of the specific gas yield '''Gy''' of the substrate and the daily substrate input '''Sd'''.
-<u>The calculation can be based on:</u>
+The calculation can be based on:
+#The volatile solids content '''VS'''<blockquote></blockquote>
 '''G''' = '''VS''' × '''Gy'''(solids) [ m<sup>3</sup>/d = kg × m<sup>3</sup>/(d×kg) ]
+#the weight of the moist mass '''B'''<blockquote></blockquote>
 '''G''' = '''B''' × '''Gy'''(moist mass) [ m<sup>3</sup>/d = kg × m<sup>3</sup>/(d×kg) ]
+#standard gas-yield values per livestock unit '''LSU'''<blockquote></blockquote>
 '''G''' = number of '''LSU''' × '''Gy'''(species) [ m<sup>3</sup>/d = ''number''× m<sup>3</sup>/(d×''number'') ]
-<u>The temperature dependency is given by:</u>
+The temperature dependency is given by:
-<blockquote>
+<blockquote>'''Gy'''('''T''','''RT''') = '''mGy''' × '''f'''('''T''','''RT''')</blockquote>
 where
-<blockquote>
+<blockquote>'''Gy'''('''T''','''RT''') = gas yield as a function of digester temperature and retention time<br/>'''mGy''' = average specific gas yield, e.g. l/kg volatile solids content<br/>'''f'''('''T''','''RT''') = multiplier for the gas yield as a function of digester temperature T and retention time RT</blockquote>
 As a rule, it is advisable to calculate according to several different methods, since the available basic data are usually very imprecise, so that a higher degree of sizing certainty can be achieved by comparing and averaging the results.
@@ Line 86: / Line 65: @@
 i.e. the daily gas generation rate per m<sup>3</sup> digester volume '''Vd''', is calculated according to the following equation
-<blockquote>
+<blockquote>'''Gp''' = '''G''' ÷ '''Vd''' [ (m<sup>3</sup>/d) / m<sup>3</sup> ]</blockquote>
 === Digester loading '''Ld''' ===
 The digester loading '''Ld''' is calculated from the daily total solids input '''TS/d''' or the daily volatile solids input '''VS/d''' and the digester volume '''Vd''':
-[[File:]] [ kg/(m<sup>3</sup> d) ]
+<math>Ld_\text{T}=\frac{TS/d}{V_\text{d}}</math> [ kg/(m<sup>3</sup> d) ]
-[[File:]] [ kg/(m<sup>3</sup> d) ]
+<math>Ld_\text{V}=\frac{VS/d}{V_\text{d}}</math> [ kg/(m<sup>3</sup> d) ]
 <br/>Then, a calculated parameter should be checked against data from comparable plants in the region or from pertinent literature.
@@ Line 107: / Line 81: @@
 The size of the gasholder, i.e. the gasholder volume '''Vg''', depends on the relative rates of gas generation and gas consumption. <u>The gasholder must be designed to:</u>
 *cover the peak consumption rate '''gc<sub>max</sub>''' (->'''Vg<sub>1</sub>''') and
 *hold the gas produced during the longest zero-consumption period '''tz<sub>max</sub>''' (->'''Vg<sub>2</sub>''')
-<blockquote>
+<blockquote>'''Vg<sub>1</sub>''' = '''gc<sub>max</sub>''' × '''tc<sub>max</sub>''' = '''vc<sub>max</sub>''' '''Vg<sub>2</sub>''' = '''G<sub>h</sub>''' × '''tz<sub>max</sub>'''</blockquote>
 with
-<blockquote>
+<blockquote>'''gc<sub>max</sub>''' = maximum hourly gas consumption [m<sup>3</sup>/h] '''tc<sub>max</sub>''' = time of maximum consumption [h] '''vc<sub>max</sub>''' = maximum gas consumption [m<sup>3</sup>] '''G<sub>h</sub>''' = hourly gas production [m<sup>3</sup>/h] = '''G''' ÷ 24 h/d '''tz<sub>max</sub>''' = maximum zero-consumption time [h]</blockquote>
 The larger '''Vg'''-value ('''Vg<sub>1</sub>''' or '''Vg<sub>2</sub>''') determines the size of the gasholder. A safety margin of 10-20% should be added:
-<blockquote>
+<blockquote>'''Vg''' = 1.15 (±0.5) × max('''Vg<sub>1</sub>''','''Vg<sub>2</sub>''')</blockquote>
 Practical experience shows that 40-60% of the daily gas production normally has to be stored.
 The ratio '''Vd''' ÷ '''Vg''' (digester volume ÷ gasholder volume) is a major factor with regard to the basic design of the biogas plant. For a typical agricultural biogas plant, the '''Vd/Vg'''-ratio amounts to somewhere between 3:1 and 10:1, with 5:1 - 6:1 occuring most frequently.
 == Further Information<br/> ==
@@ Line 135: / Line 97: @@
 *[[Portal:Biogas|Biogas Portal on energypedia]]
 == References<br/> ==

@@ Line 1: / Line 1: @@
 [[Portal:Biogas|►Back to Biogas Portal]]
 == Overview ==
@@ Line 8: / Line 10: @@
 == Determinig Gas Demand for Domestic Use ==
-The gas demand can be defined on the basis of energy consumed previously. For example, 1 kg firewood then corresponds to 200 l biogas, 1 kg dried cow dung corresponds to 100 l biogas and 1 kg charcoal corresponds to 500 l biogas.&lt;/span&gt;
+The gas demand can be defined on the basis of energy consumed previously. For example, 1 kg firewood then corresponds to 200 l biogas, 1 kg dried cow dung corresponds to 100 l biogas and 1 kg charcoal corresponds to 500 l biogas.
 The gas demand can also be defined using the daily cooking times. The gas consumption per person and meal lies between 150 and 300 liter biogas. For one liter water to be cooked 30-40 l biogas, for 1/2 kg rice 120-140 l and for 1/2 kg legumes 160-190 l are required.
@@ Line 14: / Line 16: @@
 Compared to other gases, biogas needs less air for combustion. Therefore, conventional gas appliances need larger gas jets when they are used for biogas combustion. About 5.7 liters of air are required for the complete combustion of one liter of biogas, while for butane 30.9 liters and for propane 23.8 liters are required.
 == Sizing the Digester ==
@@ Line 21: / Line 24: @@
 <br/>
-'''<math>V_\text{d}= S_\text{d}*R_\text{T}</math> ''' [ m<sup>3</sup> = m<sup>3</sup>/day × number of days ]<br/><br/>
+'''[[File:]] ''' [ m<sup>3</sup> = m<sup>3</sup>/day × number of days ]<br/><br/>
 The retention time, in turn, is determined by the chosen/given digesting temperature. For an unheated biogas plant, the temperature prevailing in the digester can be assumed as 1-2 Kelvin above the soil temperature. Seasonal variation must be given due consideration, however, i.e. the digester must be sized for the least favorable season of the year. For a plant of simple design, the retention time should amount to at least 40 days. Practical experience shows that retention times of 60-80 days, or even 100 days or more, are no rarity when there is a shortage of substrate. On the other hand, extra-long retention times can increase the gas yield by as much as 40%.
@@ Line 39: / Line 42: @@
 The amount of biogas generated each day '''G''' [m<sup>3</sup> gas/d], is calculated on the basis of the specific gas yield '''Gy''' of the substrate and the daily substrate input '''Sd'''.
-The calculation can be based on:
+<u>The calculation can be based on:</u>
-#The volatile solids content '''VS'''<blockquote></blockquote>
 '''G''' = '''VS''' × '''Gy'''(solids) [ m<sup>3</sup>/d = kg × m<sup>3</sup>/(d×kg) ]
-#the weight of the moist mass '''B'''<blockquote></blockquote>
 '''G''' = '''B''' × '''Gy'''(moist mass) [ m<sup>3</sup>/d = kg × m<sup>3</sup>/(d×kg) ]
-#standard gas-yield values per livestock unit '''LSU'''<blockquote></blockquote>
 '''G''' = number of '''LSU''' × '''Gy'''(species) [ m<sup>3</sup>/d = ''number''× m<sup>3</sup>/(d×''number'') ]
-The temperature dependency is given by:
+<u>The temperature dependency is given by:</u>
-<blockquote>'''Gy'''('''T''','''RT''') = '''mGy''' × '''f'''('''T''','''RT''')</blockquote>
+<blockquote>
 where
-<blockquote>'''Gy'''('''T''','''RT''') = gas yield as a function of digester temperature and retention time<br/>'''mGy''' = average specific gas yield, e.g. l/kg volatile solids content<br/>'''f'''('''T''','''RT''') = multiplier for the gas yield as a function of digester temperature T and retention time RT</blockquote>
+<blockquote>
 As a rule, it is advisable to calculate according to several different methods, since the available basic data are usually very imprecise, so that a higher degree of sizing certainty can be achieved by comparing and averaging the results.
@@ Line 65: / Line 86: @@
 i.e. the daily gas generation rate per m<sup>3</sup> digester volume '''Vd''', is calculated according to the following equation
-<blockquote>'''Gp''' = '''G''' ÷ '''Vd''' [ (m<sup>3</sup>/d) / m<sup>3</sup> ]</blockquote>
+<blockquote>
 === Digester loading '''Ld''' ===
 The digester loading '''Ld''' is calculated from the daily total solids input '''TS/d''' or the daily volatile solids input '''VS/d''' and the digester volume '''Vd''':
-<math>Ld_\text{T}=\frac{TS/d}{V_\text{d}}</math> [ kg/(m<sup>3</sup> d) ]
+[[File:]] [ kg/(m<sup>3</sup> d) ]
-<math>Ld_\text{V}=\frac{VS/d}{V_\text{d}}</math> [ kg/(m<sup>3</sup> d) ]
+[[File:]] [ kg/(m<sup>3</sup> d) ]
 <br/>Then, a calculated parameter should be checked against data from comparable plants in the region or from pertinent literature.
@@ Line 81: / Line 107: @@
 The size of the gasholder, i.e. the gasholder volume '''Vg''', depends on the relative rates of gas generation and gas consumption. <u>The gasholder must be designed to:</u>
 *cover the peak consumption rate '''gc<sub>max</sub>''' (->'''Vg<sub>1</sub>''') and
 *hold the gas produced during the longest zero-consumption period '''tz<sub>max</sub>''' (->'''Vg<sub>2</sub>''')
-<blockquote>'''Vg<sub>1</sub>''' = '''gc<sub>max</sub>''' × '''tc<sub>max</sub>''' = '''vc<sub>max</sub>''' '''Vg<sub>2</sub>''' = '''G<sub>h</sub>''' × '''tz<sub>max</sub>'''</blockquote>
+<blockquote>
 with
-<blockquote>'''gc<sub>max</sub>''' = maximum hourly gas consumption [m<sup>3</sup>/h] '''tc<sub>max</sub>''' = time of maximum consumption [h] '''vc<sub>max</sub>''' = maximum gas consumption [m<sup>3</sup>] '''G<sub>h</sub>''' = hourly gas production [m<sup>3</sup>/h] = '''G''' ÷ 24 h/d '''tz<sub>max</sub>''' = maximum zero-consumption time [h]</blockquote>
+<blockquote>
 The larger '''Vg'''-value ('''Vg<sub>1</sub>''' or '''Vg<sub>2</sub>''') determines the size of the gasholder. A safety margin of 10-20% should be added:
-<blockquote>'''Vg''' = 1.15 (±0.5) × max('''Vg<sub>1</sub>''','''Vg<sub>2</sub>''')</blockquote>
+<blockquote>
 Practical experience shows that 40-60% of the daily gas production normally has to be stored.
 The ratio '''Vd''' ÷ '''Vg''' (digester volume ÷ gasholder volume) is a major factor with regard to the basic design of the biogas plant. For a typical agricultural biogas plant, the '''Vd/Vg'''-ratio amounts to somewhere between 3:1 and 10:1, with 5:1 - 6:1 occuring most frequently.
 == Further Information<br/> ==
 *[[:Category:Biogas|All Biogas Articles]]
 == References<br/> ==

@@ Line 1: / Line 1: @@
+[[Portal:Biogas|►Back to Biogas Portal]]
 == Overview ==
@@ Line 14: / Line 14: @@
 Compared to other gases, biogas needs less air for combustion. Therefore, conventional gas appliances need larger gas jets when they are used for biogas combustion. About 5.7 liters of air are required for the complete combustion of one liter of biogas, while for butane 30.9 liters and for propane 23.8 liters are required.
 == Sizing the Digester ==
@@ Line 92: / Line 91: @@
 The ratio '''Vd''' ÷ '''Vg''' (digester volume ÷ gasholder volume) is a major factor with regard to the basic design of the biogas plant. For a typical agricultural biogas plant, the '''Vd/Vg'''-ratio amounts to somewhere between 3:1 and 10:1, with 5:1 - 6:1 occuring most frequently.
 == Further Information<br/> ==
@@ Line 104: / Line 99: @@
 == References<br/> ==
-<references /><br/>
+<references />
 [[Category:Biogas]]

@@ Line 99: / Line 99: @@
 == Further Information<br/> ==
-*<br/>
+*[[:Category:Biogas|All Biogas Articles]]
 == References<br/> ==

@@ Line 1: / Line 1: @@
 == Overview ==
@@ Line 15: / Line 14: @@
 Compared to other gases, biogas needs less air for combustion. Therefore, conventional gas appliances need larger gas jets when they are used for biogas combustion. About 5.7 liters of air are required for the complete combustion of one liter of biogas, while for butane 30.9 liters and for propane 23.8 liters are required.
 == Sizing the Digester ==
@@ Line 95: / Line 95: @@
 <br/>
 == Further Information<br/> ==
@@ Line 102: / Line 103: @@
 <br/>
 == References<br/> ==
@@ Line 109: / Line 111: @@
 <br/>
-[[Biogas|back to "Biogas Portal"]]
+[[Portal:Biogas|back to "Biogas Portal"]]
 [[Category:Biogas]]