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(.)

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- - - -

-

-

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(Biogas)

(Biogas)

(Anaerobic Digestion)

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3

1(Hydrolysis)

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2(Acidogenesis)

(Volatile acid) (acid former) (Acetic acid) (Propionic acid)

3 (Methanogenesis)

(CH4) (CO2) (H2S)

(N2) (H2)

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50-75

(CO2) 36-39

(H2) (H2S) 1-3

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1

( 21 )

(LPG)0.46 .

0.60

0.55

1.2 kWh

1.5 .

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(Temperature)

3 - Phychrophillic (5-15C)

- Mesophillic

(35-37

C)- Thermophillic (50-55C)

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- (pH) pH 6.5-7.5 5 4.5

(Alkalinity) - 1,000-5,000/ (CaCO3)

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(Volatile Acid)

pH 2,000/ 5,000/

(Nutrients)

COD:N:P 100:2.2:0.4 BOD:N:P 100:1.1:0.2

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(Inhibiting and Toxic Substances)

(Mixing)

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(1) (Floating drum digester)

..2519

http://4.bp.blogspot.com/_AdU3UvQ0iVk/SkzUA36SdDI/AAAAAAAACAY/GMe9WoiwITQ/s1600-h/DSC00015.jpg

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(2) (Separate Floating drum digester)

. 2

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(3)

. ..2522

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(4) (Fixed dome digester)

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(5) UASB : Up-Flow Anaerobic Sludge Blanket

2 2-5 .

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(6) H-UASB (High suspension solid-Up-Flow Anaerobic

Sludge Blanket)

UASB

Buffer tank PE Buffer tank UASB

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(7) (Plug Flow digester)

Channel digester

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(8) Mini CD ( Mini Channel Digester)

100 ..

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(9) PVC

PVC 8 .. 2 ./

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(10) Covered lagoon

Plug Flow

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(11) . 1

10 ../

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(12) . 2

2 ../

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(1)

Upflow Anaerobic Sludge Blanket (UASB)

2 (Sludge Bed) 2 SludgeBlanket (Gas-Solid Separator)

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(2) (Anaerobic Fixed Film, AFF)

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(3) Completely Stirred Tank Reactor (CSTR)

(Mixing System) (HRT)

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(4) Anaerobic Baffle Reactor (ABR)

0.2-0.4 /

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(5) Modified covered Lagoon (MCL)

High Density Polyethylene (HDPE) (PVC)

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- Hot Oil Burner StreamBoiler

-

-

()

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- - VSPP -

-

- -

-

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- -

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BGG. = Q*COD/1000*Eff. COD removed*Gas Yield

BGG. ( Biogas Generate) = (./)Q = (/)

COD = COD (./)

Efficiency COD removed = COD (%)

1,000 = (1,000 .) ..Gas yield = COD

( 0.35 ./. COD/)

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. 10 ./ COD9,000 ./ COD 80% Q = 10 ./COD = 9,000 ./

Eff. COD removed = 80 % BGG. = 10*9,000/1,0000.80 *0.35 ./ 25.20 . / 60 % 25.20/0.60 42 . /

1 . 200 10,000 (10..) = 50 .1. 0.85 .. 50 . = 50*0.85 = 42.50./

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(.)

(..)

12 13.5 .2

30 50 Fixed dome60 70 .1

60 100 Fixed dome

60 100 CD junior

120 200 CDUA

180 300 CDUA

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BGG. = Q*COD/1000*Eff. COD removed*Gas Yield *%

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Q = 2,000 ../

COD = 18,000 ./

Gas yield = 0.35 ../.COD/

Efficiency COD removed 80%

60%BGG = 2,000*18,000/1000*80/100*0.35/60%

16,800 ../

9,240/

200 / 2,000 ../ COD 18,000 ./ ../

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.. .

(11 ..) 50 . .4 .5 .6

30 .

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3

. .

3 3 200

200 3

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" 5

15.45 . 22 .. ... .. .

5

1 . .

... ...

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" " 200 50 . 3 12 5

..

4

..

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