Evaluation of Aqua-Ammonia Chiller Technologies and Field Site ...
Gas Fired Water Ammonia Absorption Chiller
Transcript of Gas Fired Water Ammonia Absorption Chiller
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GAS FIRED WATER-AMMONIA ABSORPTION CHILLERRinnal, Korea Seminar
1! In"ro#$%"ion
Gas fired water-ammonia absorption chiller (GA) use an absorption-based cooling cycle with solutionof water-ammonia. It is power by natural gas or LPG to produce chilled water down to temperature of
3°.
&! Te%'nolo()
!he GA consists mainly"
i. #urner ii. Generator iii. $ectifier i%. ondenser %. &eat 'changer (Pipe in pipe type)%i. '%aporator %ii. Absorber
%iii. irculation Pump
!he gas burner use natural gas or LPG to heat up the generator.
!he generator content concentrated water-ammonia solution. !he solution is heated up to *+°
under pressure of ,bar. !he ammonia e%aporates and separated from the water in the generator at
+° at ,bar.
!he ammonia %apor is then pipe to the rectifier to cool down to the temperature of ° by the return
water-ammonia solution from the circulation pump. !he rectifier also help to condense down the water %apor consist in the ammonia %apor.
!he ammonia %apor is the further cooled down in the condenser by eternal air flow (fan is used). !he
ammonia %apor is condensed to li/uid in condenser at the temperature of 03 °.
, bar
+°
*+°
°
, bar
03°
3 bar
31°
3 bar
*1°0 bar
*°
°
3*°
1+°
00°
+°
hilledwater
°
hilledwater
°
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!he pressure of li/uid ammonia after condenser is then reduce from , bar to 3 bar by the used of
restrictor. !he temperature of li/uid ammonia will dropped to 31° naturally after the restrictor.
!hen2 the li/uid ammonia is cooled down in the pipe-in-pipe heat echanger to the temperature of
*1°.
!he pressure of li/uid ammonia is further reduced to 0 bar by epansion restrictor again. !he
temperature is further reducing naturally to *°.
!he ammonia li/uid is then allowed to e%aporate in the e%aporator. !he e%aporation of ammonia willcool the incoming chilled water by absorbing the heat from the chilled water.
After the e%aporation process2 the ammonia %apor is then piped to the absorber2 where it meets thehot water which is remained after the separation of ammonia in the generator. &ere occurs theabsorption. !he hot water spray from the top of absorber2 absorb the ammonia %apor to becomewater-ammonia solution as initial li/uid solution. !he water-ammonia solution left the absorber at
1+°.
!he water-ammonia solution is then cooled down in the cooler by eternal air flow to 00 °2 before it is
piped to the circulation pump.
!he circulation pump pumps the water-ammonia solution to the rectifier and absorber for the purposeof absorbing heat (heat echange) and then to the generator to begin the cycle again.
*! A++li%a"ion
GA generally design for the used for air conditioning of residential2 commercial and industrialen%ironments.
!he GA can also be manufactured with an integrated heating module (chiller-heater units) to supply2
either simultaneously or alternately2 chilled water down to 3° and hot water up to 1°.
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! S+e%ii%a"ion
5ultiple basic units can be group together to pro%ide wide range of capacity as below.
De.%ri+"ion Coolin( Coolin( An# Hea"in(
ooling apacity (67) . .
&eating apacity (67) - 3*.
7ater 8low(l9h) *23 *23
Gas :G2 LPG
Gas consumption(m39h-:G)
*. *.
& - 3.;1
Power supply(67)
+.1* +.1*
& - +.+;
<perating sound (d#)
7eight (6g) 30+ 03+
=i>e (㎜2 &7?) 2*1+2*3+1+ 2*1+2*3+2*0+
C = 35 kW (30,100 kcal/h)
H = 32,5 kW (27,950 kcal/h)
C = 35 kW (30,100 kcal/h)H = 65 kW (55,900 kcal/h)
C = 52,5 kW (45,150 kcal/h)
H = 32,5 kW (27,950 kcal/h)
C = 52,5 kW (45,150 kcal/h)
H = 97,5 kW (83,850 kcal/h)
C = 52,5 kW (45,150 kcal/h)
H = 65 kW (55,900 kcal/h)
C = 69,6 kW (59,856 kcal/h)
H = 32,5 kW (27,950 kcal/h)
C = 69,6 kW (59,856 kcal/h)
H = 65 kW (55,900 kcal/h)
C = 69,6 kW (59,856 kcal/h)
H = 97,5 kW (83,850 kcal/h)
C = 69,6 kW (59,856 kcal/h)
H = 130 kW (111,800 kcal/h)
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/! E0am+le o A++li%a"ion
<ne unit of GA connected to airconditioning2 room heater2 floor heater26itchen and bath room.
Air condition
8loor&eater
itchen #ath $oom
&ot7ater