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part 1: overview of cogeneration and its status in asia - Fire

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70 Part II: Cogeneration experiences <strong>in</strong> Asia <strong>and</strong> elsewhere<br />

2.2.2 Details <strong>of</strong> the <strong>cogeneration</strong> system<br />

The gas turb<strong>in</strong>es with an ISO rat<strong>in</strong>g <strong>of</strong> 25 MW are capable <strong>of</strong> produc<strong>in</strong>g 20.7 MW at the site.<br />

S<strong>in</strong>ce the gas supplier could not guarantee lean gas supply, dual fuel configuration (lean gas<br />

as well as high-speed diesel) was specified for the gas turb<strong>in</strong>es. This was further altered to<br />

allow simultaneous fir<strong>in</strong>g <strong>of</strong> liquid <strong>and</strong> gas <strong>in</strong> such a manner that the gas gets a preference<br />

<strong>and</strong> the liquid fuel meets the balance requirement.<br />

A 25 MW capacity steam turb<strong>in</strong>e generator was selected with the option for extract<strong>in</strong>g<br />

medium pressure steam at 19 bar <strong>and</strong> low pressure steam at 3.5 bar. The condenser was<br />

designed for generat<strong>in</strong>g up to 20 MW <strong>of</strong> power without any steam extraction. The heat<br />

recovery steam generators (HRSG) have the option for auxiliary fir<strong>in</strong>g with multi-fuel option.<br />

High-speed diesel is used as a start-up fuel <strong>and</strong> the lean gas is supplied as the ma<strong>in</strong> fuel with<br />

low sulphur heavy stock as the alternate liquid fuel. By-products available from the gas<br />

crack<strong>in</strong>g unit such as pyrolysis gasol<strong>in</strong>e <strong>and</strong> <strong>of</strong>f gas can also be fired. In order to allow the<br />

HRSG to operate as a conventional boiler when the associated gas turb<strong>in</strong>e was not operat<strong>in</strong>g,<br />

a forced draft fan for supply<strong>in</strong>g combustion air is <strong>in</strong>stalled with suitable dampers <strong>and</strong> safety<br />

protections so that the boiler can run without exhaust from the gas turb<strong>in</strong>e. This change over<br />

scheme was well designed <strong>and</strong> tested <strong>and</strong> works satisfactorily at present.<br />

In order to maximize the heat extraction from the exhaust gases after economizer <strong>and</strong> to<br />

<strong>in</strong>crease the overall efficiency <strong>of</strong> the HRSG, a separate low-pressure water coil was <strong>in</strong>stalled<br />

<strong>in</strong> exhaust gas path. Such an arrangement allowed to generate hot water which, when<br />

flashed, gives low-pressure steam that is used for deaeration <strong>of</strong> boiler feed water. This<br />

feature helps to reduce the steam dem<strong>and</strong> for the deaerator by 4 ton/hour.<br />

2.3 Cogeneration <strong>in</strong> a Textile Mill<br />

Encouraged by the Thai Government policy on <strong>in</strong>dustrial <strong>cogeneration</strong> <strong>and</strong> sale <strong>of</strong> excess<br />

electricity to the utility grid, a synthetic fibre manufactur<strong>in</strong>g <strong>in</strong>dustry decided to explore the<br />

opportunity for <strong>cogeneration</strong>. The factory was <strong>part</strong>icularly susceptible to any un<strong>in</strong>tended<br />

shutdown due to power <strong>in</strong>terruption while led to high restart<strong>in</strong>g costs. In addition, the factory<br />

had a generat<strong>in</strong>g capacity to meet only 15 per cent <strong>of</strong> <strong>its</strong> dem<strong>and</strong> <strong>and</strong> the exist<strong>in</strong>g diesel<br />

generators were over 20 years old <strong>and</strong> were expensive to ma<strong>in</strong>ta<strong>in</strong>. A techno-economic<br />

feasibility study was first undertaken to identify the best <strong>cogeneration</strong> scheme <strong>in</strong> l<strong>in</strong>e with the<br />

Government’s newly announced power buy-back option. 2<br />

2.3.1 Exist<strong>in</strong>g energy situation <strong>of</strong> the factory<br />

The production processes <strong>in</strong> the factory required steam at two different pressures, 56 bar <strong>and</strong><br />

12 bar, respectively. The total dem<strong>and</strong> <strong>of</strong> steam was 101,120 tons <strong>of</strong> steam per annum,<br />

giv<strong>in</strong>g an average <strong>of</strong> about 11.5 ton/hour, though the maximum <strong>and</strong> m<strong>in</strong>imum dem<strong>and</strong>s were<br />

<strong>of</strong> the order <strong>of</strong> 17 <strong>and</strong> 9 tons/hour, respectively. To meet these dem<strong>and</strong>s, 4 boilers were<br />

employed with the follow<strong>in</strong>g capacities:<br />

- two boilers produc<strong>in</strong>g steam at 60 bar, each with a generat<strong>in</strong>g capacity <strong>of</strong> 7 tons/hour,<br />

- two others operat<strong>in</strong>g at 12 bar <strong>and</strong> generat<strong>in</strong>g 15 tons <strong>of</strong> steam per hour each.<br />

Heavy fuel oil used as fuel <strong>in</strong> the boiler was purchased at a price <strong>of</strong> US$ 0.12/litre.<br />

2 P. Srisovanna, “Case study <strong>of</strong> <strong>cogeneration</strong> <strong>in</strong> textile sector”, ESCAP South-East Asia Sub-regional<br />

Sem<strong>in</strong>ar on Promotion <strong>of</strong> Energy Efficiency <strong>and</strong> Pollution Control through Cogeneration, Hanoi, 10-11<br />

November 1998.

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