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Surabaya, 7 Mei 2013 Steam Power Plant Design Upgrading (Case Study: Khoms Steam Power Plant) Journal By : Hesham G. Ibrahim Chemical Engineering Department, Faculty of Engineering, Al-Mergheb University, , Al- Khoms City, Libya Mokhtar S. Elatrash Environmental Science Department, Faculty of Science Al-Mergheb University, Al-Khoms City, Libya Published By Canadian Center of Science and Education (www.ccsenet.org/err) Presented By Heri Purnomo Diploma Mechanical Engineering ITS 2110030023
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Page 1: Heri purnomo powerplant design

Surabaya, 7 Mei 2013

Steam Power Plant Design Upgrading

(Case Study: Khoms Steam Power Plant)

Journal By :Hesham G. IbrahimChemical Engineering Department, Facultyof Engineering, Al-Mergheb University, , Al-Khoms City, LibyaMokhtar S. ElatrashEnvironmental Science Department, Facultyof ScienceAl-Mergheb University, Al-Khoms City, Libya

Published By Canadian Center of Scienceand Education (www.ccsenet.org/err)

Presented By

Heri PurnomoDiploma Mechanical Engineering ITS2110030023

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Khoms Steam Power Plant

Khoms Thermal Power Plant Libya is located at Khoms, AlMarqab, Libya. Location coordinates are: Latitude= 32.6213,Longitude= 14.3302. This infrastructure is of TYPE Oil Power Plantwith a design capacity of 480 MWe. It has 4 unit(s). The first unitwas commissioned in 1982 and the last in 1982. It is operated byGeneral Electricity Company of Libya (GECOL).

SITELOCATION

http://globalenergyobservatory.org/geoid/41589

Oil Type Operation

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ABSTRACT

Built during the seventies and commissioned in 1980, Khoms Steam Power Plant consists of four units. Aproposed design modifications based on Hysys simulation is to improve the overall efficiency, reduce gasemissions and lower operation and maintenance costs.Five proposed modifications based on reduction of heat loss from the condenser and lowering heating rate revealthat a single open feedwater heater process is the optimum design modification of Rankinecycle to achieve thetargeted objectives.

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INTRODUCTION

Khoms Steam Power Plant

A steam power plant cycle is the group of

interconnected main equipment

components selected for optimum

thermodynamic characteristics to achieve

optimum performance to generate

electrical power. Selection of the

optimum cycle depends upon plant size,

cost, construction, operation and

maintenance.

Electrical power generation through steam

power plants in Libya constituted nearly

25.4 % of the total national

power production during 2008 (GECOL,

2008). This study presents a simulation by

HYSYS to examine the

possibility of upgrading the efficiency and

the reliability of the Rankine cycle at

Khoms steam power plant.

Proposed upgraded designs aim to

enhance the overall efficiency, reduce

cost of maintenance, fuel consumption

and heat losses.

examine thepossibility of upgrading the efficiency and the reliability of the Rankine cycle at Khoms steam power plant

Proposed upgraded designs aim to enhance the overall efficiency, reduce cost of maintenance, fuel consumptionand heat losses

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INTRODUCTION OF HYSYS

PETROLEUM

POWERPLANT

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INTRODUCTION OF HYSYS

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RANKINECYCLE

The Rankine cycle is a

mathematical model that is used to predict the performance of steam engines. The Rankine cycle is an idealisedthermodynamic cycle of a

heat engine that converts heat into mechanical work. The heat is supplied externally to a closed loop, which usually uses water as the working fluid

1-2 isentropic pump2-3 constant pressure heat addition3-4 isentropic turbine 4-1 constant pressure heat rejection

BASICTHEORY

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ACTUALRANKINECYCLE

In a real Rankine cycle such as that used in steam power

plants as shown in Figure 2, the compression by the

pump and the expansion in the turbine are not

isentropic. In other words, these processes are non-

reversible and

entropy is increased during the two processes. This

somewhat increases the power required by the pump

and

decreases the power generated by the turbine

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ACTUALMEASUREMENTPOWERPLANT

A measure of the effectiveness of an energy conversion device is its thermal efficiency which is defined as theratio of the Heat equivalent of mechanical energy transmitted to

turbine shaft to the heat supplied from externalsources. Also, overall efficiency defined as the ratio of the cycle net work to the heat supplied from externalsources

The thermal efficiency of a steam power

station is about 30% ±2

The overall efficiency of steam power

station is about 29%. It is seen that overall

efficiency is less than thermal

efficiency. A loss of about 1% occurs in

the alternator

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ACTUALMEASUREMENTPOWERPLANT

Another measure of efficiency commonly employed by power plant engineers is the heat rate, that is, the ratio ofthe rate of heat addition in conventional heat units to the net power output in conventional power units. Becausethe rate of heat addition is proportional to the fuel consumption rate, the heat rate is a measure of fuel utilizationrate per unit of power output (Singer, 1981).

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Problems associated with

steam power plant

Steam turbine efficiency is limited by water droplets formation. As steam

leaves the turbine, it is typically wet.

As water condenses, water droplets hit the turbine blades at high speed

causing pitting and erosion, which

gradually reduces the life expectancy of the blades and lowers its efficiency

The low overall efficiency of a steam power station of nearly 29% is attributed to a large amount of wasted heatin the condenser and other parts of plant. The heat loss in the condenser is unavoidable as heat energy cannot beconverted into mechanical energy

without temperature difference. The greater the temperature difference thegreater is the heat energy converted into mechanical energy

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MODIFIEDPROCESSESOF

CONVENTIONAL CYCLE

REHEAT CYCLEAllows us to increase boiler pressure without problems of low quality at turbine exit

REGENERATION

Preheats steam entering boiler using a

feedwater heater, improving

efficiencyAlso deaerates the fluid and

reduces large volume flow rates at

turbine exit.

OPEN FEED WATER HEATER

Regeneration is accomplished in all

large-scale, modern power plants

through the use of feedwater heaters.

In

open feedwater heaters, a small

amount of steam mixes directly with

the feedwater to raise its temperature

CLOSED FEED WATER HEATERFeedwater heating in open feedwater

heaters occurs by mixing of extraction steam and feedwater. Feedwaterheating can also be accomplished in shell/tube-type heat exchangers, where extraction steam does not mix with the feedwater. In closed feedwater heaters, feedwater passes through banks of tubes whereas steam condenses onthe external tube surfaces in these heaters. (Throttled Condensate & Pumped Condensate )

Reheating and closed feedwater

heaters

As the LP-turbine exhaust quality for open and closed heater

cycles are similar to the simple Rankine cycle areunacceptable

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REHEATCYCLE

Allows us to increase boiler pressure without problems of low quality at

Turbine Exit

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ReGENERATION

• Preheats steam entering boiler using a feedwater heater, improving efficiencyAlso deaerates the fluid

and reduces large volume flow rates at turbine exit.

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ReGENERATION

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Regenerative Rankine cycle with closed feedwaterheater and pumped condensate

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Regenerative Rankine cycle Reheat and one closed FWH

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HYSYSSIMULATION

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HYSYSSIMULATIONRESULT

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HYSYSSIMULATIONRESULT

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HYSYSSIMULATIONRESULT

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HYSYSSIMULATIONRESULT

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HYSYSSIMULATIONRESULT

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CONCLUSSION

Examination of a number alternative designs to upgrade the existing Khoms

Steam Plant done in order to

improve thermal and overall efficiencies is achieved by HYSYS. The efficiency

of Rankine cycle is improved by

using an intermediate reheat cycle in a number of configurations. A low

overall efficiency of a conventional

Rankin steam power plant of nearly 32.16 % is mainly attributed to a large

amount of wasted heat in condensers

and in other parts of the plant. The results indicate that configuration No.3

offers the highest efficiency and lesser

amount of energy consumption than other the configurations. Therefore,

modification of the original design

based on configuration No. 3 can improve the efficiency from 32.16% to 35%

resulting in reduced operation and

maintenance costs. The proposed modification has a positive impact on the

environment as it reduces gas

emissions as a result of decreasing the heating rate..