REDUCING THE LOAD CONSUMED BY GAS TURBINE COMPRESSOR AND MAXIMIZING TURBINE MASS FLOW

Abstract

The invention is applicable to industrial gas turbines to reduce the load consumed by the gas turbine compressor and to maximize the turbine mass flow.

Description

TECHNICAL FIELD

This invention is applicable to industrial gas turbines, and looking into reducing the load consumed by gas turbine COMPRESSOR and maximizing turbine MASS FLOW.

BACKGROUND ART

Improving gas turbines overall efficiency efforts have no limit, and more efforts are taking placed in this field, as this will lead to increase in power generated by gas turbine and reduces fuel consumption for that power.

The main problem avoiding gas turbine overall efficiency improvement is that, air compressor alone consumes most of the power being generated by the turbine. Moreover gas turbine air mass flow cannot be maximized without increasing compressor load consumption.

SUMMARY OF THE INVENTION

From example below and from steam table, it can be seen that air at compressor outlet is superheated. Excess superheating increases compressor load consumption. Therefore reducing compressor air outlet temperature and pressure safely above saturation point before leaving the compressor will reduce compressor load consumption, and will increase gas turbine overall efficiency. This can be done by injection high pressure water relatively cold into air compressor as shown in drawing (1).

Moreover, gas turbine mass flow rate can be maximized by increasing the temperature of the high pressure water being injected into the compressor as shown in the example. Increase in gas turbine mass flow will further increase gas turbine overall efficiency.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows a schematic view of the system of the present invention including a gas turbine main parts, air compressor, combustion chamber, turbine, electrical generator, and high pressure water injection system.

DETAILED DESCRIPTION OF THE DRAWINGS

FIG. 1 shows gas turbine main parts and contains, air compressor (1), combustion chamber (2), turbine #), electrical generator (4) and, the high pressure water injection system (5).

For the invention implementation, the High-pressure water injection system (5) is introduced into the gas turbine (3). At compressor (1) last stages, High-pressure injectors to be hosted between the stationary compressor blades. The high pressure nozzles are to be connected to high pressure water injection system (5). A temperature controlling device for the high pressure water being injected into the compressor (1) is essential.

DESCRIPTION OF ONE SPECIFIC EXAMPLE OR EMBODIMENT OF THE INVENTION

For a Gas turbine having the followings:

T1: Compressor-air inlet temperature ° K=283° K

T2: Compressor-air outlet temperature ° K=547° K

P2: compressor air outlet pressure=12 bar

T3: Gas turbine inlet temperature ° K=1258° K

T4: Gas turbine outlet temperature ° K=768° K

nad: adiabatic efficiency

CALCULATION

1^st: improving gas turbine efficiency by reducing energy consumed by air compressor.

From steam table the following can be extracted:

Water vapor at 12 bar and compressor outlet temperature of (274° C.)=547 ° K is in the superheated zone.

Saturation Temperature=192° C.=465° K

Degree of Superheat=547−465=82 degree

Therefore compressor air outlet temperature can be reduced by 70 degrees from 547° K to 477° K without de-superheating it.

Turbine adiabatic efficiency ηad=1−(T4−T1)/(T3−T2) . . . (Brighton cycle)

The adiabatic efficiency of the gas turbine ηad=32%

Table below shows the improvement in the adiabatic efficiency from 32% to 38% in relation to drop in compressor outlet temperature from 547° K to 477° K.

	T2 ° K
	547	537	527	517	507	497	487	477
ηad %	32	33	34	35	35	36	37	38

2^nd: Improvement gas turbine overall efficiency by increasing turbine mass flow.

From gas turbine overall thermal efficiency equation where

ηt: Turbine thermal efficiency

Wt: Work done by gas turbine=(Ma+Mf) (h3−h4)

Wc: Load consumed by compressor=Ma (h2−h1)

h: air specific heat

Ma: Air mass flow rate from compressor

Mf: Fuel mass

Mw: Mass of high pressure water injected in compressor

ηt=[(Wt−Wc)/Wt]×100=1−[Ma(h2−h1)/Ma+Mw+Mf(h3−h4)]×100

From the above equation it can be seen that the increase in injected water mass (Mw) will increase gas turbine overall efficiency.

3^rd: Improving gas turbine overall efficiency by maximizing turbine mass flow.

From fluid mixture equation

Taw=(MaTa+MwTw)/(Ma+Mw)

Therefore Mw=Ma(Ta−Taw)/(Taw−Tw)

Where:

Taw: Required air water mixture temperature=477° K

Ta: Compressor air outlet temperature=547° K

Tw: Injected water temperature=288° K

Mw/Ma=Water mass to air mass

Therefore the required mass of high pressure water injected to reduce compressor outlet temperature from 547° K to 477° K is Mw=0.37 Ma.

The below table shows the increase in injected water mass rate in relation to air mass flow rate corresponding to increase in injected water inlet temperature.

	Tw ° K
	288	300	350	400	450	460	470	475	477
Mw/	0.37	0.40	0.55	0.91	2.59	4.11	10	35	Infinity
Ma

Claims

1-2. (canceled)

3. A process for reducing a compressor load consumption of a gas turbine comprising the steps of: injecting a high pressure cold water into a compressor to reduce an air outlet temperature and pressure above a saturation point before leaving the compressor.

4. The process according to claim 3, further including the steps of adjusting a temperature of the high pressure cold water being injected into the compressor in order to increase the improvement in gas turbine overall efficiency.

5. A system to reduce a compressor load consumption of a gas turbine comprising: an electric generator;a turbine having a first end operatively connected to the electric generator;a compressor connected to a second end of the turbine;an injection device located between the turbine and the compressor;wherein the injection device includes nozzles to inject a high pressure cold water into the compressor.

6. the system according to claim 5, further including a temperature controlling device connected to the injection device to control the temperature of the high pressure cold water.