Texas A&M Universitys 36th Turbomachinery Symposium ABSTRACT. - - PowerPoint PPT Presentation

texas a m university s 36th turbomachinery symposium
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Texas A&M Universitys 36th Turbomachinery Symposium ABSTRACT. - - PowerPoint PPT Presentation

Effect of the Off-line Wash system for Gas Turbines Ruston TB5000 in high polluted conditions Carlos Daz, Fernando Aboites Dvila, Moiss Rocha CIATEQ, A.C., Turbomachinery Queretaro, Qro carlos.diaz@ciateq.mx PEMEX Refining


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SLIDE 1

Effect of the Off-line Wash system for Gas Turbines Ruston TB5000 in high polluted conditions

Carlos Díaz, Fernando Aboites Dávila, Moisés Rocha

CIATEQ, A.C., Turbomachinery Queretaro, Qro carlos.diaz@ciateq.mx

Texas A&M University’s 36th Turbomachinery Symposium

PEMEX Refining Turbomachinery Div. Mexico, D.F.

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SLIDE 2

This work shows the effect of an Off-line wash system with water based on the case of 3 gas turbines Ruston TB5000 located in high polluted conditions like ashes in the ambient, high humidity and temperature.

ABSTRACT. ABSTRACT.

This research was ran making periodical measurements of the principal turbo-pump’s variables values during 1 year of operation with nonstop charge conditions around 125 mbpd (millions of barrels per day) of gas L.P.

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SLIDE 3

All this data were inserted in a statistical program and then analyzed to create Temp./Discharge P. ratio curves and comparing with other cases, one washed with different system in the same polluted ambient and other without washed.

ABSTRACT. ABSTRACT.

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SLIDE 4

Due to their high polluted ambient the demand from the filter system is hard, and in some cases limited a very efficient wash system is required.

ABSTRACT. ABSTRACT.

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SLIDE 5

This case of study shows the effects for these turbines with a water based wash system in the off-line mode which some predictions were estimated by Basendwah A. [1] proposing this maintenance method as a very good way to reduce the consumption of fuel and to extend the period between overhauls. The turbomachinery department of CIATEQ [2] in Mexico and Conntect Inc. [3] from USA, developed a new wash system using water based and bio-degradable detergent as an alternative to the OEM’s system.

INTRODUCTION. INTRODUCTION.

[1] Basendwah A. Department of Power Engineering and Propulsion School of Engineering Cranfield University, England [2] CIATEQ is a mexican government company which is intended to support mexican industry [3] CONNTECT is a private USA Company which is related with the compressor washing

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SLIDE 6

INITIAL CONDITIONS INITIAL CONDITIONS

Transversal section schematic for the Ruston TB5000. EGT Lincoln, Uk.

Gas Generator Section Power Turbine Section

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SLIDE 7

T s

3 4 2 1

Work in Inlet heat Work Out Output heat

Considerations:

Using the Brayton Cycle and the performance principle:

in in

  • ut

H W W − = η

Where η = Performance Wout = Net Work Out Win = Work required by the compressor. Hin = Inlet heat from the fuel combustion.

INITIAL CONDITIONS INITIAL CONDITIONS

e Temperatur Operation Pressure Discharge s Station' =

a

η

Speed shaft Generator Gas the

  • f

Percentage Pressure Discharge s Station'

1 =

η

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SLIDE 8

INITIAL CONDITIONS INITIAL CONDITIONS

TWO TURBINES IN DIFFERENT STATIONS TWO STATIONS IN DIFFERENT ALTITUDE

Air filters Just Installed Air filters after 1 month working Environment Conditions: Ambient Temperature: Humidity: 20 to 40°C at noon 90% in summer

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SLIDE 9

INITIAL CONDITIONS INITIAL CONDITIONS

Operation Conditions Turbine 1 LPG Pump Station:

Date: 28/12/06 Qty Units Operation Hours: 110119 h Operation Temperature: 417 ºC Pressure Compressor Discharge (PCD): 52.3 Psi % of Gas Generador speed: 89 % Station’s Discharge Pressure: 48.6 kg/cm2 Station’s Discharge Flow: 11648 BPH

Turbine 2 LPG Pump Station:

Date: 28/01/07 Qty Units Operation Hours: 109196 h Operation Temperature: 429 ºC Pressure Compressor Discharge: 52.7 Psi % of Gas Generator Speed: 92 % Station’s Discharge Pressure: 50 kg/cm2 Station’s Discharge Flow: 11648 BPH

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SLIDE 10

A ire a 15 psi

Detergente a 7 bars

Valv . De S

  • brepresión

Valv. De S

  • br

e gir

  • C. De

Co mb. Int.

Dren

  • G. G.

T . P .

P anel de control

T anque de deter g ente

T anq ue pa r a agua de Enjuag u e C om pres

  • r

d e aire B

  • mba

C alentad or e léctrico

Bypass

WASH METHODOLOGY. WASH METHODOLOGY.

WASH SYSTEM SCHEMATIC

Wash Cart Nozzles System Drain System Surge Valve’s Hatching System Detergent and water tanks

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SLIDE 11

WASH METHODOLOGY. WASH METHODOLOGY.

Surge Control Valve Surge Control Valve Air from the wash cart Compressor Rotor Air Flow during Washing Air bleeding to seal zone Cutout Valve

Surge Surge Valve Valve’s Hatching System ’s Hatching System

This System works entering 20 psi, or less, pressure air to the surge valves in order to latch them and avoid the leakage during the wash

  • sessions. The operator need

just close one ball valve.

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SLIDE 12

WASH METHODOLOGY. WASH METHODOLOGY.

  • 1. Wash Session. Crank the compressor rotor

and inject detergent mixture (4 parts of demineralized water per 1 part of detergent) for 1 min because its starting motors may be damaged for a longer period.

  • 2. Suck time. Let the detergent for 20 min for

react with the dirt and fouling deposited on the blades and internals surfaces.

  • 3. Rinse Session. Crank the compressor again

for 1.5 min for rinse the first wash session,

  • 4. Repeat. If the drain liquid is dark it required to

inject more detergent mixture, and repeat the three first steps until the drain becomes clearer.

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SLIDE 13

RESULTS. RESULTS.

After the wash sessions these turbines were ran again and then go on with the

  • comparison. This comparison

was made once the turbine has reached the same flow and pressure in the discharge

Turbine 1 LPG Pump Station:

Date: 30/01/07 Qty Units Operation Hours: 110119 h Operation Temperature: 392.6 ºC Pressure Compressor Discharge (PCD): 47.5 PSI % of Gas Generador speed: 86.6 % Station’s Discharge Pressure: 48.6 kg/cm2 Station’s Discharge Flow: 392.6 BPH

Turbine 2 LPG Pump Station:

Date: 28/01/07 Qty Units Operation Hours: 109196 h Operation Temperature: 395 ºC Pressure Compressor Discharge: 49 PSI % of Gas Generator Speed: 90 % Station’s Discharge Pressure: 50 kg/cm2 Station’s Discharge Flow: 392.6 BPH

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SLIDE 14

RESULTS. RESULTS.

η0 = 48.6 [kg/cm2] / 392.5 [°C] = 0.1238 kg/cm2°C 24.4°C less to reach the same discharge pressure η1 = 48.6 [kg/cm2] / 90 % = .54 kg/cm2x100 rpm 2.4% = 240 rpm less in the G.G. to reach the same discharge pressure

Turbine Turbine 1’s 1’s Liquid Liquid drain drain Turbine Turbine 2’s 2’s Liquid Liquid drain drain

η0 = 50 [kg/cm2] / 395 [°C] = 0.1266 kg/cm2°C 34°C less to reach the same discharge pressure η1 = 50 [kg/cm2] / 86.6 % = .561 kg/cm2x100 rpm 2% = 200 rpm less in the G.G. to reach the same discharge pressure

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SLIDE 15

MaxVel/MaxTemp Comparison

0.205 0.21 0.215 0.22 0.225 25/04/2006 02/05/2006 09/05/2006 16/05/2006 23/05/2006 30/05/2006 06/06/2006 13/06/2006 20/06/2006 27/06/2006 04/07/2006 11/07/2006 Turbine without washing Turbine wased with ciateq- conntect skid Turbine washed with siemens-alstom wash skid

COMPARISON. COMPARISON.

The operation tendency comparison with another turbine which has not been washed is plotted as seen in the image below: Wash Wash Session Session

0.223 0.223 0.21 0.21

This This turbine turbine was was working working with with low low speed speed and and charge charge

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SLIDE 16

COMPARISON. COMPARISON.

Temperature Temperature decreasing decreasing with with alstom alstom-

  • siemens

siemens wash wash system system: : From From 460 460°C °C to to 440 440°C °C = 20 = 20°C °C less less G.G G.G. SPEED AT 90% . SPEED AT 90% Temperature Temperature decreasing decreasing with with ciateq ciateq-

  • conntect

conntect wash wash system system: : From From 429 429°C °C to to 395 395°C °C = 34 = 34°C °C less less G.G G.G. SPEED FROM 92% TO 90% . SPEED FROM 92% TO 90%

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SLIDE 17