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Issue # 1: June 2008  
Expert comments on the Issue #1- Estimation of savings due to control of de-super heater water spray - Click Here
Solutions sent by users -

1 - M G Morshad,
2 - G Subramanyam,
3 - C M Bhagia,
4 - A V Dinesh,
5 - B S Sathiamoorthi Rao,
6 - P N B V Chalapathi Rao,
7 - R V G Rao,
8 - Pramath,
9 - Santosh M Mestry


Estimation of savings due to control of de-super heater water spray

Background:

A 140 MW thermal power generating unit, operating at 110 MW, was found to having main steam flow of 390 Ton/hr (TPH) at 120 kg/cm2(g) pressure and 536oC temperature (enthalpy = 822.9 kCal/kg). To control the super heat temperature, 30 TPH of water spray at 128 kg/cm2(g) and 170oC (enthalpy = 173.4 kCal/kg) was used in the de-super heater. The other operating parameters/ assumptions of the generating unit are as under:

Parameters/ Assumptions:

(a) Main steam required at the above main steam pressure & temperature to generate
      1 MW = 3.5 TPH.
(b) Specific coal consumption = 0.65 kg/kWh
(c) Coal GCV = 4,600 kCal/kg
(d) Landed coal cost = Rs. 1,800 per ton
(e) Expected steam consumption in the soot blowers after repair = 110 ton per day
(f) Average revenue realised = Rs. 2 per kWh generated
(g) Investment towards repairing of soot blowers = Rs. 4 crores
(h) Boiler efficiency = 80%
(i)Annual plant operating hours = 7000

Proposal:

The power plant plans to repair the existing steam soot blowers in order to improve the heat transfer within the boiler and to reduce the de-super heater water spray from 30 TPH to
7 TPH.

Issue:

What will be the energy and money saving potential if the above proposal is implemented by the power plant management?

Please send your solutions latest by 10th July 2008 to Mr. K. K. Chakarvarti, Manager – Power Plant Component at ppc@energymanagertraining.com

All the best solutions received will be posted on the website latest by 17th July 2008 alongwith the names of the contributors. - Word file