Gas turbine power plant with flue gas recirculation and catalytic converter

Patent metadata

Field	Value
Publication number	US-9964003-B2
Application number	US-201514591434-A
Country	US
Kind code	B2
Filing date	Jan 7, 2015
Priority date	Jul 13, 2012
Publication date	May 8, 2018
Grant date	May 8, 2018

Abstract

The invention pertains to a power plant including a gas turbine, a heat recovery boiler arrangement with at least a boiler inlet, and an outlet side with a first exit connected to a stack and a second exit connected to a flue gas recirculation, which connects the second exit to the compressor inlet of the gas turbine. The heat recovery boiler arrangement includes a first boiler flue gas path from the boiler inlet to the first boiler exit, and a separate second boiler flue gas path from the boiler inlet to the second boiler exit. Additionally, a supplementary firing and a subsequent catalytic NOx converter are arranged in the first boiler flue gas path. Besides the power plant a method to operate such a power plant is an object of the invention.

First claim

The invention claimed is:

1. A power plant, comprising:
a gas turbine including a compressor, a combustor and a turbine;
a heat recovery boiler arrangement with at least a boiler inlet connected to a turbine outlet, and an outlet side with a first exit connected to a stack and a second exit connected to a flue gas recirculation which connects the second exit to an inlet of the compressor, wherein the heat recovery boiler arrangement includes:
a first boiler flue gas path from the boiler inlet to the first boiler exit;
a separate second boiler flue gas path from the boiler inlet to the second boiler exit, and
a supplementary firing and a subsequent catalytic NOx converter in the first boiler flue gas path;
wherein the catalytic NOx converter includes a NOx adsorbing catalyst,
wherein the first boiler flue gas path is divided into at least two sectors with at least two supplementary sector firings installed upstream of the NOx adsorbing catalyst in the at least two separate sectors, with independent fuel supply control for the supplementary sector firings, to allow independent operation of the supplementary sector firings in each sector for regeneration of the subsequent NOx adsorbing catalyst.

2. The power plant according to claim 1 , wherein the gas turbine includes a diffuser arranged downstream of the turbine and upstream of the heat recovery boiler arrangement and the first boiler flue gas path includes a first sector, which connects a diffusor inlet to the NOx adsorbing catalyst, for loading the NOx adsorbing catalyst with NOx from a gas turbine flue gas and a second sector which connects the diffusor inlet to the NOx adsorbing catalyst, with the supplementary firing installed between the diffusor inlet and NOx adsorbing catalyst for regenerating the NOx adsorbing catalyst.

3. The power plant according to claim 1 , wherein the heat recovery boiler arrangement includes a control member arranged to control a mass flow split between flue gas entering the first boiler flue gas path and the separate second boiler flue gas path.

4. The power plant according to claim 1 , wherein a compressor intake is split into sectors connected with a flow passage of the compressor, with a fresh air intake sector leading fresh air to the inlet of the compressor, and with flue gas intake sector leading recirculated flue gas flow to the inlet of the compressor.

5. A method for operating a power plant with a gas turbine with at least a compressor, a combustor and a turbine,
a heat recovery boiler arrangement with at least a boiler inlet connected to a turbine outlet, and an outlet side with a first exit connected to a stack and a second exit connected to a flue gas recirculation, which connects the second exit to an inlet of the compressor; the method comprising:
splitting the flue gas into two flows in the heat recovery boiler arrangement, with a first boiler flue gas path flow flowing from the boiler inlet to the first boiler exit and a second boiler flue gas path flow flowing from the boiler inlet to the second boiler exit;
recirculating the second boiler flue gas path flow from the second boiler exit into the compressor inlet of the gas turbine;
reducing the oxygen content in at least a fraction of the first boiler flue gas path flow at least for a period of time by a supplementary firing and in that NOx is removed from the first boiler flue gas path flow in a catalytic NOx converter before the first boiler flue gas path flow is released from the first boiler exit;
wherein the NOx is removed in a NOx adsorbing catalyst;
wherein the first boiler flue gas path flow is further divided into sectors with at least one supplementary firing arranged in each sector; and
turning the supplementary sector firings alternatingly on and off to respectively regenerate the corresponding sector of the NOx adsorbing catalyst and load the corresponding sector of the NOx adsorbing catalyst with NOx.

6. The method according to claim 5 , comprising:
feeding the fraction of the first boiler flue gas path flow with reduced oxygen content to a first sector in the NOx adsorbing catalyst for regeneration of the first sector of the NOx adsorbing catalyst; and
feeding a remaining first boiler flue gas path flow to a second sector of the NOx adsorbing catalyst, wherein NOx is removed from the first boiler flue gas path flow in the first sector as well as in the second sector of the NOx adsorbing catalyst.

7. The method according to claim 5 , comprising:
turning the supplementary firing alternatingly on for regeneration of the adsorbing catalyst and off to minimize fuel consumption while the adsorbing catalyst is filling with NOx.

Assignees

• Ansaldo Energia Ip Uk Ltd

Inventors

• Benz Eribert
• Döbbeling Klaus
• Hoevel Michael

Classifications

• F02C6/18

  using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants (using waste heat as source of energy for refrigeration plants F25B27/02; using the waste heat of a gasturbine for steam generation or in a steam cycle see F01K23/10) · CPC title

• F02C3/34 Primary

  with recycling of part of the working fluid, i.e. semi-closed cycles with combustion products in the closed part of the cycle · CPC title

• F01K23/103 Primary

  with afterburner in exhaust boiler · CPC title

• F05D2270/082

  with as little NOx as possible · CPC title

• F01N3/28

  Construction of catalytic reactors · CPC title