Method and a system for recovering thermal energy in a system comprising a chemical recovery boiler and a lime kiln

Patent metadata

Field	Value
Publication number	US-10920622-B2
Application number	US-201816760606-A
Country	US
Kind code	B2
Filing date	Nov 30, 2018
Priority date	Dec 13, 2017
Publication date	Feb 16, 2021
Grant date	Feb 16, 2021

Abstract

Disclosed is a system for producing electricity, the system comprising a chemical recovery boiler adapted to supply superheated steam to a steam turbine driving a generator, the chemical recovery boiler comprising a first flue discharge channel with a first heat exchanger arrangement; and a lime kiln comprising a second flue discharge channel with a second heat exchanger arrangement; and a circulation for heat transfer medium between the said heat exchanger arrangements. Also disclosed is a method for producing electricity, wherein said heat transfer medium is circulated between said heat exchanger arrangements such that thermal energy may be transferred from the flue gases in the first flue charge channel and/or the second flue discharge channel into the feed water of the chemical recovery boiler and/or into a heat-consuming process.

First claim

The invention claimed is:

1. A system for producing electricity, the system comprising:
a chemical recovery boiler adapted to supply superheated steam to a steam turbine driving a generator, the chemical recovery boiler comprising:
a first flue gas discharge channel adapted to discharge the flue gases of the chemical recovery boiler, and
a first heat exchanger arrangement arranged in the first flue gas discharge channel and adapted to recover thermal energy from the flue gases of the chemical recovery boiler;

a lime kiln adapted to oxidize calcium carbonate (CaCO 3 ) of lime mud to produce lime (CaO), the lime kiln comprising:
a second flue gas discharge channel adapted to discharge the flue gases of the lime kiln, and
a second heat exchanger arrangement arranged in the second flue gas channel and adapted to recover thermal energy from the flue gases of the lime kiln; and

a circulation for heat transfer medium, the circulation comprising:
the first heat exchanger arrangement,
the second heat exchanger arrangement, and
a pipeline adapted to convey at least some of the heat transfer medium between the first heat exchanger arrangement and the second heat exchanger arrangement.

2. The system according to claim 1 , wherein the circulation for the heat transfer medium further comprises at least a primary heat exchanger downstream from the second heat exchanger arrangement and before the first heat exchanger arrangement, the primary heat exchanger adapted to transfer thermal energy from the heat transfer medium into the feed water of the chemical recovery boiler.

3. The system according to claim 1 , wherein:
the pipeline is configured to convey at least some of the heat transfer medium from the first heat exchanger arrangement to the second heat exchanger arrangement, and
the circulation for the heat transfer medium further comprises one or more secondary heat exchangers, the one or more secondary heat exchangers arranged downstream from the second heat exchanger arrangement and before the first heat exchanger arrangement and adapted to transfer thermal energy from the heat transfer medium to a heat-consuming process.

4. The system according to claim 3 , wherein the heat-consuming process comprises heating lignin slurry.

5. The system according to claim 1 , comprising a feed water pump, wherein:
the circulation for the heat transfer medium further comprises a superheater, the superheater adapted to produce superheated steam and arranged in a chemical recovery boiler, and
the first heat exchanger arrangement and the second heat exchanger arrangement are arranged in the circulation for the heat transfer medium in between the feed water pump and the superheater.

6. The system according to claim 1 , the system further comprising:
a line branching off from the circulation for the heat transfer medium in between the first heat exchanger arrangement and the second heat exchanger arrangement, and
at least a tertiary heat exchanger adapted to recover thermal energy from the line.

7. The system according to claim 6 , wherein the tertiary heat exchanger is configured to transfer thermal energy into the feed water of the chemical recovery boiler, into the combustion air of the chemical recovery boiler and/or into another heat-consuming process.

8. The system according to claim 1 , the system further comprising at least one of:
a first filtering arrangement in the first flue gas discharge channel, the first filtering arrangement configured to clean flue gases and arranged in the flow direction of the flue gases before the first heat exchanger arrangement, or
a second filtering arrangement in the second flue gas discharge channel, the second filtering arrangement configured to clean flue gases and arranged in the flow direction of the flue gases before the second heat exchanger arrangement.

9. A method for producing electricity, the method comprising:
supplying superheated steam with a chemical recovery boiler to a steam turbine driving a generator, the chemical recovery boiler comprising:
a first flue gas discharge channel adapted to discharge the flue gases of the chemical recovery boiler, and
a first heat exchanger arrangement arranged in the first flue gas discharge channel and adapted to recover thermal energy from the flue gases of the chemical recovery boiler;

oxidizing calcium carbonate (CaCO 3 ) of lime mud to produce lime (CaO) with a lime kiln, the lime kiln comprising:
a second flue gas discharge channel adapted to discharge the flue gases of the lime kiln, and
a second heat exchanger arrangement arranged in the second flue gas channel and adapted to recover thermal energy from the flue gases of the lime kiln; and

circulating heat transfer medium in a heat transfer medium circulation, the circulation comprising:
the first heat exchanger arrangement,
the second heat exchanger arrangement, and
a pipeline adapted to convey at least some of the heat transfer medium between the first heat exchanger arrangement and the second heat exchanger arrangement.

10. The method according to claim 9 , wherein:
the circulation for the heat transfer medium further comprises at least a primary heat exchanger downstream from the second heat exchanger arrangement and before the first heat exchanger arrangement, and
the method further comprises transferring thermal energy with the primary heat exchanger from the heat transfer medium into the feed water of the chemical recovery boiler.

11. The method according to claim 9 , wherein:
the pipeline is configured to convey at least some of the heat transfer medium from the first heat exchanger arrangement to the second heat exchanger arrangement,
the circulation for the heat transfer medium further comprises one or more secondary heat exchangers, the one or more secondary heat exchangers arranged downstream from the second heat exchanger arrangement and before the first heat exchanger arrangement, and
the method further comprises transferring thermal energy with the one or more secondary heat exchangers from the heat transfer medium to a heat-consuming process.

12. The method according to claim 11 , wherein the heat-consuming process comprises heating lignin slurry.

13. The method according to claim 9 , further comprising a feed water pump, wherein:
the circulation for the heat transfer medium further comprises a superheater, the superheater adapted to produce superheated steam and arranged in a chemical recovery boiler, and
the first heat exchanger arrangement and the second heat exchanger arrangement are arranged in the circulation for the heat transfer medium in between the feed water pump and the superheater.

Assignees

• Valmet Technologies Oy

Inventors

• Mansikkasalo Jarmo

Classifications

• Y02P40/40

  Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills · CPC title

• F01K13/00 Primary

  General layout or general methods of operation of complete plants · CPC title

• D21C11/12

  Combustion of pulp liquors · CPC title

• F22D1/32

  arranged to be heated by steam, e.g. bled from turbines · CPC title

• F01K11/02 Primary

  the engines being turbines · CPC title