IHI PCC Technologies Demonstration at a Coal-fired Power Plant

18
Copyright © 2019 IHI Corporation All Rights Reserved. 17th.Sep.2019 IHI PCC Technologies Demonstration at a Coal-fired Power Plant 1 Takumi Endo a* , Jun Arakawa a , Wonyoung Choi a , Kenji Takano a , Hisashi Tomita a , Aaron Cottrell b , Paul Feron b , Sanger Huang b a : IHI Corporation b : CSIRO Energy 5 th Post Combustion Capture Conference (PCCC5)- Kyoto 2019

Transcript of IHI PCC Technologies Demonstration at a Coal-fired Power Plant

Page 1: IHI PCC Technologies Demonstration at a Coal-fired Power Plant

Copyright © 2019 IHI Corporation All Rights Reserved.

17th.Sep.2019

IHI PCC Technologies Demonstration

at a Coal-fired Power Plant

1

Takumi Endoa*, Jun Arakawaa, Wonyoung Choia, Kenji Takanoa,

Hisashi Tomitaa, Aaron Cottrellb, Paul Feronb, Sanger Huangb

a: IHI Corporationb: CSIRO Energy

5th Post Combustion Capture Conference (PCCC5)- Kyoto 2019

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1. PICA project

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3

IHI Corporation・ Design, construction, operation and evaluation

of the PCC pilot plant / IHI system

AGL Loy Yang Pty Ltd・ Operator of Loy Yang A Power Station using brown coal

・ Host of PCC pilot plant in this power plant.

CSIRO (the Commonwealth Scientific and Industrial Research Organisation)

・ Supporting design, site preparation, operation and evaluation of the pilot

plant / CSIRO system

PICA (Post-combustion carbon capture, IHI, CSIRO, AGL)

Organization and roles

BCIA

IHI CSIRO AGL

Loy Yang

Steering committee

IHI,CSIRO and AGL

Partially funded by BCIA (Brown Coal Innovation Australia is

succeeded by Australian Carbon

Innovation)

Loy Yang A Power Station & Loy Yang coal mine

Australia

Victoria

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• Evaluate performance of advanced PCC system:

• Energy efficiency performance,

• CO2 capture ratio,

• Evaluate effects of the long term operation:

• Operation stability,

• Reliability,

• Breakdown products and treatments,

• Assess the environmental impacts :

• Emission measurement/ analysis,

• Evaluation of emission reduction technologies

PICA Project technical aims

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- Design, construction and commission of PICA pilot plant

- Operation using IHI’s advanced system

- Operation using CSIRO’s advanced system

Tasks & schedule

2015 2016 2017 2018 2019

1 Construction/Test of plant

(by IHI in Japan)

Transport of the plant

to Australia

2 Re-construction and re-

commission in Loy Yang A power

station

3 Operation using IHI’s

solvent/process

4 Operation using CSIRO’s

solvent/process

Scope of this presentation

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2. IHI PCC technologies

and PICA Pilot Plant

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・ With IHI technologies, approx. 40% reduction in CO2 capture energy

was achieved compared to the conventional technology by 2014.

IHI 20TPD Pilot Plant

100

62

0

20

40

60

80

100

120

Conventionaltechnology

IHI's advancedtechnology

Ene

rgy

con

sum

pti

on

[%]

Energy Saving

Approx. 40%

MEA 30wt%

Conventional Process

Normal Packing

IHI solvent

IHI Process

IHI Packing

IHI PCC Technology performance by 20TPD P.P.

Advanced

Packing

System

Advanced

Solvent

PCC

Technology

Advanced

Process

IHI packing

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Flue gas flow rate 80 Nm3/h

CO2 capacity 0.4 t-CO2/d

Capture ratio 90%

Absorber dia. 0.125 m

Packing type IHI proprietary packing

Process

configurations

-Conventional process

-IHI advanced process

-CSIRO advanced process

Design standards JIS, AS, ASME

Emissions

measurement

Continuous FTIR

Continuous NDIR

Schematics/specs of PICA Pilot Plant

Conventional,

IHI advanced, and

CSIRO advanced

process can be applied

(Schematic view)(PICA pilot plant)

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PICA Pilot Plant in Loy Yang A Power plant

ID Fan

Flue gas duct

StackID

FanStackESP

PICA

Pilot Plant

Flue gas duct

Boiler

Unit 2

PICA Pilot Plant

Flue gas →

flue gas line to

PICA pilot plant

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3. Results

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Last Result and next challenge

1. The 5,000-hour-operation using IHI advanced system

completed by the end of Mar. 2017.

Stable Operation at high CO2 absorbing efficiency for Long Term

Period can be performed.

2. Observed heat stable salts formation rate in ISOL-162 was

considerably less than that of MEA.

ISOL-162 have a potential to reduce the deterioration of Amine

solvent.

3. Significant reduction in amine emission was observed in

specific wash process conditions.

More environmental friendly process can be proposed.

Next Challenge 1

Next Challenge 2

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Next Challenge 1

:Reduce the solvent deterioration

0

0.2

0.4

0.6

0.8

1

1.2

1.4

1.6

0 1,000 2,000 3,000 4,000 5,000

Norm

arize

d H

SS C

oncentr

ation [

-]

Operation Hours [h]

2016

0

0.2

0.4

0.6

0.8

1

1.2

1.4

1.6

0 1,000 2,000 3,000 4,000 5,000

Norm

arize

d H

SS C

oncentr

ation [

-]

Operation Hours [h]

2016

2018

Reduce to 30% of original

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Next Challenge 2

:Reduce the Amine Emission

Emission

Washing

Tower

Measurement of amine emissions from IHI system were conducted

on different wash process conditions.

Significant reduction in amine

emission was observed in specific

wash process conditions.

Wash

Process Variation

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Next Challenge 2:Reduce Emission

Target analytes: Amines.

<Wash process: Number of beds/Circulation rate, circulation liquids>

Pre-

Treatment

Tower

Absorber

Stripper

Washing

Tower

Outlet Flue Gas

Product CO2

Reboiler

Cooler

Lean Amine Pump

Rich Amine Pump

Blower

Condenser

Washing tower outlet

Absorber outlet

Impinger set

Sampling point

Sampling

port

Ball valve

Cooler box

Filter

paper

Silica-gel

trap

Impinger train

Ball valve

Needle

valve

To gas

sampling unit

Charged

solution

Conditions:

- Without Wash(Abs. out)

- Washing Type 1

- Washing Type 2

- Washing Type 4

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Next Challenge 2:Reduce Emission

0

0.2

0.4

0.6

0.8

1

1.2

Without Wash

(Abs.out)

Wash

Type 1

0.012 0.009

1

Em

issio

n R

atio

[-]

(Relative value of emission where

the value for No Wash condition =1)

Wash

Type2

0

0.2

0.4

0.6

0.8

1

1.2

1

0.18Em

issio

n R

atio

[-]

Wash

Type2

Wash

Type4

(Relative value of emission where the

value for Wash Type 2 condition =1)

Wash Type 1 and Wash Type 2 allow to reduce the

Amine emission significantly.

With further development from Wash Type 2 to Wash

Type 4, the emission could be reduced to

approximately one fifth.

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5. Summary & Conclusions

Through the long term stable operation at PICA pilot plant with the

project team(IHI, CSIRO and AGL Loy Yang) in Loy Yang A Power

Station, Australia in 2017-2019, we have developed as follows,

1. ISOL-162α(2018) can decrease solvent deterioration other than

former ISOL-162.

2. Various Wash types are evaluated and then Wash Type 4 can

reduce the amine emission significantly.

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Acknowledgements

The Authors wish to acknowledge

- Brown Coal Innovation Australia Limited (BCIA)

- Australian National Low Emissions Coal Research and

Development Ltd. (ANLEC R&D)

- the Victorian State Government

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Thank you for your attention !

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