CFB-FGD f 660MW C lFGD for 660MW Coal-fi d U itfired … 2014/CFB-FGD for...CFB-FGD f 660MW C lFGD...

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CFB FGD f 660MW C l fi dU it CFB-FGD for 660MW Coal-fired Units Introduction of Hanfeng Project Introduction of Hanfeng Project ji E i T h l Lonjing Environment T echnology Dr. Jianchun Wang

Transcript of CFB-FGD f 660MW C lFGD for 660MW Coal-fi d U itfired … 2014/CFB-FGD for...CFB-FGD f 660MW C lFGD...

Page 1: CFB-FGD f 660MW C lFGD for 660MW Coal-fi d U itfired … 2014/CFB-FGD for...CFB-FGD f 660MW C lFGD for 660MW Coal-fi d U itfired Units Introduction of Hanfeng ProjectIntroduction of

CFB FGD f 660MW C l fi d U itCFB-FGD for 660MW Coal-fired UnitsIntroduction of Hanfeng ProjectIntroduction of Hanfeng Project

ji E i T h lLonjing Environment TechnologyDr. Jianchun Wang

Page 2: CFB-FGD f 660MW C lFGD for 660MW Coal-fi d U itfired … 2014/CFB-FGD for...CFB-FGD f 660MW C lFGD for 660MW Coal-fi d U itfired Units Introduction of Hanfeng ProjectIntroduction of

FujianLongking Introduction of Hanfeng Project

Content - Background

- Design

- Construction- Construction

- Commissioningg

- Operation

- By-product utilization

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FujianLongking Introduction of Hanfeng Project

B k dBackground

Project : Hanfeng 2X660MW Power Plant FGD Retrofit Project

Boiler: 2 boilers, 660MW each, FW supply, Peak load operation.pp y p

Fuel: Anthracite + lean coal, 1.5% sulfur content.

Conditions:

- Low space available- Low space available

- Water shortage region

Short outage time required- Short outage time required

CFB FGD t f L ki d t dCFB-FGD system from Longking was adopted

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FujianLongking Introduction of Hanfeng Project

Content - Background

- Design

- Construction- Construction

- Commissioningg

- Operation

- By-product utilization

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FujianLongking Introduction of Hanfeng Project

D iDesign

Item Unit Value

Flue gas temperature (inlet) ℃ 135

Flue gas flow rate (inlet) Nm3/h 2,550,000

SO2 concentration (inlet) mg/Nm3 (STD, 6%O2) 3200

Dust concentration (inlet) mg/Nm3 1000Dust concentration (inlet) mg/Nm 1000

DeSOx efficiency % ≥90

SO2 concentration (outlet) mg/Nm3(STD, 6%O2) ≤200

D t t ti ( tl t) /N 3 30Dust concentration (outlet) mg/Nm3 ≤30

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FujianLongking Introduction of Hanfeng Project

D iDesign

Physical modeling of flue path to improve and verify the design

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FujianLongking Introduction of Hanfeng Project

D i Layout DrawingDesign

Reactor Fabric filter

Fabric filter

Hydrated lime silo Lime silo

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FujianLongking Introduction of Hanfeng Project

Content - Background

- Design

- Construction- Construction

- Commissioningg

- Operation

- By-product utilization

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FujianLongking Introduction of Hanfeng Project

C t tiConstruction

Transport/Package

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FujianLongking Introduction of Hanfeng Project

C t ti The construction progress 1Construction

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FujianLongking Introduction of Hanfeng Project

C t ti The construction progress 2Construction

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FujianLongking Introduction of Hanfeng Project

C t ti The end of construction (Oct. 2008)Construction

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FujianLongking Introduction of Hanfeng Project

Content - Background

- Design

- Construction- Construction

- Commissioningg

- Operation

- By-product utilization

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FujianLongking Introduction of Hanfeng Project

C i i iCommissioning

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FujianLongking Introduction of Hanfeng Project

C i i i13th Dec. 2008, unit 2# went through 168h commissioning.

Commissioning

31th Dec. 2008, unit 1# went through 168h commissioning.

EPC project, 11 months in total

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FujianLongking Introduction of Hanfeng Project

Content - Background

- Design

- Construction- Construction

- Commissioningg

- Operation

- By-product utilization

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FujianLongking Introduction of Hanfeng Project

O ti Performance Acceptance CertificationOperation

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FujianLongking Introduction of Hanfeng Project

O ti

序号 项目名称 单位设计 实际运行

Performance Acceptance Certification DataOperation

序号 项目名称 单位1#炉 2#炉 1#炉 2#炉

1 机组大小 MW 660 660

2 设备可用率 % 97 982 设备可用率 % 97 98

3 脱硫入口烟气量 万Nm3/h 255 229.9 223.6

4 脱硫入口烟气温度 ℃ 135 122.7 124.3

5 脱硫入口含尘量 mg/Nm3 200 764 729.9

6 脱硫入口SO2浓度 mg/Nm3 3200 2741.4 2434.2

7 脱硫出口烟气温度 ℃ 70 71.7 72.5脱硫出口烟气温度 ℃ 0 5

8 脱硫出口含尘量 mg/Nm3 50 8.5 8.2

9 脱硫出口SO2浓度 mg/Nm3 400 190.7 133.5

脱硫效率10 脱硫效率 % 90 93.04 94.52

11 石灰消耗量 t/h 9.6 9.58 9.76

12 水消耗量 t/h 101.4 82.98 82.65

13 脱硫系统电耗 kW 8600 7946.5 7819

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FujianLongking Introduction of Hanfeng Project

Content - Background

- Design

- Construction- Construction

- Commissioningg

- Operation

- By-product utilization

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FujianLongking Introduction of Hanfeng Project

B d t tili tiBy-product utilization

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FujianLongking Introduction of Hanfeng Project

B d t tili tiBy-product utilization

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FujianLongking Introduction of Hanfeng Project

Thank youThank youyy