THERMAL ENGINEERING & TECHNOLOGY DEVELOPMENT DIVISION, CEA

Similar documents
Meeting New Environment Norms - Challenges and Possibilities. Presented by: A.K.Sinha General Manager NTPC Limited

Worldwide Pollution Control Association. August 3-4, 2010

New Indian emissions requirements: Advanced DeSOx solutions for a sustainable power generation

Emission Control for Power Sector in the Pearl River Delta (PRD) Region, China (#46)

SCR for NO x Control in Coal-fired Power Plants

Post Combustion CO 2 Capture Scale Up Study

POWER PLANT AIR QUALITY CONTROL and FLY ASH QUALITY & AVAILABILITY

The Future of Coal Ash

LICONOX Linde s new technology for removal of NOx and SOx integrated in the CO 2 processing unit

Operating Experience of Circulating Fluidized Bed Scrubbing Technology in Utility Size Power Plants

Flue Gas Desulphurization (FGD) plant 2 x 600 MW Coal based Thermal power plant Cuddalore, Tamil Nadu. By MK Parameswaran 23 rd Dec, 2016

Integrating ADAir Mixer Technology to Optimize System Performance with DSI Applications

Worldwide Pollution Control Association

Flue Gas Desulphurisation -Commissioning & Operation "A New Beginning in NTPC" By

Projects in NRW. Development of Power plant technology at the Ruhr area using the example of Evonik Steag

NOx processing experiences for removal in the CO 2 plant for the Oxyfuel combustion process

Excerpt of Thermal Power Guidelines for New Plants

Customized Solutions for Environmental Compliance. Combining proven experience, technology and reliable performance for our customers

Economics of Lime and Limestone for Control of Sulfur Dioxide

CANSOLV SO2 Scrubbing System - 10 Years of Reliable Operation Integration with SRU Tail Gas Incineration

Panel II Jänschwalde Oxyfuel demonstartion plant.

WHITE PLUME REMOVAL USING FUEL ADDITIVES IN THERMAL POWER PLANTS

ESKOM APPLICATION FOR EXEMPTION FROM THE MINIMUM EMISSIONS STANDARDS FOR THE KRIEL POWER STATION. DATE: 28 October 2013

Zero Liquid Discharge Effluent Guidelines Compliance Strategies for Coal-Fired Power Plants FGD Wastewater

INTERNATIONAL O&M CONFERENCE

Biomass Boiler Emission Abatement Technologies. Simon Wakefield

Demonstrating CCS in Italy The Zero Emission Porto Tolle Project

Catalytic Activated Ceramic Dust Filter a new technology for combined removal of dust, NOx, dioxin, VOCs and acids from off gases.

Senator Thomas Carper 513 Hart Building Washington, DC November 3, Dear Senator Carper:

Adoption of USC CFB Technology to Achieving Lower Cost Generation and Environmental Sustainability. Gerd Heiermann & Douglas Spalding

Diode laser analyser LS4000 Ammonia slip measurement for DeNOx process

Circulating Fluidised Bed Technology for Indian and other coals Dr John Topper IEA Clean Coal Centre, London

Steinmüller Engineering Conference Modernization and Optimization of Flue Gas Cleaning Plants

Environmental Improvement Plan. Sohar Refinery

COAL WATER SLURRY FUEL Alternate Fuel for Thailand

Particulate Emission Monitoring HN Pathak Supdtg Engr Madhya Pradesh Power Generation Co. Ltd

FLUE GAS DESULFURIZATION FOR 2 X 6 MW COAL FIRED POWER PLANT

Mercury and SO3 Mitigation Issues for Scrubber Technology

The Introduction of Foster Wheeler s 660 MWe Supercritical CFBC Technology for the India Market

Evaluation of Carbonate Looping. for Post-Combustion CO 2 -Capture from a Utility's Perspective. Energie braucht Impulse

Optimal Design and Operation of SNCR System for a 150t/h CFB Boiler and Discussion on the Measurement of Flue Gas Components

The Growth of Dry Sorbent Injection (DSI) and the impact on Coal Combustion Residue

Integrated Environmental Controls - Program 75

Effluent Guidelines and Water Quality Management - Program 56

Using Hydrated Lime and Dolomite for Sulfur Dioxide Removal from Flue Gases

CHAPTER 65 AIR POLLUTION-CONTROL TECHNOLOGIES

GE solutions for NOx compliance and increased availability for WtE / Biomass plants

WET FLUE GAS DESULFURIZATION (FGD) SYSTEMS ADVANCED MULTI-POLLUTANT CONTROL TECHNOLOGY

SCR RETROFIT FOR NO X REDUCTION EXPERIENCES IN CHINA & POLAND TWO COUNTRIES WITH COAL AS DOMINATING FUEL SOURCE

FACT SHEET. Whelan Energy Center 4520 East South Street Hastings, Nebraska March 26, 2004

Ensuring Sustainable Coal Supply. Power Generation

Emission Challenges in Cement Making due to alternative Fuels

The choice for innovative flue gas treatment. Sorbacal SPS, the most effective calcium sorbent on the market

BENEFICIAL USE OF COAL COMBUSTION PRODUCTS AN AMERICAN RECYCLING SUCCESS STORY

PPC specializes in maximum efficiency air pollution control equipment using a variety of different

Traditional and Advanced Air Quality Control Solutions

Controlling Emissions and Saving Money with Highly Engineered Cartridge Filter Technology

Topsoe s Emission Management Solution--DeNOx

Kazushige KUROSAWA*, Zhibao ZHANG**, and Zhengbing WANG** [Delivered Products & Systems] 1. Introduction. 2. Overview of Nanjing

FACILITY PROFILE. New Brunswick Power Corporation for the Belledune Thermal Generating Station

Babcock Borsig Steinmüller GmbH. Bełchatów - Retrofitting the EU s Largest Power Plant Site

Control Options For FPI Boilers to Meet Proposed Boiler MACT Limits

ENVIRONMENTAL FACTORS

Torrevaldaliga Nord Civitavecchia. High-efficiency thermoelectric power plant

Flexibility in Indian Power System

State of the art CFB technology for flexible large scale utility power production

Oxyfuel retrofit to coal power plant (Part1) - FS of 500MW class plant

Clearance Letter no. : MoEF Vide Letter no. J-11011/79/2003-IA-II (I) dated April 21, 2004

Conventional vs. LNG Fuelled RoPax - Case Study -

Technical Supplement to Opening Statement April 28, 2016 Clean Air Council Hearing The Clean Power Plan: Impact on New Jersey

High efficient multi-fuel CYMIC concept for biomass, rejects and coal for Hamburger Hungaria Katriina Jalkanen Valmet Technologies Oy

BOILER/HEATER < 5 MMBTU BACT Size: Small Emitter BACT (PTE < 10 lb/day) BOILER. BACT Determination Information

SOME ENERGY-EFFICIENT TECHNOLOGIES IN JAPAN

NTPC O&M Conference Performance and Optimization of Water Utilisation Increase of Existing Power Plants. Speaker Name; Tufani Ram 13-14/02/2013

JOINT ENVIRONMENTAL PROGRAMME

What is FGD Gypsum? Presented By E. Cheri Miller Gypsum Parameters, LLC Tennessee Valley Authority (Retired)

Continuous Emissions Monitoring - Program 77

CIRCULATING FLUIDIZED BED- FLUE GAS DESULFURIZATION TECHNOLOGY EVALUATION PROJECT NUMBER

REPORT ON THE LAND REQUIREMENT OF THERMAL POWER STATIONS

Particulate and Opacity Control - Program 76

India Kothagudem A Thermal Power Station Rehabilitation Project. Field Survey: July Project Profile and Japan s ODA Loan

MIT Carbon Sequestration Forum VII Pathways to Lower Capture Costs

GASP comments regarding Air Quality Plan Approval C - Tenaska Pennsylvania Partners, LLC Westmoreland Generating Station

Environmental Control Solutions

Hot Gas Filters for Control of Emissions to Atmosphere

Power-Cost Alternative De-NOx Solutions for Coal-Fired Power Plants

2 No. Continuous Ambient Air Quality Monitoring System (CAAQMS) installed in downwind & upwind direction and are connected to APPCB server.

Coal Fired Boiler Optimization and the Impact on Emission Control Devices

OPTIMISATION OF WATER USAGES IN THERMAL POWER PLANTS AND A STUDY ON DRY COOLING SYSTEM

Flue Gas Desulphurisation (FGD) Vertical Gypsum Centrifuges

Sustainable, Clean Energy from Waste

Form V is to be filled before 30th September annually; for the period from 1st April to 31st March PART A. Company Information

Potentials and Limitations with respect to NO x -Reduction of Coke Plants

PRISM 2.0: THE VALUE OF INNOVATION IN ENVIRONMENTAL CONTROLS

Evaluating Impacts on Ash Quality of Powdered Activated Carbon for Mercury Control. CONFERENCE: 2015 World of Coal Ash (

2. How can the University have an expansion of the Cogeneration Facility without an increase in the amount of coal used?

Flue Gas Desulfurization: The State of the Art

Oklahoma Department of Environmental Quality Air Quality Division

Lünen State-of-the-Art 813MW Coal-Fired USC Boiler with High Efficiency and Flexibility

FLUE GAS CLEANING WE MAKE THE WORLD A CLEANER PLACE

Transcription:

New Environment Norms Issues and Challenges By: Sanjeev Kumar Kassi Director (TETD), CEA

INSTALLED CAPACITY (MW) AS ON 29-02-2016 Type Capacity Share (%) Hydro 42703.42 14.79% Thermal 201360.04 69.76% Coal 175857.88 60.92% Gas 24508.63 8.49% Diesel 993.53 0.34% Nuclear 5780.00 2.00% Renewable 38821.51 13.45% Total 288664.97 100.00% THERMAL GENERATION ~ 80% of total generation

UNIT WISE BREAK UP OF INSTALLED CAPACITY (MW) Unit Size Installed Before 31.12.2003 Installed After 31.12.2003 Up to 250 MW From 250-500 MW More than 500 MW No of Units Total Capacity (MW) No of Units Total Capacity (MW) 313 47, 628 110 19,014 27 13, 500 49 15,220 - - 137 80,495 TOTAL 340 61,128 296 1,14,729 Total Feb, 2016 Units-636 Capacity 1,75,857 MW

EXISTING EMISSION NORMS Emission parameter Suspended Particulate Matter (SPM) Limiting Values Less than 210 MW 300 mg/nm3 * 210 MW or more 150 mg/nm3 * NOx SOx None for coal based stations None, stack provided for dispersion <500 MW - 220 m. >=500 MW - 275 m FGD space provision for units size 500 MW and above * Depending upon the requirement of local situations, which may warrant stricter standards as in case of protected areas the State Pollution Control Board and other implementing agencies within the provisions of the EPA, 1980 may prescribe limit of 150 mg/nm3 irrespective of the generation capacity of the plant. Andhra Pradesh Pollution Control Board and Delhi Pollution Control Committees have stipulated stringent standards of 115 and 50 mg/nm3 respectively for control of particulate matter emission.

EXISTING EMISSIONS Emission parameter Suspended Particulate Matter (SPM) NOx * SOx Values within 150 mg/nm3 with ESP Around 600-1000 mg/nm3 without secondary NOx control system Around 1200 mg/nm3 without De-SOx equipment * As per current specifications NOx emission from the unit shall not be more than 260 grams of NOx per giga joule of heat input (from thermal as well as fuel). This is equivalent to 700 mg/nm3

NEW EMISSION NORMS (as notified on 07.12.2015) Emission parameter TPPs (units) installed before 31 st December, 2003 TPPs (units) installed after 31 st December 2003 and upto 31 st December 2016 TPPs (units) to be installed from 1 st January 2017 Particulate Matter 100 mg/nm 3 50 mg/nm 3 30 mg/nm 3 Sulphur Dioxide (SO 2 ) 600 mg/nm 3 for units less than 500MW capacity 600 mg/nm 3 for units less than 500MW capacity 100 mg/nm 3 Oxides of Nitrogen (NOx) 200 mg/nm 3 for units 500MW and above capacity 200 mg/nm 3 for units 500MW and above capacity 600 mg/nm 3 300 mg/nm 3 100 mg/nm 3 To be complied within 2 years by existing stations and w.e.f 01.01.2017 for new stations

TECHNOLOGY FOR SOx and NOx control DE-SOx / Flue-gas desulfurization (FGD) WET LIME STONE PROCESS SPRAY DRY SCRUBBER SEA WATER SCRUBBING DE-NOx COMBUSTION CONTROL SELECTIVE CATALYST REDUCTION (SCR) SELECTIVE NON-CATALYST REDUCTION (SNCR)

BASIC PRINCIPLE - FGD FGD process typically involve SOx scrubbing with a alkali solid or solution CaCO 3 + SO 2 CaSO 3 + H 2 O Ca(OH) 2 + SO 2 CaSO 3 + H 2 O Mg(OH) 2 + SO 2 MgSO 3 + H 2 O 2NaOH + SO 2 Na 2 SO 3 + H 2 O A natural alkaline usable to absorb SO 2 is seawater. Generally Calcium based alkali are used in the form of lime or limestone. Seawater is also used wherever feasible in coastal regions.

BASIC PRINCIPLE-DeNOx DE-NOx process typically involve reaction of NOx with ammonia

Issues and Challenges De-SOx About 80000 MW of total installed capacity of less than 500 MW units will be affected due to non-availability of space for FGD installation. Even where space is available, Flue Gas Desulphurisation installation may take around 2 to 3 years and involve plant shutdown of 4-6 months. Dismantling / Relocation of existing plant facilities may be required in certain cases, affecting plant operation Installation of FGD on over 2 lakh MW capacity would need limestone of around 24 MTPA and produce 34 MTPA of gypsum. These figures would progressively increase with increase in FGD installations. Disposal of gypsum in environmentally friendly manner.

Issues and Challenges De-SOx Marketing avenues of gypsum. Some utilities having installed FGD are already facing problems of gypsum disposal The Auxiliary Power Consumption shall increase for FGD operation by 1.0-1.5% affecting the plant efficiency. The mining capacity of limestone in the country and its transportation to plants and associated challenges need to be addressed. Quality of Indigenous Lime Stone / suitability or arrangements for its import.

Issues and Challenges De-NOx Installations of Selective Catalytic Reduction(SCR) systems and associated issues. Combustion control system modification may lead to NOx levels of around 600-700 mg/nm 3 The NOx emission limits of 300 mg/nm 3 & 100 mg/nm 3 cannot be met without installation of SCR System. Globally available SCR system for reducing NOx emissions are not proven for Indian coal having high ash contents. No proven and established control technology suited to our high ash Indian coals exists and pilot studies needed before deploying any technology.

Issues and Challenges De-NOx Installation of DeNOx system in the existing units shall be a difficult task in view of the lay-out issues. Installation of SCR systems require extensive change in duct work, change of ID fan etc. for which no provision has been kept in the existing plants. Consumption of about 2500 tons ammonia per year for a 500 MW unit, its availability, transportation, handling & storage at plants. Environmental hazards of Ammonia.

Issues and Challenges De-NOx Catalyst for the SCR system is very expensive and has limited life (around 3 years). Impact on O&M charges and increased power consumption due to increased pressure drop in the system.

Issues and Challenges Vendor Availability Biggest constraint even if technical feasibility exists FGD & DeNOx systems have to be imported from other countries as the same is not manufactured indigenously. Installation of @ 20,000 MW / annum in about 2,56,000 MW capacity (1,75,200 existing+ 80,800 MW under construction) would take more than 10 years.

Issues and Challenges Limited time period for implementation for new and old plants. Newer plants will get delayed due to the new norms The expected capacity may not come to the grid affecting power supply and financial hardship to stations. The power utilities have raised their concerns and expressed their difficulties about the implementation of new environmental norms Two years is not sufficient for implementation in view of time required for Design and Engineering, approvals, arrangement of funds, tendering and erection, testing & commissioning.

Issues and Challenges The impact on power supply position due closure of most of coal based capacity due to non-fulfilment of environmental norms, as the modifications/retrofits would require long shut downs of units. Units operating at very low PLF of 10-20 % or have intermittent/ seasonal plant operation cannot recover the huge investment made, in their remaining life span without a steep rise in power tariff.

Issues and Challenges The implementation will have to be staggered for plant units to ensure power supply. Units under advanced stage of installation, the environmental control systems would have to be considered only as retrofits. Holding back commissioning of the units on account of environmental Standards may not be advisable as it could lead to contractual issues with equipment suppliers, establishment of guarantees etc. Delayed commissioning may lead to performance guarantee issues in the equipment later.

Issues and Challenges Commensurate plans would have to be taken up by other organization/ministries for mining of limestone, transportation of gypsum of requisite quality and handling ammonia & environmental approval thereon. CAPEX of around Rs. 1.0 Cr/MW (Rs.0.5 Cr/MW for FGD, 0.4 Cr/MW for SCR) and OPEX would have to be allowed by the Regulators in tariff which ultimately would burden the consumers. Huge capital requirement in the next two years to make the coal based power plants compliant with new norms Modification of existing PPAs to include revised tariffs

Issues and Challenges Due to limited supply of DeSOx systems and no supplier for proven DeNOx system, excessive outflow of foreign exchange shall take place. Also prices could increase sharply due to sudden requirements from large number of power utilities. As a rough estimate the power tariff may increase by 45 to 55 paise/kwh. Steep rise in tariff for 15-20 years old plants, as it would not be possible to recover the investment in their remaining life span.

WAY FORWARD Pilot studies for technology suitability for SCR systems with Indian coal new and retrofits Stations specific studies for SOx control systems Configurations Space requirements for different areas/systems Modifications etc. in other stations systems Limestone availability & logistics and Gypsum disposal Additional water consumption and treatments / disposal Definitive cost and time estimates Such measures would help utilities in devising stations specific strategies for implementation