ATMOSPHERIC EMISSIONS FROM GAS FIRED HOME HEATING APPLIANCES



Similar documents
Experimental study on atmospheric pollutant emissions from heating systems, in Italy

Continuous flow direct water heating for potable hot water

COMBUSTION. In order to operate a heat engine we need a hot source together with a cold sink

EcoDesign & Labelling Directive (ErP)

High-efficient gas boiler CompactGas

Zero Emission Engine. An Economic and Environmental Benefit

Boiler NOx Emissions and Energy Efficiency

Emissions estimate from forest fires: methodology, software and European case studies

Boiler efficiency measurement. Department of Energy Engineering

Carbon Dioxide Membrane Separation for Carbon Capture using Direct FuelCell Systems

Boiler Tune-up Guide

Effects of Ultra-High Turndown in Hydronic Boilers By Sean Lobdell and Brian Huibregtse January 2014

Half the cost Half the carbon

NITROGEN OXIDES FORMATION in combustion processes COMBUSTION AND FUELS

Continuous Monitoring of Flue and Combustible or Hazardous Gases and Vapors

WORKING DOCUMENT ON. Possible requirements for air heating products, cooling products and high temperature process chillers TRANSITIONAL METHODS

PELLEXIA COMFORT ENVIRONMENT COMPATIBLE

Biomass Boiler House Best Practices. Irene Coyle & Fernando Preto CanmetENERGY

RESIDENTIAL AND COMMERCIAL/INSTITUTIONAL NATURAL GAS AND LIQUEFIED PETROLEUM GAS (LPG) COMBUSTION

The prediction of flue gas emissions from the combustion in the industrial tubular heaters

Advantage of Using Water-Emulsified Fuel on Combustion and Emission Characteristics

THE HUMIDITY/MOISTURE HANDBOOK

This article provides a basic primer on an

Optimising Glass Melting Processes with Energy & Mass Balance Calculations

Improving comfort and energy efficiency in a nursery school design process S. Ferrari, G. Masera, D. Dell Oro

Evaluation of portable flue gas analysers for monitoring carbon dioxide in ambient workplace air HSL/2006/42. Project Leader: Peter Walsh.

AVL FUEL MASS FLOW METER & FUEL TEMPERATURE CONTROL

LABELLING OF GAS BOILERS - AN EFFICIENT MARKET REGULATOR

Online Infrared Flue Gas Analyzer Gasboard 3000

An Experimental Study on Industrial Boiler Burners Applied Low NOx Combustion Technologies

OXYGEN AND OPACITY STACK EMISSION MONITORING SYSTEMS TO OPTIMIZE COMBUSTION EFFICIENCY AND MEET EPA REQUIREMENTS

Boiler efficiency for community heating in SAP

The Use of Exhaust Gas Recirculation (EGR) Systems in Stationary Natural Gas Engines. The Engine Manufacturers Association August 2004

Energy Efficient Operations and Maintenance Strategies for Boilers

SNAP CODE: SOURCE ACTIVITY TITLE: Flaring in Gas and Oil Extraction NOSE CODE:

Automotive Air Quality Sensors: industrial innovations to protect people s health

(Adopted December 1, 1978)(Amended July 8, 1983)(Amended November 6, 2009) (Amended September 5, 2014)

1.0 What Are the Purpose and Applicability of Performance Specification 11?

A Review of Biomass Boiler Technologies. Fernando Preto CanmetENERGY, Natural Resources Canada

Control Device Requirements Charts For Oil and Gas Handling and Production Facilities

Approved baseline and monitoring methodology AM0056

Tips for burner modulation, air/fuel cross-limiting, excess-air regulation, oxygen trim and total heat control

Module 5: Combustion Technology. Lecture 34: Calculation of calorific value of fuels

Micro cogeneration. Affordable, efficient and innovative

The Fate of Ammonia and Mercury in the Carbon Burn-Out (CBO ) Process

STOICHIOMETRY OF COMBUSTION

Source: EIA Natural Gas Issues and Trends 1998

HOW TO SELECT A LOW VOLUME (L.V ) BOILER

Power-Gen International 2008 Orlando, Florida

Gas Absorption Heat Pumps. Future proofing your heating and hot water

Efficiency on a large scale CFB Steam Boilers

PART 11: START-UP PROCEDURES FOR THE INSTALLER

Layman Report. Stirling Power Station. Mini CHP with longlife Stirling engine. Mayer & Cie. GmbH & Co. P.O. Box D Albstadt

Copyright 1984 by ASME. NOx ABATEMENT VIA WATER INJECTION IN AIRCRAFT-DERIVATIVE TURBINE ENGINES. D. W. Bahr. and T. F. Lyon

Offshore Gas Turbines and Dry Low NOx Burners. An analysis of the Performance Improvements (PI) Limited Database

LMS The modular management system for condensing boilers. Control Products & Systems OEM. Answers for infrastructure.

Point Source Emission Inventory For Non-Electric Companies in Georgia

ENERGY EFFICIENCY IN POWER PLANTS

Improving Steam Methane Reformer Performance with the ZoloSCAN-SMR

It s time for H.E.R.O. Energy Saving Strategy for. Tunnel & Shuttle Kilns

CSP-gas hybrid plants: Cost effective and fully dispatchable integration of CSP into the electricity mix

Hot Water Heating: Technologies and Use

Daikin Altherma Hybrid Heat Pump

EPA Requirements for Diesel Standby Engines In Data Centers. Bob Stelzer / CTO / Safety Power Inc. For 7x24 Fall 2014 Conference. 1.

Malmö Hydrogen and CNG/Hydrogen filling station and Hythane bus project

Emissions Uncertainty: Focusing on NOx Emissions from Electric Generating Units

Thermal Mass Flow Meters


Drying of Woody Biomass. Process Engineering / GEA Barr-Rosin

ROTEX gas hybrid heat pump. A strong team.

Texas Commission on Environmental Quality Page 1 Chapter Control of Air Pollution from Nitrogen Compounds

The Concept of Condensing Boilers

CFD Analysis of a MILD Low-Nox Burner for the Oil and Gas industry

Gas Burner Technology & Gas Burner Design for Application

Adapting Gas-Power Generation to New Role in Low-Carbon Energy Systems

Top Technology for Industry, Agriculture, Business and Communities

COMBUSTION. By: Michael Biarnes. In collaboration with: Bill Freed and Jason Esteves. E Instruments International LLC -

2nd IEA Oxyfuel Combustion Conference

Danish stoves - a cosy and eco-friendly heat source

CAT CG132. Series Gas Generator Sets

FEASIBILITY OF A BRAYTON CYCLE AUTOMOTIVE AIR CONDITIONING SYSTEM

Appendix 5A: Natural Gas Use in Industrial Boilers

PERFORMANCE EVALUATION OF NGCC AND COAL-FIRED STEAM POWER PLANTS WITH INTEGRATED CCS AND ORC SYSTEMS

Calculate Available Heat for Natural Gas Fuel For Industrial Heating Equipment and Boilers

NOVEL ENERGY PROVISION SYSTEM FOR THE SUSTAINABLE CONNECTED HOME

Outlook on Integrated Gasification Combined Cycle (IGCC) Technology

Heat Recovery Dehumidification (HRD) system. Designed for municipal swimming pools

Vitocaldens 222-F Compact Gas-Hybrid appliance

Improving Energy Efficiency through Biomass Drying

INDEX GENERAL

Technique of Monitoring Dioxins in Flue Gas from MSW Incinerators using Dioxin Precursor Analyzer

EMISSIONS OF AIR POLLUTANTS IN THE UK, 1970 TO 2014

Process Integration of Chemical Looping Combustion with Oxygen Uncoupling in a Coal-Fired Power Plant

Stack Sampling Stack sampling or source sampling

Design and Test Operation Performance of 1,500 C Class Gas Turbine Combined-Cycle Power Plant:

GAS HEATING IN COMMERCIAL PREMISES

Development of Air-to-Water Heat Pump for Home Air conditioning/hot Water Supply Combination System with Chilled/Hot Water in European Markets

A REVIEW OF GAS APPLIANCE CO EMISSIONS LEGISLATION

Technologies for small scale Biomass CHP-Plants an actual survey

R&D on Oil-Burning, Environment-Friendly, High-Efficiency Boiler

Transcription:

ATMOSPHERIC EMISSIONS FROM GAS FIRED HOME HEATING APPLIANCES Stefano Cernuschi, Stefano Consonni, Giovanni Lonati, Michele Giugliano, Senem Ozgen DIIAR Environmental Sect., Politecnico di Milano, P.za L. da Vinci, Milano (Italy) stefano.cernuschi@polimi.it, giovanni.lonati@polimi.it, michele.giugliano@polimi.it, senem.ozgen@polimi.it Dept. of Energetics, Politecnico di Milano, P.za L. da Vinci, Milano (Italy) stefano.consonni@polimi.it Abstract Atmospheric emissions from natural gas domestic appliances for combined ambient heating/hot water production were determined experimentally on a laboratory test bench. Measurements were performed on different types of boilers, covering the actual range of configurations available, at full and partial constant heat loads as well as in variable load conditions. Results obtained for pollutants of interest (CO, NO x, VOC, NMVOC and particulate matter) are reported and analysed in terms of concentrations and emission factors for the different boilers and operating regimes investigated. Keywords: residential combustion, natural gas, emission factors, conventional pollutants, variable load. Introduction Small residential heating installations make up a significant share of the total air pollutant emissions budget in Italian urban areas, where their spatial concentration and limited flue gas release height might lead to important impacts on air quality. Nevertheless, reliable information on their emission characteristics is generally lacking or very poorly documented, either in data bases generally used for emission inventories (EEA, 5; US EPA, ) or in the available scientific literature, thus making rather difficult the evaluation of their contribution in local inventories and their apportionment to pollutant levels in the atmosphere. Data shortage is a particular concern for natural gas fuelled appliances of low heat output (< 5 kw th ) for combined ambient heating and hot water production, already largely present in single family homes. Most of the reported emission factors in this sector are derived from limited base data, normally referred to operating regimes far from most typical real practice conditions, and they generally do not cover the range of recently commercialized best available technologies. These advanced units, which are equipped to reduce pollutant emissions and simultaneously increase heat generation efficiencies, are predicted to increase significantly their actual market share in the very near future. With the main purpose of enlarging the data base of emission factors applicable for the source activity sector in the development of pollutant inventories for Italian urban areas, an experimental evaluation was designed to include explicitly all the main factors affecting the emissions regime representative of the source category, in terms of both the different technological configurations of commercially available boilers and of the most typical operating regimes. The investigation was conducted with a standard certification laboratory test rig, where flue gas concentration levels of conventional pollutants from combustion (CO, NO x, VOC and NMVOC) as well as of particulate matter were measured. The paper reports the main results obtained, in terms of concentrations and emission factors derived and their observed variability with boiler type and exercise conditions.. Materials and methods The study was conducted on three different types of boilers (Table ), selected through available informations about their actual and prospected distribution among installed units at the national level (AMA, ; ATIG, ) and considering the different technological options commercially available in the selected heat output range (< 5 kw th ). The boilers investigated included:. natural draft boiler with conventional atmospheric burner;. forced draft condensing boiler with premixed modular air/fuel ratio burner;. forced draft boiler with premixed low NO x burner ( carpet type flame with water cooling). The unit is included in the highest class of NO x emissions according to European Regulations (CEN, 999),

corresponding to the lowest NO x emission factor (7 mg/kwh);. forced draft boiler with conventional atmospheric burner. The first three boilers were tested in brand new conditions whilst the last unit, already utilized for performance endurance laboratory testing, was evaluated to indicate potential modifications in emissions arising from ageing effects. Table : Main technical characteristics of the boilers investigated Boile r (kw) (%) Draft Burner,6 9,5 Natural Conventional 95,9 Forced + Premixed + condensing gas/air control 9,9 Forced Premixed low NO x, 9, Forced Conventional (*) Nominal output P n (*) E (**) (**) Useful efficiency at P n Emission measurements were conducted with a standard laboratory test rig for certification procedures (CEN, 999), during boiler operation at different heat output conditions, selected by considering the most typical operating regimes in real utilization conditions as well as the heat load regulation capabilities of every apparatus. The test included operation at continuous full and minimum heat loads (% and % of nominal heat output, respectively), following the actual requirements of European boiler certification procedures (CEN, 999) as well as in variable load conditions, with two different operating cycles specifically developed for simulating real exercise regimes of utilization and intended to reproduce repeated start up/shut down cycles (Figure ) and continuous heat load modulations over time (Figure ). Test runs in continuous operating mode were conducted for all the boilers, whilst variable load cycles were utilized for the units expected to be representative of the extremes of technical configurations of burners actually available in terms of emissions and heat generation performances (boiler - conventional atmospheric burner and boiler - premixed modular air/fuel burner with flue gas condensation, respectively). Gas measurements were performed with a multiparametric analyzer, equipped with electrochemical cell detectors for CO and NO x and additional sensors for flue gas parameters of interest (O, temperature, CO ), and with a VOC analyzer, equipped with a GC/FID detector for speciation of NMVOC and unburned CH. Total particulates were sampled with an isokinetic probe and collected on glass fibre filters for gravimetric determination. Heat load (% nominal output) Heat load (% nominal output) 8 6 Nominal output s Total time = 5 - min Mean output 5 s 75 s Minimum output Time Figure. Variable load test cycle in intermittent operating mode (shut down/start up intervals: 5 sec) 8 6 Nominal output (9,5 min) Mean output (,5 min) Minimum output (9,5 min) Total time = 5 - min Time Figure. Variable load test cycle in continuous operating mode. Results and discussion Concentrations and emission factors for all the pollutants investigated are illustrated and discussed in the following paragraphs. All the figures are mean values of single data acquired at -5 min time intervals during the whole test duration; concentrations are normalized at % O in dry flue gas at normal conditions (7 K,. kpa), whilst emission factors are referred to unit heat released from combustion. Results obtained for CO during constant full load operation (Figure ) ranged between 7.5 and g/gj, corresponding to concentrations in the range 5- mg/m. The boiler with the premixed low NO x burner resulted in the lowest emissions, whilst the unit equipped with a similar advanced burner design but with modular air/fuel ratio control showed the highest emission level, even higher than the conventional atmospheric unit (5, g/gj) and the used boiler (9, g/gj). The resulting increase is attributed to the limited excess air maintained by the modular burner design for obtaining maximum thermal efficiencies from flue gas condensation, thus confirming the well known drawbacks related to CO emissions with rich

combustion mixtures. Despite the influence on combustion related to the different designs of the burners investigated, the effect of oxygen on CO formation is further confirmed by the observable reduction in emission factors with increasing oxygen concentration in the flue gas (Figure ). In accordance with the corresponding decrease in fuel consumption, continuous operation at minimum load results in a generalized reduction of CO emission factors for all the heaters (Figure ). The only exception is related to the atmospheric boiler, whose operating conditions at minimum loads with extremely lean mixtures (6.% O in flue gas) and the conventional design of the burner appear to influence negatively the combustion process: in the same operating conditions, some advanced premixed burners (boiler ) are indeed capable of maintaining very low CO emissions with high excess air levels (Figure ). The results obtained do not point to any significant influence of aging, with the used apparatus (boiler ) resulting in emission levels at full load essentially comparable with those measured from the new most similar unit (boiler ) and with the same decreasing trend in emission factors for load reductions already illustrated, with the lowest absolute value at minimum load operation measured for all the boilers investigated. Variable load discontinuous regimes give rise, as expected, to higher emission factors (Figure 5), mostly attributable to the technical difficulties in maintaining optimum combustion conditions during shut down/start up episodes: the latter influence is substantially confirmed by the results obtained for boiler during the variable load continuous operation test, where the absence of any interruption in exercising the unit results in CO emission levels comparable with those obtained in continuous operation at constant loads (8. g/gj in variable regime,. g/gj and. g/gj in continuous full and minimum load regimes, respectively). CO (g/gj) 5 5..6.. 7.5 9. 9. 6.9 Boiler Boiler Boiler Boiler Figure. CO emissions at constant heat load CO (g/gj) CO (g/gj) 7 6 5 5 5 Flue gas oxygen (% vol) Figure. CO emissions variations with flue gas oxygen content. (Boiler numbers for single dot points as in Table ) 5..6 5... 58. 8. Boiler Boiler Full constant load Minimum constant load Intermittent variable load Continuous variable load Figure 5. CO emissions at constant and variable heat load Emissions of NO x in constant full load tests (Figure 6) ranged between 8 g/gj and 85 g/gj, corresponding to concentrations in the range 5-5 mg/m. Units equipped with advanced design burners (boilers and ) achieved significant reductions with respect to conventional atmospheric burners, with the latter resulting in rather higher emissions and with the used boiler characterized by the highest absolute value. Very interesting results were obtained for the premixed modular air/fuel unit, characterized by the lowest absolute emissions (8 g/gj), even lower than those measured for the low NO x dedicated burner (9 g/gj): extreme reductions in excess air appears thus to affect positively NO x production rather than CO, confirming the well known technical difficulties in achieving optimal simultaneous reductions for both pollutants by regulating only the excess air. Emissions obtained during constant operation at minimum heat loads result in appreciable reductions with respect to full load operation, with the higher values still obtained for the conventional new and aged units. The reductions appear well correlated to the corresponding variations in excess air (Figure 7): the effect of oxygen on emitted NO x might be further observed with the premixed modular burner

(boiler ), whose operation with constant air/fuel ratios under variable load conditions result in rather small differences between emission factors measured in either load condition. Variable load emission results (Figure 8) appear essentially comparable to continuous data, with rather small observable increase in emission factors for the conventional apparel (69 g/gj vs. 5,9 g/gj - 6, g/gj at constant load) and no appreciable variations for the advanced unit. Tests with shut down/start up episodes, applied to boiler, also result in no practical influence. NOx (g/gj) NO x (g/gj) NO x (g/gj) 8 6 9 75 6 5 5 8 7 6 5 6. 5.9 7.8. 8.6 9.9 8.6 67. Boiler Boiler Boiler Boiler Figure 6. NO x emissions at constant heat load 5 5 Flue gas oxygen (% vol) Figure 7. NO x emissions variations with flue gas oxygen content. (Boiler numbers for single dot points as in Table ) 6. 5.9 69 Full constant load Minimum constant load Intermittent variable load Continuous variable load 7.8. 6. 9.9 Boiler Boiler Figure 8. NO x emissions at constant and variable heat load Due to technical operating problems, test failure occurred during VOC measurement runs for the atmospheric conventional boiler (boiler ) and for the variable load continuous regime with the premixed modular boiler (boiler ). Results available for all the boilers and conditions properly measured are reported in Figures 9 and. Constant full load test conditions (Figure 9) were generally characterized by rather low emissions, with VOC values between. and.8 g C /GJ (concentrations of. - 6. mg c /m ). Operation at minimum load results, with the exception of the premixed modular burner (boiler ), in appreciably increased emissions, with VOC emission factors as high as nearly 6 g C /GJ (concentration of mg c /m ). VOC emissions performance is more difficult to interpret in general terms, with the observed values and their corresponding load variations strictly related to single boiler characteristics. Higher emissions in either load conditions were recorded for the premixed low NO x burner (boiler ), with a substantial increase from full to minimum load conditions: the relatively large prevailing fraction of unburned methane measured in both conditions (over 8% of total VOCs) might indicate technical problems arising from burner design in feeding properly all the fuel to the burner nozzles at decreasing loads. The unit equipped with premixed modular burner (boiler ) resulted in the lowest emission levels, essentially independent from load conditions and with almost negligible VOC values in the range. -. g c /GJ; almost all measured VOCs were unburned hydrocarbons (NMVOC) thus indicating, as already observed for CO, emissions arising probably from incomplete combustion. Emission levels from the used conventional unit (boiler ) were intermediate between the values recorded for the two advanced burners, with higher emissions at lower load conditions and with a prevailing fraction of unburned methane detected only during minimum load tests. Variable load test results, available for the premixed modular unit in intermittent operating mode (Figure ), resulted rather clearly in higher total VOC emissions with respect to continuous operation at constant loads, with an increase from.-. g C /GJ to nearly 7 g c /GJ and with a very significant fraction of unburned methane detected (over 75%). The difference might thus be related to fuel losses arising from the technical difficulties, already claimed also for CO, in maintaining optimum burner feeding conditions during shut down/start up episodes. The investigation was also extended to particulate matter emissions, normally not considered for natural gas combustion sources and thus very poorly documented, particularly for small heating appliances. Measurements were conducted

at continuous full load operation on the atmospheric conventional unit (boiler ) and the premixed modular condensing boiler (boiler ), in order to obtain indications about the emissions performance expected over the whole range of technical configurations investigated. Results obtained (Table ) show almost negligible emissions, with concentrations typical of background conditions and emission factors essentially independent from boiler configuration, as expected from the nature of the fuel utilised. Emission factor (g C /GJ) Emission factor (g C /GJ) 7 6 5 8 6 Boile r VOC CH NMVOC....8....... 5.9 5.9 Minimum load..7. Boiler Boiler Boiler Boiler Boiler Boiler Figure 9. VOCs emissions at constant load. VOC CH NMVOC.... 7.9 5. 7.7 Full constant Min.constant Interm.variable Figure. VOCs emissions at constant and intermittent load measured with boiler Table : Particulate emissions measured in the study. Concentration (µg/m @ % O,dry normal flue gas) Emission factor (mg/gj) 9... Conclusions Following progressive regulatory restrictions introduced in recent years, the technological options adopted in small gas fired heating appliances have experienced a significant development towards highly sophisticated designs, with particular attention addressed, through proper burner design and control, to the optimization of combustion conditions for reducing pollutant emissions while maintaining higher heat production efficiencies and secure operating conditions. However, proper documentation on emission levels expected from most advanced units is generally lacking, particularly in most typical utilization regimes characterized by variable load and intermittent operating conditions. The experimental laboratory investigation conducted on several different commercial boilers in a range of continuous and variable load operating conditions result in the following main indications about emissions performance: simultaneous emissions minimization and heat recovery optimization appear rather compatible even in advanced boilers with dedicated burner designs (premixed flames with modular air/fuel control). On the other hand, even with most recent options available for emissions reduction (low NO x premixed burners) air/fuel ratios are far from constant during variable heat load operation; very significant reductions in NO x are achieved through advanced premixed burners, whilst for CO the low air/fuel ratios maintained for optimizing heat efficiencies at variable loads in modular burners appear to increase emissions at full output. On the other hand, the low NO x premixed burner shows substantial VOC emissions, mostly of unburned methane fuel; results available from variable load operating conditions indicate a significant increase in CO and VOC emissions during intermittent operation with shut down/start up episodes; ageing of the boiler seems to mainly influence emissions of NO x and unburned CH, with CO and VOC emissions being essentially comparable with those measured with new units in the same operating conditions; primary particulate emissions are almost negligible, as expected from the fuel utilised, with levels comparable to typical concentrations measured in background air. Acknowledgments The study was conducted within a research contract between Politecnico di Milano and CESI. The authors greatly appreciate the cooperation of Unical during the laboratory tests.

References AMA (Agenzia Milanese Mobilità Ambiente). State of the environment in Milan municipality, chapter (in Italian). Milano (Italy). ATIG, Natural gas utilization in Italy: general market situation of commercial heating boilers (in Italian), ATIG, Italian Technical Gas Association, Milano (Italy). CEN (European Committee for Standardization) 999, Gas fired central heating boilers - Type C boilers of nominal heat input not exceeding 7 kw, European Standard EN 8:999. EEA (European Environmental Agency), EMEP/CORINAIR Emission Inventory Guidebook - Third edition, October update, EEA, Copenhagen (Denmark). Available online at: http://reports.eea.europa.eu/emepcorinair/e n/page.html. US EPA, Compilation of Air Pollutant Emission Factors, Volume : Stationary Point and Area Sources, 5th Edition, update, U.S. EPA Office of Air Quality Planning and Standards, Washington D.C. (USA). Available online at: http://www.epa.gov/ttn/chief.