Experimental Study on Preheated Air and Flue Gas Recirculation in Solid Waste Incineration (original) (raw)

Treatments of polluted emissions from incinerator gases: a succinct review

Reviews in Environmental Science and Bio/Technology, 2012

Due to the incomplete mineralisation of some organic compounds during the incineration of municipal solid waste, gaseous emissions are loaded with a large amount of particulate matter, undesirable elements and toxic molecules. Typically, an incinerator of urban solid waste produces large flows of hot gaseous emissions to be purified before being released into the atmosphere. In this paper, treatments of flue gas from a typical municipal waste incinerator are described. The first step is an energy recovery system through heat exchangers to make steam or hot water. Steam is used to produce electricity via a turbine. The economic balance of the total system is very often dependent on the heat recovery. The second step involves particle removal technologies. Different systems are available such as cyclones, scrubbers, electrostatic precipitators or baghouse filters. The third step is the removal of numerous molecule families such as acid compounds (SO x , HCl, HF), nitrogen oxides (NO x), metal species and many organic compounds. The latter include dioxins, furans and volatile organic compounds. Some treatment processes are described according to the pollutant family.

Identification of two combustion regimes depending of the excess air of combustion during waste incineration

An experimental study has been conducted with a fixed bed reactor to simulate, in a laboratory scale, industrial municipal waste incineration using moving grates. Carbon monoxide, nitrogen oxide, temperatures and mass loss rate measurements have been used to establish the importance of the operating parameters of a municipal waste incinerator in the characteristics of the combustion process. The present work is concerning the study of the impact of the airs of combustion. Two different regimes have been identified and that are controlled by the airflow through the fuel (primary airflow). The two combustion regimes established has served to show the potential impact of the operating conditions on the comportment of the combustion, the temperatures and the yields of carbon monoxide and nitrogen oxide : the production of NO seems to be controlled only by the oxygen concentration in the secondary zone of combustion. An increase in total airflow, thus, results in an increase in the yield of NO.

In-Depth Experimental Study of Solid-Waste Destruction by High Temperature Air Combustion

Energy Sources, Part A: Recovery, Utilization, and Environmental Effects, 2009

The objective of this article is to investigate the application of high temperature air combustion in thermal destruction of solid waste. The secondary air was preheated at different temperatures and burned with low calorific value and high content of diluted inert gas released from solid waste. It was discovered that the combustion with the higher preheated secondary air temperature had affected an increase in average flame temperature, and reduction in supplementary fuel consumption, but caused higher NO X emission. The maximum percentage of energy saving and NO X emission increasing occurred in the case of preheated secondary air at 900 ı C with a value of 56% and 40%, respectively.

Pollutant emissions from modern incinerators

Emissions of dioxins are mainly from incinerators, domestic and industrial coal combustion, and traffic. However, the major public concern and research effort are associated with the emissions of organic micropollutants from waste incinerators. This paper gives a brief overview of the more recent research and development for the removal of dioxins and heavy metals from flue-gas streams. Special attention is devoted to the origin and control of emissions from incinerators. It appears that flue-gas cleaning systems in modem incinerators are very reliable in removing almost all polluting emissions from flue-gas streams. However, the fly ash residues generated pose a significant disposal problem, as they are enriched with heavy metals and organic micropollutants. Incineration 1 The incineration process consists of a number of stages: drying (mainly at 50-200 °C), degasification (mainly at 250-400 °C), gasification (mainly at 400-600 °C) and combustion (mainly at > 600 °C) [I]. In the past, about 30 municipal solid waste incinerators were operated in the UK, some of which had no flue-gas cleaning system. However, over the last 15 years, advances in incinerator research and development as well as more stringent emission limits have resulted in equipping the majority of municipal waste incinerators with flue-gas cleaning systems and energy recovery boilers. Energy recovery, via district heating and electricity generation as illustrated in ~Figure I, is an exemplary way of ensuring economic as well as ecological viability of the incineration process.

Emissions from waste incineration plants - primary methods of emission reduction

2003

Emissions from waste incineration plants-primary methods of emission reduction Products of incomplete waste incineration identified on the basis of investigations carried out in the real waste incineration systems, the mechanism of formation of some of them and primary methods for emission reduction are discussed in the paper. It was shown that preservation of good incineration conditions which are similar to those of complete incineration, enables a significant reduction of emission of many pollutants to the atmosphere.

Flue Gas Composition and Treatment Potential of a Waste Incineration Plant

Applied Sciences

Waste-to-energy (WtE) incineration is an important technique in waste management systems and waste hierarchy. It is used to treat approximately 63% of the waste in European countries. The flue gas volumetric rate and its composition are essential to determine and monitor the emissions from waste incineration plants. This paper presents two methodologies used to evaluate the emissions from incinerators during the design phase. The first consists of a set of equations applicable in Excel (calculation model), while the second is the built-in components in Ebsilon 13.2 software which simulates the emissions from a furnace. This paper also proposes a comprehensive flue gas cleaning system for a simulated waste incineration plant in Jordan. According to Ebsilon, the results showed that for a 25 kg/s loading rate, there was 258,514 mg/Nm3, 749.90 mg/Nm3, 890.20 mg/Nm3, and 717 mg/Nm3 of CO2, NO2, SO2, and HCL, respectively. It was noted that these values relate to 1.5 of excess air ratio, ...

Incineration of Hazardous Waste: A Sustainable Process?

Waste and Biomass Valorization, 2014

The first objective of any waste policy should be to minimize the negative effects of the generation and management of waste on human health and the environment. Re-use and recycling of waste, although of high priority in the waste hierarchy, is not necessarily always the best treatment method. In the case of hazardous waste containing toxic components, thermal treatment with energy recovery constitutes a cost effective treatment option, complying with the pillars of ''Sustainability'' and the requirements of ''Resource Efficient and Cleaner Production''. Iron recovery from the incineration ashes, water recycling, substitution of fossil fuel by high calorific waste in the incineration process, and energy recovery, avoid the use of non-renewable resources. Emissions to air and discharges to water of a typical rotary kiln for the incineration of hazardous waste, are far below the European emission limit values. Furthermore, recent studies on health effects of modern, state-of-the art waste incinerators show that any potential damage to the health of those living close-by or working in a hazardous waste incineration plant, is likely to be very small, if detectable.

Environmental impact of emissions from incineration plants in comparison to typical heating systems

E3S Web of Conferences

In recent years, five modern municipal waste incineration plants have been built in Poland. Next ones are being constructed and at the same time building of several others is being considered. Despite positive experience with the operation of the existing installations, each project of building a new incinerator raises a lot of emotions and social protests. The main argument against construction of an incineration plant is the emission of pollutants. The work compares emissions from municipal waste incineration plants with those from typical heating plants: in the first part, for comparison large heating plants equipped with pulverized coal-fired boilers (OP-140), stoker-fired boilers (three OR-32 boilers) or gas blocks with heat output of about 100 MW have been selected, while the second part compares WR-10 and WR-25 stoker-fired boilers most popular in our heating industry with thermal treatment systems for municipal waste or refuse-derived-fuel (RDF) with similar heat output. Bot...