Electrical Operation of Electrostatic Precipitators
This book will be of interest to both users and suppliers of electrostatic precipitators as well as advanced students on environmental based courses. The author identifies the physical and engineering basis for the development of electrical equipment for electrostatic precipitators and thoroughly explores the technological factors which optimise the efficiency of the precipitator and hence minimise emissions, as well as future developments in the electrical field.
Inspec keywords: fault location; electrostatic precipitators; electrical resistivity
Other keywords: online monitoring; electrical energisation equipment; fault identification; high frequency energisation system; mechanical impact; electrical resistivity impact; electrostatic precipitator design; mains frequency energisation system
Subjects: Electrostatic devices; Power system protection
- Book DOI: 10.1049/PBPO041E
- Chapter DOI: 10.1049/PBPO041E
- ISBN: 9780852961377
- e-ISBN: 9780863419850
- Page count: 284
- Format: PDF
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Front Matter
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1 The range and application of electrostatic precipitators
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One of the most suitable forms of arrestment device for meeting these levels of emission, particularly for process plants producing large gas flow rates, is the electrostatic precipitator. Following the installation of the first pulverised coal steam raising plant in the 1920s, where some 90 per cent of the ash can be carried forward with the waste gases, the electrostatic precipitator has been almost universally used to control particulate emissions in the power generation industry.
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2 Fundamental operation of an electrostatic precipitator
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Although the initial investigators, such as Lodge (1886), employed an electrostatic generator such as a Wimshurst Machine successfully to demonstrate the precipitation phenomenon, once the development was applied in the field, it became apparent that more electrical power, in terms of current, was necessary to ensure satisfactory particle charging such that the particles could be continuously precipitated. More correctly the process should be referred to as electrical precipitation, because with modern installations one can find rectifier equipment having outputs up to 200 kW and for large power station applications a power consumption up to 2 MW.
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3 Factors impinging on design and performance
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As will be appreciated from the preceding chapters, there are a large number of factors relating to both the carrier gas and particulates that affect the design, operation and performance of an electrostatic precipitator. This chapter will examine some of these characteristics in greater detail to explain how they impact on the electrostatic precipitator both mechanically and electrically.
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4 Mechanical features impacting on electrical operation
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This chapter presents the design and operation of an electrostatic precipitator. It discusses the production of ions, discharge electrode and its spacing, collector electrodes, precipitator sectionalism, high tension insulators, electrical clearances, deposit removal from the collector and discharge systems, hopper dust removal, and the reentrainment from hoppers.
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5 Development of electrical energisation equipment
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The first commercial application of electrostatic precipitation was that installed at the lead smelter of Parker, Walker and Co. at Baguilt in North Wales. This plant resulted from Lodge's investigations and findings from his work at Liver pool University in 1884. This repeated in more detail earlier work by Holfeld (1824) and Guitard (1850) when it was found that particles of smoke could be precipitated from a smoke filled vessel by applying a charge to the particles by means of a Voss or Wimshurst electrostatic generator.
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6 Modern mains frequency energisation and control
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Most modern precipitator installations are invariably energised from mains fre quency rectified equipment utilising the latest electrical and electronic components as described in Chapter 5. Generally the transformer input conditions are controlled by anti-parallel connected thyristors/silicon controlled rectifiers, which in turn are controlled by some form of microprocessor based automatic voltage control (AVC) system. Although the supply is generally a fully rectified voltage, many modern equipment designs have the facility of intermittent ener gisation to cater for specific fly ash conditions, or for power saving while meeting a target emission. The basic operating characteristics of a mains frequency rec tified power supply and the types of control will be examined in the following sections.
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7 Alternative mains frequency energisation systems
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Although the majority of existing operational single-stage precipitators use full wave mains rectification for energisation, there is a growing trend to adopt other means of energisation to overcome the deleterious effects of reverse ionisation when handling high resistivity dusts, and/or to optimise power consumption on large installations. These alternative systems are reviewed in this chapter.
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8 High frequency energisation systems
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There have been few departures in the past from the use of traditional mains frequency rectified supplies for precipitator energisation, owing, in part, to the lack of availability of suitable high frequency high voltage transformers and high speed switching power thyristors; consequently the conventional 50/60 Hz design has dominated the precipitation market. The circuit architecture of the conventional design, whilst being robust and simple has, however, a number of technical drawbacks.
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9 The impact of electrical resistivity on precipitator performance and operating conditions
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In this chapter, the methods of overcoming the difficulties of a highly resistive fly ash are based on changing the properties of the gas or particulate at the inlet to the precipitator, whether it is upstream or downstream of the air heater. There are, however, alternative methods of mitigating the effect of reverse ionisation on performance, which are of an electrical nature. These methods include intermittent energisation, where instead of a continuous energising voltage, the supply is intermittent, thereby allowing any charge arriving at the collector sufficient time during the non-energising period to neutralise before the next arrival of corona following re-energisation. Another approach is to superimpose a high voltage -60 kV, short duration 100 μs, pulse onto a reduced energising voltage. Again the mechanism is that during the pulse period sufficient corona is produced to charge the particles and that there is sufficient time between successive pulses for the particle charge to neutralise. Thus with either approach, voltage build up on the fly ash surface is avoided, which would have given rise to a positive ion emission, i.e. reverse ionisation operation.
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10 'On-line' monitoring, fault finding and identification
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In terms of performance, the modern electrostatic precipitator can be designed to operate and produce particulate collection efficiencies in excess of 99.8 per cent. To meet this level of performance, however, it is essential that all elements comprising the precipitator installation operate satisfactorily. As the unit is composed of a large number of mechanical and electrical items, the perform ance can suffer from various limitations, either because of component failure or changes in the inlet conditions presented to the precipitator. These limitations can be often identified by careful examination and interpretation of the output of installed monitoring equipment and the electrical operating conditions.
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Back Matter
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