Status and Problems of Regenerable Flue Gas Desulfurization Processes

Fourteen sulfur and/or sulfuric acid producing regenerate FGD processes were discussed at the 1974 FGD Symposium in Atlanta. During the period elapsed since then, considerable status change has occurred on many of these regenerable processes. Other regenerable processes which were not as well known during 1974 have surfaced in 1975. The problems of obtaining reducing gases (hydrogen sulfide, carbon monoxide, and hydrogen) for the reduction of sulfur dioxide product streams to elemental sulfur have become severe due to shortages of natural gas or other petroleum based feedstock. A new sulfur producing process which employs CO and H₂ directly (rather than the H₂S required for liquid and vapor base Claus reactions) is gaining attention. This paper discusses briefly: (1) the announced status of the many regenerable FGD processes, (2) the problem of reductant gas supply, and (3) the effect on FGD processes of using coal based reducing gas instead of reformed natural gas.     

Capital and Operating Costs of Selected Air Pollution Control Systems—IV

Previous articles in this series discussed the equipment costs of control devices, gas conditioning equipment, hoods, ductwork, and dampers. In this article, the discussion will concern the fans and associated components required to convey the gas stream from the initial pollutant source to the control device.     

Capital and Operating Costs of Selected Air Pollution Control Systems-III

Pollution control systems will normally require some auxiliary equipment to capture and carry the gas stream to the control device. In general, this auxiliary equipment will consist of a hood or similar device to isolate and collect the pollutant-laden gas, ductwork to convey the gas stream to the control device, and dampers to control and modulate the flow. In this article, the equipment cost of canopy hoods, ducting, and dampers will be considered, together with their effect on the size, cost, and operation of the control device.     

Capital and Operating Costs of Selected Air Pollution Control Systems—V

Several methods are available for estimating the capital costs of systems and each has its own degree of accuracy. These methods range from presenting overall installed costs on a per unit basis, to detailed cost estimates based on preliminary designs, schematics, and contractor quotes. The least accurate method is the equating of overall capital costs to a basic operating parameter such as tons per hour or cfm since this method only produces accuracies in the "order of magnitude" category, at best. The detailed cost estimate, in turn, can produce accuracies of ±5 % depending on the amount of preliminary engineering involved. These estimates, however, take many months of engineering effort and require process and engineering flow sheets, material and energy balances, plot plans, and equipment arrangement drawings before a cost estimate can be developed. For first-cut estimating purposes, the technique described in this article for developing capital costs for a specific pollution control system is based on the factored method of establishing direct and indirect installations costs as a function of known equipment costs. The cost factors developed are based on both quoted and estimated installation costs of pollution control systems. The annual operating costs for these systems are based on unit costs for utilities and operating and maintenance labor together with fixed percentages of capital costs for the indirect costs.     

Capital and Operating Costs of Selected Air Pollution Control Systems — I

This is the first installment of a 4-part series which will present capital and operating costs of selected air pollution control systems. The objective of the Series is to identify the individual component costs so that realistic system cost estimates can be determined for any specific application. In Part I, cost estimating procedures and curves are provided to develop the equipment costs for electrostatic pre-cipitators, venturi scrubbers, fabric filters, incinerators, and adsorbers.