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| Safety and Health Topics > Mineral Processing Dust Control > Dust Control Handbook > Ch. 6 - Estimating Costs of Dust Control Systems | ||||||||||
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Chapter 6 Estimating Costs of Dust Control Systems | ||||||||||
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Necessity for Cost Estimates Since adequate control of dust emissions can usually be achieved by more than one dust control method, a considerable economic burden may result if the appropriate method is not selected. This burden can be higher capital costs, higher operating and maintenance costs, or both. Preliminary cost estimates can prevent this unnecessary economic burden by-
Cost Estimating Procedures Several methods, with varying degrees of accuracy, are available for estimating costs. They range from presenting an overall installed cost on a per-unit basis to presenting detailed cost estimates based on preliminary designs, schematics, and/or vendors' cost estimates. The lease accurate method is to equate overall costs to a basic operating parameter such as tons per hour or cubic feet per minute. This approach is not recommended. Where possible, detailed cost estimates should be arrived at by preparing preliminary designs and schematics. However, if time does not permit this approach, equipment vendors may be contacted. Based on their current knowledge of the technology and experience in the industry, they can provide reasonably accurate cost estimates. Cost Components To prepare and analyze cost estimates, a basic knowledge of the cost components and their relationship to the total cost of the system is essential. Total costs for any system can be divided into-
Capital costs consist of the delivered costs for major control equipment, auxiliary equipment and accessories, and field installation. Capital costs can be grouped as follows: Summary of Capital Costs
* Average percent of the capital investment ** Additional costs, expressed as a percentage of total capital costs
- Baghouses - Electrostatic precipitators - Scrubbers - Cyclones - Water-spray bars - Nozzles - Air-moving equipment
-- Electrical motors, starters, wire, conduit, switches, etc. -- Hoods, ductwork, gaskets, dampers, etc.
-- Compressors -- Electrical motors, starter, wire, conduit, switches, etc. -- Piping and valves -- Settling tanks (for wet scubbers)
--Sludge pits --Drag lines, trackway, etc.
-- Cement foundation -- Thermal insulation -- Vibration and antiwear materials -- Protection covers
-- Temperature and pressure -- Operation and capacity -- Power -- Opacity of flue gas -- Dust concentration - Labor required for delivery, assembly, removal or relocation of equipment - Freight, taxes, and subcontractors' fees - Engineering supervision - Startup and performance testing - Extending or increasing utilities The capital costs of a baghouse depend on the following:
The capital costs of an electrostatic precipitator depend on the net plate area (NPA). The NPA, in turn, depends on the efficiency required of the precipitator. Following are the factors that affect the cost of an electrostatic precipitator:
The capital costs of a scrubber depend, generally, on the following three factors:
Operating pressure also affects scrubber efficiency and price. The higher the air volume and/or operating pressure, the greater the plate thickness of the shell must be to prevent buckling of the shell. The cost of a scrubber can also increase if it is constructed of special materials, such as stainless steel or fiber-reinforced plastics to protect against corrosion or lining the scrubber shell with PVC, rubber, or refractories to protect against erosion. Cyclones/Multiclones The capital costs of a cyclone or multiclone are a function of the particulate-removal efficiency, which, in turn, depends on the inlet gas velocity and inlet diameter. Theoretically, the higher the velocity or the smaller the inlet diameter, the greater the efficiency and pressure drop. The material of construction also affects the cost. For handling highly abrasive dust, the cyclone/multiclone may have to be constructed of abrasion-resistant material or lined with ceramic material. For a highly corrosive gas stream, stainless steel or fiber-reinforced plastic may be necessary. Fans and Motors The capital costs of a fan are based on-
Although pump prices vary with the design of the pump, they are generally a function of-
Note: Generally, the capital cost of the pump and motor combination varies inversely with the revolutions per minute; however, maintenance costs may be higher as the revolutions per minute increase. Operating and Maintenance Costs Operating and maintenance costs consist of direct expenses of labor and materials for operating and maintenance, the cost of replacement parts, utility costs, and waste disposal costs. They may also include indirect costs of overhead, taxes, insurance, general administration, and capital recovery charges. However, only direct costs are discussed here. Operating Costs Operating costs include-
Direct Labor and Material Costs - Labor and materials costs for operation and maintenance of dust control systems vary substantially among plants due to factors such as the degree of automation, equipment age, and operating periods. Generally speaking, labor costs can be reduced by increased system automation. For small- to medium-size systems with an installed cost of approximately $100,000 or less, the total cost of maintenance is approximately 5% of the installed cost. ![]() Utility Costs - the utility costs for equipment such as pumps and electrical motors are a function of power/energy requirements, which can be calculated as follows: ![]() ![]() Horsepower requirements for baghouse shaker motors, reverse-air fan motors, etc. can be estimated at approximately 0.5 hp per 1,000 ft2 of cloth area. Power usage depends on dust loading and cleaning frequency. Assuming a 50% usage factor, power requirements are approximately 0.2 kW·h for 1,000 ft2 of cloth area. Electrostatic Precipitator Power The power requirements for an electrostatic precipitator are approximately 1.5 W/ft2 of collection plate area. The range varies from 0.3 to 3 W/ft2. Once the power requirement is known, the annual power costs can be calculated using the following equation: Annual power cost ($) = Power usage x Cost of power x Total annual (kW·h) ($/kW·h) operating hrs. Waste Disposal Costs The cost of waste disposal included the removal and hauling of dry contaminants to a nearby site. This cost varies with the particular plant and available landfill site. Water Costs Water costs vary in different areas. Maintenance Costs Maintenance costs include-
Cost Justification A 10-15% return on investment is necessary to justify and capital investment. However, when dust controls are considered, such a return is not always practical. The following are some tangible benefits that may assist in economic justification of a dust control system:
- Property tax exemption
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