1993
DOI: 10.1080/1073161x.1993.10467114
|View full text |Cite
|
Sign up to set email alerts
|

The Potential of Pulse-Jet Baghouses for Utility Boilers Part 3: Comparative Economics of Pulse-Jet Baghouse, Precipitators and Reverse-Gas Baghouses

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
12
0

Year Published

1994
1994
2023
2023

Publication Types

Select...
3
3
3

Relationship

0
9

Authors

Journals

citations
Cited by 16 publications
(13 citation statements)
references
References 2 publications
1
12
0
Order By: Relevance
“…Compared to an electrostatic precipitator installation handling a 'difficult fly ash', the cost of the equivalent bag filter would be somewhat cheaper, but operating power, the maintenance of compressors and cleaning mechanisms, plus the cost of a complete media (bag filter) replacement, probably every three years or so, to ensure emission compliance, must be borne in mind and added to the overall cost comparison. Figure 3 compares the total 15-year levelized costs of various arrestment systems for a typical 250 MW power plant designed to meet an emission of 50 mg/N m 3 at 6 per cent dry oxygen (1). These indicate that, for either a reverse gas bag house or pulse jet fabric filter, the cost remains constant irrespective of the ash resistivity, i.e.…”
Section: Comparative Costingsmentioning
confidence: 96%
“…Compared to an electrostatic precipitator installation handling a 'difficult fly ash', the cost of the equivalent bag filter would be somewhat cheaper, but operating power, the maintenance of compressors and cleaning mechanisms, plus the cost of a complete media (bag filter) replacement, probably every three years or so, to ensure emission compliance, must be borne in mind and added to the overall cost comparison. Figure 3 compares the total 15-year levelized costs of various arrestment systems for a typical 250 MW power plant designed to meet an emission of 50 mg/N m 3 at 6 per cent dry oxygen (1). These indicate that, for either a reverse gas bag house or pulse jet fabric filter, the cost remains constant irrespective of the ash resistivity, i.e.…”
Section: Comparative Costingsmentioning
confidence: 96%
“…Given that the A/C ratio is the primary determinant of the unit size, and hence the capital and operating costs, it is desirable to operate at the highest A/C ratio that comfortably meets the performance specifications. Table 1 provides the typical values used for A/C ratio for various baghouse types based on industry experience (Belba, et al, 1992;Bustard, Cushing, & Chang, 1992;Cushing, et al, 1990;Puille, 1985;Sloat, et al, 1993).…”
Section: Fabric Filter Designmentioning
confidence: 99%
“…For purposes of this analysis, a generic unit cost is used for both capital and O&M costs for installing either a baghouse or ESP. The capital cost to install a particulate control unit is estimated to be about $57/kW; the O&M cost is estimated to be about $5.9/kW per year (adapted from Shoat et al 1993). The capital cost to retrofit all eligible plants with particulate controls would be about $2.7 billion.…”
Section: Strategymentioning
confidence: 99%
“…It is an established technology that has been used for many years in developed countries and is capable of removing more than 95% of the particulates from the exhaust gases. In utility applications, capital costs of baghouses are about $56/kW, and annual O&M costs are about $7.5/kW-yr (adapted from Shoat et al 1993). …”
Section: Particulate Controlmentioning
confidence: 99%