Page 355 - Air Pollution Control Engineering

07_Chap_Wang.qxd 05/05/2004 4:19 pm Page 332

7 (c) (c) (c) (c) (c) (c) (c) (c) (c) 17.8% vol CH 4 180 Btu/scf/ none

Mr. John Leake (999) 555–5024 Mr. Efrem Johnson No. of Emission Streams Under Review #3/Acetaldehyde Manufacturing Absorber Vent (3)

FORM * Telephone No. Agency contact Organic Content (1)*** Content (1) Heat/O 2 Particulate Content (3) Particle Mean Diam. (3) Drift Velocity/SO 3

EMISSION STREAM DATA Plant contact (b) (b) (b) (b) (b) (b) (b) (b) (b) P. Q. R. S. T. * The data presented are for an emission stream (single or combined streams) prior to entry into the selected control method(s). Use extra forms, if additional combustibles shown on lines D and F.

HAP (a) absorber vent (a) process plant (a) methylene chloride (a) organic vapor (a) 44,000 ppmv. (a) 436 mmHg of 77°F (a) insoluble in water (a) not given (a) 85 lb/lb-mole none 100ºF 30,000 scfm expected atmospheric none/none assume 98% removal flare, boiler, process heater ** The numbers in parentheses denote what data should be supplied depending on
Effluent Characteristics for Emission Stream 3

Glaze Chemical Company 87 Octane Drive Somewhere (State, Zip) Emission Stream Number/Plant Identification Emission Source Source Classification Emission Stream HAPs Class and Form Content (1,2,3) ** Vapor Pressure (1,2) Solubility (1,2) HAP Adsorptive Prop. (1,2) Molecular Weight (1,2) Moisture Content (1,2,3) Halogen/Metals (1,2) Applicable Regulation(s) Required

Table 1 Company Location (Street) (City) A. HAP B. C. D. HAP E. HAP F. HAP G. HAP H. I. HAP J. K. Temperature (1,2,3) L. Flow Rate (1,2,3) M. Pressure (1,2) N. O. U. V. W. = 1 = 2 = 3

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