[Code of Federal Regulations]
[Title 40, Volume 9]
[Revised as of July 1, 2003]
From the U.S. Government Printing Office via GPO Access
[CITE: 40CFR63.11]

[Page 59-60]
 
                   TITLE 40--PROTECTION OF ENVIRONMENT
 
         CHAPTER I--ENVIRONMENTAL PROTECTION AGENCY (CONTINUED)
 
PART 63--NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES--Table of Contents
 
                      Subpart A--General Provisions
 
Sec. 63.11  Control device requirements.

    (a) Applicability. The applicability of this section is set out in 
Sec. 63.1(a)(4).
    (b) Flares. (1) Owners or operators using flares to comply with the 
provisions of this part shall monitor these control devices to assure 
that they are operated and maintained in conformance with their designs. 
Applicable subparts will provide provisions stating how owners or 
operators using flares shall monitor these control devices.
    (2) Flares shall be steam-assisted, air-assisted, or non-assisted.
    (3) Flares shall be operated at all times when emissions may be 
vented to them.
    (4) Flares shall be designed for and operated with no visible 
emissions, except for periods not to exceed a total of 5 minutes during 
any 2 consecutive hours. Test Method 22 in appendix A of part 60 of this 
chapter shall be used to determine the compliance of flares with the 
visible emission provisions of this part. The observation period is 2 
hours and shall be used according to Method 22.
    (5) Flares shall be operated with a flame present at all times. The 
presence of a flare pilot flame shall be monitored using a thermocouple 
or any other equivalent device to detect the presence of a flame.
    (6) An owner/operator has the choice of adhering to the heat content 
specifications in paragraph (b)(6)(ii) of this section, and the maximum 
tip velocity specifications in paragraph (b)(7) or (b)(8) of this 
section, or adhering to the requirements in paragraph (b)(6)(i) of this 
section.
    (i)(A) Flares shall be used that have a diameter of 3 inches or 
greater, are nonassisted, have a hydrogen content of 8.0 percent (by 
volume) or greater, and are designed for and operated with an exit 
velocity less than 37.2 m/sec (122 ft/sec) and less than the velocity 
Vmax, as determined by the following equation:

Vmax=(XH2-K1)* K2

Where:

Vmax=Maximum permitted velocity, m/sec.
K1=Constant, 6.0 volume-percent hydrogen.
K2=Constant, 3.9(m/sec)/volume-percent hydrogen.
XH2=The volume-percent of hydrogen, on a wet basis, as 
calculated by using the American Society for Testing and Materials 
(ASTM) Method D1946-77. (Incorporated by reference as specified in 
Sec. 63.14).

    (B) The actual exit velocity of a flare shall be determined by the 
method specified in paragraph (b)(7)(i) of this section.
    (ii) Flares shall be used only with the net heating value of the gas 
being combusted at 11.2 MJ/scm (300 Btu/scf) or greater if the flare is 
steam-assisted or air-assisted; or with the net heating value of the gas 
being combusted at 7.45 M/scm (200 Btu/scf) or greater if the flares is 
non-assisted. The net heating value of the gas being combusted in a 
flare shall be calculated using the following equation:
[GRAPHIC] [TIFF OMITTED] TR04MY98.004

Where:

HT=Net heating value of the sample, MJ/scm; where the net 
enthalpy per mole of offgas is based on combustion at 25  deg.C and 760 
mm Hg, but the standard temperature for determining the volume 
corresponding to one mole is 20  deg.C.
K=Constant=
[GRAPHIC] [TIFF OMITTED] TR04MY98.005

where the standard temperature for (g-mole/scm) is 20  deg.C.
Ci=Concentration of sample component i in ppmv on a wet 
basis, as measured for organics by Test Method 18 and measured for 
hydrogen and carbon monoxide by American Society for Testing and 
Materials (ASTM) D1946-77 or 90 (Reapproved 1994) (incorporated by 
reference as specified in Sec. 63.14).
Hi=Net heat of combustion of sample component i, kcal/g-mole 
at 25  deg.C and 760 mm Hg. The heats of combustion may be determined 
using ASTM D2382-76 or 88 or D4809-95 (incorporated by reference as 
specified in Sec. 63.14) if published values are not available or cannot 
be calculated.
n=Number of sample components.


[[Page 60]]


    (7)(i) Steam-assisted and nonassisted flares shall be designed for 
and operated with an exit velocity less than 18.3 m/sec (60 ft/sec), 
except as provided in paragraphs (b)(7)(ii) and (b)(7)(iii) of this 
section. The actual exit velocity of a flare shall be determined by 
dividing by the volumetric flow rate of gas being combusted (in units of 
emission standard temperature and pressure), as determined by Test 
Method 2, 2A, 2C, or 2D in appendix A to 40 CFR part 60 of this chapter, 
as appropriate, by the unobstructed (free) cross-sectional area of the 
flare tip.
    (ii) Steam-assisted and nonassisted flares designed for and operated 
with an exit velocity, as determined by the method specified in 
paragraph (b)(7)(i) of this section, equal to or greater than 18.3 m/sec 
(60 ft/sec) but less than 122 m/sec (400 ft/sec), are allowed if the net 
heating value of the gas being combusted is greater than 37.3 MJ/scm 
(1,000 Btu/scf).
    (iii) Steam-assisted and nonassisted flares designed for and 
operated with an exit velocity, as determined by the method specified in 
paragraph (b)(7)(i) of this section, less than the velocity 
Vmax, as determined by the method specified in this 
paragraph, but less than 122 m/sec (400 ft/sec) are allowed. The maximum 
permitted velocity, Vmax, for flares complying with this 
paragraph shall be determined by the following equation:

Log10(Vmax)=(HT+28.8)/31.7

Where:

Vmax=Maximum permitted velocity, m/sec.
28.8=Constant.
31.7=Constant.
HT=The net heating value as determined in paragraph (b)(6) of 
this section.

    (8) Air-assisted flares shall be designed and operated with an exit 
velocity less than the velocity Vmax. The maximum permitted 
velocity, Vmax, for air-assisted flares shall be determined 
by the following equation:

V4max=8.71 = 0.708(HT)

Where:

Vmax=Maximum permitted velocity, m/sec.
8.71=Constant.
0.708=Constant.
HT=The net heating value as determined in paragraph 
(b)(6)(ii) of this section.

[59 FR 12430, Mar. 16, 1994, as amended at 63 FR 24444, May 4, 1998; 65 
FR 62215, Oct. 17, 2000; 67 FR 16605, Apr. 5, 2002]