INDUSTRIAL
GAS DATA "ARGON"
AWS
SG-A

ARGON NORTH AMERICA CYL VALVE CGA 580
ARGON
MANUFACTURED FROM AIR DISTILLATION
ARGON
CONTENT IN AIR 0.93% BY VOLUME
Ar
BOILING POINT AT 1 atm 101.3kPa 302.53oF -187.87oC
Ar
CRITICAL DENSITY 33.44 lb/CF 535.6 kg/cum
Ar
CRITICAL PRESSURE 707.2 psi 4874 kPa
Ar
CRITICAL TEMPERATURE -188.33oF -122.43oC
Ar
DENSITY 32oF 0oC 1 atm 101.3 kPa = 0.111 lb/CF 1.784 kg/cum
ARGON
HEAVIER THAN AIR AIR=1 ARGON = 1.38
ARGON
FREEZE POINT AT 1 atm -308.66oF -189.28oC
ARGON
NON TOXIC WILL CAUSE ASPHYXIATION AT 50% AIR VOLUME
ARGON
LIQUID CAUSES FREEZE BURNS
ARGON
GAS INSTALLATION USE MOST COMMON METALS
ARGON
LIQUID INSTALLATION USE AUSTENITIC NON FERROUS METALS
ARGON
CONVERSION DATA
1-lb
= 0.4536kg
1-lb = 9.671 CF 0.2543 cu m
1-lb
= 0.86 LIQ GAL 0.3255 L
1kg = 2.205-lb
1-kg
= 21.32 CF 0.5605 cu m
1-kg = 0.1896 LIQ GAL 0.7176 L
1cu
m = 3.933 lb 1.7840 kg
1cu m = 38.04 CF
1cu
m = 0.3382 LIQ GAL 1.2802 L
1 LIQ GAL = 112.5 CF 2.957 cu m
1
LIQ GAL = 3.785 LIQ liter
1 liter LIQ = 3.072 lb 1.394 kg
1
liter LIQ = 0.2642 LIQ GAL
1 liter = 29.71 CF 0.7812 cu m
1
CF GAS = 0.02628 cu m
1 CF GAS = 0.1034 lb 0.0469 kg
1
CF GAS = 0.008893 LIQ GAL
1 CF GAS = 0.03366 LIQ liter
INDUSTRIAL
GASES
"CARBON DIOXIDE"
AWS
SG-C
CO2
PROPERTIES AND CONVERSIONS
CO2
NORTH AMERICA CYL VALVE 320
CARBON
DIOXIDE CO2 DATA MANUFACTURED FROM WASTE PRODUCTS
CO2
FROM COMBUSTION OF CARBON COMPOUND - OXY eg ETHYLENE IN O2
CO2
CRITICAL DENSITY 29.2 lb/CF 468 kg/cum
CO2
CRITICAL PRESSURE 1070.8 psi 7380 kPa
CO2
CRITICAL TEMPERATURE 87.8oF 31oC
CO2
DENSITY 32oF 0oC 1 atm 101.3 kPa = 0.1234 lb/CF 1.977 kg/cum
CO2
TRIPLE POINT 60 psi 416 kPa -69.9oF -56.6oC
CO2
HEAVIER THAN AIR. AIR = 1 CO2 = 1.5291
CO2
CAN BE ABSORBED BY THE BLOOD FROM LUNGS AND SKIN
CO2
STIMULATES RESPIRATORY RATE 3% CAN INCREASE BREATHING RATE
CO2
TO 5% IN AIR CAUSES HEADACHE TO 10% INCREASES BLOOD PRESSURE
CO2
TO 20% IN AIR CAUSES CRAMPS UNCONSCIOUSNESS STROKE
AT
ANY SIGN OF AFFECT MOVE TO VENTILATED AREA
LIQUID
CO2 FREE STATE PRODUCES DRY ICE -108oF -78oC FREEZE BURNS
PROVIDE
VENTILATED AREA WITH CO2 KEEP CYLINDER UP RIGHT
CO2
HEAVIER THAN AIR - IF LEAKS OCCUR BEWARE GAS AT GROUND LEVEL
DRY
CO2 NON CORROSIVE GAS USE WITH MOST METALS
AT
HI TEMP ABOVE 1292oF 700oC, CO2 OXIDIZING EFFECT SOME METAL
MOIST
CO2 USE ACID RESISTANT STEEL ALLOYS WITH HIGH COPPER
MOIST
CO2 USE COPPER BRASS BRONZE - AVOID AIR WITH CO2 MIX
AVOID
AMMONIA TRYMETHYAMINE ETHYLAMINE METHYLAMINE WITH CO2
AVOID
DIMETHYLAMINE CO2 MAY CAUSE VIOLENT ACTION
CO2
CONVERSION DATA
1-lb
= 0.0005 TONS 0.4536kg
1-lb = 8.741 CF 0.2294 cu m
1-lb
= 0.118 LIQ GAL
0.4469 L
1kg = .0011 TONS 2.205-lb
1kg
= 19.253 CF 0.5058 cu m
1kg = 0.2603 LIQ GAL 0.986 L
1
CF GAS = 0.1144 lb 0.05189 kg
1 CF GAS = 0.02628 cum 0.05113 L
1
CF GAS = 0.0135 GAL
1cu m GAS = 4.36 lb 0.00218 TONS
1cu
m GAS = 0.5146 GAL 1.948 L
1cu m GAS = 1.977 kg 38.04 CF
1
LIQ GAL = 8.47 lb 0.00424 TONS
1 LIQ GAL = 3.842 kg 74.04 CF
1
LIQ GAL = 1.9431 cu m 3.785 L
1 LIQ L = 2.238 lb 0.001119 TONS
1
LIQ L = 1.0151 kg 19.562 CF
1 LIQ L = 0.5134 cu m 0.2642 GAL
INDUSTRIAL
GASES NITROGEN
AWS SG-N

NORTH
AMERICA N2 CYL VALVE CGA 580
N2
MANUFACTURED SAME AS OXYGEN DISTILLATION OF AIR
N2
COLORLESS TASTELESS NONFLAMMABLE
N2
CANNOT SUPPORT COMBUSTION INERT EXCEPT AT HI TEMP
N2
BOILING POINT AT 1 atm 101.3 kPa -320oF -195.8oC
N2
IONIZATION ENERGY 14.5 VOLTS
N2
CRITICAL LIMITS DENSITY 19.6 lb/CF 314 kg/cum
N2
CRITICAL LIMITS PRESSURE 493 psia 3400 kPa
N2
CRITICAL LIMITS TEMPERATURE -232.29oF -146.85oC
N2
DENSITY AT 70oF 1atm 101.3kPa 0.0724 lb/CF
N2
DENSITY 21.1oC 101.3kPa 1atm 1.1605 kg/cum
N2
MELTING POINT 1atm 101.3kPa -345.7oF -209.8oC
N2
RELATIVE DENSITY AT 68oF 20oC 1atm = 0.967 AIR=1
N2
CAN CAUSE ASPHYXIATION 50% IN AIR CAUSES SUFFOCATION
N2
LIQUID CAUSES FREEZE BURNS
GASEOUS
N2 INSTALLATION COMMON METALS MAY BE USED
USE
AUSTENITIC METALS FOR LIQUID NITROGEN
N2
CONVERSION DATA
1-lb = 13.803 CF 0.3627 cum
1-lb
= 0.1481 LIQ GAL 0.5606 L
1-lb = 0.4536kg
1kg
= 2.205-lbs
1kg = 30.42 cf 0.7996 cum
1kg
= 0.3262 LIQ GAL
1kg = 1.2349 liter
1
cum = 2.757 lb 1.2506 kg
1 cum = 0.408 LIQ GAL 1.544 L
1
LIQ GAL = 6.745 lb 3.06 kg
1 LIQ GAL = 93.11 cf
1
LIQ GAL = 2.447 cum 3.785 L
1 Liter = 1.782 lb LIQUID
1
liter = 0.8083 kg 0.2642 GAL
1 liter = 24.6 cf 0.6464 cum
N2
GAS 1 cf = 0.02628 cum
1 cf = 0.0724 lb 0.0329 kg
N2
GAS 1 cf = 0.01074 LIQ GAL
1 cf = 0.04065 liter
INDUSTRIAL
GAS DATA
HELIUM
AWS SG-He

HELIUM NORTH AMERICA CYL VALVE CGA 580
HELIUM
DATA - AN INERT GAS He MOLECULAR WEIGHT 4.003
HELIUM
EXTRACTED FROM HELIUM BEARING NATURAL GAS
HELIUM
BOILING POINT 1 atm 101.3kPa = -452oF -268.9oC
HELIUM
DENSITY AT 32oF OoC 1 atm 0.0111 lb/cf 0.1785 kg/cum
He
RELATIVE DENSITY 32oF 0oC 1 atm 101.3kPa = 0.138 AIR=1
HELIUM
IONIZATION ENERGY 24.6 VOLTS
HELIUM
CRITICAL DENSITY 4.347 lb/cf 69.64 kg/cum
HELIUM
CRITICAL PRESSURE 33.82 psi 233.1 kPa
He
CRITICAL TEMPERATURE -450.27oF -267.95oC
He
MELTING POINT AT 0.037 atm 3.757 kPa = -456.03oF -271.15oC
He
CAN CAUSE ASPHYXIATION 50% IN AIR CAUSES SUFFOCATION
He
LIQUID CAN CAUSE SERIOUS FREEZE BURNS
AUSTENETIC
GRADES MAXIMUM 0.08% CARBON MAGNESIUM
AUSTENETIC
GRADES 0.5-6% MAGNESIUM FOR LIQUID He
He
GOOD DIFFUSION CAPABILITY SEALS GASKETS MADE FROM TEFLON
HELIUM
CONVERSION DATA
1-lb = 96.71 cf 2.542 cu m
1-lb
= 0.9593 LIQ GAL 3.631 L
1-lb = 0.4536kg
1kg
= 2.205-lb 213.2 cf
1kg = 2.115 GAL 8.006 L
1
cf GAS = 0.01034 lb 0.0047 kg
1 cf GAS = 0.02628 cu m
1
cf GAS = 0.00992 GAL 0.0375 L
1cu m GAS = 0.3935 lb 0.1785 kg
1cu
m GAS = 38.04 cf
1cu m GAS = 0.3775 GAL 1.429 L
1
LIQ GAL = 1.0423 lb 0.4728 kg
1 LIQ GAL = 100.80 cf 2.649 cu m
1
LIQ GAL = 3.785 liter
HELIUM
INDUSTRIAL GAS DATA
HYDROGEN
SG-H

HYDROGEN
NORTH AMERICA CYL VALVE CGA 350
HYDROGEN
DATA MANUFACTURED BY ELECTROLYSIS
HYDROGEN
ALSO MANUFACTURED BY OXIDIZING COAL OR HYDROCARBONS
HYDROGEN
COMBUSTION TEMP IN AIR 3713oF 2045oC OXY 4820oF 2660oC
H2
AUTO IGNITION TEMP AT 1 atm 101.3kPa IN AIR 1060oF 572oC
H2
AUTO IGNITION TEMP AT 1 atm 101.3kPa IN OXY 1040oF 560oC
H2
BOILING POINT AT 1 atm -422.96oF -252.76oC
H2
EXPLOSIVE LIMIT IN AIR 4.1-74.2% IN OXY 4.7-93.9%
H2
CRITICAL DENSITY 1.94 lb/cf 31 kg/cum
H2
CRITICAL PRESSURE 188.2 psi 1297 kPa
H2
CRITICAL TEMPERATURE -399.80oF -239.91oC
H2
DENSITY AT 70oF 21oC 1 atm 101.3kPa 0.0052 lb/cf 0.0834 kg/cum
H2
IONIZATION POTENTIAL 13.5V H2 IS COLORLESS AND FLAMMABLE
H2
IS LIGHTER THAN AIR AIR=1 H2 = 0.069
H2
BURNS IN AIR IN AN ALMOST INVISIBLE FLAME
H2
IGNITES EASY H2 + OXY OR AIR FORM AN EXPLOSIVE GAS
H2
COOLED TO ITS BOILING POINT
IS TRANSPARENT ODORLESS LIQUID
AS
LIQUID H2 IS ABOUT 25% AS HEAVY AS WATER
H2
LIQUID TO GAS EXPANDS APPROXIMATELY 850 TIMES
H2
CAUSES ASPHYXIATION AT 50% VOLUME IN AIR
H2
AS LIQUID CAN CAUSE SERIOUS FREEZE BURNS
AVOID
CHLORINE FLUORINE BROMINE WITH H2 - EXPLOSIVE RESULTS
H2
IGNITES ON CONTACT WITH PLATINUM - Cu OXIDE N2 OXIDES
H2
WILL REACT VIOLENTLY WITH PULVERIZED NICKEL - MAGNESIUM
H2
WILL REACT VIOLENTLY WITH ISOPROPYL ALCOHOL Ca CARBONATE
H2
ESCAPING GAS IGNITES SPONTANEOUSLY
BEFORE
OPENING CYLINDER VALVE VERIFY REGULATOR CONNECTION
STORE
H2 IN A NO FLAME AREA WITHOUT OXIDIZING GASES
H2
MOST METALS THAT SUPPORT OPERATING PRESSURE MAY BE USED
H2
DON'T USE POROUS METALS DIFFUSION THROUGH POROUS METALS
H2
LEAKS OCCUR EASY THROUGH REGULAR GAS JOINTS
USE
FLASHBACK PREVENTION DEVICES WITH H2
H2
CONVERSION DATA
1-lb = 192 cf 5.047 cu m
1-lb
= 1.6928 LIQ GAL 6.408 L
1-lb = 0.4536kg
1kg
= 423.3 cf 11.126 cu m
1kg = 3.733 GAL 14.128 liter
1kg
= 2.205-lb
1 GAL = 0.5906 lb 0.2679 kg
1
GAL = 113.41 cf
1 GAL = 2.981 cu m 3.785 liter
1cu
m = 0.1982 lb 0.0899 kg
1cu m = 0.336 LIQ GAL 1.27 L
1cu
m = 38.04 cf
1 liter = 30 cf 0.788 cu m
1
liter = 0.2642 GAL
1 cf GAS H2 = 0.0052 lb
1
cf GAS H2 = 0.00236 kg
1 cf GAS = 0.02628 cu m
1
cf GAS = 0.0088 LIQ GAL
1 cf GAS = 0.0334 liter LIQ