CRYOGENIC FLOW CONTROLS (CFC VIETNAM)
[A] : 9th Floor, C.T Building, 56 Yen The Str., Ward 2, Tan Binh Dist., HCMC, Vietnam
[P] : (+84) 28 5449 2068 - [F] : (+84) 28 5449 2069
[E] : hung.nguyen@cfc-vietnam.vn
[W] : www.cfc-vietnam.vn
|
APPLICATIONS |
|||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND
|
TELEDYNE MODEL |
Ethyl Benzene / Styrene Monomer Raytheon Badger, ABB Lummas
|
Styrene vent gas |
PPM oxygen |
0-2000 ppm O2 |
H2 / N2 / CO2 / mix |
|
Transalkylation regen gas |
Percent oxygen |
0-15% O2 |
O2 / N2 / CO / CO2 |
||
Transalkylation regen gas |
Percent CO / percent CO2 |
0-20% CO / 0 - 20% CO2 |
O2 / N2 / CO / CO2 |
||
Stacked gas (2-4 sets) |
Percent O2 |
0-5% O2 |
Flue gas |
||
Stripped condensate |
Hydrocarbons |
0-10 ppm HC |
Condensate (H20) |
||
Cooled condensate |
Hydrocarbons |
0-100 ppm HC |
Condensate (H20) |
||
EB recycle stream |
PPM H2O (L) |
0-300 ppm H20 |
Benzene |
5020 (NIR) |
|
|
|||||
Polystyrene |
Headspace of styrene tanks |
Percent O2 |
0-5% O2 |
N2 / Styrene vapors |
Series 3220 |
|
|||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
Ethylene oxide / Ethylene glycol Scientific Design |
Ethylene feed / Reactor inlet and reactor outlet |
Percent C2H4 |
0-20%, 0-40% C2H4 |
CO2 / AR / CH4 |
|
Ethylene feed / Reactor inlet and reactor outlet |
Percent O2 |
0-10%, 0-25% O2 |
CO2 / AR / CH4 |
3020M |
|
EO purification unit |
Percent LEL |
0-100% combustibles |
Ambient air |
||
Ethylene glycol product |
Percent H2O (L) |
0-5% H2O |
Ethylene glycol |
5020 |
|
|
|||||
Acetone / Phenol / Cumene M.W. Kellogg |
Oxidizer vent gas (No. 1 & 2) |
Percent O2 |
0-10%, 0-25% O2 |
N2, Cumene, H2O |
|
Recycle compressor drum gas |
Percent H2 |
50-100% H2 |
N2, CH4 |
||
Acetone product to storage |
Percent H2O (L) |
0 - 0.5%, 0-5% H2O (L) |
Acetone |
5020 (NIR) |
|
Heavy ends fired boiler |
Percent O2 |
0-5% O2 |
Flue gas |
||
|
|||||
EDC / VCM B.F. Goodrich |
Absorber vent gas |
Percent O2 |
0-5% O2 |
CO2 / H20 / CL2 / HCL |
Htd Paramagnetic required |
Stripper vent gas |
Percent O2 |
0-5% O2 |
CO2 / H20 / CL2 / HCL |
Htd Paramagnetic required |
|
VCM vent gas |
PPM O2 |
0-10 / 0-100 PPM O2 |
VCM (G) |
||
H2O in EDC |
PPM H20 (L) |
0-50 / 0-200 PPM H2O |
EDC (pure) |
5020 (NIR) |
|
CL2 in EDC |
PPM CL2 (L) |
0-1000 PPM CL2 |
EDC (pure) |
||
H20 in TCE / PCE |
Percent CO |
0-20% |
N2 / CO2 / C2H4 |
||
Percent CO2 |
0-20% |
N2 / CO2 / C2H4 |
|||
Percent C2H4 |
0-40% |
N2 / CO2 / C2H4 |
|||
|
|||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
Acrylonitrite B.P. Chemical |
Product storage inhibitor |
PPM / Percent H2O (L) |
0-2000 PPM, 0 - 1% |
Acrylonitrile (pure) |
5020 (NIR) |
Product storage inhibitor |
MethylHydroquinone |
0-100 PPM MEHQ (L) |
Acrylonitrile (pure) |
||
Product storage / N2 blanket |
Percent O2 |
0-10% O2 |
AcryloVapors + N2 |
||
|
|||||
Methyl Methacrylate ICI |
ACH vent blower - safety |
Percent O2 |
0-5% O2 (Alarm @ 2%) |
N2 + HCN + Acetone |
|
|
|||||
Acetic Acid B.P. Chemical |
Reactor system - liquid effluent |
Percent H2O (L) |
0-20% |
Acetic acid - HOAC |
5020 (NIR) |
Drying column - side |
Percent H2O (L) |
0-20% |
Acetic acid - HOAC |
5020 (NIR) |
|
Drying column - bottoms |
PPM H2O |
0-1500 PPM |
Acetic acid - HOAC |
5020 (NIR) |
|
Flare gas header |
PPM methyl iodide |
0-1000 PPM |
CO / CO2 / N2 / H2 |
||
Combined off gas |
PPM methyl iodide |
0-1000 PPM |
CO / CO2 / N2 / H2 |
||
Combined off gas |
Percent H2 |
0-30% |
CO / CO2 / N2 / H2 |
2020 (TCD) |
|
Promoter off gas |
Percent H2 |
0-30% |
CO / CO2 / N2 / H2 |
2020 (TCD) |
|
Steam condensate / leaving plant |
PPM Hydrocarbons |
0-10 PPM |
Condensate (H2O) |
||
PPM O2 |
0-150 PPM |
CO (90%) |
|||
|
|||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
Titanium Dioxide DuPont; Kronos; Kemira; Kerr-McGee; SCM Chemicals |
Chlorinator exit gas |
PPM CL2 |
0-1000 PPM |
TiCL / N2 / CO2 |
|
Stack vent gas |
PPM CL2 |
0-500 PPM |
CO2 / N2 / CO |
||
Stack vent gas |
PPM SO2 |
0-500 PPM |
CO2 / N2 / CO |
||
Process |
PPM Vanadium (L) |
0-10 PPM |
CCL4 |
||
|
|||||
Ammonia / Urea Fertilizer Plants Snamprogetti; M.W. Kellogg |
Primary and secondary reformer outlet |
Percent CH4 - 3 sets |
0 - 0.5% up to 0-20% |
H2 / CO2 / CO / N2 |
|
HTS / LTS shift converter outlet |
Percent CO - 2 sets |
0 - 0.5% up to 0-5% |
H2 / CO2 / CO / N2 |
||
Absorber outlet |
Percent CO2 - 2 sets |
0 - 0.3% and 0 - 1.5% |
H2 / CO2 / CO / N2 |
||
Methanator and NH3 converter outlet |
Percent H2 - 2 sets |
50-100% |
N2 / CH4 |
2020 (TCD) |
|
Percent O2 - 2 sets |
0 - 0.5% O2 |
N2 / H2 / CO2 |
3020MParamagnetic |
||
CO2 Feed to urea plant |
Percent O2 |
0-1% |
CO2, H2, N2, Ar |
||
Stack gas |
Percent O2 - 2 sets |
0-5% and 0-10% O2 |
N2 / CO2 / O2 / H2Ov |
||
Treated waste water |
Oil / Hydrocarbons |
0-150 PPM |
Water |
||
|
|||||
Vinyl Chloro Monomer (VCM) |
Inlet of recovered VCM compressor |
Percent O2 |
0-1 and 0-5% |
VCM (96%), H2Ov |
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
||||
Polpropylene (PP) |
N2 blanketing appls |
Percent and PPM O2 |
0-1% and 0-10 ppm O2 |
N2 |
|||||
2. Random copolymer |
Pellitizing building |
Percent oxygen |
0-1 and 0-5% O2 |
N2 |
3220 - 4 system |
||||
3. Impact copolymer |
Ethylene and propylene feeds |
PPM O2 |
0-10 PPM |
Ethylene / propylene |
|||||
Amoco PP Process |
Main powder conveying |
O2 |
0-1% O2 |
N2 |
|||||
Recycle gas - 4 sets |
O2 |
0-1, 0-10, 0-100 ppm |
Propylene |
||||||
Extruder inlet (mixed feed chute) |
O2 |
0-1% |
N2 |
||||||
|
|||||||||
Maleic Anhydride (MAN) |
Reactor feed duct to mixer |
Butane |
0-3% |
N2, H2Ov |
7500Z (NDIR) Z-purged |
||||
H2Ov |
0-5% |
N2, Butane |
|||||||
Reactor off-gas / Switch cooler |
Butane |
0-1% |
HC / CO / CO2 / N2 |
7500Z (NDIR) Z-purged |
|||||
CO / CO2 |
0-2% / 0-2% |
HC / CO / CO2 / N2 |
7500Z (NDIR) Z-purged |
||||||
Maleic Anhydride |
0-2% |
HC / CO / CO2 / N2 |
|||||||
Absorber |
O2 / Combustibles |
0-5% O2 / 0-5% CH4eq |
N2, CO2, CO, H2Ov |
9700 (Z purged) |
|||||
Incinerator stack |
O2 / CH4 |
0-25% O2 & 0-15 ppm |
N2, CO2, CO, H2Ov |
7500Z (NDIR) Z-purged |
|||||
|
|||||||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
||||
Butadiene |
Oxygen in vent vapor |
O2 |
0-1000 ppm |
N2 / Trace styrene |
|||||
O2 in Butadiene product |
O2 |
0-30 ppm |
Butadiene |
||||||
Process vent - 2 sets |
O2 |
0-1000 ppm |
N2 / Hexane |
||||||
Above bed #4 of mainwasher |
1, 3 Butadiene |
0-70% |
Multihydrocarbons |
||||||
Above bed #4 of rectifier |
Cis-2-Butene |
0-10% |
Multihydrocarbons |
||||||
BASF |
Butadiene extraction solvent recovery process |
H2O (L) |
0-10% |
NMP solvent |
5020 NIR |
||||
Nippon Zeon |
Butadiene extraction |
H2O (L) |
0-300 / 0-3000 ppm H2O |
DMF |
5020 NIR |
||||
|
|||||||||
Polycarbonate |
Product conveying system |
Percent O2 |
0-5% & 0-10% O2 |
N2 blanket gas |
Insta Trans |
||||
Phosgene in N2 atmosphere |
PPM COCL2 |
0-100 / 0-1000 ppm |
N2 / CO |
7500Z NDIR - 3 sets |
|||||
NaOH in water |
Percent NaOH |
0-12% |
H2O |
Series 5000 NIR - 2 sets |
|||||
Bisphenol-A in water |
Bisphenol-A |
0-25, 0-100 ppm |
H2O / NaCl |
Series 6000(UV - 2 sets |
|||||
|
|||||||||
Hexamethylene Diamine |
Tank car headspace / N2 blanketing |
PPM - Percent O2 |
0-1000 ppm, 0-1% |
N2 / HMD vapors |
|||||
|
|||||||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
||||
Butyl rubber plant |
Water in MethylChloride |
PPM H2O |
0-1000 and 0-5000 PPM |
MethylChloride |
5020 (NIR) |
||||
|
|||||||||
Synthetic rubber |
Water in Acetone |
PPM H2O |
0-5000 ppm |
Acetone |
5020 (NIR) |
||||
|
|||||||||
Tert-Butyl Alcohol |
Water in Tert-Butyl Alcohol |
Percent H2O |
0-50% |
T-Butyl Alcohol |
5020 (NIR) |
||||
|
|||||||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
||||
Copolymers |
PTA dust explosion monitor |
Percent O2 |
0-10% O2 |
N2 |
|||||
O2 in vacuum pump seal tank off gas |
Percent O2 |
0-5%, 0-10% |
N2 |
||||||
|
|||||||||
Pure Terephthalic Acid (PTA) |
Oxidation reactor - safety |
Percent O2 |
0-10% O2 |
CO2, H2Ov, HOAC |
3020P |
||||
Percent CO2 |
0-10% and 0-20% CO2 |
O2, H2Ov, HOAC |
|||||||
Percent CO |
0-1% |
HOAC = Acetic Acid |
|||||||
Before catalytic oxidation reactor |
Percent LEL |
0-100% |
N2, HC's, O2 |
1220 / 177 |
|||||
After catalytic oxidation reactor |
PPM hydrocarbons |
0-30 ppm |
N2, O2 |
4020 system (x-purged) |
|||||
Pneumatic conveying system and PTA storage silos |
Percent O2 |
0-10% |
N2, Trace HOAC |
||||||
Stack gas application / CEM |
PPM NOx |
0-500 ppm |
Flue gas |
||||||
Percent O2 |
0-5% |
Flue gas |
|||||||
Flow velocity |
0-5% |
Flue gas |
MT-91 (FCI) |
||||||
|
|||||||||
INDUSTRY |
SERVICE |
PARAMETER |
RANGE |
BACKGROUND |
TELEDYNE MODEL |
||||
PET |
N2 blanketing / Amorphous |
PPM O2 |
0-10 ppm |
N2 blanketing gas |
|||||
Upgrade of PET chips |
PPM hydrocarbons |
0-10 ppm |
N2 blanketing gas |
||||||
Ambient / Safety |
Percent LEL |
0-100% (Acetaldhyde) |
Air |
||||||
|
|||||||||
Nylon 6, 6 |
Transfer conveying system and storage - N2 blanketing |
PPM O2 |
0-10 / 0-100 ppm |
N2 |
3000TBC - 8 sets or sequenced solution |
||||
|
|||||||||
Polyster Filament Yarn |
Slurry mix tank (PTA + glycol) |
Percent H2O in MEG (L) |
0-5% |
MonoethyyleneGlycl |
5020 (NIR) |
||||
Percent H20 (L) |
0-2% |
MEG + PTA |
5020 (NIR) |
||||||
Distillation column - bottoms |
Percent H2O (L) |
0-5% |
MEG |
5020 (NIR) |
|||||
|
|||||||||
Chlorine Manufacturing |
Electrolysis of NaCl + H2O |
PPM O2 |
0-10 / 0-100 ppm |
H2 (99%) |
|||||
PPB Hg |
0-100 ppb |
H2 (99%) |
Series 6000(UV) |
||||||