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Brand Name : YUHONG
Model Number : T9, X11CrMo9-1 + I, X11CrMo9-1 + NT , 1.7386, Steel 629, TUZ10CD9, X12CrMo9-1,STBA 26
Certification : ASME , U STAMP , TEMA, PED, API, ABS, BV, LR, DNV-GL, CCS, ISO , TS, KR
Place of Origin : China,Korea
MOQ : 1PC
Price : 1----10000 USD
Payment Terms : L/C, T/T
Supply Ability : 5000 tons / month
Delivery Time : 7----75 days
Packaging Details : Iron/Ply Wooden Case , Bundle + cap
Standard : ASME SA213, ASTM A213, ASME SA335, ASTM A335
Material Grade : T9, X11CrMo9-1 + I, X11CrMo9-1 + NT , 1.7386, Steel 629, TUZ10CD9, X12CrMo9-1,STBA 26
Application : Fire Furnace, Fired Heater, Raffinate Heaters, Extract Heater, Refinery Furnace, Radiant Tube,Convection coil, Convection Tube
Type : Seamless Tube , Coil Tube , Fin Tube
Packing : Bundle , ply wooden case
NDT : MT, ET, UT, HT, PT, PMI
ASME SA213 T9 Alloy Steel Seamless Tube For Fired Furnace, Fired Heater, Convection Tube, Radiant Tube
Yuhong Group supply a lot of Steel Pipes and tubes for different industries :
Stainless Steel Seamless Pipe ( ASME SA213 / ASTM A213 , ASME A312/ ASTM A312,ASME SA376/ ASTM A376: TP304, TP304H, TP310H, TP310S, TP316L , TP316H , TP317L , TP321, TP321H, TP347, TP347H );
Alloy Steel Seamless Pipe ( ASME SA213/ASTM A213, ASME SA335/ASTM A335: P1, P11, P12, P22, P23, P5, P9, P91, P92 , T1, T11, T12, T22, T23, T5, T9, T91, T92);
Carbon Steel Seamless Pipe:ASME SA106 GR.B;
Raffinate Heaters | Oil fired heater |
Extract Heaters | Gas fired heater |
Reactor | Helical coil fired heater |
Solvent | Vertical cylindrical fired heater |
Fractionator | Radiant Tube |
Refinery Furnace | Tube Coil |
Crude oil heater | Radiation Tube coil |
Vacuum Heater | Economizer |
Hydrotreater Heater | Convection coil |
Horizontal tube cabin fired heaters | Hoop-tube fired heater |
ASTM A-213/A-213M, ASME SA-213/SA-213M Specification for seamless Ferritic and Austenitic Alloy-Steel Boliler, Superheater, and heat-exchanger tubes
ASTM A-1016/A-1016M, ASME SA-1016/SA-1016M Specification for General Requirements for Ferritic Alloy Steel, Austenitic Alloy Steel, and Stain- less Steel Tubes
Chemical Components (%) | ||||||||||||
Grade | C | Mn | P | S | Si | Cr | Mo | V | Nb | N | Al | others |
T9 | 0.15 | 0.30-0.60 | ≤0.025 | ≤0.025 | 0.25-1.0 | 8.0-10.0 | 0.90-1.10 |
Grade | UNS Number | Heat Treat Type | Austenitizing / Solutioning Temperature, min or range ºF (ºC) | Subcritical Annealing or Tempering Temperature, Min or range ºF (ºC) |
T9 | K50400 | full or isothermal anneal normalize and temper | … | 1250 (675) |
Mechanical properties | ||||
Grade | Tensile | Yield | Elongation | Hardness |
Strength (Mpa) | Strength (Mpa) | (%) | ||
T9 | ≥415 | ≥205 | ≥30 | ≤89HRB |
Air Preheater :Heat exchanger device that uses some of the heat in the flue gases to raise the temperature of the air supply to the burners. |
Breeching:The hood that collects the flue gas at the convection section exit. |
Bridge:Wall Temperature - The temperature of the flue gas leaving the radiant section |
Bulk Temperature: The average temperature of the process fluid at any tube cross section. |
Center Wall:A refractory wall in the radiant section, which divides it into two separate cells. |
Coil: A series of straight tube lengths connected by 180 o return bends, forming a continuous path through which the process fluid passes and is heated. |
Convection Section: The portion of a heater, consisting of a bank of tubes, which receives heat from the hot flue gases, mainly by convection. |
Corbelling: Narrow ledges extending from the convection section side walls to prevent flue gas from flowing preferentially up the side of the convection section, between the wall and the nearest tubes. |
Crossover:Piping which transfers the process fluid either externally or internally from one section of the heater to another. |
Damper: A device to regulate flow of gas through a stack or duct and to control draft in a heater. |
Draft:The negative pressure (vacuum) at a given point inside the heater, usually expressed in inches of water. |
Excess Air - The percentage of air in the heater in excess of the stoichiometric amount required for combustion. |
Extended Surface - Surface added to the outside of bare tubes in the convection section to provide more heat transfer area. |
Film - A thin fluid layer adjacent to a pipe wall that remains in laminar flow, even when the bulk flow is turbulent. |
Film Temperature - The maximum temperature in the film, at the tube wall. |
Fire Box - A term used to describe the structure which surrounds the radiant coils and into which the burners protrude. |
Flue Gas - A mixture of gaseous products resulting from combustion of the fuel. |
Fouling - The building up of a film of dirt, ash, soot or coke on heat transfer surfaces, resulting in increased resistance to heat flow. |
Forced Draft - Use of a fan to supply combustion air to the burners and to overcome the pressure drop through the burners. |
Fired Heater Efficiency - The ratio of heat absorbed to heat fired, on a lower heating value basis. |
Header Box - The compartment at the end of the convection section where the headers are located. |
Heat Available - The heat absorbed from the products of combustion (flue gas) as they are cooled from the flame temperature to a given flue gas temperature. |
Heat Density - The rate of heat transfer per unit area to a tube, usually based on total outside surface area. |
Heat Duty - The total heat absorbed by the process fluid, usually expressed in MBtu/hr |
Induced Draft - Use of a fan to provide the additional draft required over that supplied by the stack, to draw the flue gas through the convection section, and any downstream heat recovery equipment. |
Lower Heating Value (LHV) - The theoretical heat of combustion of a fuel, when no credit is taken for the heat of condensation of water in the flue gas. |
Mass Velocity - The mass flow rate per unit of flow area through the coil. Typical units are lb/s-sq. ft. |
Natural Draft - System in which the draft required to move combustion air into the heater and flue gas through the heater and out the stack is provided by stack effect alone. |
Net Fuel - The fuel that would be required in the heater if there were no radiation losses. |
One-Side Fired Tubes - Radiant section tubes located adjacent to a heater wall have only one side directly exposed to a burner flame. Radiation to the back side of the tubes is by reflection/ re-radiation from the refractory wall. |
Pass - A coil that transports the process fluid from fired heater inlet to outlet. |
Radiant Section - The section of the fired heater in which heat is transferred to the heater tubes primarily by radiation from high-temperature flue gas. |
Service Factor – A measure of the continuity of operation, generally expressed as the ratio of total running days for a given time period to the total calendar days in the period. |
Shield Section - The first two tube rows of the convection section. |
Sootblower - A steam lance (usually movable) in the convection section for blowing soot and ash from the tubes using high-pressure steam. |
Stack - A cylindrical steel, concrete or brick shell which carries flue gas to the atmosphere and provides necessary draft. |
Stack Effect - The difference between the weight of a column of high-temperature gases inside the heater and/or stack and the weight of an equivalent column of external air,usually expressed in inches of water per foot of height. |
Stack Temperature - The temperature of the flue gas as it leaves the convection section,or air preheater directly upstream of the stack. |
Two-Side Fired Tubes - Radiant section tubes which are exposed on both sides to direct radiation from the burners. |
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ASME SA213 T9 Alloy Steel Seamless Tube For Fired Furnace Fired Heater Convection Tube Radiant Tube Images |