US3399117A - Tube for tube heater - Google Patents
Tube for tube heater Download PDFInfo
- Publication number
- US3399117A US3399117A US594707A US59470766A US3399117A US 3399117 A US3399117 A US 3399117A US 594707 A US594707 A US 594707A US 59470766 A US59470766 A US 59470766A US 3399117 A US3399117 A US 3399117A
- Authority
- US
- United States
- Prior art keywords
- tube
- tubes
- furnace
- temperature
- sections
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
- C10G9/18—Apparatus
- C10G9/20—Tube furnaces
- C10G9/203—Tube furnaces chemical composition of the tubes
Definitions
- FIG. 2 TUBE FOR TUBE HEATER Filed Nov. 16, 1966 FIG. 2
- the present invention relates to liquid heating furnaces, and more particularly to the tubes through which the liquid to be heated flows and the manner in which the tubes are fabricated.
- the metal used for the tubes is of material importance.
- the tubes must have chemical and physical characteristics that are capable of withstanding the maximum temperatures and pressures that are encountered. Usually the maximum stress imposed on a tube is at its exit end where the tube and liquid being heated are hottest. The entire tube, however, has to be capable of withstanding this maximum severity condition even though it may occur in only the last third or fourth of the tube.
- the cost of the tubes used in a furnace with severe heating requirements is a large portion ofthe cost of a furnace. This is both because of the length of the tubes, that may be up to sixty feet long, and because they must be of high alloy steel to withstand the service. Anything that can be done to reduce the cost of the tubes is of importance in the construction of such equipment.
- FIG. 1 is a section through one type of furnace in which a tube of the invention can be used.
- FIG. 2 is a view through a different type of furnace.
- a furnace of this type includes a structure 1 forming a furnace chamber having parallel side walls 2 and 3 and having an exhaust opening 4 at the upper end in one of the sides.
- the furnace is heated by horizontally extending parallel rows of burners 5 with the rows located one above the other in the side walls.
- the burners are directed toward a row of tubes, one of which is shown at 6, that extend vertically through the furnace chamber.
- Each horizontal row of burners 5 will be fired at a rate to raise the temperature of the portion of the tube in front of it to the desired value.
- the fluid to be heated which for example, if the product is to be hydrogen, can be a combination of methane and steam, will be directed vertically through the tube from either the top or the bottom.
- the tube for reasons to be described below, is made of a plurality of sections 7, 8 and 9 welded together at joints 10.
- the furnace shown in FIG. 2 is constructed similar to that of FIG. ,1 except that it is a dual furnace having two chambers one of which is indicated at 11 and the other at 12. These chambers are provided with exhaust passages 13 and 14 respectively that lead to a convection heating chamber 15 at the base of a stack.
- the exhaust gases flowing to the stack flow past a group of tubes 16 in chamber 15, known as a convection section, in which the tubes are heated by convection from the exhaust gases.
- the material flowing through the tubes of convection section 16 is directed to tubes 17 which are located in the chambers formed in furnace sections 11 and 12.
- the arrangement can be such that the material flowing through convection section 16 can go to a manifold which in turn supplies the various tubes 17 or it can go through a plurality of connecting pipes 18 directly into each of the tubes 17.
- the manner in which the piping is fabricated will depend entirely upon the operation which is to be performed by the furnace.
- the fluid to be treated is preheated in the convection section and is directed to tubes 17 in the two sections 11 and 12 of the furnace which are generally known as the radiant sections. In this section the fluid is raised from its preheat temperature to the final treatment temperature.
- the tube 18 is welded to the upper end of tube 17 and this latter tube is made up of two sections 19 and 21 that are joined together by a weld 20.
- the materials of which the tubes are fabricated will depend upon the severity of the service and the temperature to which the tubes and the material flowing through them is heated.
- the cost of the tubes will vary with their composition. It is almost axiomatic, however, the more severe the service and the higher the temperature and pressure required, the more expensive the tubes.
- the tube will have a temperature gradient of from about 1000 F. to 1850 F.
- a tube composition which is satisfactory for 1000 F. service is completely unsatisfactory for 1800 F. service.
- the entire tube has been made of a material capable of operating satisfactorily at the highest temperature encountered.
- the tubes are made in sections, and welded together, with each section of an analysis capable of withstanding the temperatures encountered along that portion of its length. Examples of materials that will withstand various temperatures are:
- the temperature of tube and the temperature of the m'at'erial'in it can'be determined at any point along its length by conventional methods. When this has been done, the proper alloy for any particular location can be determined. Ordinarily it will not be advisable to have the tube made of more than three sections for a tube forty feet in length. a
- the furnace or heater of FIG. 1 shows a tube fabricated of three sections each of which will be from ten to fifteen feet in length for a forty foot tube. The direction'of flow of the fluid being heated will determine whether the more expensive alloy is the top or bottom section.
- the tube 17 in FIG. 2 is shown as being of two sections. In a heater of this type the fluid is heated in convection section 16 to about 900 P. so that the convection coil and connecting portion 18 will be made of carbon steel tubes. For the higher temperatures in chamber 11 alloys suitable for the temperatures encountered will be used.
- the amount of expensive alloy used in a tube can be materially reduced by matching the alloy to the temperature encountered.
- a tube heating furnace for the pyrolysis of hydrocarbons
- the combination of structure forming a furnace "chamber having opposed walls, a plurality of vertically spaced burners located in said walls, a tube extending vertically through said chamber between said walls and in front of said burners to be heated thereby, said tube being adapted to transport fluid to be raised in temperature as it flows from first end to asecond end, said tube being made in a plurality of end to end sections with each section in the direction of fiuid flow beingmade of a different metal capable of withstandingsuccessively higher temperatures and-morefsevere service than the metal in the preceding section.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US594707A US3399117A (en) | 1966-11-16 | 1966-11-16 | Tube for tube heater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US594707A US3399117A (en) | 1966-11-16 | 1966-11-16 | Tube for tube heater |
Publications (1)
Publication Number | Publication Date |
---|---|
US3399117A true US3399117A (en) | 1968-08-27 |
Family
ID=24380040
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US594707A Expired - Lifetime US3399117A (en) | 1966-11-16 | 1966-11-16 | Tube for tube heater |
Country Status (1)
Country | Link |
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US (1) | US3399117A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3704590A (en) * | 1969-11-17 | 1972-12-05 | John O Van Derbeck | Vapor generating manifold and control system |
FR2522126A1 (en) * | 1982-02-22 | 1983-08-26 | Toyo Engineering Corp | OVEN FOR HEAT TREATMENT OF HYDROCARBONS |
FR2760465A1 (en) * | 1997-03-04 | 1998-09-11 | Procedes Petroliers Petrochim | Steam cracker for hydrocarbon, especially ethylene or propylene |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1647570A (en) * | 1926-05-15 | 1927-11-01 | Fred E Kling | Hot-blast stove |
US3062197A (en) * | 1959-07-23 | 1962-11-06 | Selas Corp Of America | Tube heater |
US3274978A (en) * | 1964-02-24 | 1966-09-27 | Lummus Co | Vertical tube fluid heater |
US3276436A (en) * | 1964-07-23 | 1966-10-04 | Lummus Co | Process heater |
-
1966
- 1966-11-16 US US594707A patent/US3399117A/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1647570A (en) * | 1926-05-15 | 1927-11-01 | Fred E Kling | Hot-blast stove |
US3062197A (en) * | 1959-07-23 | 1962-11-06 | Selas Corp Of America | Tube heater |
US3274978A (en) * | 1964-02-24 | 1966-09-27 | Lummus Co | Vertical tube fluid heater |
US3276436A (en) * | 1964-07-23 | 1966-10-04 | Lummus Co | Process heater |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3704590A (en) * | 1969-11-17 | 1972-12-05 | John O Van Derbeck | Vapor generating manifold and control system |
FR2522126A1 (en) * | 1982-02-22 | 1983-08-26 | Toyo Engineering Corp | OVEN FOR HEAT TREATMENT OF HYDROCARBONS |
FR2760465A1 (en) * | 1997-03-04 | 1998-09-11 | Procedes Petroliers Petrochim | Steam cracker for hydrocarbon, especially ethylene or propylene |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: FIRST PENNSYLVANIA BANK N A 19TH FL.CENTRE SQ WEST Free format text: SECURITY INTEREST;ASSIGNOR:SELAS CORPORATION OF AMERICA A CORP OF PA;REEL/FRAME:003997/0981 Effective date: 19820217 |
|
AS | Assignment |
Owner name: SELAS CORPORATION OF AMERICA A CORP. OF PA Free format text: RELEASED BY SECURED PARTY;ASSIGNOR:FIRST PENNSYLVANIA BANK N.V., FOR ITSELF AND AS AGENT FOR THE PHILADELPHIA NATIONAL BANK;REEL/FRAME:004096/0520 Effective date: 19821231 |
|
AS | Assignment |
Owner name: LINDE AKTIENGESELLSCAFT WIESBADEN, GERMANY A CORP. Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:SELAS CORPORATON OF AMERICA A CORP. OF PA;REEL/FRAME:004156/0552 Effective date: 19830523 Owner name: LINDE AKTIENGESELLSCAFT A CORP. OF GERMANY,GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SELAS CORPORATON OF AMERICA A CORP. OF PA;REEL/FRAME:004156/0552 Effective date: 19830523 |