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US3919073A - Heat resistant alloy for carburization resistance - Google Patents

Heat resistant alloy for carburization resistance Download PDF

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Publication number
US3919073A
US3919073A US501220A US50122074A US3919073A US 3919073 A US3919073 A US 3919073A US 501220 A US501220 A US 501220A US 50122074 A US50122074 A US 50122074A US 3919073 A US3919073 A US 3919073A
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US
United States
Prior art keywords
metal
manganese
hydrocarbon
alloy
carburization
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
Application number
US501220A
Inventor
Donald L Bagnoli
Anthony R Ciuffreda
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ExxonMobil Technology and Engineering Co
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Exxon Research and Engineering Co
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Filing date
Publication date
Priority claimed from US387946A external-priority patent/US3865634A/en
Application filed by Exxon Research and Engineering Co filed Critical Exxon Research and Engineering Co
Priority to US501220A priority Critical patent/US3919073A/en
Application granted granted Critical
Publication of US3919073A publication Critical patent/US3919073A/en
Anticipated expiration legal-status Critical
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14Thermal 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
    • C10G9/18Apparatus
    • C10G9/20Tube furnaces
    • C10G9/203Tube furnaces chemical composition of the tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006Controlling or regulating processes
    • B01J19/002Avoiding undesirable reactions or side-effects, e.g. avoiding explosions, or improving the yield by suppressing side-reactions
    • B01J19/0026Avoiding carbon deposits
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40Characteristics of the process deviating from typical ways of processing
    • C10G2300/4075Limiting deterioration of equipment

Definitions

  • This invention relates to the pyrolysis of hydrocarbons. More particularly, it relates to a technique for minimizing carburization of furnace tubes exposed to hydrocarbons under pyrolysis and reforming conditions.
  • Processes for the controlled pyrolytic decomposition of hydrocarbons are well known.
  • the hydrocarbon is decomposed at high temperatures, for example in the range of 1,700 to 2,000F. under varying pressure conditions ranging from atmospheric up to about 1,200 psi.
  • Such pyrolytic techniques are frequently used, for example, in producing ethylene.
  • the hydrocarbons are cracked at elevated temperatures in the presence of predetermined amounts of steam.
  • Pyrolytic techniques are also used for increasing the octane rating of gasoline.
  • a method of heating hydrocarbon carbons in contact with metal surfaces under conditions which normally would cause difficulties clue to carburization of the metal surfaces which comprises contacting the hydrocarbons of the metal surface containing adherent oxide layer of manganese and chromium, whereby heat is passed from the metal surface to the hydrocarbon without significant carburization of the metal.
  • the present invention contemplates a method of rendering metal surfaces exposed to hydrocarbons under pyrolysis and reforming conditions resistant to carburization by providing on such metal surfaces in contact with the hydrocarbons an adherent layer of manganese and chromium oxide.
  • an adherent layer of manganese and chromium oxide is formed on a metal alloy surface by oxidizing a nickelchromium-iron alloy that has at least 36 percent nickel and from 1.25 percent to 2.0 percent manganese.
  • the present invention can be carried out for example by passing a hydrocarbon through a heating means having one or more tubes or conduits which are heated directly or indirectly to transfer heat to the hydrocarbon.
  • the metal surfaces to be used in accordance with this invention should have an adherent coating of manganese and chromium oxide.
  • the metal tubes are formed from an alloy consisting essentially of chromium, nickel and iron and having at least 1.25 percent manganese and at least 36 percent nickel.
  • the alloy may have from 36 to 38 percent nickel, from 23 to 27 percent chromium, and from 1.25 percent to 2 percent manganese.
  • the metal surfaces are pretreated with steam at temperatures in the range of 500F. to about 2,000F., and preferably at about l,500F. for from about 24 hours to about 96 hours, such as about 72 hours.
  • the grain structure of the contact surface Equally important in providing an adequate protective coating of manganese and chromium oxide on the surface of the metal is the grain structure of the contact surface. It has been discovered that with furnace tubes, for example, the interior contact surface should be made up of equiaxed grain structure. Basically the grain structure is achieved by casting the alloy into a tube and controlling the thermal gradient during solidi fication. Any other technique known in the art for controlling grain structure can be employed.
  • a nickel content, in a nickel-chromiumiron alloy, of greater than 36 percent and a manganese content of greater than L percent is necessary to provide a good protective scale of manganese and chromium oxide in the interior surface of the furnace tube.
  • a method for heating hydrocarbons by contact with heated metal surfaces containing nickel and iron under conditions which are likely to result in carburization of the metal which comprises contacting said hydrocarbons with a heated metal surface that has an adherent layer of manganese and chromium oxide on the metal surface which is in contact with the hydrocarbon, whereby the metal is protected against carburization and heat is passed from the metal to the hydrocarbon.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The catastrophic carburization of metal furnace tubes used in cracking and pyrolyzing hydrocarbons is minimized by forming a protective scale of manganese and chromium oxide on the surface of the metal. A nickel content of about 36 to 38 percent and a manganese content of 1.25 to 2.0 percent in a nickel-chromiumiron alloy promotes the formation of the oxide scale upon treatment of the alloy with steam.

Description

United States Patent n 1 Bagnoli et al.
[ HEAT RESISTANT ALLOY FOR CARBL'RIZATION RESISTANCE [75] Imentors: Donald L. Bagnoli, Oak Ridge:
Anthony R. Ciuffreda, COlOfiltL both of NJ.
[73] Assignee: Exxon Research and Engineering Company Linden, NJ.
[22] Filed: Aug. 28. i974 [2|] App]. No: SOLZZO Related US. Application Data [62] Dnision olSer No 3X7,)4(1 Aug l3. I973 Put. No
.RSfiiM-t.
[52] L15. Cl. 208/47; 208/48 R {5|} lnt. Cl. C100 9/l6; ClOG 9/22 [58] Field of Search w. 208/47, 48
[561 References Cited UNITED STATES PATENTS lJtllU-W 3/193) Norwood r r r r v i i i i v r ZEN/6X3 NOV. 11, 1975 2.543.710 2/195! Schmidt et ul Y r H Hit/(x15 167M150 3/I954 Shortsleew et ul.. .7 19ml 35 290m 9/1959 ShilplLighi 21mm 3.260.594 7/l966 Ornitz et ill i i v i i. 757138 A Prl'mm' EmminerDclbert E. Gantz Assisnmr Examiner-G. E. Schmitkons Attorney, i-lgenl 0r FirmJoseph J. Dvorak [57] ABSTRACT 3 Claims. N0 Drawings HEAT RESISTANT ALLOY FOR CARBURIZATION RESISTANCE RELATED APPLICATION This is a division, of application Ser. No. 387,946, filed Aug. 13, 1973, now US. Pat. No. 3,865,634.
BACKGROUND OF THE INVENTION This invention relates to the pyrolysis of hydrocarbons. More particularly, it relates to a technique for minimizing carburization of furnace tubes exposed to hydrocarbons under pyrolysis and reforming conditions.
Processes for the controlled pyrolytic decomposition of hydrocarbons are well known. Typically, the hydrocarbon is decomposed at high temperatures, for example in the range of 1,700 to 2,000F. under varying pressure conditions ranging from atmospheric up to about 1,200 psi. Such pyrolytic techniques are frequently used, for example, in producing ethylene. The hydrocarbons are cracked at elevated temperatures in the presence of predetermined amounts of steam. Pyrolytic techniques are also used for increasing the octane rating of gasoline.
It has been well recognized that the above-mentioned cracking and reforming processes when conducted in the presence of certain metals and metal alloys often lead to excessive deposition of carbon. These carbon deposits not only tend to reduce the size of the furnace tubes with concomitant problems of plugging, but most importantly they also affect the strength of the metal furnace tubes resulting in strucutral failure of the metal tubes. In such instances such failure is frequently referred to as catastrophic carburization of the metal.
It is know for example that iron surfaces will have a catalytic effect upon the pyrolysis of hydrocarbons, promoting carbon formation. The carbon formed is absorbed or diffused into the metal resulting in the structural failure of the metal. Consequently, numerous techniques have been proposed for avoiding such catastrophic carburization of metal tubes by alloying the iron and/or by forming protective coatings of an oxide on the surface of the metal to be contacted with the hydrocarbon under the reforming or pyrolysis conditions. None of these techniques have provided a complete panacea and there is more than definite commercial interest in prevent carburization of fumace tubes exposed to hydrocarbons under pyrolysis and reforming conditions.
SUMMARY OF THE INVENTION According to the present invention, there is provided a method of heating hydrocarbon carbons in contact with metal surfaces under conditions which normally would cause difficulties clue to carburization of the metal surfaces which comprises contacting the hydrocarbons of the metal surface containing adherent oxide layer of manganese and chromium, whereby heat is passed from the metal surface to the hydrocarbon without significant carburization of the metal.
Thus, in one aspect the present invention contemplates a method of rendering metal surfaces exposed to hydrocarbons under pyrolysis and reforming conditions resistant to carburization by providing on such metal surfaces in contact with the hydrocarbons an adherent layer of manganese and chromium oxide.
2 In yet another aspect of the present invention an adherent layer of manganese and chromium oxide is formed on a metal alloy surface by oxidizing a nickelchromium-iron alloy that has at least 36 percent nickel and from 1.25 percent to 2.0 percent manganese.
DETAILED DESCRIPTION OF THE INVENTION The present invention can be carried out for example by passing a hydrocarbon through a heating means having one or more tubes or conduits which are heated directly or indirectly to transfer heat to the hydrocarbon. The metal surfaces to be used in accordance with this invention should have an adherent coating of manganese and chromium oxide.
In a particularly preferred embodiment of the present invention the metal tubes are formed from an alloy consisting essentially of chromium, nickel and iron and having at least 1.25 percent manganese and at least 36 percent nickel. For example, the alloy may have from 36 to 38 percent nickel, from 23 to 27 percent chromium, and from 1.25 percent to 2 percent manganese. Indeed such an alloy when contacted with steam at elevated temperatures for a time sufficient to oxidize some of the manganese present in the alloy results in the formation of an adherent protective coating of manganese and chromium oxide which is resistant to carburization. For example, the metal surfaces are pretreated with steam at temperatures in the range of 500F. to about 2,000F., and preferably at about l,500F. for from about 24 hours to about 96 hours, such as about 72 hours.
Equally important in providing an adequate protective coating of manganese and chromium oxide on the surface of the metal is the grain structure of the contact surface. It has been discovered that with furnace tubes, for example, the interior contact surface should be made up of equiaxed grain structure. Basically the grain structure is achieved by casting the alloy into a tube and controlling the thermal gradient during solidi fication. Any other technique known in the art for controlling grain structure can be employed.
The invention will be better understood by reference to the following examples and demonstrations.
EXAMPLE I TABLE I Alloy l Alloy 2 Carbon, 0.4-0.5 0.43 Manganese, *2 L09 L30 Silicon. I.0l LIO Chromium, 28.0 23.5 Nickel, l9.0 37.0 Molybdenum, 0 L89 Iron, Balance Balance At the end of 30,000 hours on stream the furnace tubes were physically inspected. Those tubes of alloy 1 were, at least in some instances, carburized as much as 3 80 percent and had as little as 2/3 of an effective wall thickness remaining. Those of alloy 2 were effectively protected against carburization. Magnetic readings of the tubes of both alloy 1 and alloy 2 showed that the protected regions were predominantly oxides of manganese and chromium whereas the unprotected areas were predominantly oxides of iron. v
in a more detailed analysis performed with a microprobe analyzer, it was surprisingly discovered that a continuous layer of manganese oxide was lying outside the chromium oxide layer and close to the surface and the highly protected layers. Indeed, in alloy 2 the thickness of the manganese oxide scale was about times greater than the amount of manganese oxide scale in alloy 1.
Apparently, a nickel content, in a nickel-chromiumiron alloy, of greater than 36 percent and a manganese content of greater than L percent is necessary to provide a good protective scale of manganese and chromium oxide in the interior surface of the furnace tube.
Although the present invention has been described in conjunction with preferred embodiments, it is to be un 4 derstood that modifications or variations may be resorted to without departing from the spirit and scope of the invention. Those skilled in the art will readily understand that such modifications and variations are considered to be within the purview and scope of the invention and appended claims.
What is claimed is:
l. A method for heating hydrocarbons by contact with heated metal surfaces containing nickel and iron under conditions which are likely to result in carburization of the metal, which comprises contacting said hydrocarbons with a heated metal surface that has an adherent layer of manganese and chromium oxide on the metal surface which is in contact with the hydrocarbon, whereby the metal is protected against carburization and heat is passed from the metal to the hydrocarbon.
2. The method of claim 1 wherein said hydrocarbon is contacted with said metal surface at an initial temperature in the range of about l,700F. to 2,000F.
3. The method of claim 1 wherein the metallic surface comprises the inner walls of heat exchanger tubes suitable for heating said hydrocarbon.

Claims (3)

1. A METHOD FOR HEATING HYDROCARBONS BY CONTACT WITH HEATED METAL SURFACES CONTAINING NICKEL AND IRON UNDER CONDITIONS WHICH ARE LIKELY TO RESULT IN CARBURIZATION OF THE METAL, WHICH COMPRISES CONTACTING SAID HYDROCARBONS WITH A HEATED METAL SURFACE THAT HAS AN ADHERENT LAYER OF MANGANESE AND CHROMIUM OXIDE ON THE METAL SURFACE WHICH IS IN CONTACT WITH THE HYDROCARBON, WHEREBY THE METAL IS PROTECTED AGAINST CARBURIZATION AND HEAT IS PASSED FROM THE METAL TO THE HYDROCARBON.
2. The method of claim 1 wherein said hydrocarbon is contacted with said metal surface at an initial temperature in the range of about 1,700*F. to 2,000*F.
3. The method of claim 1 wherein the metallic surface comprises the inner walls of heat exchanger tubes suitable for heating said hydrocarbon.
US501220A 1973-08-13 1974-08-28 Heat resistant alloy for carburization resistance Expired - Lifetime US3919073A (en)

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US387946A US3865634A (en) 1973-08-13 1973-08-13 Heat resistant alloy for carburization resistance
US501220A US3919073A (en) 1973-08-13 1974-08-28 Heat resistant alloy for carburization resistance

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Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2500468A1 (en) * 1981-02-25 1982-08-27 Kubota Ltd TUBE FOR THE THERMAL CRACKING OR REFORMING OF HYDROCARBONS
US4379745A (en) * 1980-11-21 1983-04-12 Exxon Research And Engineering Co. Carburization resistance of austenitic stainless steel tubes
US4454021A (en) * 1981-12-17 1984-06-12 Showa Denko Kabushiki Kaisha Method for thermal cracking of hydrocarbons in an apparatus of an alloy having alkali or alkaline earth metals in the alloy to minimize coke deposition
US4756819A (en) * 1983-11-21 1988-07-12 Elf France Process for the thermal treatment of hydrocarbon charges in the presence of additives which reduce coke formation
US5202589A (en) * 1988-06-16 1993-04-13 Robert Bosch Gmbh Apparatus for detecting the condition of switches in one transmission line
WO1995018849A1 (en) * 1994-01-04 1995-07-13 Chevron Chemical Company Cracking processes
US5593571A (en) * 1993-01-04 1997-01-14 Chevron Chemical Company Treating oxidized steels in low-sulfur reforming processes
US5723707A (en) * 1993-01-04 1998-03-03 Chevron Chemical Company Dehydrogenation processes, equipment and catalyst loads therefor
US5849969A (en) * 1993-01-04 1998-12-15 Chevron Chemical Company Hydrodealkylation processes
US5873950A (en) * 1996-06-13 1999-02-23 Inco Alloys International, Inc. Strengthenable ethylene pyrolysis alloy
US6258256B1 (en) * 1994-01-04 2001-07-10 Chevron Phillips Chemical Company Lp Cracking processes
US6274113B1 (en) 1994-01-04 2001-08-14 Chevron Phillips Chemical Company Lp Increasing production in hydrocarbon conversion processes
WO2002022905A2 (en) * 2000-09-12 2002-03-21 Nova Chemicals (International) S.A. Stainless steel and stainless steel surface
US6419986B1 (en) 1997-01-10 2002-07-16 Chevron Phillips Chemical Company Ip Method for removing reactive metal from a reactor system
US6548030B2 (en) 1991-03-08 2003-04-15 Chevron Phillips Chemical Company Lp Apparatus for hydrocarbon processing
USRE38532E1 (en) 1993-01-04 2004-06-08 Chevron Phillips Chemical Company Lp Hydrodealkylation processes
US20060257675A1 (en) * 2005-05-10 2006-11-16 Chun Changmin High performance alloys with improved metal dusting corrosion resistance
US11435138B2 (en) * 2014-03-04 2022-09-06 Conocophillips Company Heat exchanger for a liquefied natural gas facility

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1703949A (en) * 1927-10-11 1929-03-05 Electro Metallurg Co Process and apparatus for thermally decomposing hydrocarbons
US2543710A (en) * 1948-01-15 1951-02-27 Westinghouse Electric Corp Process for producing insulating iron oxide coatings
US2671050A (en) * 1950-03-31 1954-03-02 Standard Oil Co Stainless steel alloy and apparatus for converting hydrocarbons
US2904497A (en) * 1952-05-31 1959-09-15 Hercules Powder Co Ltd Process for the high temperature reaction of hydrocarbons
US3260594A (en) * 1965-01-11 1966-07-12 Blaw Knox Co High temperature alloys

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1703949A (en) * 1927-10-11 1929-03-05 Electro Metallurg Co Process and apparatus for thermally decomposing hydrocarbons
US2543710A (en) * 1948-01-15 1951-02-27 Westinghouse Electric Corp Process for producing insulating iron oxide coatings
US2671050A (en) * 1950-03-31 1954-03-02 Standard Oil Co Stainless steel alloy and apparatus for converting hydrocarbons
US2904497A (en) * 1952-05-31 1959-09-15 Hercules Powder Co Ltd Process for the high temperature reaction of hydrocarbons
US3260594A (en) * 1965-01-11 1966-07-12 Blaw Knox Co High temperature alloys

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4379745A (en) * 1980-11-21 1983-04-12 Exxon Research And Engineering Co. Carburization resistance of austenitic stainless steel tubes
FR2500468A1 (en) * 1981-02-25 1982-08-27 Kubota Ltd TUBE FOR THE THERMAL CRACKING OR REFORMING OF HYDROCARBONS
US4454021A (en) * 1981-12-17 1984-06-12 Showa Denko Kabushiki Kaisha Method for thermal cracking of hydrocarbons in an apparatus of an alloy having alkali or alkaline earth metals in the alloy to minimize coke deposition
US4756819A (en) * 1983-11-21 1988-07-12 Elf France Process for the thermal treatment of hydrocarbon charges in the presence of additives which reduce coke formation
US5202589A (en) * 1988-06-16 1993-04-13 Robert Bosch Gmbh Apparatus for detecting the condition of switches in one transmission line
US6548030B2 (en) 1991-03-08 2003-04-15 Chevron Phillips Chemical Company Lp Apparatus for hydrocarbon processing
USRE38532E1 (en) 1993-01-04 2004-06-08 Chevron Phillips Chemical Company Lp Hydrodealkylation processes
US5593571A (en) * 1993-01-04 1997-01-14 Chevron Chemical Company Treating oxidized steels in low-sulfur reforming processes
US5723707A (en) * 1993-01-04 1998-03-03 Chevron Chemical Company Dehydrogenation processes, equipment and catalyst loads therefor
US5849969A (en) * 1993-01-04 1998-12-15 Chevron Chemical Company Hydrodealkylation processes
US5866743A (en) * 1993-01-04 1999-02-02 Chevron Chemical Company Hydrodealkylation processes
WO1995018849A1 (en) * 1994-01-04 1995-07-13 Chevron Chemical Company Cracking processes
US6258256B1 (en) * 1994-01-04 2001-07-10 Chevron Phillips Chemical Company Lp Cracking processes
US6274113B1 (en) 1994-01-04 2001-08-14 Chevron Phillips Chemical Company Lp Increasing production in hydrocarbon conversion processes
US5575902A (en) * 1994-01-04 1996-11-19 Chevron Chemical Company Cracking processes
US5873950A (en) * 1996-06-13 1999-02-23 Inco Alloys International, Inc. Strengthenable ethylene pyrolysis alloy
US6419986B1 (en) 1997-01-10 2002-07-16 Chevron Phillips Chemical Company Ip Method for removing reactive metal from a reactor system
US6551660B2 (en) 1997-01-10 2003-04-22 Chevron Phillips Chemical Company Lp Method for removing reactive metal from a reactor system
WO2002022905A2 (en) * 2000-09-12 2002-03-21 Nova Chemicals (International) S.A. Stainless steel and stainless steel surface
WO2002022905A3 (en) * 2000-09-12 2002-11-21 Nova Chem Int Sa Stainless steel and stainless steel surface
US20060257675A1 (en) * 2005-05-10 2006-11-16 Chun Changmin High performance alloys with improved metal dusting corrosion resistance
US7354660B2 (en) * 2005-05-10 2008-04-08 Exxonmobil Research And Engineering Company High performance alloys with improved metal dusting corrosion resistance
US11435138B2 (en) * 2014-03-04 2022-09-06 Conocophillips Company Heat exchanger for a liquefied natural gas facility

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