US3148238A - Oxygen converter linings - Google Patents
Oxygen converter linings Download PDFInfo
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- US3148238A US3148238A US132788A US13278861A US3148238A US 3148238 A US3148238 A US 3148238A US 132788 A US132788 A US 132788A US 13278861 A US13278861 A US 13278861A US 3148238 A US3148238 A US 3148238A
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- zone
- vessel
- cone section
- barrel
- lining
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- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims description 18
- 229910052760 oxygen Inorganic materials 0.000 title claims description 18
- 239000001301 oxygen Substances 0.000 title claims description 18
- 239000011449 brick Substances 0.000 claims description 30
- 239000002893 slag Substances 0.000 claims description 27
- 239000002184 metal Substances 0.000 claims description 17
- 229910052751 metal Inorganic materials 0.000 claims description 17
- 239000001095 magnesium carbonate Substances 0.000 claims description 16
- 229910000021 magnesium carbonate Inorganic materials 0.000 claims description 16
- 235000014380 magnesium carbonate Nutrition 0.000 claims description 15
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 claims description 15
- 239000011822 basic refractory Substances 0.000 claims description 14
- 230000001681 protective effect Effects 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 49
- 239000000395 magnesium oxide Substances 0.000 description 24
- 239000000203 mixture Substances 0.000 description 21
- 239000000463 material Substances 0.000 description 12
- 239000010459 dolomite Substances 0.000 description 9
- 229910000514 dolomite Inorganic materials 0.000 description 9
- QDOXWKRWXJOMAK-UHFFFAOYSA-N dichromium trioxide Chemical compound O=[Cr]O[Cr]=O QDOXWKRWXJOMAK-UHFFFAOYSA-N 0.000 description 7
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 6
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 5
- 235000011941 Tilia x europaea Nutrition 0.000 description 5
- 238000005299 abrasion Methods 0.000 description 5
- 239000004571 lime Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000009844 basic oxygen steelmaking Methods 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 239000011819 refractory material Substances 0.000 description 3
- 229910052814 silicon oxide Inorganic materials 0.000 description 3
- 238000004901 spalling Methods 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000009628 steelmaking Methods 0.000 description 2
- 235000005749 Anthriscus sylvestris Nutrition 0.000 description 1
- 238000009618 Bessemer process Methods 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000007767 bonding agent Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000002801 charged material Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- LFEUVBZXUFMACD-UHFFFAOYSA-H lead(2+);trioxido(oxo)-$l^{5}-arsane Chemical compound [Pb+2].[Pb+2].[Pb+2].[O-][As]([O-])([O-])=O.[O-][As]([O-])([O-])=O LFEUVBZXUFMACD-UHFFFAOYSA-H 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/42—Constructional features of converters
- C21C5/44—Refractory linings
Definitions
- the furnace structure fundamentally consists of a metal shell having a refractory lining disposed therein.
- the lining for oxygen steel vessels has heretofore been extremely simple, consisting of an inner or working lining of tar-bonded, chemically bonded or burned basic brick, an exterior r tank lining of burned magnesite brick and usually an intermediate layer of a tar-bonded ramming mix of composition similar to that of the working lining.
- the object of King et al. is to provide a tar-bonded brick composed of grain of at least 96 percent combined magnesite (MgO) and lime (CaO) which has the maximum resistance to the siliceous early slag produced in oxygen converter operation.
- McO combined magnesite
- CaO lime
- Davies teaches the addition of up to 5 percent chromic oxide to a composition as in King et al. in order to improve the resistance to iron oxide (FezOs) which is present in the slag at all times and is particularly high in the late slag.
- the following are typical analyses of the early and late slags just referred to:
- an oxygen converter vessel with a working lining having a plurality of compositions.
- the specic compositions used and their location have been determined by extensive commercial size tests of different lining materials as well as mineralogical studies of samples from such tests. yFrom these data and information, I have determined that the lining material that is normally below the usual surface of metal in the vessel is not particularly critical. Accordingly, I line such portion with a basic refractory, the composition of which normally is determined by economics.
- this portion of the lining is composed of brick made from stabilized dolomite, dead burned dolomite, dead burned lime, dead burned natural magnesite, and dead burned synthetic magnesite or any combination of the foregoing in various proportions and in each of which the essential chemistry is not particularly critical.
- the second major zone of a converter vessel in accordance with this invention is.
- each zone of the converter is characterized by the best combination of properties, as determined by operating conditions, that can be attained and, therefore, maxi-l mum life of the lining is achieved.
- the vessel comprises a metal tank indicated generally by the numeral 5.
- the tank is cylindrically shaped throughout most of its body portion 7 and has a rounded bottom zone 8.
- Above the main body portion 7 is a cone section 9 having a mouth cut on a bias.
- the tank 5 is provided with lugs 14 whereby it can be moved as by tilting or the like for charging and discharging operations.
- the immediate inside surface of the tank 5 is provided with a lining 18 of the conventional type, usually consisting of burned magnesite brick, and that is covered with a tar bonded ramming mix 20 of the same general character. Over the ramming mix 20 is the working lining that is zoned in accordance with the teachings of the present invention.
- the metal melt 22 normally covers about 40 percent of the height of the side Wall of the cylindrical body portion 7.
- the portion of the working lining in the vessel below the melt, which includes the bottom of the vessel, and is indicated by the numeral Z4 is, in accordance with this invention, made with the conventional basic refractories.
- conventional basic refractories I mean a refractory product that is basic in character without regard to the remainer of the composition.
- These conventional refractories are quite satisfactory for this portion of the working lining because there is no direct impingement of oxygen on it nor significant contact with the slags. Moreover, conditions are rather steady and neither abrasion nor spalling are significant problems.
- MgO plus CaO are at least 96 percent of MgO plus CaO, the MgO ranging from 50 to 95 percent and the CaO from 50 to 5 percent, and there being present no more than about 4 percent total of SiOZ, A1203, and Fe2O3.
- the MgO plus CaO content is at least 97 percent and the remaining oxides are less than 3 percent.
- Those compositions can be prepared by normal refractory practices using a tar or pitch bonding agent in an amount of about 4 to 8 weight percent. Those products are frequently and advantageously made by first preparing high density grain from lime, magnesia, dolomite or mixtures of the foregoing.
- Such grain can be prepared by pressing calcined dolomite or lime or magnesia at a pressure of at least 20,000 p.s.i. and then burning at a temperature of at least 3400 F.
- Other procedures also can be used and will be apparent to those skilled in the art upon consideration of the copending application of King et al. mentioned above.
- the Davies compositions comprise 50 to 5 percent of CaO, 50 to 94 percent of MgO and 1 to 5 percent of Cr2O3, with the SiOz, A1203, and Fe203 content not over 4 percent, and the MgO plus CaO being at least 94 per; cent.
- the third major portion, indicated generally by the numeral 30, of the Working lining is that about the mouth of the vessel and at the side wall where charge materials impinge. This area is subject to change to various locations higher or lower in the vessel depending upon where the scrap andhot metal strike. That portion of the lining is subject to conditions that bring about substantial abrasion and spalling.
- the brick used must be tar impregnated to avoid undue slag attack. Broadly, these brick are burned magnesite brick having an MgO content of at least 96 percent, and preferably higher. Brick for these locations can be made from high purity magnesite grain as disclosed in the copending application of Snyder et al., Serial No. 847,864, now U.S. Patent 3,060,000.
- dead burned magnesia is made through a series of steps whereby caustic calcined magnesia maintained at a temperature of at least 600 F. and under conditions where hydration is avoided, is pressed dry at a. pressure of at least 20,000 p.s.i.
- Dead burning is then accomplished, without permitting the bodies produced from the second compression step to fall in temperature, at a temperature usually on the order of at least 2900 F.
- the crushed dead burned magnesia is used to form brick and are burned in the conventional manner.
- Theburned brick are impregnated with tar, as by boiling in tar or by causing impregnation by application of pressure. Generally, about 8 percent of tar is used.
- Brick formed in this general manner are outstandingly resistant to abrasion under repeated impact as well as resistant to spalling brought about by rapid and frequent temperature changes. Typical physical properties of brick of this type are:
- An oxygen converter vessel comprising a metal vessel having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone to the cone section zone, the cone section zone being of downwardly opening truncated cross sectional configuration, the working lining of at least the upper peripheral lip area of the cone section zone being fabricated of tar impregnated, ceramically bonded magnesite brick having an MgO of at least 96%, substantially the remainder of the cone section zone, the barrel zone, and the bottom zone portions of the working lining being fabricated of tar bonded basic refractory, the basic refractory used to fabricate
- An oxygen converter vessel in accordance with claim 1 said barrel zone and bottom zone being lined with a basic refractory in which the basic constituents thereof are selected from the group consisting of dead burned dolomite, stabilized dolomite, dead burned lime, dead burned natural magnesite, and combinations thereof.
- An oxygen converter vessel comprising a metal vessel having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone, and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone to the cone section zone, the cone section being of a downwardly opening truncated cross sectional configuration, the major extent of the cone section zone and a limited upper portion of the barrel zone Where it joins the cone section zone being lined with tar impregnated, ceramically bonded magnesite brick having an MgO content of at least 96%, that limited portion of the barrelv zone working lining which is fabricated of the ceramically bonded brick arranged to oppose the charging of scrap to the vessel, both the remainder of
- An oxygen converter vessel comprising a metal vessel having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said Working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone to the cone section zone, the cone section zone being of downwardly opening truncated cross section configuration, and there being a tap hole opening through the cone section which tap hole is lined with basic refractory, the basic refractory used to fabricate a circumferential band portion of the barrel zone being especially slag resistant refractory composed of at least 96% MgO-l-CaO, the MgO ranging from 50 to 95% and the CaO from 510 to 5%, and there being present no more
- An oxygen converter vessel comprising a metal vessel .having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone -to the cone section zone, the cone section being of downwardly opening truncated cross sectional configuration, the working lining of at least the upper peripheral lip area of the cone section zone being fabrica-ted of tar impregnated, ceramically bonded magnesite brick having an MgO content of at least 96%, substantially the remainder 'of the cone section zone, the barrel zone, and the bottom zone portions of the working lining being fabricated of tar bonded basic refractory, the basic re
Description
Sept 8 1964 H. c. wlLLENBRocK, JR 3,148,238
OXYGEN CONVERTER LININGS Filed Aug. 2l, 1961 2.# l Ill? United States Patent C) 3,148,233 @XY EN CNVERTER LNGS Henry Carl Wiilenbrock, Jr., Pittsburgh, Pa., assigner to Harbison-Walker Refractor-ies Company, Pittsburgh, Pa., a corporation o Pennsyivania Filed Aug. 21, 1961, Ser. No. 132,788 5 Claims. (Cl. 266-43) This invention relates to furnace structure for the oxygen steel making process. More particularly this invention relates to the composition of the working lining for such structures.
In the oxygen steel making process, which has been variously designated as the LD process, oxygen Bessemer process, and the oxygen converter process, the furnace structure fundamentally consists of a metal shell having a refractory lining disposed therein. The lining for oxygen steel vessels has heretofore been extremely simple, consisting of an inner or working lining of tar-bonded, chemically bonded or burned basic brick, an exterior r tank lining of burned magnesite brick and usually an intermediate layer of a tar-bonded ramming mix of composition similar to that of the working lining.
During the evolution of the oxygen converter process, many different materials have been tried for the working linings, with varying degrees of success, in attempts to 0btain an even longer service life. Because these processes Operate with basic slags, the working lining materials have of necessity been constituted of basic materials, principally dolomite and magnesite in a variety of forms and combinaations. Although many different types of lining materials have been tried in attempts to improve service life, it has been the general practice to use only one particular type in any given lining. In general, it appears that the greatest success from the standpoint of both service and economy has been with working linings consisting of tarbonded lirne-magnesite compositions of the chemistry disclosed by King et al., in United States patent application Serial Number 38,43 8, filed June 24, 1960 and now abandoned and by Davies in United States patent application Serial Number 108,989, led May 10, 1961, where Cr2O3 is added to such compositions.
The object of King et al. is to provide a tar-bonded brick composed of grain of at least 96 percent combined magnesite (MgO) and lime (CaO) which has the maximum resistance to the siliceous early slag produced in oxygen converter operation. Davies teaches the addition of up to 5 percent chromic oxide to a composition as in King et al. in order to improve the resistance to iron oxide (FezOs) which is present in the slag at all times and is particularly high in the late slag. The following are typical analyses of the early and late slags just referred to:
Since bon King et al. and Davies aim at achieving maximum resistance to the oxygen converter slags, it is apparent that these brick, while of high quality, might not be the most desirable for use in those portions of the lining where resistance to slag is not the most important consideration.
It is a major object of the present invention to provideY an improved oxygen converter vessel characterized by an improved life in consequence of the use of a working 11n- 3,148,238 Patented Sept. 8, 1964 ing most suited to the varying conditions experienced therein.
Other objects will be evident from the following description.
This and other objects are attained in accordance with this invention by providing an oxygen converter vessel with a working lining having a plurality of compositions. The specic compositions used and their location have been determined by extensive commercial size tests of different lining materials as well as mineralogical studies of samples from such tests. yFrom these data and information, I have determined that the lining material that is normally below the usual surface of metal in the vessel is not particularly critical. Accordingly, I line such portion with a basic refractory, the composition of which normally is determined by economics. Typically, this portion of the lining is composed of brick made from stabilized dolomite, dead burned dolomite, dead burned lime, dead burned natural magnesite, and dead burned synthetic magnesite or any combination of the foregoing in various proportions and in each of which the essential chemistry is not particularly critical. The second major zone of a converter vessel in accordance with this invention is.
section joins the body portion of the converter. Theseareas of the linings have been found to be subject to severe abrasion and thermal shock. This is a primary result of the impact of the charging materials on this particular area. The impact, of course, can abrade the surfaces of the lining. Since the charged materials are usually at a temperature quite low relative to the temperature experienced by the lining during use, thermal shock also develops. In these Zones, I provide burned, tar impregnated, magnesite brick having an MgO content of at least 96 weight percent. The remainder of the lining and, in all events, at least that portion thereof that extends from immediately below the metal line or level of metal to the top of the splash area above the slag level is lined with a refractory that is particularly slag resistant. For this purpose, tar bonded MgO.CaO brick and particularly those having a small Cr203 content are used. In this manner, each zone of the converter is characterized by the best combination of properties, as determined by operating conditions, that can be attained and, therefore, maxi-l mum life of the lining is achieved.
The invention will be described further in conjunction with the attached drawing which shows a sectional View of a converter vessel having a zoned lining in accordance with this invention.
Referring now to the drawing, the vessel comprises a metal tank indicated generally by the numeral 5. Usually, the tank is cylindrically shaped throughout most of its body portion 7 and has a rounded bottom zone 8. Above the main body portion 7 is a cone section 9 having a mouth cut on a bias. In the embodiment shown, the tank 5 is provided with lugs 14 whereby it can be moved as by tilting or the like for charging and discharging operations.
The immediate inside surface of the tank 5 is provided with a lining 18 of the conventional type, usually consisting of burned magnesite brick, and that is covered with a tar bonded ramming mix 20 of the same general character. Over the ramming mix 20 is the working lining that is zoned in accordance with the teachings of the present invention.
Referring to the lower portion of the vessel, the metal melt 22 normally covers about 40 percent of the height of the side Wall of the cylindrical body portion 7. The portion of the working lining in the vessel below the melt, which includes the bottom of the vessel, and is indicated by the numeral Z4 is, in accordance with this invention, made with the conventional basic refractories. By the term conventional basic refractories I mean a refractory product that is basic in character without regard to the remainer of the composition. These conventional refractories are quite satisfactory for this portion of the working lining because there is no direct impingement of oxygen on it nor significant contact with the slags. Moreover, conditions are rather steady and neither abrasion nor spalling are significant problems. It is possible, therefore, to use tar-containing basic brick of a composition largely determined by economics. Dead burned dolomite, stabilized dolomite, dead burned lime, dead burned natural magnesite and the like, alone or in various combinations can be used. It should be understood, however, that under some operating conditions the use of the special refractories subsequently specied for the upper portion of the vessel may be required. Typical properties of two of the brick that can be used for this purpose are as follows:
The brick 26 in the working lining at and immediately above the level of the melt contact slag during most of the heat. Splashing extends this area to above the normal level of slag as well as to a course or two below the melt level. To resist the unusual conditions presented by slag, particularly that of the changing composition as noted above, this zone of the working lining is lined with tar bonded slag resistant brick, for example those made in the manner taught in the aforementioned King et al. application, Serial No. 38,438, or preferably those made in accordance with the teachings of Davies, Serial No'. 108,989. Typically, compositions or refractory products of King et al. are at least 96 percent of MgO plus CaO, the MgO ranging from 50 to 95 percent and the CaO from 50 to 5 percent, and there being present no more than about 4 percent total of SiOZ, A1203, and Fe2O3. Preferably, the MgO plus CaO content is at least 97 percent and the remaining oxides are less than 3 percent. Those compositions can be prepared by normal refractory practices using a tar or pitch bonding agent in an amount of about 4 to 8 weight percent. Those products are frequently and advantageously made by first preparing high density grain from lime, magnesia, dolomite or mixtures of the foregoing. Such grain can be prepared by pressing calcined dolomite or lime or magnesia at a pressure of at least 20,000 p.s.i. and then burning at a temperature of at least 3400 F. Other procedures also can be used and will be apparent to those skilled in the art upon consideration of the copending application of King et al. mentioned above.
Brick for the slag splash area can also be made in accordance with the teachings of the copending application of Davies, Serial No. 108,989. Generally speaking, Davies refractory shapes are similar to those of King et al. with the only major change being the incorporation of an amount of abouty 1 to 5 weight percent of chromic oxide. As set forth in. the-Davies application just mentioned, all the advantages of the King et al. application are obtained in that manner and the brick are further advantageous in that they are also particularly resistant to the late slag that is encountered in practicing the 3. oxygen converter process. Typical data on the composition of properties of these slag resistant tar bonded brick are as follows:
The Davies compositions comprise 50 to 5 percent of CaO, 50 to 94 percent of MgO and 1 to 5 percent of Cr2O3, with the SiOz, A1203, and Fe203 content not over 4 percent, and the MgO plus CaO being at least 94 per; cent.
It will be understood that besides the foregoing examples, large blocks or monolithic materials of these compositions are not excluded. The manufacture of large tarbonded blocks by vibration, air ramming, jolting, and the like is Well-known as is the practice of ramming or vibrating monolithic materials into place in the lining.
The third major portion, indicated generally by the numeral 30, of the Working lining is that about the mouth of the vessel and at the side wall where charge materials impinge. This area is subject to change to various locations higher or lower in the vessel depending upon where the scrap andhot metal strike. That portion of the lining is subject to conditions that bring about substantial abrasion and spalling. For this portionof the lining, the brick used must be tar impregnated to avoid undue slag attack. Broadly, these brick are burned magnesite brick having an MgO content of at least 96 percent, and preferably higher. Brick for these locations can be made from high purity magnesite grain as disclosed in the copending application of Snyder et al., Serial No. 847,864, now U.S. Patent 3,060,000. In that process, dead burned magnesia is made through a series of steps whereby caustic calcined magnesia maintained at a temperature of at least 600 F. and under conditions where hydration is avoided, is pressed dry at a. pressure of at least 20,000 p.s.i. Thev resulting dry compresses, and while still heated to at least 600 F., are briquetted under a pressure of at least 20,000 p.s.i., while recirculating to the feed at least 15 weight percent of the previously compressed material. Dead burning is then accomplished, without permitting the bodies produced from the second compression step to fall in temperature, at a temperature usually on the order of at least 2900 F. and preferably higher to produce a dead burned magnesia of at least 98 percent Mg() of an eX- tremely high bulk specific gravity, e.g. at least 3.30. That high bulk density dead burned magnesia upon crushing results in a minimum of platey grains that theretofore seemed to obstruct densification in the forming of refractory shapes. The crushed dead burned magnesia is used to form brick and are burned in the conventional manner. Theburned brick are impregnated with tar, as by boiling in tar or by causing impregnation by application of pressure. Generally, about 8 percent of tar is used. Brick formed in this general manner are outstandingly resistant to abrasion under repeated impact as well as resistant to spalling brought about by rapid and frequent temperature changes. Typical physical properties of brick of this type are:
Load Test, 25 p.s.i. failures at 3000 F. None It is to be noted that the requirements of great strength and abrasion resistance for this portion of the lining indicates that brick must be used to the exclusion of other shapes such as monolithic linings.
With a working lining zoned in the manner disclosed, maximum life and best economy are experienced. Each zone is provided with characteristics best suited to the conditions that are experienced. Thus, maximum service life is attained by using the best possible lining materials at those locations, and using less expensive compositions in zones (ie. the bottom) where lining wear or failure is not a significant threat.
All percentages in this specification are by weight unless otherwise indicated.
In accordance with the provisions of the patent statutes, I have explained the principle of my invention and have described what I now consider to represent its best embodiment. However, I desire to have it understood that, within the scope of the appended claims, the invention may be practiced otherwise than as specifically described.
I claim:
l. An oxygen converter vessel comprising a metal vessel having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone to the cone section zone, the cone section zone being of downwardly opening truncated cross sectional configuration, the working lining of at least the upper peripheral lip area of the cone section zone being fabricated of tar impregnated, ceramically bonded magnesite brick having an MgO of at least 96%, substantially the remainder of the cone section zone, the barrel zone, and the bottom zone portions of the working lining being fabricated of tar bonded basic refractory, the basic refractory used to fabricate a limited circumferential band portion of the barrel zone being an especially slag resistant refractory composed of at least 96% MgO -l-CaO, the MgO ranging from 50 to 95% and the CaO from 50 to 5%, and there being present no more than 4% of SiO-2, A1203, and Fe203, said band in the barrel zone being positioned in said barrel zone above its point of contact with the bottom zone, and just beyond molten metal in the vessel in the slag splash area of the vessel when it is in operation.
2. An oxygen converter vessel in accordance with claim 1, said barrel zone and bottom zone being lined with a basic refractory in which the basic constituents thereof are selected from the group consisting of dead burned dolomite, stabilized dolomite, dead burned lime, dead burned natural magnesite, and combinations thereof.
3. An oxygen converter vessel comprising a metal vessel having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone, and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone to the cone section zone, the cone section being of a downwardly opening truncated cross sectional configuration, the major extent of the cone section zone and a limited upper portion of the barrel zone Where it joins the cone section zone being lined with tar impregnated, ceramically bonded magnesite brick having an MgO content of at least 96%, that limited portion of the barrelv zone working lining which is fabricated of the ceramically bonded brick arranged to oppose the charging of scrap to the vessel, both the remainder of the barrel zone and the cone section zone and the bottom zone portions of the working lining being fabricated of tar bonded basic refractory, the basic refractory used to fabricate a circumferential band portion of the barrel zone being an especially slag resistant refractory composed of at least 96% MgO-l-CaO, the MgO ranging from 50 to 95% and the CaO from 50 to 5%, and there being present no more than 4% of Si02, A1203 and Fe203, said band in the barrel zone being positioned in said barrel zone above its point of contact with the bottom zone, and just beyond molten metal in the vessel in the slag splash area of the vessel when it is in operation.
4. An oxygen converter vessel comprising a metal vessel having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said Working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone to the cone section zone, the cone section zone being of downwardly opening truncated cross section configuration, and there being a tap hole opening through the cone section which tap hole is lined with basic refractory, the basic refractory used to fabricate a circumferential band portion of the barrel zone being especially slag resistant refractory composed of at least 96% MgO-l-CaO, the MgO ranging from 50 to 95% and the CaO from 510 to 5%, and there being present no more than 4% of SiOz, A1203, and Fe203, said band being positioned in said barrel zone just beyond molten metal in the vessel in the slag splash area of the vessel when it is in operation, and a major portion of the lining of the cone section zone being fabricated of ceramically bonded 96% MgO refractory impregnated throughout with tar.
5. An oxygen converter vessel comprising a metal vessel .having a mouth at its top, a shell protective lining in contact with the inside surface of said vessel and a working lining having a surface exposed to the interior of said vessel, said working lining being constructed of three major zones, these three zones being the bottom zone, the barrel zone and the cone section zone, the bottom zone being generally dish shaped and of upwardly opening concave configuration, the barrel zone extending from the dish shaped bottom upwardly to the cone section zone, the barrel zone being of substantially uniform cross sectional dimension from the bottom zone -to the cone section zone, the cone section being of downwardly opening truncated cross sectional configuration, the working lining of at least the upper peripheral lip area of the cone section zone being fabrica-ted of tar impregnated, ceramically bonded magnesite brick having an MgO content of at least 96%, substantially the remainder 'of the cone section zone, the barrel zone, and the bottom zone portions of the working lining being fabricated of tar bonded basic refractory, the basic refractory used to fabricate a limited circumferential band portion of the barrel zone being an especially slag resistant refractory composed of at least 96% the MgO ranging from 50 to 94% and the CaO from 50 to 5 the Cr2O3 from 1 to 5%, and there being present no more than 4% of SiOz, A1203 and Fe2O3, said band in the barrel zone being positioned in said barrel zone above its point of Contact with the bottom zone, and 3,058,834 just beyond molten metal in the vessel in the slag splash 3,060,000 area of the vessel when it is in operation. 3,060,042 3,070,449 References Crted 1n the le of thls patent 5 3,074,806
UNITED STATES PATENTS 484,181 Darby Oct. 11, 1892 499,248 Reese June 13, 1893 583050 540,465 Talbot June y4, 1895 648,756 Keck May 1, 1900 10 1,479,997 McCafery Jan. 8, 1924 S Koehegyi Oct. 16, 1962 Snyder et a1. Oct. 23, 1962 Leatham et al. Oct. 23, 1962 Davies et al. Dec. 25, 1962 Atlas et al. Ian. 22,y 1963 FOREIGN PATENTS Great Britain Dec. 5, 1946 OTHER REFERENCES Holt, I.: Tar Bonds Oxygen Vessel Bricks, in Steel, Vol. 143, pp. 74-78, July 7, 1958.
Claims (1)
1. AN OXYGEN CONVERTER VESSEL COMPRISING A METAL VESSEL HAVING A MOUTH AT ITS TOP, A SHELL PROTECTIVE LINING IN CONTACT WITH THE INSIDE SURFACE OF SAID VESSEL AND A WORKING LINING HAVING A SURFACE EXPOSED TO THE INTERIOR OF SAID VESSEL, SAID WORKING LINING B EING CONSTRUCTED OF THREE MAJOR ZONES, THESE THREE ZONES BEING THE BOTTOM ZONE, THE BARREL ZONE AND THE CONE SECTION ZONE, THE BOTTOM ZONE BEING GENERALLY DISH SHAPED AND OF UPWARDLY OPENING CONCAVE CONFIGURATION, THE BARREL ZONE EXTENDING FROM THE DISH SHAPED BOTTOM UPWARDLY TO THE CONE SECTION ZONE, THE BARREL ZONE BEING OF SUBSTANTIALLY UNIFORM CROSS SECTIONAL DIMENSION FROM THE BOTTOM ZONE TO THE CONE SECTION ZONE, THE CONE SECTION ZONE BEING OF DOWNWARDLY OPENING TRUNCATED CROSS SECTIONAL CONFIGURATION, THE WORKING LINING OF AT LEAST THE UPER PERIPHERAL LIP AREA OF THE CONE SECTION ZONE BEING FABRICATED OF TAR IMPREGNATED, CERAMICALLY BONDED MAGNESITE BRICK HAVING AN MGO OF AT LEAST 96%, SUBSTANTIALLY THE REMAINDER OF THE CONE SECTION ZONE, THE BARREL ZONE, AND THE BOTTOM ZONE PORTIONS OF THE WORKING LINING BEING FABRICATED OF TAR BONDED BASIC REFRACTORY, THE BASIC REFRACTORY USED TO FABRICATE A LIMITED CIRCUMFERENTIAL BAND PORTION OF THE BARREL ZONE BEING AN ESPECIALLY SLAG RESISTANT REFRACTORY COMPOSED OF AT LEAST 96% MGO+CAO, THE MGO RANGING FROM 50 TO 95% AND THE CAO FROM 50 TO 5%, AND THERE BEING PRESENT NO MORE THAN 4% OF SIO2, AL2O3, AND FE2O3, SAID BAND IN THE BARREL ZONE BEING POSITIONED IN SAID BARREL ZONE ABOVOE ITS POINT OF CONTACT WITH THE BOTTOM ZONE, AND JUST BEYOND MOLTEN METAL IN THE VESSEL IN THE SLAG SPLASH AREA OF THE VESSEL WHEN IT IS IN OPERATION.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US132788A US3148238A (en) | 1961-08-21 | 1961-08-21 | Oxygen converter linings |
GB28209/62A GB977784A (en) | 1961-08-21 | 1962-07-23 | Oxygen converter linings |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US132788A US3148238A (en) | 1961-08-21 | 1961-08-21 | Oxygen converter linings |
Publications (1)
Publication Number | Publication Date |
---|---|
US3148238A true US3148238A (en) | 1964-09-08 |
Family
ID=22455589
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US132788A Expired - Lifetime US3148238A (en) | 1961-08-21 | 1961-08-21 | Oxygen converter linings |
Country Status (2)
Country | Link |
---|---|
US (1) | US3148238A (en) |
GB (1) | GB977784A (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3238051A (en) * | 1964-01-20 | 1966-03-01 | Harbison Walker Refractories | Refractory with improved resistance to certain slag |
US3287144A (en) * | 1961-06-20 | 1966-11-22 | Veitscher Magnesitwerke Ag | Carbon-impregnated refractive magnesia bodies and method of preparing the same |
US3295845A (en) * | 1965-09-20 | 1967-01-03 | Harbison Walker Refractories | Basic oxygen steelmaking vessels |
US3329420A (en) * | 1966-10-05 | 1967-07-04 | Harbison Walker Refractories | Prefabricated taphole assembly for metallurgical furnaces |
US3330676A (en) * | 1964-10-02 | 1967-07-11 | Dolomitwerke Gmbh | Manufacture of tar impregnated refractories |
US3468526A (en) * | 1965-10-25 | 1969-09-23 | Kaiser Aluminium Chem Corp | Copper converter having tar impregnated fired chromite brick lining |
US3752643A (en) * | 1971-12-27 | 1973-08-14 | W Robinson | Portable gas fired art pottery kiln and method |
US3810610A (en) * | 1972-09-11 | 1974-05-14 | Andco Inc | Bosh construction for metallurgical furnaces |
US4432536A (en) * | 1981-04-08 | 1984-02-21 | Didier-Werke Ag | Molten iron containing vessel with improved refractory lining |
US4637823A (en) * | 1981-06-19 | 1987-01-20 | Texaco Inc. | High temperature furnace |
US4734031A (en) * | 1985-10-30 | 1988-03-29 | Micropore International Limited | Vessel for holding high temperature bulk materials |
US4773852A (en) * | 1985-06-11 | 1988-09-27 | Denki Kagaku Kogyo Kabushiki Kaisha | Pyrolytic boron nitride crucible and method for producing the same |
US5501431A (en) * | 1994-05-28 | 1996-03-26 | Abb K.K. | Melting furnace for residues from waste incineration plants |
CN101726188B (en) * | 2009-12-05 | 2011-04-27 | 永兴特种不锈钢股份有限公司 | Masonry structure for 18TAOD furnace lining |
CN102787204A (en) * | 2012-08-23 | 2012-11-21 | 武汉钢铁(集团)公司 | Energy-saving environmentally-friendly converter slag splashing protecting charging and production process thereof |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH671955A5 (en) * | 1987-01-15 | 1989-10-13 | Fischer Ag Georg |
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US3058834A (en) * | 1959-11-17 | 1962-10-16 | Joseph N Koehegyi | Process of making basic refractory and basic refractory composition |
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US3074806A (en) * | 1959-12-18 | 1963-01-22 | Basic Inc | Dolomitic refractory |
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US484181A (en) * | 1892-10-11 | John henry darby | ||
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US540465A (en) * | 1895-06-04 | Lining metallurgical furnaces | ||
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Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3287144A (en) * | 1961-06-20 | 1966-11-22 | Veitscher Magnesitwerke Ag | Carbon-impregnated refractive magnesia bodies and method of preparing the same |
US3238051A (en) * | 1964-01-20 | 1966-03-01 | Harbison Walker Refractories | Refractory with improved resistance to certain slag |
US3330676A (en) * | 1964-10-02 | 1967-07-11 | Dolomitwerke Gmbh | Manufacture of tar impregnated refractories |
US3295845A (en) * | 1965-09-20 | 1967-01-03 | Harbison Walker Refractories | Basic oxygen steelmaking vessels |
US3468526A (en) * | 1965-10-25 | 1969-09-23 | Kaiser Aluminium Chem Corp | Copper converter having tar impregnated fired chromite brick lining |
US3329420A (en) * | 1966-10-05 | 1967-07-04 | Harbison Walker Refractories | Prefabricated taphole assembly for metallurgical furnaces |
US3752643A (en) * | 1971-12-27 | 1973-08-14 | W Robinson | Portable gas fired art pottery kiln and method |
US3810610A (en) * | 1972-09-11 | 1974-05-14 | Andco Inc | Bosh construction for metallurgical furnaces |
US4432536A (en) * | 1981-04-08 | 1984-02-21 | Didier-Werke Ag | Molten iron containing vessel with improved refractory lining |
US4637823A (en) * | 1981-06-19 | 1987-01-20 | Texaco Inc. | High temperature furnace |
US4773852A (en) * | 1985-06-11 | 1988-09-27 | Denki Kagaku Kogyo Kabushiki Kaisha | Pyrolytic boron nitride crucible and method for producing the same |
US4913652A (en) * | 1985-06-11 | 1990-04-03 | Denki Kagaku Kogyo Kabushiki Kaisha | Pyrolytic boron nitride crucible and method for producing the same |
US4734031A (en) * | 1985-10-30 | 1988-03-29 | Micropore International Limited | Vessel for holding high temperature bulk materials |
US5501431A (en) * | 1994-05-28 | 1996-03-26 | Abb K.K. | Melting furnace for residues from waste incineration plants |
CN101726188B (en) * | 2009-12-05 | 2011-04-27 | 永兴特种不锈钢股份有限公司 | Masonry structure for 18TAOD furnace lining |
CN102787204A (en) * | 2012-08-23 | 2012-11-21 | 武汉钢铁(集团)公司 | Energy-saving environmentally-friendly converter slag splashing protecting charging and production process thereof |
Also Published As
Publication number | Publication date |
---|---|
GB977784A (en) | 1964-12-16 |
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