US2085811A - Method of treating steel ingots and regenerative soaking pit therefor - Google Patents
Method of treating steel ingots and regenerative soaking pit therefor Download PDFInfo
- Publication number
- US2085811A US2085811A US54973A US5497335A US2085811A US 2085811 A US2085811 A US 2085811A US 54973 A US54973 A US 54973A US 5497335 A US5497335 A US 5497335A US 2085811 A US2085811 A US 2085811A
- Authority
- US
- United States
- Prior art keywords
- pit
- air
- regenerative
- waste gases
- ingots
- 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
Links
- 230000001172 regenerating effect Effects 0.000 title description 15
- 229910000831 Steel Inorganic materials 0.000 title description 13
- 239000010959 steel Substances 0.000 title description 13
- 238000002791 soaking Methods 0.000 title description 10
- 238000000034 method Methods 0.000 title description 9
- 239000002912 waste gas Substances 0.000 description 29
- 238000002485 combustion reaction Methods 0.000 description 16
- 239000000446 fuel Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 9
- 238000010276 construction Methods 0.000 description 7
- 230000001276 controlling effect Effects 0.000 description 7
- 238000010304 firing Methods 0.000 description 6
- 230000003134 recirculating effect Effects 0.000 description 6
- 230000001105 regulatory effect Effects 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000002893 slag Substances 0.000 description 4
- 230000006872 improvement Effects 0.000 description 3
- 206010022000 influenza Diseases 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000010804 inert waste Substances 0.000 description 2
- 239000003570 air Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
- C21D9/70—Furnaces for ingots, i.e. soaking pits
Definitions
- my invention is primarily for a method 0 and means of heating steel ingots preparatory to rolling, by transmitting heat to the ingots within the heat absorptive capacity of the steel and without fusing or washing the skin or surface of the ingot.
- Among the other objects of the present invention is to provide a novel methodof heating steel ingots in a regenerative pit furnace by controlling the flame with hot waste gases.
- Another object of the present invention is the 0 provision of a novel improvement in'regenerative soaking pits for regenerative furnaces.
- a further object of this invention is the provision of a novel method of firing the pit in which the invention comprehends a recirculation of the 45 hot waste gases from the pit and thereby emciently and accurately controlling the flame temperature, while at the same time utilizing a substantial and desired amount of the heat in the waste gases by transferring it to the air for supporting 50 combustion.
- a still further object of the present invention is the provision of a novel burner construction.
- the invention comprehends a set of aspirating burners so constructed and ar- 55 ranged as to draw preheated air from one regenerator and hot inert waste gas from another source, and such mixture being then drawn into the pit with the fuel supp y.
- Yet another object of the invention is the provision of a novel regenerative pit furnace in which it is not necessary to reverse the fuel supply.
- Another object is the provision of a regenerative pit fumaceconstruotion in which the regenerators are positioned on one side of the pit only, thereby saving floor space and making possible the installation of greater capacities in the space occupied.
- Still another object of the invention is the provision of a regenerative pit furnace in which there is provision between the pit and regeneratorfor the columns and disposal of slag overflowing from the pit proper, thereby preventing the slag from entering the checker work.
- Fig. 1 is a. longitudinal view in vertical cross section through the novel furnace construction
- Fig. 2 is a view in a horizontal cross section taken on the line 2-4 of Fig. 1;
- Fig. 3 is a view in vertical cross section taken on the irregular line 3-3 of Fig. 1;
- Fig. 4 is a diagrammatic plan view of a four hole battery.
- the soaking pit isdesignated generally as I, and the checker work or regenerator chambers as 2.
- the pit I is of sufllcient size to receive the necessary ingots 3 and relatively deep to permit the fuel to beburnt over and above the top of the ingots being heated since the heat can be applied over the top of the ingots much more safely than across the bottom or butts thereof without the possibility of damaging the salable portion of the ingots.
- the tops of the ingots are of little value, due to defects formed during the process of solidification, and
- the diluted burning fuel column discharged from the burner blocks 4 passes through the firing port 9 and thence'across the pit over the top of the ingots, thence down toward the bottom of the pit, thence in a reverse direction and discharged through the outlet port l0 positioned in the same wall as the firing port, at or near the bottom of the pit by means of the draft exerted by a stack or the like.
- the length and path of travel of the gas is controlled largely by the intensity of the draft applied.
- the waste gases not used to dilute the air gasmixture,then pass to the stack through one of the flues l l of the checker chambers while the combustion air is preheated and supplied through the flue l l in the other checker chamber.
- Each battery is preferably provided with an air valve l2 having a valve member l3 regulating flues i4 and l 5, whereby the checker chambers or regenerators alternatelyserve air and waste gas through these ports. This is accomplished by a reversal of the valve member whereby an operation of this valve simultaneously shifts the air supply and the source of draft from one chamber or regenerator to the other.
- the air valve through which the regenerator receives air is so regulated as to establish a negative pressure at the top of the checker work of approximately the same intensity as the negative pressure existing at restricted port I regulated by the damper 8 p'osi-- the top of the checker work or regenerator receiving the waste gases. The pressure at these points tioned immediately below the aspirating burners,
- the tops must be sheared or cropped-1 and'adapted to adjust the ratio of the waste gas to the combustion air for the purpose of regulating the flame temperature.
- -'I'his flow is caused bygthe fact that the pressure at or near the exitof the outlet port is greater than the pressure in the'chamber at the entrance to the burners.
- The-balance of the waste gases passes through the checkerfl chamber "serving the waste gases and thence to the stack through the flue M or I5.
- the burners 4 are fired continuously and it is, therefore, not necessary to reverse the fuel supply to shut it off during reversal as the length of time required to reverse will be very short.
- The. fixed burner and port construction are so designed and constructed as to burn fuel only and are not utilized as a passage for waste gases leaving the pit furnace.
- a regenerative pit furnace for heating steel ingots, the combination of a soaking pit, means for firing the pit, means for recirculating hot waste gases as they are drawn from the bot- 5.
- a' regenerative pit furnace for heating tom of the pit directly into the preheated air supply for diluting the preheated air for supporting combustion and thereby controlling the flame temperature and additionally preheating the combustion supporting air, and a damper for regulating the proportion of waste gases to that of the combustion air.
- a soaking pit for receiving steel ingots, aspirating burners po-' sitioned to discharge a diluted burning fuel col umn over the top of the ingots, regenerators for supplying preheated air to the burners and for discharging waste gases issuing from the pit, and means for drawing preheated air from one regenerator and a desired quantity of the hot inert waste gas issuing directly from the pit and adding such mixture to the fuel supply to dilute the fuel mixture in order to reduce or control the flame temperature.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
July 6, 1937. F. H. LOFTUS' METHOD OF; TREATING STEEL INGOTS AND REGENERATIVE SOAKING PIT THEREFOR Filed Dec. 18, 1935 2 Sheefs-Sheet J.
July 6, 1937. F. H. LOFTUS 2, METHOD OF TREATING STEEL INGOTSAND REGENERATIVE SOAKING PIT THEREFOR Filed Dec, 18, 1955 2 Sheets-Sheet-2 Patented July 6, 1937 UNITED STATES METHOD OF TREATING STEEL INGOTS AND BEGENERATIVE SOAKING PIT THEREFOR Fred H. Loftus, Pittsburgh, Pa.
Application December 18, 1935, Serial No. 54,973
8 Claims.
introduced through a set of reversing valves and flues to each regenerator where it is preheated l and unites in the inlet port near the pit hole. Combustion occurs at this point and the flame travels across the pit hole, passing out of the pit through the opposite ports and then through the regenerators to the stack. 'The cycle is reversed l periodically. This set-up and method of treating steel ingots has many objections and disadvantages long recognized in the art among others,
excessive flame temperatures, the bane of the industry, are developed transmitting heat to the 20 ingot faster than the steel will absorb it,..the
result being that the skin or surface of the ingot is fused or washed. It has been attempted to overcome this by burning the fuel with a deficiency of air thereby heating the ingots by 5 means of a hot column of partially burnt gas, but
due to the fact that the flame temperature must be held within certain limits, the efliciency of the present method is very low.
lBroadly, my invention is primarily for a method 0 and means of heating steel ingots preparatory to rolling, by transmitting heat to the ingots within the heat absorptive capacity of the steel and without fusing or washing the skin or surface of the ingot.
Among the other objects of the present invention is to provide a novel methodof heating steel ingots in a regenerative pit furnace by controlling the flame with hot waste gases.
Another object of the present invention is the 0 provision of a novel improvement in'regenerative soaking pits for regenerative furnaces.
A further object of this invention is the provision of a novel method of firing the pit in which the invention comprehends a recirculation of the 45 hot waste gases from the pit and thereby emciently and accurately controlling the flame temperature, while at the same time utilizing a substantial and desired amount of the heat in the waste gases by transferring it to the air for supporting 50 combustion.
A still further object of the present invention is the provision of a novel burner construction. In the preferred form, the invention comprehends a set of aspirating burners so constructed and ar- 55 ranged as to draw preheated air from one regenerator and hot inert waste gas from another source, and such mixture being then drawn into the pit with the fuel supp y.
Yet another object of the invention is the provision of a novel regenerative pit furnace in which it is not necessary to reverse the fuel supply.
Another object is the provision of a regenerative pit fumaceconstruotion in which the regenerators are positioned on one side of the pit only, thereby saving floor space and making possible the installation of greater capacities in the space occupied.
Still another object of the invention is the provision of a regenerative pit furnace in which there is provision between the pit and regeneratorfor the columns and disposal of slag overflowing from the pit proper, thereby preventing the slag from entering the checker work.
Further objects are to provide a construction of maximum simplicity, efllciency, economy and ease of assembly and operation, and such further objects, advantages and capabilities as will later more fully appear and. are inherently possessed thereby. c
The invention further resides in the construction, combination and arrangement of parts illustrated in the accompanying drawings, and while I have shown therein a preferred embodiment, it is to be understood that the same is susceptible of modification and change, and comprehends other details, arrangements of parts, features and constructions without departing from the spirit of the invention.
In the drawings:
. Fig. 1 is a. longitudinal view in vertical cross section through the novel furnace construction;
Fig. 2 is a view in a horizontal cross section taken on the line 2-4 of Fig. 1;
Fig. 3 is a view in vertical cross section taken on the irregular line 3-3 of Fig. 1;
Fig. 4 is a diagrammatic plan view of a four hole battery.
Referring more particularly to the embodiment disclosed in the drawings, the soaking pit isdesignated generally as I, and the checker work or regenerator chambers as 2. The pit I is of sufllcient size to receive the necessary ingots 3 and relatively deep to permit the fuel to beburnt over and above the top of the ingots being heated since the heat can be applied over the top of the ingots much more safely than across the bottom or butts thereof without the possibility of damaging the salable portion of the ingots. Qrdinarily, the tops of the ingots are of little value, due to defects formed during the process of solidification, and
ergy from a source of low pressure, primarily air." or steam from the, pipe or line'5. The energy from the source or line passing into a burner'land thence into the mixing chamber 8, is utilized to' aspirate a mixture of preheatedscombustion air and flue or waste gas from the passage or port I intermediate the pit l and regenerators 2. Hot waste gases from the pit arerecirculated in order to control the flame temperature and at the same time utilize a substantial amount of heat in the waste gases by transferring it to the combustion air.
Excessive flame temperatures, such as would result by utilizing combustion air, preheatedto approximately 2000 normally cannot be applied when heating the ingotsn Therefore, in order to reduce the quantity of fuel consumed by salvaging the maximum quantity of heat from the waste gas and returning it to the system through the medium of the combustion air, it is essential that the air gas mixture be diluted in order to reduce the flame temperature to the proper working' limit. This is accomplished by recirculating some of the hot waste gases issuing from the pit I and port I. For regulating the amount of waste gases for this purpose I provide the damper 8.
The diluted burning fuel column discharged from the burner blocks 4 passes through the firing port 9 and thence'across the pit over the top of the ingots, thence down toward the bottom of the pit, thence in a reverse direction and discharged through the outlet port l0 positioned in the same wall as the firing port, at or near the bottom of the pit by means of the draft exerted by a stack or the like. The length and path of travel of the gas is controlled largely by the intensity of the draft applied. The waste gases not used to dilute the air gasmixture,then pass to the stack through one of the flues l l of the checker chambers while the combustion air is preheated and supplied through the flue l l in the other checker chamber.
Each battery is preferably provided with an air valve l2 having a valve member l3 regulating flues i4 and l 5, whereby the checker chambers or regenerators alternatelyserve air and waste gas through these ports. This is accomplished by a reversal of the valve member whereby an operation of this valve simultaneously shifts the air supply and the source of draft from one chamber or regenerator to the other. The air valve through which the regenerator receives air is so regulated as to establish a negative pressure at the top of the checker work of approximately the same intensity as the negative pressure existing at restricted port I regulated by the damper 8 p'osi-- the top of the checker work or regenerator receiving the waste gases. The pressure at these points tioned immediately below the aspirating burners,
. j $2 0 therefore, the tops must be sheared or cropped-1 and'adapted to adjust the ratio of the waste gas to the combustion air for the purpose of regulating the flame temperature. -'I'his flow is caused bygthe fact that the pressure at or near the exitof the outlet port is greater than the pressure in the'chamber at the entrance to the burners. The-balance of the waste gases passes through the checkerfl chamber "serving the waste gases and thence to the stack through the flue M or I5.
In the'novel and preferred construction, the burners 4 are fired continuously and it is, therefore, not necessary to reverse the fuel supply to shut it off during reversal as the length of time required to reverse will be very short. The. fixed burner and port construction are so designed and constructed as to burn fuel only and are not utilized as a passage for waste gases leaving the pit furnace.
In order to eliminate the possibility of slag yfromthe pit over-fiowing -the levelof the waste gas-ports and entering the checker work there is'provided a pocket IQ between the pit and checker work for the purpose. of receiving the slag and from which it may be removedthrough a suitable opening provided therefor. From the above description and the disclosure 'in the drawings, it will be readily appreciated =-that the invention comprehends a novel method of treating the steel ingots, and in the novel means for carrying out such method. Having thus described the invention, I claim: 1. The improvement in the heating of steel ingots in a soaking pit of a regenerative furnace, which comprises controlling the flame temperature by recirculating a part of the hot waste gases directly from the pit into the preheated incoming combustion supporting air supply.
2. The improvement in heating of steel ingots in, a soaking pit of a regenerative furnace, which comprises recirculating and directing a part of the hot waste gases passing from the pit directly into the preheated incoming air supply for supporting combustion and mixing-these waste gases which have previously passed over the ingots, with the preheated combustion supporting air for controlling the flame temperature.
3. The method of regenerative furnace operation which consists in drawing from the soaking pit, hot waste gases which have previously passed 'over the ingots, and delivering these waste gases direct from the pit into the preheated air supply whereby to dilute this air and control the flame temperature.
4. In a regenerative pit furnace for heating steel ingots, the combination of a'soaking pit, means for firing the pit, and means for recirculating hot waste gases issuing from, the pit and directly mixing these waste gases with the preheated combustion supporting air for controlling the fiame'temperature. i
steel ingots, the combination of a soaking pit, means for firing the pit, and means for recirculating a desired quantity of the hot waste gases passing directly from the pit into the preheated incoming air supply and mixing these waste gases with the preheated air for supporting combustion and for controlling the flame temperature, and also transferring a substantial amount of the heat in the waste gases to the combustion supporting air.
6. In a regenerative pit furnace for heating steel ingots, the combination of a soaking pit, means for firing the pit, means for recirculating hot waste gases as they are drawn from the bot- 5. In a' regenerative pit furnace for heating tom of the pit directly into the preheated air supply for diluting the preheated air for supporting combustion and thereby controlling the flame temperature and additionally preheating the combustion supporting air, and a damper for regulating the proportion of waste gases to that of the combustion air.
7. In a regenerative pit furnace, a soaking pit for receiving steel ingots, aspirating burners po-' sitioned to discharge a diluted burning fuel col umn over the top of the ingots, regenerators for supplying preheated air to the burners and for discharging waste gases issuing from the pit, and means for drawing preheated air from one regenerator and a desired quantity of the hot inert waste gas issuing directly from the pit and adding such mixture to the fuel supply to dilute the fuel mixture in order to reduce or control the flame temperature.
8. In a regenerative pit tfi'nace, a soakingpit FRED H. LOFTUS.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US54973A US2085811A (en) | 1935-12-18 | 1935-12-18 | Method of treating steel ingots and regenerative soaking pit therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US54973A US2085811A (en) | 1935-12-18 | 1935-12-18 | Method of treating steel ingots and regenerative soaking pit therefor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2085811A true US2085811A (en) | 1937-07-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US54973A Expired - Lifetime US2085811A (en) | 1935-12-18 | 1935-12-18 | Method of treating steel ingots and regenerative soaking pit therefor |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2085811A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2458624A (en) * | 1942-04-15 | 1949-01-11 | Amsler Morton Corp | Method and apparatus for artificially compensating for thermal load changes in heat-treatment furnaces |
| US2478190A (en) * | 1945-03-08 | 1949-08-09 | Loftus Engineering Corp Inc | Pit type furnace |
| US2540806A (en) * | 1945-10-04 | 1951-02-06 | Selas Corp Of America | Heat-treating furnace |
| US2638334A (en) * | 1948-01-29 | 1953-05-12 | Jones John Frederick Robert | Furnace for the heat treatment of materials |
| US2849221A (en) * | 1955-04-06 | 1958-08-26 | Surface Combustion Corp | Heat treating furnace |
| US4191525A (en) * | 1978-03-30 | 1980-03-04 | N L Industries, Inc. | Aspiration circulation system and method |
| USRE33814E (en) * | 1978-03-06 | 1992-02-04 | Toledo Engineering Co., Inc. | Manifold inputs and outputs for furnace regenerators |
| ITMI20131093A1 (en) * | 2013-06-28 | 2014-12-29 | Tenova Spa | "INDUSTRIAL OVEN AND PROCEDURE FOR CHECKING THE COMBUSTION IN ITS INTERIOR" |
-
1935
- 1935-12-18 US US54973A patent/US2085811A/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2458624A (en) * | 1942-04-15 | 1949-01-11 | Amsler Morton Corp | Method and apparatus for artificially compensating for thermal load changes in heat-treatment furnaces |
| US2478190A (en) * | 1945-03-08 | 1949-08-09 | Loftus Engineering Corp Inc | Pit type furnace |
| US2540806A (en) * | 1945-10-04 | 1951-02-06 | Selas Corp Of America | Heat-treating furnace |
| US2638334A (en) * | 1948-01-29 | 1953-05-12 | Jones John Frederick Robert | Furnace for the heat treatment of materials |
| US2849221A (en) * | 1955-04-06 | 1958-08-26 | Surface Combustion Corp | Heat treating furnace |
| USRE33814E (en) * | 1978-03-06 | 1992-02-04 | Toledo Engineering Co., Inc. | Manifold inputs and outputs for furnace regenerators |
| US4191525A (en) * | 1978-03-30 | 1980-03-04 | N L Industries, Inc. | Aspiration circulation system and method |
| ITMI20131093A1 (en) * | 2013-06-28 | 2014-12-29 | Tenova Spa | "INDUSTRIAL OVEN AND PROCEDURE FOR CHECKING THE COMBUSTION IN ITS INTERIOR" |
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