Apparatus for continuous heat treatment of elongated material
专利摘要:
公开号:SU993826A3 申请号:SU792783156 申请日:1979-07-02 公开日:1983-01-30 发明作者:Шток Гюнтер;Вейанд Карл 申请人:Трефиларбед С.А. (Фирма); IPC主号:
专利说明:
The invention relates to a device for continuous heat treatment of a long metal product, in particular wire or steel strips. 5 A known installation for heat treatment of long metal material containing an unwinding device; heating chamber, cooling bath and winding drums. The heating of the Yu wire to the patenting temperature in this installation occurs through radiation til. The disadvantage of this installation is that, for large wire diameters, relatively high long metal material, in particular wire, containing successively arranged heating and quenching baths with liquid metal, connected to a transformer [2 3. A disadvantage of the known installation is that it requires a significant amount of energy to heat a preheating bath. In addition, the thermal energy introduced by the strongly heated wire into the quenching bath must be diverted all the time, which entails the need for further energy and technical costs. Electric patenting uses more energy for operating bathtubs than for self-heating by wire resistance. The purpose of the invention is the reduction of energy costs. . This goal is achieved by the fact that in the known installation for continuous heat treatment, containing successively arranged heating and quenching baths with liquid metal, connected to a transformer, the heating bath is installed partially20 essence to the proposed is the installation for continuous heat treatment but immersed in the quenching, while its body is made electrically insulated from a material having a large heat conductive 1b with respect to liquid metal. In FIG. 1 shows the proposed installation with a symmetrical arrangement in relation to each other pre-heating and quenching baths; in FIG. 2 - the same with quenching! long tub. Installation (FIG. I) contains installation 993826 4 450-500 ° C, then this wire passes through the high-heating section 10, where it quickly reaches a temperature of 1000 ° C. During subsequent passage through the quenching bath 2, the wire is cooled to 500 ° C and maintained at this temperature for about 20 seconds to form the desired sorbitol structure, The quenching bath 2 is equipped with a pump 13 which can be a conventional apparatus, which is suitable for pre-heating 1 and quenching 2 baths. The shell 3 of the pre-heating bath is mounted on supports 4 and is provided with internal insulation 5, which electrically isolates the pre-heating bath 1 from the quenching 2 and allows only the transfer of thermal energy. The sheath 3 of the preheating bath, as well as the sheath 6 of the quenching bath, is connected to the secondary winding 7 of the transformer 8. The metal baths 1 and 2 thereby act as electric contact baths for the wire 9 drawn in the direction of the arrow. The dashed section of the wire Yu corresponds to the jg section high heating, on which the wire quickly heats up to approximately 10.00 ° C. Inside the quenching bath 2 there is a combined heating - cooling device II, which is activated when the unit is started, as well as when removing excessive amounts of energy. After passing through the pre-heater 40 but the heating bath I and the high heating section 10, the wire passes the quenching bath 2 in the opposite direction and the cooling section 12 cooled by the flowing air. In the second embodiment of the proposed installation (Fig. 2), a pump 13 is provided for transferring thermal energy to the immediately adjacent region to the preheating bath. The supply of wires is carried out continuously in the same direction, as a result of which the pump unit 13 acts here in the direction opposite to the movement of the wire. Installation works as follows. The pre-heating bath I heats the passing wire until the liquid metal circulates in the metal baths. The continuous circulation of liquid metal in the quenching bath 2 serves, on the one hand, to transfer thermal energy to the immediately adjacent region to the bottom of the preheating bath 1 and, on the other hand, to prevent overheating phenomena in the aeon of the inlet and wire. The energy required for strong heating and austenitization of the wire, which 25 during the subsequent sorbitization is almost completely transferred to the quenching bath 2, is used to heat the preheating bath I, since the latter is almost completely washed by the liquid metal in the quenching bath. The quenching bath 2 is equipped with a combined heating-cooling device II to create the necessary temperature ratios at the start of the installation, and, accordingly, to divert possible excessive amounts of thermal energy. Using the proposed installation, it is possible to continuously maintain a pre-heating bath 1 without a significant additional supply of energy at a satisfactory high temperature. In this case, it is achieved that the conditions necessary for the formation of the desired sorbitol structure are maintained in the quenching bath 2, namely, a homogeneous temperature of 500-550 ° C. In addition, the thermal energy transferred to the quenching bath 2 by a highly heated wire is used expediently. In the proposed installation, compared with the known energy savings reaches up to 5O% " If the dimensions of the quenching bath 2 are twice as large as those of the preheating bath 1, then it is possible to provide for the quenching bath to be made in the form that is as long as possible. In the consistent development of this design principle, it is also possible to provide for the separation, on the one hand, of the quenching bath into 5 two sections with a jumper or, on the other hand, the installation of two separated exchange baths, one of which contains a pre-heating bath and connected to the other by proton 10 channels. The shells of the baths are made of steel, as appropriate. It is possible when installing the shell of the preheating bath to install an insulating layer in the form of a binder 15. The construction in the form of SENVIG is also possible, in which an insulating layer predominantly made of ceramic material is included between two steel shells. 20
权利要求:
Claims (2) [1] but immersed in quenching, while its body is made of electrically insulated from a material that has a large goplooprovodnosch on fire to the liquid metal, FIG. I shows the proposed installation with a symmetrical arrangement with respect to each other pre-heating and quenching baths; Fig. 2 is the same, with quenching bath in extended form. The installation (FIG. I) contains preheating I and 2 quenching baths installed one into another. The shell 3 of the preheating bath is installed with supports 4 and is provided with internal insulation 5, which electrically isolates the preheating bath I from the hardening 2 and allows only the transfer of thermal energy. The shell 3 of the preheating bath and the shell 6 of the quenching bath are connected to the secondary winding 7 of the transformer 8, the metal baths I and 2 thus act as electrical contact baths for the wire 9 drawn in the direction of the arrow, the wire segment marked with a dot corresponds to the section high heat, on which the wire is quickly heated to approximately tO.OO ° C, inside the quenching bath 2 nd, the cooling device II combined, which is iJ) HBo-. It is activated when starting the installation and also when excess energy is removed. After passing through the preheat heating bath I and high heating, the wire passes the quenching bath 2 in the opposite direction and cooling section 12 cooled by flowing air. In the second variant of the proposed installation (FIG. 2), having provided the pump 1.3 for transferring the thermal energy directly to the reel area to the pre-heated bath. Wire feeding is performed continuously in one and the same direction, as a result of which the pumping unit 13 operates here in a directional positioning and moving the wire. The setting works as follows. The preliminary setting of the wire heats up the 5th wire to 264,450-500 ° C. Further, this wire passes a section of high heating 1O, where it quickly reaches a temperature of 1OOO ° C. During the subsequent passage through the quenching bath 2, the wire is cooled to 5OO ° C and maintained at this temperature for about 2 O sec to form the desired sorbitol structure. The quenching bath 2 is equipped with a pump 13 which can be used by a conventional apparatus that is suitable for circulating carbon dioxide. metal in metal baths. The continuous circulation of iron metal in the quenching vanzb 2 serves, on the one hand, to transfer thermal energy into the immediately adjacent area to the shell of the preheating heating bath I and, on the other, to prevent overheating in the entrance zone, the wire. The energy required for strong heating and austenitization of the wire, which during the subsequent sorbitization is almost completely transferred to the quenching bath 2, is used to heat the preheating bath I, since the latter is almost completely washed by the liquid metal in the quenching bath. -Hander II to create the necessary temperature ratios at the start-up of the installation, and accordingly, to divert possible excessive t he thermal energy with the help of the proposed installation making it possible to maintain .posto nnogo u) edvaritelvo vagrevatelvoy vavvy 1 without significantly supplying dopolvntelvogo avergii satisfactorily at vyuokoy temperature. In this case, it is achieved that the conditions necessary for the formation of the desired sorbitol structure are maintained in the quenching vessel 2, and the tempo of the 5OO-550 C is also homogeneous. With notable savings, Evergin reaches up to 50%. If the dimensions of the quenching vavva 2 are superior to the dimensions of the u), it is only twice as large, then it can be harmful to carry out the quenching bath in a form as long as possible. In the sequential development of this design, it is also possible to provide for the separation of the quenching bath into two sections with a jumper or, on the other hand, the installation of two separated exchange baths, of which one is preheated and connected to the other through flow paths. channels. The shell of the baths, in view of its integrity, is made of steel. It is possible to install the shell of a pre-heating bath to install an insulating layer in the form of a core material ... It is also possible to construct a transducer in which an insulating layer is predominantly made of ceramic material between two steel shells. An apparatus for continuous heat treatment of a lengthy metallic material, in particular a wire, comprising successive heating and quenching baths with a liquid metal, connected to a transformer, in order to reduce energy costs, the heating bath is installed partially immersed in the quench bath, In this case, its casing is made of electro-isolated from the material that has a high thermal conductivity with respect to the liquid metal. An exponent of a formatio, 1 finite in attention during examination I 1. Sokolov KN. Mechanization and automation in thermal workshops. M., Mashgiz, 1962 p. 72, 74., [2] 2.Patent of England No. 1422316.cn. C 21 D 9/52, 1975.
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同族专利:
公开号 | 公开日 DE2960456D1|1981-10-15| EP0006841A3|1980-01-23| AU521204B2|1982-03-18| JPS5822526B2|1983-05-10| US4249720A|1981-02-10| AU4860279A|1980-02-07| AT102T|1981-07-15| EP0006841B1|1981-07-08| EP0006841A2|1980-01-09| PL216796A1|1980-03-24| JPS5514891A|1980-02-01| LU79911A1|1980-02-14| PL116624B1|1981-06-30| CS209814B2|1981-12-31|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 US2300329A|1938-02-18|1942-10-27|William H Wood|Method of heat treating steel wire and apparatus therefor| GB560599A|1942-05-01|1944-04-12|William Harry Wood|Improved apparatus for the heat treatment of metal wire, strip and the like| US2463412A|1942-07-25|1949-03-01|John S Nachtman|Electric resistance heat-treating of electroplated coatings| FR948545A|1946-07-09|1949-08-03|Improvements in the heat treatment of metal wires| DE1167866B|1959-10-31|1964-04-16|Siemens Ag|Device for the heat treatment of wires or tapes by means of electrical resistance heating| GB985022A|1960-04-28|1965-03-03|British Iron Steel Research|Improvements in or relating to the continuous heat treatment of elongate metal material| LU40026A1|1960-04-28|1961-06-15| DE1205572B|1962-03-30|1965-11-25|Schloemann Ag|Vacuum annealing tower with an annealing and a cooling section for continuous heat treatment of endless metal strips| NL6513832A|1964-10-28|1966-04-29| US3277270A|1965-04-09|1966-10-04|Oscar C Trautman|Continuous heat treating of strapping and the like| DE1583406C3|1967-11-15|1974-07-25|Siemens Ag, 1000 Berlin Und 8000 Muenchen|Arrangement for the heat treatment of strand material by means of electrical resistance heating| BE793716A|1972-01-06|1973-07-05|Procedes Ind S E P R I S A Soc|METAL WIRE PATENTAGE PROCESS AND TANK| US4168995A|1973-04-20|1979-09-25|December 4 Drotmuvek|Steel wire patenting process|JPS549643B2|1975-02-04|1979-04-26| FR2607519B1|1986-11-27|1989-02-17|Michelin & Cie|METHOD AND DEVICE FOR HEAT TREATING A STEEL WIRE| EP0864006B1|1995-11-30|2003-02-19|Kimberly-Clark Worldwide, Inc.|Superfine microfiber nonwoven web| DE102005054014B3|2005-11-10|2007-04-05|C.D. Wälzholz-Brockhaus GmbH|Method for continuously forming bainite structure in carbon steel involves austenitizing steel and passing it through bath quenchant, removing quenchant residue converting remaining parts of steel into bainite isothermal tempering station| US9004327B2|2012-08-31|2015-04-14|Wfk & Associates, Llc|Insertion guide for animal footwear|
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申请号 | 申请日 | 专利标题 LU79911A|LU79911A1|1978-07-03|1978-07-03|DEVICE FOR CONTINUOUS HEAT TREATMENT OF METAL GOODS| 相关专利
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