CN115679048A - Stainless steel wire drawing machine graded heating annealing oxygen-blocking system - Google Patents
Stainless steel wire drawing machine graded heating annealing oxygen-blocking system Download PDFInfo
- Publication number
- CN115679048A CN115679048A CN202211559105.1A CN202211559105A CN115679048A CN 115679048 A CN115679048 A CN 115679048A CN 202211559105 A CN202211559105 A CN 202211559105A CN 115679048 A CN115679048 A CN 115679048A
- Authority
- CN
- China
- Prior art keywords
- stainless steel
- steel wire
- pipe section
- annealing
- section
- 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.)
- Pending
Links
- 229910001220 stainless steel Inorganic materials 0.000 title claims abstract description 84
- 238000000137 annealing Methods 0.000 title claims abstract description 70
- 238000010438 heat treatment Methods 0.000 title claims abstract description 44
- 238000005491 wire drawing Methods 0.000 title claims abstract description 14
- 239000007789 gas Substances 0.000 claims abstract description 61
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000001301 oxygen Substances 0.000 claims abstract description 24
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 24
- 238000001816 cooling Methods 0.000 claims abstract description 19
- 230000004888 barrier function Effects 0.000 claims abstract description 10
- 239000010935 stainless steel Substances 0.000 claims abstract description 8
- 230000000903 blocking effect Effects 0.000 claims abstract 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 10
- 239000002912 waste gas Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 3
- 238000005984 hydrogenation reaction Methods 0.000 claims description 2
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000003915 air pollution Methods 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 description 18
- 229910052739 hydrogen Inorganic materials 0.000 description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 13
- 229910000831 Steel Inorganic materials 0.000 description 13
- 239000010959 steel Substances 0.000 description 13
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 150000001335 aliphatic alkanes Chemical class 0.000 description 7
- 230000001681 protective effect Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 229910021529 ammonia Inorganic materials 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 5
- 150000002431 hydrogen Chemical class 0.000 description 5
- 239000011261 inert gas Substances 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 239000001273 butane Substances 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000002918 waste heat Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000001345 alkine derivatives Chemical class 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- -1 ethylene, propylene, butene Chemical class 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000005496 tempering Methods 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
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/26—Methods of annealing
-
- 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
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
-
- 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
- C21D9/0062—Heat-treating apparatus with a cooling or quenching zone
-
- 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
- C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
- C21D9/54—Furnaces for treating strips or wire
- C21D9/56—Continuous furnaces for strip or wire
- C21D9/561—Continuous furnaces for strip or wire with a controlled atmosphere or vacuum
-
- 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
- C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
- C21D9/54—Furnaces for treating strips or wire
- C21D9/56—Continuous furnaces for strip or wire
- C21D9/573—Continuous furnaces for strip or wire with cooling
- C21D9/5732—Continuous furnaces for strip or wire with cooling of wires; of rods
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- 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)
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Abstract
本发明公开的一种不锈钢拉丝机分级加热退火阻氧系统,具有平行设置的多根不锈钢丝行走路线;每根不锈钢丝依次穿过各自的烘箱管段、裸露段、进丝管段、退火加热管段、冷却管段、出丝管段。不锈钢在丝退火炉段在还原性气氛中被加热至退火温度,再经过冷却池冷却后从出丝管出去。还原性气体从退火炉管段与冷却管段的交接处进入,朝着进丝管段逆向流动,在裸露段燃烧消耗氧气后排放。本发明的不锈钢丝退火设备,结构简单巧妙,还原性气体兼具阻隔氧气、预热、减小空气污染的多种功能,不锈钢丝退火后的外观质量高。
A graded heating annealing oxygen barrier system for a stainless steel wire drawing machine disclosed in the present invention has multiple stainless steel wires running in parallel; each stainless steel wire passes through its own oven pipe section, exposed section, wire feeding pipe section, annealing heating pipe section, Cooling pipe section and wire outlet pipe section. The stainless steel wire annealing furnace section is heated to the annealing temperature in a reducing atmosphere, and then goes out of the wire outlet pipe after being cooled by the cooling pool. The reducing gas enters from the junction of the annealing furnace tube section and the cooling tube section, flows in the reverse direction towards the wire feeding tube section, and is discharged after burning and consuming oxygen in the exposed section. The stainless steel wire annealing equipment of the present invention has a simple and ingenious structure, the reducing gas has multiple functions of blocking oxygen, preheating, and reducing air pollution, and the appearance quality of the stainless steel wire after annealing is high.
Description
技术领域technical field
本发明涉及一种钢丝拉丝过程中的退火技术。The invention relates to an annealing technology in the steel wire drawing process.
背景技术Background technique
不锈钢热处理一般是在退火炉中采取固溶热处理,也就是人们平常所谓的“退火”,温度范围为1040~1120℃。退火气氛一般都是采用纯氢作为退火气氛,气氛纯度最好是99.99%以上,如果气氛中另一部分是惰性气体的话,纯度也可以低一点,但是绝对不能含有过多氧气、水汽。The heat treatment of stainless steel is generally a solution heat treatment in an annealing furnace, which is usually called "annealing", and the temperature range is 1040~1120 °C. The annealing atmosphere generally uses pure hydrogen as the annealing atmosphere, and the purity of the atmosphere is preferably above 99.99%. If the other part of the atmosphere is an inert gas, the purity can be lower, but it must not contain too much oxygen or water vapor.
2014107925319的发明提供了一种不锈钢焊丝用原丝的退火工艺,在拉丝之前,将原丝的盘圆在退火炉中进行退火热处理,使得炉温逐步升至工艺所需温度后降温冷却。该技术可作为本发明技术的参考内容。The invention of 2014107925319 provides an annealing process for raw wire for stainless steel welding wire. Before wire drawing, the coil of the raw wire is annealed in an annealing furnace, so that the furnace temperature gradually rises to the temperature required by the process and then cools down. This technology can be used as the reference content of the technology of the present invention.
2021.9《化工管理》中刊登了“冷轧不锈钢退火酸洗线的几种工艺”,文章中介绍目前行业中主要采用氢气作为保护气体,由于氢气是一种强还原剂,故在冷轧不锈钢退火处理时,炉内的保护气体越纯、浓度越高,退火后的带钢表面也就越清洁光亮。但由于氢气的易爆炸,目前行业中普遍采取氨分解气,导致了保护气体在纯度上的可变因素较大,这就需要在设备的设计和使用过程中更多去从气密性上控制,确保保护气体的浓度达到要求,达到再结晶光亮退火的目的。但是对于氨分解气的使用设备仅仅局限于退火炉,成本较高,周期较长。2021.9 "Chemical Management" published "Several Processes for Cold-rolled Stainless Steel Annealing and Pickling Lines". The article introduced that hydrogen is mainly used as a protective gas in the industry at present. Since hydrogen is a strong reducing During processing, the purer and higher the concentration of the protective gas in the furnace, the cleaner and brighter the surface of the strip after annealing. However, due to the explosive nature of hydrogen, ammonia decomposition gas is generally used in the industry at present, resulting in a large variable factor in the purity of the protective gas, which requires more airtight control in the design and use of equipment , to ensure that the concentration of the protective gas meets the requirements and achieve the purpose of recrystallization bright annealing. However, the equipment used for the ammonia decomposition gas is limited to the annealing furnace, and the cost is high and the cycle is long.
发明内容Contents of the invention
发明目的:Purpose of the invention:
提供一种多段加热、阻氧、环保、内在质量和外观质量都能够提高的不锈钢拉丝机分级加热退火阻氧系统。Provide a stainless steel wire drawing machine graded heating annealing oxygen barrier system with multi-stage heating, oxygen barrier, environmental protection, internal quality and appearance quality can be improved.
技术方案:Technical solutions:
本发明的不锈钢拉丝机分级加热退火阻氧系统,具有多根平行设置的不锈钢丝,按照行走路线,每根不锈钢丝依次穿过各自的烘箱管段、裸露段、进丝管段、退火炉管段、冷却管段、出丝管段。The graded heating annealing oxygen barrier system of the stainless steel wire drawing machine of the present invention has multiple stainless steel wires arranged in parallel. Pipe section, wire outlet pipe section.
进丝管段、退火炉管段、冷却管段、出丝管段为相互连通连续的管路。The wire inlet pipe section, the annealing furnace pipe section, the cooling pipe section and the wire outlet pipe section are interconnected and continuous pipelines.
另外,在冷却管段与退火炉管段之间连接有还原性气体管路(还原性气体管路通过流量阀控制流量或压力,保证压力大于大气压,便于逆向流动)。In addition, a reducing gas pipeline is connected between the cooling pipe section and the annealing furnace pipe section (the flow or pressure of the reducing gas pipeline is controlled by a flow valve to ensure that the pressure is greater than atmospheric pressure, which is convenient for reverse flow).
在冷却管段与退火炉管段之间连接有高于大气压的还原性气体管路,还原性气体为与不锈钢丝的行走方向逆向流动,使得不锈钢丝在退火温度热处理过程中同时被氢化热处理,还原性气体然后从进丝管段与裸露段连接处的敞口处流出。A reducing gas pipeline with a pressure higher than atmospheric pressure is connected between the cooling pipe section and the annealing furnace pipe section. The reducing gas flows in the opposite direction to the running direction of the stainless steel wire, so that the stainless steel wire is simultaneously hydrogenated during heat treatment at the annealing temperature. The gas then exits through the opening at the junction of the feed tube section and the bare section.
出丝管段的出口处为束口(基本密闭,进丝管尾端的管径逐渐缩小至不锈钢丝直径略大的尺寸,并且在尾端的内部设置有阻气堵料;只能供不锈钢丝传出,不能供还原性气体流出)。The outlet of the outlet pipe section is the bundle opening (basically airtight, the diameter of the tail end of the wire inlet pipe is gradually reduced to a size slightly larger than the diameter of the stainless steel wire, and a gas-blocking material is installed inside the tail end; it can only be used for the stainless steel wire to pass out , not for the reducing gas to flow out).
使得保护性气体只能朝向进丝管段方向流出,不能朝向出丝管段流出。So that the protective gas can only flow out toward the direction of the wire inlet pipe section, and cannot flow out toward the wire outlet pipe section.
所述的还原性气体为氨气分解炉分解的氢气和氮气,氮气是惰性气体(氢气和氮气无需分离,在退火炉管段,其分解后不具有再次合成为氨气的条件),可以保护不锈钢丝。或者,还原性气体为比较纯净(纯度高也不易爆炸)的烷烃气体(燃烧值较高,安全性优于氢气,而且化学性质比较稳定,没有烯、炔类活泼);优选烷烃气体为丁烷,丁烷的燃烧值高于其他常见还原气体(氢气、一氧化碳、甲烷、乙烷、丙烷、乙烯、丙稀、丁烯、乙炔。戊烷燃烧值虽高于丁烷,但常温为液体,不能作为还原性的保护性气体,所以不予考虑),远高于氢气,其瞬间燃烧产生的热量能够使得不锈钢丝在下述第二次加热过程中快速升温150-350℃。还原性气体与空气接触时能够被点燃燃烧,给予出丝管段加热,传热给不锈钢丝。The reducing gas is hydrogen and nitrogen decomposed by the ammonia decomposition furnace. Nitrogen is an inert gas (hydrogen and nitrogen do not need to be separated, and in the annealing furnace tube section, there is no condition for resynthesis into ammonia after decomposition), which can protect stainless steel Silk. Alternatively, the reducing gas is relatively pure (high purity and not easy to explode) alkane gas (higher combustion value, better safety than hydrogen, and relatively stable chemical properties, less active than alkenes and alkynes); the preferred alkane gas is butane , the combustion value of butane is higher than that of other common reducing gases (hydrogen, carbon monoxide, methane, ethane, propane, ethylene, propylene, butene, and acetylene. Although the combustion value of pentane is higher than that of butane, it is liquid at room temperature and cannot As a reducing protective gas, it is not considered), much higher than hydrogen, and the heat generated by its instantaneous combustion can make the stainless steel wire rapidly rise in temperature by 150-350°C during the second heating process described below. When the reducing gas comes into contact with air, it can be ignited and burned, heating the wire outlet pipe section, and transferring heat to the stainless steel wire.
上述还原性气体,在退火管段中的高温,可以给予不锈钢丝表面渗氢,在其内部退火热处理的同时,进行表面氢化处理。The above-mentioned reducing gas, at high temperature in the annealing pipe section, can give the surface of the stainless steel wire hydrogen permeation, and the surface hydrogenation treatment is carried out while the internal annealing heat treatment is carried out.
同时逆向行走后排出的高于大气压的还原性气体,能够阻止大气中的氧气从敞口处进入进丝钢管内部,保证其中的被加热到较高温度的不锈钢丝不会接触氧气被氧化,还原性气体逆行阻挡氧气进入,同时氧气被氢气燃烧消耗,进一步确保不锈钢丝在进丝管中不会被氧化。At the same time, the reducing gas higher than the atmospheric pressure discharged after reverse walking can prevent the oxygen in the atmosphere from entering the wire-feeding steel pipe from the opening, ensuring that the stainless steel wire heated to a higher temperature will not be oxidized and reduced by contact with oxygen. The inert gas is retrograde to block the entry of oxygen, while the oxygen is consumed by hydrogen combustion, further ensuring that the stainless steel wire will not be oxidized in the wire feeding tube.
保护性还原气氛(氢气或烷烃气体)在惰性气氛(氮气)保护或者纯度较高时,也可以不需要惰性气体保护,不爆炸不氧化。When the protective reducing atmosphere (hydrogen or alkane gas) is protected by an inert atmosphere (nitrogen) or the purity is high, it does not need to be protected by an inert gas, and it will not explode or oxidize.
氢气或烷烃气体燃烧加热产生的水蒸气和氮气可以直接排空,或者其中的热量可以会用于烘箱中预热。The water vapor and nitrogen generated by hydrogen or alkane gas combustion heating can be directly evacuated, or the heat can be used for preheating in an oven.
所述的烘箱管段预置并穿越于烘箱中,烘箱中的高温烟气给烘箱管段预热,并将其管壁的热量传递给在烘箱管段中行走的不锈钢丝,使得不锈钢丝被第一次加热(温度为100-150℃),表面的水汽被烘干,同时不锈钢丝不接触烘箱中的腐蚀性烟气。The oven pipe section is preset and passes through the oven. The high-temperature flue gas in the oven preheats the oven pipe section, and transfers the heat of the pipe wall to the stainless steel wire running in the oven pipe section, so that the stainless steel wire is heated for the first time. Heating (temperature 100-150°C), the water vapor on the surface is dried, and the stainless steel wire does not contact the corrosive fume in the oven.
裸露段为较短的一段,使得不锈钢丝被第一次加热产生的水汽散发到大气中,而且由于第一次预热的温度较低,不锈钢丝不会被周围空气中的氧气所氧化。The bare section is a shorter section, so that the stainless steel wire is emitted into the atmosphere by the water vapor generated by the first heating, and because the first preheating temperature is lower, the stainless steel wire will not be oxidized by the oxygen in the surrounding air.
进丝钢管的直径约为不锈钢丝直径的5-12倍,优选为5-6倍(太小时还原性气体的量较小,燃烧产生的热量不够;太大时,需要燃烧气体的量过大,资源消耗较多,而且容易产生回火,影响系统安全;而且燃烧的温度过高,不利于分阶段加热使得不锈钢丝的金相组织趋于合理)。The diameter of the wire feeding steel pipe is about 5-12 times the diameter of the stainless steel wire, preferably 5-6 times (the amount of reducing gas is too small, and the heat generated by combustion is not enough; when it is too large, the amount of combustion gas is too large , more resources are consumed, and tempering is easy to occur, which affects the safety of the system; and the burning temperature is too high, which is not conducive to staged heating to make the metallographic structure of stainless steel wire tend to be reasonable).
还原性气体排出,在出气孔处被点燃,与空气中的氧气反应,产生热量,使得不锈钢丝被第二次加热,给予不锈钢丝在线的瞬间加热升至退火需要的第二阶段温度(控制还原性气体的气压为2-10atm、不锈钢丝的直径1-2.5mm、不锈钢丝行走的速度1-5米/秒,通过还原性气体的数量和燃烧值,以及不锈钢丝的比热单位时间行走的质量等参数,结合不锈钢丝在烘箱管道中被预热的温度,就可以计算控制不锈钢丝被第二次加热升温100-400℃,达到温度200-550℃)。The reducing gas is discharged, ignited at the air outlet, and reacts with the oxygen in the air to generate heat, so that the stainless steel wire is heated for the second time, and the instantaneous heating of the stainless steel wire on the line rises to the second stage temperature required for annealing (controlled reduction The air pressure of the reactive gas is 2-10atm, the diameter of the stainless steel wire is 1-2.5mm, and the walking speed of the stainless steel wire is 1-5 m/s. The amount of the reducing gas and the combustion value, as well as the specific heat of the stainless steel wire travel per unit time. Quality and other parameters, combined with the preheating temperature of the stainless steel wire in the oven pipeline, can be calculated and controlled to heat the stainless steel wire for the second time by 100-400°C, reaching a temperature of 200-550°C).
由于焊接用不锈钢丝经过粗拉以后的不锈钢丝的直径已经比较细(第二次加热退火的温度更容易精确控制),其经过氢气或烷烃气体燃烧瞬间(在进丝管中行走的时间)所产生温度可以减少在退火炉中加热需要的时间和热量,减少了生产周期。Since the diameter of the stainless steel wire for welding is already relatively thin after rough drawing (the temperature of the second heating and annealing is easier to control accurately), it passes through the moment of hydrogen or alkane gas combustion (the time it takes to travel in the wire feeding tube). Generating temperature can reduce the time and heat required for heating in the annealing furnace, reducing the production cycle.
不锈钢丝继续在退火炉管段行走,被退火炉中的燃料(如煤气或天然气与空气的混合气体)从退火炉钢管外进行加热(第三次加热),使得行经其中的不锈钢丝继续升温至1000-1100℃,达到不锈钢丝退火所需要的最高温度,实现退火过程。The stainless steel wire continues to walk in the annealing furnace tube section, and is heated by the fuel in the annealing furnace (such as gas or a mixture of natural gas and air) from the outside of the annealing furnace steel pipe (the third heating), so that the stainless steel wire passing through it continues to heat up to 1000 -1100℃, reaching the highest temperature required for stainless steel wire annealing, and realizing the annealing process.
然后,不锈钢丝行经设置在冷却池中(其中储放有大量的水溶液)的冷却管段,被快速冷却降温至常温。最后,从出丝管段的出口引出。Then, the stainless steel wire passes through the cooling pipe section set in the cooling pool (where a large amount of aqueous solution is stored), and is rapidly cooled down to normal temperature. Finally, it is drawn out from the outlet of the silk outlet pipe section.
退火炉中煤气或天然气燃烧产生的废气通过废气管反流到烘箱中,其中残余的热量用于给烘箱中的烘箱管段预热(不直接接触不锈钢丝,避免不锈钢丝被高温废气腐蚀),进而使得在烘箱管段中行走的不锈钢丝被预热(第一次加热)达到一定的初始温度;再接受后续第二次和第三次加热的热量,热量叠加使得不锈钢丝达到退火需要的高温,废热充分利用,减少氢气(氨气)或烷烃类气体的消耗,经过烘箱中余热利用后的烟气从烘箱上方的排气管直接排空,可减少废热的排放,基本不影响车间的环境温度。The waste gas generated by the combustion of coal gas or natural gas in the annealing furnace flows back into the oven through the waste gas pipe, and the residual heat is used to preheat the oven pipe section in the oven (do not directly contact the stainless steel wire to avoid corrosion of the stainless steel wire by high-temperature waste gas), and then The stainless steel wire walking in the oven tube section is preheated (first heating) to a certain initial temperature; then it receives the heat of the subsequent second and third heating, and the superposition of heat makes the stainless steel wire reach the high temperature required for annealing, waste heat Make full use of it to reduce the consumption of hydrogen (ammonia) or alkane gas. After the waste heat in the oven is used, the flue gas is directly emptied from the exhaust pipe above the oven, which can reduce the emission of waste heat and basically does not affect the ambient temperature of the workshop.
有益效果:Beneficial effect:
本发明的不锈钢丝退火加热分为三阶段:(1)烘箱预热烘箱管段第一次加热,使得不锈钢丝在前面工序的清洗中的水分蒸发;(2)裸露段与进丝管段敞口处,点燃管内从出气孔出来的还原性气体后加热,不锈钢丝第二次加热;(3)退火炉钢段加热,通过煤气等燃料在管子下方加热,传热到其内部的不锈钢丝,使得加热温度达到1000-1100℃。The stainless steel wire annealing heating of the present invention is divided into three stages: (1) The oven preheats the oven pipe section for the first time, so that the water of the stainless steel wire in the cleaning of the previous process evaporates; (2) The exposed section and the wire feeding pipe section are exposed , ignite the reducing gas coming out of the air outlet in the tube and heat it, and the stainless steel wire is heated for the second time; (3) The steel section of the annealing furnace is heated, and the fuel such as gas is heated under the tube, and the heat is transferred to the stainless steel wire inside, so that the heating The temperature reaches 1000-1100°C.
三级加热,使得温度逐级提升,退火后的不锈钢丝的金相组织更好,便于进行后续的精细拉丝过程(能够再次拉丝为直径0.3mm-1.2mm,尤其达到0.3-0.6mm),传统退火工艺不能拉丝到如此细小的直径。Three-stage heating makes the temperature increase step by step, and the metallographic structure of the annealed stainless steel wire is better, which is convenient for the subsequent fine wire drawing process (it can be drawn again to a diameter of 0.3mm-1.2mm, especially 0.3-0.6mm), traditional The annealing process cannot draw to such a fine diameter.
本发明中,不采用价格较高体积较大(放置钢丝卷)的退火炉,而是采用一根根独立的进丝管和退火炉钢管代替退火炉炉膛,减少设备投入费用。In the present invention, the annealing furnace with high price and large volume (steel wire coils placed) is not used, but independent wire feeding pipes and annealing furnace steel pipes are used instead of the annealing furnace hearth to reduce equipment investment costs.
退火后的不锈钢丝行走到冷却管段浸渍在冷却池的水溶液中(不是空冷或者惰性气体冷却),减少冷却消耗的时间和热源,使得拉丝生产能够不停顿地连续进行,燃料成本较低。The annealed stainless steel wire walks to the cooling pipe section and is immersed in the aqueous solution of the cooling pool (not air cooling or inert gas cooling), which reduces the time and heat source consumed by cooling, so that the wire drawing production can be carried out continuously without stopping, and the fuel cost is low.
本发明的不锈钢丝退火系统设备,结构简单,设计巧妙,使用成本低。拉丝生产效率高,安全可靠,节能环保。The stainless steel wire annealing system equipment of the present invention has simple structure, ingenious design and low use cost. Drawing production efficiency is high, safe and reliable, energy saving and environmental protection.
氨气分解气中的氢气或烷烃气体具有四种用途:燃烧产生退火需要的高温;维持进丝管中还原气氛;消耗敞口处的氧气,并隔绝氧气进入高温的退火管段,避免对不锈钢丝的氧化腐蚀;形成水蒸气或及二氧化碳可以直接排放到大气中,没有环境污染。The hydrogen or alkane gas in the ammonia decomposition gas has four purposes: burning to generate the high temperature required for annealing; maintaining the reducing atmosphere in the wire feeding tube; consuming the oxygen at the opening and isolating oxygen from entering the high-temperature annealing tube section to avoid damage to the stainless steel wire Oxidation and corrosion; the formation of water vapor or carbon dioxide can be directly discharged into the atmosphere without environmental pollution.
而退火炉中燃气产生的热源二次利用,进一步节约燃料消耗,减少热量排放。冷却水溶液不与不锈钢丝直接接触,不易污染成品,也不易泄漏保证车间良好的生产环境。The secondary use of the heat source generated by the gas in the annealing furnace further saves fuel consumption and reduces heat emissions. The cooling water solution is not in direct contact with the stainless steel wire, so it is not easy to pollute the finished product, and it is not easy to leak to ensure a good production environment in the workshop.
附图说明Description of drawings
图1是本发明的一种系统立体结构示意图;Fig. 1 is a kind of system three-dimensional structure schematic diagram of the present invention;
图2是在本发明的一种钢丝在几个管段中的剖面结构示意图。Fig. 2 is a schematic cross-sectional structure diagram of a steel wire of the present invention in several pipe sections.
图中,1-钢丝;2-烘箱;3-裸露段;6-出丝管段;8-还原气体管;9-退火炉管段;10-进丝管段;11-排气管;12-出气孔;13-废气管;14-煤气管;15-空气管;16-堵料;20-火苗;22-烘箱管段。In the figure, 1-steel wire; 2-oven; 3-bare section; 6-wire outlet pipe section; 8-reducing gas pipe; 9-annealing furnace pipe section; 10-wire inlet pipe section; 11-exhaust pipe; 12-air outlet 13-exhaust gas pipe; 14-gas pipe; 15-air pipe; 16-blocking material; 20-flame; 22-oven pipe section.
具体实施方式Detailed ways
实施例一:Embodiment one:
如图1所示的不锈钢拉丝机分级加热退火阻氧系统,具有多根平行设置的不锈钢丝1,按照行走路线,每根不锈钢丝1依次穿过各自的烘箱管段22、裸露段3、进丝管段10、退火炉管段9、冷却管段、出丝管段6。The graded heating annealing oxygen barrier system of the stainless steel wire drawing machine shown in Figure 1 has a plurality of parallel
进丝管段10、退火炉管段9、冷却管段、出丝管段6为相互连通的管路。The wire
在冷却管段与退火炉管段9之间连接有还原性气体氢气的管路8,进丝管段10的入口处为具有供还原性气体流出敞口,供还原性气体排出,并与空气中的氧气反应,在出气孔12处被点燃产生热量,给予管壁加热,使得不锈钢丝1被第二次加热,给予不锈钢丝1在线的瞬间加热升至退火需要的第二阶段温度。氢气燃烧产生水汽直接排空,没有污染。A
出丝管段6的出口处为束口,只能供不锈钢丝1传出,不能供还原性气体流出。The outlet of the wire
实施例二:Embodiment two:
如图2所示,as shown in
在实施例一中,第二次加热使用的还原气体换成正丁烷。In Example 1, the reducing gas used in the second heating was replaced by n-butane.
通过控制钢丝1行走速度、进丝管10的直径数据、钢丝1直径数据、丁烷气体的压力或流量等参数,可以控制钢丝三段被逐段加热,最后的温度达到退火所需要的温度。By controlling the walking speed of the
正丁烷燃烧时产生的热量计算公式:Q=Cm1ΔT=m2q(或者V2q,视q单位而定)。The formula for calculating the heat generated when n-butane is burned: Q=Cm1ΔT=m2q (or V2q, depending on the q unit).
其中C为不锈钢丝1的比热460J/kg*℃,m1为进丝管段10长度内行走的不锈钢丝1及可折算部分管壁的质量,ΔT为第二段加热不锈钢丝1提升的温度;m2为进丝管段10长度内流出的正丁烷气体的质量,V2为正丁烷气体的体积,q为正丁烷的燃烧值。Where C is the specific heat of the
进丝钢管的内径约为6-10mm(壁厚0.4-0.6mm),进丝管段10长度100-200mm,正丁烷气体的气压为2-5atm(常温时的压力)、不锈钢丝1的直径1.0-1.5mm、不锈钢丝1行走的速度1-3米/秒,通过还原性气体以及不锈钢丝1的各种参数、传热效率、进丝管段10管壁持续被加热(有部分热流散失,可假1/3的管壁需要持续加热升温,其余管壁为基本恒温)以及其热量散失等因素。The inner diameter of the wire-feeding steel pipe is about 6-10mm (wall thickness 0.4-0.6mm), the length of the wire-feeding
再应用气体的德拉克龙方程PV=nRT,就可以近似计算不锈钢丝1被第二次加热升温150-250℃。Applying the Delacron equation PV=nRT of gas again, it can be approximated to calculate that the temperature of the
加上第一次预热后的温度,在进丝管段10的不锈钢丝1温度达到200-400℃,在第三段的退火加热只需要升温600-800℃,即可达到退火需要的温度1000-1100℃,第三次加热需要消耗的燃气得以节约。In addition to the temperature after the first preheating, the temperature of the
而且,分段加热,使得不锈钢丝1的金相组织得以优化,晶粒较细,排列均匀,冷却后可以再进行细拉丝,拉丝的直径可以达到0.4-0.6mm左右。Moreover, the staged heating optimizes the metallographic structure of the
Claims (5)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2022101169295 | 2022-02-08 | ||
CN202210116929.5A CN114540588A (en) | 2022-02-08 | 2022-02-08 | Stainless steel wire annealing and heating process system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115679048A true CN115679048A (en) | 2023-02-03 |
Family
ID=81673445
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210116929.5A Pending CN114540588A (en) | 2022-02-08 | 2022-02-08 | Stainless steel wire annealing and heating process system |
CN202211559105.1A Pending CN115679048A (en) | 2022-02-08 | 2022-12-06 | Stainless steel wire drawing machine graded heating annealing oxygen-blocking system |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210116929.5A Pending CN114540588A (en) | 2022-02-08 | 2022-02-08 | Stainless steel wire annealing and heating process system |
Country Status (1)
Country | Link |
---|---|
CN (2) | CN114540588A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116984404A (en) * | 2023-07-28 | 2023-11-03 | 浙江创特新材科技有限公司 | Movable multi-section thin tungsten wire heating module and high-strength thin tungsten wire drawing equipment |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101988148A (en) * | 2010-11-16 | 2011-03-23 | 江苏科技大学 | Energy-saving stainless steel wire hydrogen retreat furnace |
CN203080026U (en) * | 2012-03-19 | 2013-07-24 | 东莞市粤钢不锈钢制品有限公司 | Stainless steel wire continuous annealing furnace |
CN104131149A (en) * | 2014-08-04 | 2014-11-05 | 浙江腾龙精线有限公司 | Annealing device for stainless steel wires |
CN109055675A (en) * | 2018-09-08 | 2018-12-21 | 嘉兴市合工业电炉有限公司 | A kind of heat-tinting of stainless steel work-piece and annealing process |
CN212223062U (en) * | 2020-03-28 | 2020-12-25 | 新万鑫(福建)精密薄板有限公司 | Furnace end device of oriented silicon steel decarburization annealing furnace |
-
2022
- 2022-02-08 CN CN202210116929.5A patent/CN114540588A/en active Pending
- 2022-12-06 CN CN202211559105.1A patent/CN115679048A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101988148A (en) * | 2010-11-16 | 2011-03-23 | 江苏科技大学 | Energy-saving stainless steel wire hydrogen retreat furnace |
CN203080026U (en) * | 2012-03-19 | 2013-07-24 | 东莞市粤钢不锈钢制品有限公司 | Stainless steel wire continuous annealing furnace |
CN104131149A (en) * | 2014-08-04 | 2014-11-05 | 浙江腾龙精线有限公司 | Annealing device for stainless steel wires |
CN109055675A (en) * | 2018-09-08 | 2018-12-21 | 嘉兴市合工业电炉有限公司 | A kind of heat-tinting of stainless steel work-piece and annealing process |
CN212223062U (en) * | 2020-03-28 | 2020-12-25 | 新万鑫(福建)精密薄板有限公司 | Furnace end device of oriented silicon steel decarburization annealing furnace |
Non-Patent Citations (2)
Title |
---|
(英)普里查德(R.PRITCHARD)著;刘麟贞译.: "燃气应用技术", 31 July 1983, pages: 227 * |
方韶剑 等: "工程材料与热加工基础", 31 March 2016, 北京:北京理工大学出版社, pages: 166 - 167 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116984404A (en) * | 2023-07-28 | 2023-11-03 | 浙江创特新材科技有限公司 | Movable multi-section thin tungsten wire heating module and high-strength thin tungsten wire drawing equipment |
CN116984404B (en) * | 2023-07-28 | 2024-04-26 | 浙江创特新材科技有限公司 | Movable multi-section thin tungsten wire heating module and high-strength thin tungsten wire drawing equipment |
Also Published As
Publication number | Publication date |
---|---|
CN114540588A (en) | 2022-05-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN115679048A (en) | Stainless steel wire drawing machine graded heating annealing oxygen-blocking system | |
CN203360550U (en) | Ammonia-containing tail gas treatment device in nitridation heat treatment technology | |
CN106215664A (en) | Danger waste burning system flue gas combination method of denitration and device | |
CN108548179A (en) | One kind is from preheated burning formula directed radiation pipe heating device | |
CN105642108B (en) | The method and system of CO recovery processing in a kind of metallurgy industry | |
CN204301532U (en) | A kind of reheat furnace system | |
WO2020144237A1 (en) | Process for producing potassium sulphate | |
RU2008148668A (en) | METHOD AND DEVICE OF THE BURNER | |
CN203295556U (en) | Heat-treatment furnace system for waste heat recovery | |
JPH02272208A (en) | Low nox combustion method | |
CN205175150U (en) | Device is recycled in reduction of industrial stoves polyoxy burning flue gas | |
CN201778068U (en) | Quenching furnace tail gas combustion heat recycling system | |
CN211411518U (en) | RTO three-compartment off-line back burning device | |
CN204115495U (en) | A kind of carbonization treatment apparatus | |
CN209893428U (en) | Waste gas treatment equipment for heat exchanger enamelling machine | |
CN105371670A (en) | Reducing and reusing device for multi-oxygen combustion smoke of industrial kiln and operation method thereof | |
CN213840953U (en) | Tail gas treatment device | |
CN222298530U (en) | Cold and hot blank mixed pure oxygen combustion steel rolling heating furnace system | |
CN202177316U (en) | Waste gas purification device of vertical furnace | |
CN210874774U (en) | Multistage energy utilization dispersion oxidation waste gas treatment device | |
CN204283568U (en) | Off-gas recovery vaporizer | |
CN204848270U (en) | Sulfur recovery system for petrochemical field | |
CN222438535U (en) | Comprehensive utilization system of tablet vanadium calcination flue gas | |
CN221336588U (en) | Baking structure of total oxygen steel ladle | |
CN213396522U (en) | High-efficiency energy-saving blast furnace gas chamber type heating furnace with double heat storage heating modes |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination |