[go: up one dir, main page]

CN1302146C - Dynamic control system for low-pressure carburating heat treament furnace - Google Patents

Dynamic control system for low-pressure carburating heat treament furnace Download PDF

Info

Publication number
CN1302146C
CN1302146C CNB2004100163700A CN200410016370A CN1302146C CN 1302146 C CN1302146 C CN 1302146C CN B2004100163700 A CNB2004100163700 A CN B2004100163700A CN 200410016370 A CN200410016370 A CN 200410016370A CN 1302146 C CN1302146 C CN 1302146C
Authority
CN
China
Prior art keywords
carburizing
vacuum
furnace
heating chamber
pressure
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 - Fee Related
Application number
CNB2004100163700A
Other languages
Chinese (zh)
Other versions
CN1560317A (en
Inventor
陈明志
杨景峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BAOHUAWEI HEAT TREATMENT EQUIPMENT Co Ltd SHANGHAI
Original Assignee
BAOHUAWEI HEAT TREATMENT EQUIPMENT Co Ltd SHANGHAI
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by BAOHUAWEI HEAT TREATMENT EQUIPMENT Co Ltd SHANGHAI filed Critical BAOHUAWEI HEAT TREATMENT EQUIPMENT Co Ltd SHANGHAI
Priority to CNB2004100163700A priority Critical patent/CN1302146C/en
Publication of CN1560317A publication Critical patent/CN1560317A/en
Application granted granted Critical
Publication of CN1302146C publication Critical patent/CN1302146C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)

Abstract

一种涉及真空渗碳热处理技术的控制系统,尤指一种应用于低压渗碳热处理炉的动态控制装置及其热处理方法。该发明包括该系统的装置及热处理制程方法的具体工作步骤,该装置主要由计算机及控制软件、热电偶、真空计及淬火室等组成,采用多参数输入计算机做为控制基础,使用两种以上的真空计,计算机根据已输入的各项参数,演算并作实时的动态控制,并通过控制马达变频器来达成指挥真空泵系统的必要抽吸量外,反复多次直到渗碳层深。本发明的优点是:可以节省渗碳材料量;增加炉装载量;增加渗碳之均匀性;减少真空系统之积碳;能以动态控制方式,自动产生复杂之制程;可以完成计算机自动控制,免除人为操作可能的错误。

Figure 200410016370

A control system related to vacuum carburizing heat treatment technology, especially a dynamic control device and heat treatment method applied to a low-pressure carburizing heat treatment furnace. The invention includes the device of the system and the specific working steps of the heat treatment process method. The device is mainly composed of a computer and control software, a thermocouple, a vacuum gauge, and a quenching chamber. The vacuum gauge, the computer calculates and performs real-time dynamic control according to the input parameters, and controls the motor inverter to achieve the necessary suction volume of the vacuum pump system, and repeats it many times until the carburizing layer is deep. The advantages of the present invention are: it can save the amount of carburizing material; increase the loading capacity of the furnace; increase the uniformity of carburizing; reduce the carbon deposit in the vacuum system; can automatically generate complex process in a dynamic control mode; can complete computer automatic control, Eliminate possible human errors.

Figure 200410016370

Description

应用于低压渗碳热处理炉的动态控制装置及其热处理方法Dynamic control device and heat treatment method applied to low-pressure carburizing heat treatment furnace

技术领域technical field

本发明涉及一种真空渗碳热处理技术的控制系统,尤指一种应用于低压渗碳热处理炉的动态控制系统。The invention relates to a control system of vacuum carburizing heat treatment technology, especially a dynamic control system applied to a low-pressure carburizing heat treatment furnace.

背景技术Background technique

真空渗碳亦称作低压渗碳;由于无火焰帘的设计,澈底解决了油烟及高热对工作环境的影响,加上近年来逐渐克服技术的困难,渗碳的品质与再现性明显的优于传统气体渗碳热处理,因此本技术已受到汽车工业,精密组件工业与航天工业的重视,并且逐步用来取代传统气体渗碳热处理制程,甚至与机械加工制程整合在同一厂区.Vacuum carburizing is also called low-pressure carburizing; due to the design of no flame curtain, the influence of oil fume and high heat on the working environment is thoroughly solved. In addition, the technical difficulties have been gradually overcome in recent years. Traditional gas carburizing heat treatment, so this technology has been valued by the automobile industry, precision component industry and aerospace industry, and gradually used to replace the traditional gas carburizing heat treatment process, and even integrated with the machining process in the same factory area.

1.真空渗碳热处理的技术于1960年代已开始进行研究,利用最普遍的渗碳材料如甲烷CH4或丙烷C3H8直接导入加热状态之真空炉,直接进行表面渗碳,其原始之用意是克服一般气体渗碳时,对盲孔或深孔渗碳不均的现象,然而初期产生严重积碳及渗碳品质仍然不能达到理想,所以此技术仅在实验室阶段,无法进入量产。1. The technology of vacuum carburizing heat treatment has been studied in the 1960s. The most common carburizing materials such as methane CH 4 or propane C 3 H 8 are directly introduced into the vacuum furnace in the heating state, and the surface carburizing is directly carried out. The purpose is to overcome the phenomenon of uneven carburizing of blind holes or deep holes during general gas carburizing. However, serious carbon deposits in the early stage and carburizing quality are still not ideal. Therefore, this technology is only in the laboratory stage and cannot enter mass production. .

2.于1970年代,采用其它参数进行更多的实验,例如将气体流量加大,的确可改善渗碳深度,但炉内产生严重积炭,仍然无法达成量产。2. In the 1970s, more experiments were carried out using other parameters, such as increasing the gas flow rate, which could indeed improve the carburizing depth, but the serious carbon deposits in the furnace still failed to achieve mass production.

3.1980年代,采用PLASMA装置加速甲烷CH4或丙烷C3H8气体的渗碳作用,可大幅降低气体导入量,改善积炭现象,但仍然有维护上的困扰,并且设备太过昂贵。3. In the 1980s, PLASMA equipment was used to accelerate the carburization of methane CH 4 or propane C 3 H 8 gas, which could greatly reduce the amount of gas introduced and improve the carbon deposition phenomenon, but there were still maintenance problems and the equipment was too expensive.

4.1990年代,因乙炔C2H2、乙烯C2H4、己烷C6H12及各种混合气体等非饱和之渗碳材料陆续被发现,可应用在真空渗碳制程,如此可将气体导入量降至很低,而且可得到良好的渗碳效果,因为导入量低所以积炭的情况已大幅度的改善至可进行量产的阶段。4. In the 1990s, unsaturated carburizing materials such as acetylene C 2 H 2 , ethylene C 2 H 4 , hexane C 6 H 12 and various mixed gases were discovered one after another, which can be applied in the vacuum carburizing process. The amount of introduction is reduced to a very low level, and a good carburizing effect can be obtained. Because of the low amount of introduction, the situation of carbon deposition has been greatly improved to the stage where mass production can be carried out.

5.然而目前之低压渗碳热处理炉,采取阶段式之固定炉压设定值,借着管路出口之真空计来控制渗碳材料的注入量。5. However, the current low-pressure carburizing heat treatment furnace adopts a staged fixed furnace pressure setting value, and the injection amount of carburizing material is controlled by a vacuum gauge at the outlet of the pipeline.

目前之低压渗碳热处理炉均配置有一套真空泵系统,为了能快速将炉内之空气排出以便进行热处理及渗碳的制程,该真空泵系统均配备极大容量,当进行低压渗碳时,其设定的渗碳压力约在10Torr甚至更低,此时大容量的真空泵的抽量常导致渗碳之碳氢化物必须大量注入,而且泵抽取口的实际压力小于远处的压力,易导致渗碳不均,所以现有设备均限定最大面积之装载量,才能均匀渗碳,另外真空系统的污染情况仍然无法免除。此外,真空计安置在管线出口,除了无法正确反应真实的炉内压力,并且无法确实反应渗碳化学反应后产生之多种气体如氢气及甲烷等,所以常导致制程不稳定。The current low-pressure carburizing heat treatment furnace is equipped with a set of vacuum pump system. In order to quickly discharge the air in the furnace for heat treatment and carburizing process, the vacuum pump system is equipped with a large capacity. When performing low-pressure carburizing, its design The fixed carburizing pressure is about 10 Torr or even lower. At this time, the pumping capacity of the large-capacity vacuum pump often leads to a large amount of carburizing hydrocarbons to be injected, and the actual pressure at the pump suction port is lower than the pressure at the far end, which easily leads to carburizing. Uneven, so the existing equipment is limited to the maximum area of loading, in order to be evenly carburized, and the pollution of the vacuum system is still unavoidable. In addition, the vacuum gauge is placed at the outlet of the pipeline. In addition to not accurately reflecting the real furnace pressure, it also cannot accurately reflect the various gases such as hydrogen and methane produced after the carburizing chemical reaction, so it often leads to process instability.

例如以低压渗碳制程以乙炔为渗碳材料的主反应如下: For example, the main reaction of using acetylene as the carburizing material in the low-pressure carburizing process is as follows:

在渗碳温度(900度-1050度C)时,被渗工件具触媒的作用,使C2H2裂解,产生2个活性碳及2个氢气,该2个活性碳便直接渗入工件表面,此时氢气在炉内,作为还原性气体。At the carburizing temperature (900°C-1050°C), the workpiece to be infiltrated acts as a catalyst to crack C2H2 to produce 2 activated carbons and 2 hydrogens, and the 2 activated carbons directly penetrate into the surface of the workpiece, and the hydrogen gas In the furnace, as a reducing gas.

常知技术之配置主要是由派拉尼真空计安置在管路的出口,然后将测得的数据送入真空控制器,再指挥控制阀控制C2H2的注入量。其主要缺失如下:The configuration of the known technology is mainly to install the Pirani vacuum gauge at the outlet of the pipeline, then send the measured data to the vacuum controller, and then direct the control valve to control the injection amount of C2H2. Its main deficiencies are as follows:

1)、派拉尼真空计无法在渗碳进行中测得实际炉内压力1) The Pirani vacuum gauge cannot measure the actual furnace pressure during carburizing

派拉尼真空计是采用气体冷却FILAMENT时,产生惠斯登电路不平衡,而测出气体之多少,即真空度之数值。因气体之重量及冷却率不同,所以必须以已知的一种气体,预设真空表的参数,以计算真空度。When the Pirani vacuum gauge is used to cool the FILAMENT with gas, the Wheatstone circuit is unbalanced, and the amount of gas measured is the value of the vacuum degree. Because the weight and cooling rate of the gas are different, a known gas must be used to preset the parameters of the vacuum gauge to calculate the vacuum degree.

在渗碳开始之初期,全部是C2H2气体,所以派拉尼真空计可测得真实的真空度,随着渗碳进行,产生H2气,此时派拉尼真空计准度下降,所以此时控制之C2H2注入量便非正确量。At the beginning of carburizing, it is all C2H2 gas, so the Pirani vacuum gauge can measure the real vacuum degree. As carburizing progresses, H2 gas is generated. At this time, the accuracy of the Pirani vacuum gauge decreases, so at this time The controlled C2H2 injection amount is not the correct amount.

2)、大排气量的真空泵系统造成炉内压力不均2) The large displacement vacuum pump system causes uneven pressure in the furnace

常知技术之真空泵容量的配置,以加热室容量7.8m3(有效工作区1.2m×0.76m×0.76m)为例,真空泵的每小时之抽气量约为450m3。主要是顾及大型的泵可缩短开始加热前的排气时间。然而,泵的抽气太大,在施放渗碳材料时,造成炉内的压力不均。一般低压渗碳之压力设定在0.1TORR-10TORR,此时由于泵之抽气能力太大,抽气口真空计位置与炉内最远处之压力差可达30%-50%。The configuration of vacuum pump capacity in conventional technology, taking the heating chamber capacity of 7.8m 3 (effective working area 1.2m×0.76m×0.76m) as an example, the pumping capacity of the vacuum pump per hour is about 450m 3 . The main consideration is that a large pump can shorten the exhaust time before heating starts. However, the suction of the pump is too large, causing uneven pressure in the furnace when the carburizing material is applied. Generally, the pressure of low-pressure carburizing is set at 0.1TORR-10TORR. At this time, due to the large pumping capacity of the pump, the pressure difference between the position of the vacuum gauge at the pumping port and the farthest point in the furnace can reach 30%-50%.

另外由于泵之抽气能力太大,为了维持炉内压力,所以渗碳材料之流量必须远超过所须。In addition, due to the large pumping capacity of the pump, in order to maintain the pressure in the furnace, the flow rate of the carburizing material must be much higher than necessary.

6.欧洲专利EP0818555A1,使用C2H2作为渗碳材料,于渗碳时,将C2H2导入并且控制在压力1~7.5Torr的范围,扩散阶段,则炉内保低真空状况,本方式无法精确掌握渗碳过程气体反应的变化,而且不断的导入C2H2,消耗较多C2H2,并造成炉内及真空系统的污染。6. European patent EP0818555A1 uses C 2 H 2 as carburizing material. During carburizing, C 2 H 2 is introduced and controlled in the pressure range of 1 to 7.5 Torr. In the diffusion stage, the furnace maintains a low vacuum state. This This method cannot accurately grasp the change of gas reaction in the carburizing process, and continuously introduces C 2 H 2 , consumes more C 2 H 2 , and causes pollution in the furnace and vacuum system.

7.美国US6187111在类似于FIG1装置上,于渗碳时,将C2H4导入并且控制在一定的压力范围,扩散阶段,则炉内保低真空状况,本方式无法精确掌握渗碳过程气体反应的变化,而且不断的导入C2H4,消耗较多C2H4,并造成炉内及真空系统的污染。7. The United States US6187111 is similar to the FIG1 device. When carburizing, C 2 H4 is introduced and controlled within a certain pressure range. During the diffusion stage, the vacuum in the furnace is kept low. This method cannot accurately grasp the gas reaction in the carburizing process. Changes, and the continuous introduction of C 2 H 4 consumes more C 2 H 4 and causes pollution in the furnace and vacuum system.

8.JP2003-71756在类似于FIG1装置上,采用C2H2做为渗碳压力维持在1.5~3.5KPA并且使用二段扩散,第一段CO2压力在0.3~15KPA,第二段扩散是真空进行,其优点是可以在可控情况下,进行CO2的表面脱碳,但是C2H2的渗碳仍祗是定压进行,不但表面较难控制,而且气体耗量大,造成真空系统严重的污染。8. JP2003-71756 uses C 2 H 2 as the carburizing pressure on a device similar to FIG1 to maintain the pressure at 1.5-3.5KPA and uses two-stage diffusion. The first-stage CO 2 pressure is 0.3-15KPA, and the second-stage diffusion is The advantage is that the surface decarburization of CO 2 can be carried out under controllable conditions, but the carburization of C 2 H 2 is still only carried out at a constant pressure. Not only is the surface difficult to control, but also the gas consumption is large, resulting in a vacuum The system is seriously polluted.

9.WO03/048405-A1,在似FIG3装置上,采用C2H4+H2做为渗碳压,利用C2H4及H2的检测装置,检测出C2H4及H2的分压,然后计算出渗碳的碳势再利用材料种类,渗碳规格得到之设定值,去实际做控制,本装置之缺点C2H4及H2的检知测定设备不但昂贵而且实际运作时稳定性不佳,另为其利用旁路阀来控制炉压的方式亦比较不稳定。9. WO03/048405-A1, on a device similar to FIG3, C 2 H 4 +H 2 is used as the carburizing pressure, and the C 2 H 4 and H 2 detection device is used to detect the C 2 H 4 and H 2 Partial pressure, and then calculate the carbon potential of carburizing and then use the material type and the setting value obtained from carburizing specifications to actually do control. The disadvantage of this device is that the detection and measurement equipment of C 2 H 4 and H 2 is not only expensive but also practical The stability is not good during operation, and the method of using the bypass valve to control the furnace pressure is also relatively unstable.

10.US2003-020214-A1在本装置上是采用C6H12做为渗碳材料,C6H12在注入炉内后,立刻挥发为气体,利用排气真空泵来控制其炉压,其缺点仍是控制较差,并且耗费大量渗碳材料。10. US2003-020214-A1 uses C 6 H 12 as the carburizing material in this device. After C 6 H 12 is injected into the furnace, it immediately volatilizes into gas, and the exhaust vacuum pump is used to control the furnace pressure. Its disadvantages It is still poorly controlled and consumes a lot of carburizing material.

11.JP2003-119558在类似FIG1的装置上进行真空渗碳热处理,其制程主要是分为二段渗碳。11. JP2003-119558 performs vacuum carburizing heat treatment on a device similar to FIG1, and its process is mainly divided into two-stage carburizing.

第一段采用C2H2,压力设定在11.3Torr~26.3TorrThe first stage adopts C 2 H 2 , and the pressure is set at 11.3Torr~26.3Torr

第二段采用13A都市瓦斯,压力设定在3.76Torr~60Torr,扩散仍采用真空状态下进行,本方法的缺点和以前相同。The second stage uses 13A urban gas, the pressure is set at 3.76Torr~60Torr, and the diffusion is still carried out in a vacuum state. The disadvantages of this method are the same as before.

12.JP2002-173759在真空渗碳热处理时,利用压力计测得的炉压与氢检测仪测得的氢分压,然后计算碳势以便控制碳氮化物的进入量,本技术采用氢检测仪之主要结构是利用一支陶瓷管,在端点真空焊接一片薄膜(proton质子)作为氢气探测头,即通过薄膜来读出数据,陶瓷管中间通标准氢气,外面则接触炉气,利用二侧氢分压的砧不同,产生一个电位差,藉由这个电位差的大小,换算出氢气的含量,这个结构及原理和以化锆做成之氧探头极为相似。但在实际渗碳热处理时,渗碳材料很容易在探头上,形成一层媒灰,严重的影响侦测的确度,所以氧探头在渗碳热处理应用时必须搭配一套烧碳机构,利用渗碳炉气将积存的媒灰烧掉,然而在真空渗碳时,并没有足够的炉气可以烧掉媒灰,所以本结构之设计并不适合量产使用。12. JP2002-173759 uses the furnace pressure measured by the pressure gauge and the hydrogen partial pressure measured by the hydrogen detector during the vacuum carburizing heat treatment, and then calculates the carbon potential to control the amount of carbonitride. This technology uses the hydrogen detector The main structure is to use a ceramic tube, vacuum weld a thin film (proton proton) at the end as a hydrogen detector, that is, read the data through the thin film, the standard hydrogen is passed through the middle of the ceramic tube, and the outside is exposed to the furnace gas, using hydrogen on both sides Different anvils for partial pressure produce a potential difference, and the hydrogen content is converted by the size of the potential difference. This structure and principle are very similar to the oxygen probe made of zirconium oxide. However, in the actual carburizing heat treatment, the carburizing material is easy to form a layer of soot on the probe, which seriously affects the detection accuracy. The carbon furnace gas burns the accumulated soot. However, during vacuum carburizing, there is not enough furnace gas to burn off the soot, so the design of this structure is not suitable for mass production.

13.JP2002-2167658在真空渗碳热处理时,采用C2H2或C2H2与H2的混合气,做为渗碳的材料,设定一个渗碳的上限值及下限值,于炉压上限时打开真空泵,于下限时关闭真空泵,以便节省渗碳材料消耗量,然而以炉压设定无法真实反应炉内渗碳反应的进行,所以容易产生渗均匀的状况。13. JP2002-2167658 uses C 2 H 2 or a mixture of C 2 H 2 and H 2 as the carburizing material during vacuum carburizing heat treatment, and sets a carburizing upper limit and lower limit. Turn on the vacuum pump at the upper limit of the furnace pressure, and turn off the vacuum pump at the lower limit to save the consumption of carburizing materials. However, the carburizing reaction in the furnace cannot be realistically set by setting the furnace pressure, so it is easy to cause uniform infiltration.

14.JP2001-262313在类似FIG1的装置上进行真空渗碳热处理,采用C2H4及H2的混合气做为渗碳材料,其混合比例氢气在15%~50%,炉内压力设定在40~65Torr,本方式的缺点和其它相同。14. JP2001-262313 conducts vacuum carburizing heat treatment on a device similar to FIG1, using a mixture of C 2 H 4 and H 2 as the carburizing material, the mixing ratio of hydrogen is 15% to 50%, and the pressure in the furnace is set At 40-65Torr, the disadvantages of this method are the same as others.

15.JP2001-240954 FIG8,装置上进行真空渗碳热处理采用C2H4及H2的混合气做为渗碳材料,利用C2H4检测器检测C2H4之含量,以便控制真空抽气系统的阀门,本技术采用C2H4之检测设备昂贵而且可靠度差,另外使用阀门来控制真空抽气系统,其精度亦不佳。15. JP2001-240954 FIG8, the vacuum carburizing heat treatment on the device uses the mixed gas of C 2 H 4 and H 2 as the carburizing material, and uses the C 2 H 4 detector to detect the content of C 2 H 4 in order to control the vacuum pumping For the valves of the gas system, the C 2 H 4 detection equipment used in this technology is expensive and has poor reliability. In addition, the valves are used to control the vacuum pumping system, and its accuracy is not good.

16.JP2001-81543 FIG9装置上进行真空渗碳热处理,利用雷射光检测碳氢化物的注入量,然后控制其需要量,本技术采用雷射光检测可靠度在有炉内积炭时,可靠度下降。16. JP2001-81543 FIG9 device performs vacuum carburizing heat treatment, uses laser light to detect the injection amount of hydrocarbons, and then controls its required amount. This technology uses laser light to detect reliability. When there is carbon deposit in the furnace, the reliability decreases .

17.US6187111类似FIG1的装置上进行真空渗碳热处理,使用乙烯为渗碳原料其渗碳的炉压为1-10KPA,扩散阶段,则炉内保低真空状况,本方式无法精确掌握渗碳过程气体反应的变化,而且不断的导入C2H2,消耗较多C2H2,并造成炉内及真空系统的污染。17. US6187111 performs vacuum carburizing heat treatment on a device similar to FIG1. Using ethylene as the carburizing raw material, the carburizing furnace pressure is 1-10KPA. In the diffusion stage, the vacuum in the furnace is kept low. This method cannot accurately grasp the carburizing process. The change of gas reaction and the continuous introduction of C 2 H 2 consume more C 2 H 2 and cause pollution in the furnace and vacuum system.

18.US PAT NO.5.702.540使用乙烯作为渗碳原料,并将炉压降至1KPA以下,但是乙烯的价格非常昂贵,并且不易大量储存处理,由于将压力设定在1KPA,所以使用大容量的真空泵,使气体耗量很大。18. US PAT NO.5.702.540 uses ethylene as the raw material for carburizing, and reduces the furnace pressure to below 1KPA, but the price of ethylene is very expensive, and it is not easy to store and handle in large quantities. Since the pressure is set at 1KPA, a large capacity is used The vacuum pump makes the gas consumption very large.

19.US PAT NO.5.205.873使乙烯及氢气做为渗碳原料,将炉压控制在1~10KPA,但是氢气有爆炸性,安全性必须考虑。19. US PAT NO.5.205.873 uses ethylene and hydrogen as carburizing raw materials, and controls the furnace pressure at 1~10KPA, but hydrogen is explosive, and safety must be considered.

20.US PAT 6.187.111采用较小容量原,拟降低气体的耗量,但是它会影响初期真空抽吸的时间。20. US PAT 6.187.111 adopts a smaller capacity original to reduce gas consumption, but it will affect the initial vacuum suction time.

以上为已有技术。The above is prior art.

发明内容Contents of the invention

为了克服上述不足之处,本发明的主要目的旨在提供一种采用多参数输入计算机为控制基础,使用两种以上的真空计,以真实反应炉内渗碳气体的化学变化,并通过控制马达变频器来达成指挥真空泵系统的必要抽吸量的应用于低压渗碳热处理炉的动态控制装置及其热处理方法。In order to overcome the above disadvantages, the main purpose of the present invention is to provide a control based on multi-parameter input computer, using more than two kinds of vacuum gauges, to truly react the chemical changes of carburizing gas in the furnace, and control the motor The frequency converter is used to achieve the necessary suction volume of the vacuum pump system, which is applied to the dynamic control device and heat treatment method of the low-pressure carburizing heat treatment furnace.

本发明要解决的技术问题是:要解决多参数输入计算机的控制问题;如何使用两种以上的真空计;如何安装控制马达变频器的位置,控制及达成指挥真空泵系统的必要抽吸量等问题。The technical problems to be solved in the present invention are: to solve the control problem of multi-parameter input computer; how to use more than two kinds of vacuum gauges; .

本发明解决其技术问题所采用的技术方案是:该装置主要有计算机及控制软件、可编程控制器、热电偶、真空计、电源、工件及淬火室等组成,其可编程控制器、计算机及控制软件模块相互连接,可控硅整流器的一端与可编程控制器的输入端相连接,可控硅整流器的另一端与电源的一端相连接,电源的另一端与加热室的输入端相连接,可编程控制器与加热室之间由主控炉温热电偶及过温控制热电偶相互连接,可编程控制器的一输出端通过数位信号输出线与加热室的输入端相连接,可编程控制器的一输出端通过数位信号输入线与加热室的输出端相连接,PIRANI真空计显示器的一端通过真空计与加热室相连接,其输出端与可编程控制器的输入端相连接,薄膜式真空计显示器的一端直接与加热室相连接,其输出端与可编程控制器的输入端相连接,加热室内安置有热处理工件,加热室与淬火室连为一体,中间有门隔离,其中:The technical solution adopted by the present invention to solve its technical problems is: the device mainly consists of computer and control software, programmable controller, thermocouple, vacuum gauge, power supply, workpiece and quenching chamber, etc., its programmable controller, computer and The control software modules are connected to each other, one end of the silicon controlled rectifier is connected with the input end of the programmable controller, the other end of the silicon controlled rectifier is connected with one end of the power supply, and the other end of the power supply is connected with the input end of the heating chamber, The programmable controller and the heating chamber are connected to each other by the main control furnace temperature thermocouple and the over-temperature control thermocouple. One output end of the programmable controller is connected to the input end of the heating chamber through a digital signal output line. One output end of the controller is connected to the output end of the heating chamber through a digital signal input line, one end of the PIRANI vacuum gauge display is connected to the heating chamber through a vacuum gauge, and its output end is connected to the input end of the programmable controller. One end of the type vacuum gauge display is directly connected to the heating chamber, and its output end is connected to the input end of the programmable controller. The heat treatment workpiece is placed in the heating chamber, and the heating chamber and the quenching chamber are connected as a whole, and there is a door isolation in the middle. Among them:

加热室的外部依次与真空阀、真空泵、真空泵马达与真空泵马达的变频控制器相互串接,PIRANI真空计与加热元件相互连接,薄膜式真空计与加热元件相互连接。The outside of the heating chamber is connected in series with the vacuum valve, the vacuum pump, the vacuum pump motor and the frequency conversion controller of the vacuum pump motor. The PIRANI vacuum gauge is connected to the heating element, and the thin-film vacuum gauge is connected to the heating element.

所述的应用于低压渗碳热处理炉的动态控制装置的真空计至少有两种以上组成。The vacuum gauge applied to the dynamic control device of the low-pressure carburizing heat treatment furnace has at least two or more components.

一种应用于低压渗碳热处理炉的动态控制系统的热处理方法,该方法通过多参数输入计算机为控制基础,用两种以上的真空计反应炉内渗碳气体的化学变化,通过控制马达变频器来达成指挥真空泵系统的必要抽吸量,拉地完成计算机及控制软件模快的工作,其中:A heat treatment method applied to the dynamic control system of a low-pressure carburizing heat treatment furnace. The method uses multi-parameter input to the computer as the control basis, uses more than two vacuum gauges to react the chemical changes of the carburizing gas in the furnace, and controls the motor frequency converter. To achieve the necessary suction volume to command the vacuum pump system, pull the ground to complete the computer and control software simulation work, of which:

输入计算机的参数包括两种方式:渗碳过程中实时测得的参数以及在操作之前预先输入的参数,包括:a)、工件的材料;b)、工件之总表面积;c)、渗碳层深度要求;d)、表面含碳量要求;e)、最高工作温度限制;f)、渗碳材料的种类;g)、电源的频率,其特征在于:该方法具体工作步骤是:The parameters input into the computer include two ways: the parameters measured in real time during the carburizing process and the parameters input before operation, including: a), the material of the workpiece; b), the total surface area of the workpiece; c), the carburized layer Depth requirement; d), surface carbon content requirement; e), maximum operating temperature limit; f), type of carburizing material; g), frequency of power supply, it is characterized in that: the specific working steps of this method are:

步骤1.工件送入加热室Step 1. The workpiece is sent into the heating chamber

工件备妥后,淬火室前门及加热室前门打开,直接送入加热室;After the workpiece is ready, the front door of the quenching chamber and the front door of the heating chamber are opened, and it is directly sent into the heating chamber;

步骤2.抽真空Step 2. Vacuum

真空系统的真空阀及淬火室真空系统打开,开始抽真空,真空泵马达变频器设定在正常供电频率;The vacuum valve of the vacuum system and the vacuum system of the quenching chamber are opened to start vacuuming, and the frequency converter of the vacuum pump motor is set at the normal power supply frequency;

步骤3.加热运行Step 3. Heat Run

当真空度达1torr或小于1torr后,开始加热,并且真空泵持续运行;When the vacuum reaches 1torr or less than 1torr, start heating, and the vacuum pump continues to run;

步骤4.持续均热Step 4. Continue soaking

温度抵达渗碳温度后,持续运行均热程序直到工件温度均匀;After the temperature reaches the carburizing temperature, continue to run the soaking program until the workpiece temperature is uniform;

步骤5.变频器工作Step 5. Inverter working

进入渗碳制程后,根据制程,变频器将频率降至正常频率之60%-5%,真空泵维持小抽吸量;After entering the carburizing process, according to the process, the frequency converter will reduce the frequency to 60%-5% of the normal frequency, and the vacuum pump will maintain a small suction volume;

步骤6.注入渗碳材料Step 6. Inject carburizing material

渗碳剂控制阀打开,开始注入一定量的渗碳材料;The carburizing agent control valve is opened and a certain amount of carburizing material is injected;

步骤7.设定值Step 7. Set the value

当炉内压力至设定值时,利用变频器控制真空泵的抽吸量,并将炉压维持在设定值;When the pressure in the furnace reaches the set value, use the frequency converter to control the suction volume of the vacuum pump and maintain the furnace pressure at the set value;

步骤8.真空计显示器工作Step 8. Vacuum Gauge Display Working

当炉内气体进行渗碳反映时,PIRANI真空计显示器V1及薄膜式真空计显示器V2开始出现不同的读数,当PIRANI真空计显示器V1/薄膜式真空计显示器V2比值为一定时,变频器将频率调整为正常供电频率,抽真空;When the gas in the furnace undergoes carburizing reaction, PIRANI vacuum gauge display V1 and film vacuum gauge display V2 begin to show different readings. When the ratio of PIRANI vacuum gauge display V1/film vacuum gauge display V2 is constant, the frequency converter will Adjust to normal power supply frequency, vacuumize;

步骤9.重复执行Step 9. Repeat execution

停留一段时间进行扩散后,重复步骤5、6、7、8的制程;After staying for a period of time for diffusion, repeat the process of steps 5, 6, 7, and 8;

步骤10.自动控制Step 10. Automatic Control

步骤9重复的次数及每次停留扩散时间,由计算机根据渗碳要求,自动控制其次数及时间长短;The number of repetitions of step 9 and the time of each residence and diffusion are automatically controlled by the computer according to the carburizing requirements;

步骤11.降温Step 11. Cool down

当渗碳及扩散的阶段完成,开始进行降温;When the carburizing and diffusion stages are completed, the cooling begins;

步骤12.工件搬入Step 12. Workpiece loading

当温度降至淬火温度时,加热室前门打开,工件搬入淬火窒;When the temperature drops to the quenching temperature, the front door of the heating chamber is opened, and the workpiece is moved into the quenching chamber;

步骤13.规定压力Step 13. Specified pressure

工件送至淬火升降台,关上加热室前门,将氮气N2通过冲压管线注入加热室,直到规定压力;Send the workpiece to the quenching lifting table, close the front door of the heating chamber, and inject nitrogen N2 into the heating chamber through the stamping pipeline until the specified pressure;

步骤14.淬火行程Step 14. Quenching Stroke

淬火升降台浸入油槽内,进行淬火行程。The quenching lifting platform is immersed in the oil tank to perform the quenching stroke.

采用多参数输入计算机做为控制基础,使用两种以上的真空计,以真实反应炉内渗碳气体的化学变化。制程中,计算机根据已输入的各项参数,含有工件总表面积,层深要求,材料种类,最高设定温度等参数,并接受实时输入的温度值及两种以上的真空度值,立刻演算并作实时的动态控制,其控制机制,除了通过控制马达变频器来达成指挥真空泵系统的必要抽吸量外,并由上述的多种参数,控制渗碳材料的注入量,注入时间及行程,反复多次直到渗碳层深。The multi-parameter input computer is used as the control basis, and more than two vacuum gauges are used to truly react the chemical changes of the carburizing gas in the furnace. During the process, the computer calculates and calculates immediately based on the input parameters, including the total surface area of the workpiece, layer depth requirements, material type, maximum set temperature and other parameters, and accepts the real-time input temperature value and two or more vacuum degree values. For real-time dynamic control, the control mechanism, in addition to controlling the necessary suction volume of the vacuum pump system by controlling the motor frequency converter, controls the injection volume, injection time and stroke of the carburizing material by the above-mentioned various parameters, and repeats Multiple times until the carburized layer is deep.

所述的应用于低压渗碳热处理炉的动态控制系统的热处理制程方法的计算机及控制软件利用输入的参数进行动态全程控制,其计算机利用输入的参数决定以下控制条件:The computer and control software of the heat treatment process method applied to the dynamic control system of the low-pressure carburizing heat treatment furnace use the input parameters to perform dynamic full-range control, and the computer uses the input parameters to determine the following control conditions:

a)、渗碳的压力;a), carburizing pressure;

b)、渗碳与扩散的时间。b), carburization and diffusion time.

渗碳初期,表面立刻建立很高炭量,表面以下含碳很低,碳迅速扩散,第一次之后的扩散时间逐渐拉长,至于完成每一小段渗碳的时间,(为2秒-100秒)由PIRANI真空计显示器(V1)与薄膜式真空计显示器(V2)的差值,决定渗碳材料已完成渗碳作用。In the early stage of carburizing, a high amount of carbon is immediately established on the surface, and the carbon content below the surface is very low, and the carbon diffuses rapidly. The diffusion time after the first time gradually elongates. As for the time to complete each small section of carburizing, (2 seconds-100 seconds) The difference between the PIRANI vacuum gauge display (V1) and the film vacuum gauge display (V2) determines that the carburizing material has completed carburization.

本发明的有益效果是:可以节省渗碳材料量;增加炉装载量;增加渗碳之均匀性;减少真空系统之积碳;能以动态控制方式,自动产生复杂之制程;并可以完成计算机自动控制,免除人为操作可能的错误。The beneficial effects of the present invention are: it can save the amount of carburizing material; increase the loading capacity of the furnace; increase the uniformity of carburizing; reduce the carbon deposition in the vacuum system; Control to avoid possible errors of human operation.

附图说明Description of drawings

下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.

附图1是本发明的系统架构示意图;Accompanying drawing 1 is a schematic diagram of the system architecture of the present invention;

附图2是本发明的装置与真空泵、真空泵马达的变频控制器等相互串接的实施方式示意图;Accompanying drawing 2 is the schematic diagram of the implementation of the device of the present invention and the vacuum pump, the frequency conversion controller of the vacuum pump motor, etc. connected in series;

附图3是本发明实施例的第一次测试示意图;Accompanying drawing 3 is the first test schematic diagram of the embodiment of the present invention;

附图4是本发明实施例的第二次测试示意图;Accompanying drawing 4 is the second test schematic diagram of the embodiment of the present invention;

附图中标号说明:Explanation of the numbers in the accompanying drawings:

1-计算机及控制软件                 17-真空泵马达的变频控制器;1-Computer and control software 17-Variable frequency controller of vacuum pump motor;

2-可编程控制器;                   18-加热元件;2-programmable controller; 18-heating element;

3-PIRANI真空计显示器(V1);         19-渗剂控制阀;3-PIRANI vacuum gauge display (V1); 19-Infiltration agent control valve;

4-薄膜式真空计显示器(V2);         20-调压阀;4-film vacuum gauge display (V2); 20-pressure regulating valve;

5-可控硅整流器;                   21-渗剂储存钢瓶;5-silicon controlled rectifier; 21-infiltration agent storage cylinder;

6-电源供应器;                     22-PIRANI真空计;6-Power supply; 22-PIRANI vacuum gauge;

7-工件;                           23-薄膜式真空计;7-workpiece; 23-thin-film vacuum gauge;

8-主控炉温热电偶;                 24-加热室前门;8-The main control furnace temperature thermocouple; 24-The front door of the heating room;

9-过温控制热电偶;                 25-冲压管线;9-over-temperature control thermocouple; 25-stamping pipeline;

10-输入(D1);                      26-淬火室真空系统;10-input (D1); 26-quenching chamber vacuum system;

11-输出(D2);                      27-淬火室;11-Output (D2); 27-Quenching chamber;

13-加热室;                        28-淬火室前门;13-heating room; 28-quenching room front door;

14-真空阀;                        29-淬火升降台;14-vacuum valve; 29-quenching lifting platform;

15-真空泵;                        30-油槽搅拌;15-vacuum pump; 30-oil tank stirring;

16-真空泵马达;16 - Vacuum pump motor;

具体实施方式Detailed ways

请参阅附图1所示,本发明系统的装置主要由计算机及控制软件1、可编程控制器2、热电偶、真空计、电源6、工件7及淬火室27等组成,其可编程控制器2、计算机及控制软件1模块相互连接,可控硅整流器5的一端与可编程控制器2的输入端相连接,可编程控制器2与加热室13之间由主控炉温热电偶8及过温控制热电偶9相互连接,可编程控制器2的一输出端通过数位信号输出(D2)11线与加热室13的输入端相连接,加热室13的输出端通过数位信号输入(D1)10线与可编程控制器2的输入端相连接,PIRANI真空计显示器3的一端与加热室13相连接,其输出端与可编程控制器2的输入端相连接,薄膜式真空计显示器4的一端与加热室13相连接,其输出端与可编程控制器2的输入端相连接,加热室13内安置有热处理工件7,加热室13与淬火室27连为一体,但中间有门隔离。Please refer to shown in accompanying drawing 1, the device of the system of the present invention is mainly made up of computer and control software 1, programmable controller 2, thermocouple, vacuum gauge, power supply 6, workpiece 7 and quenching chamber 27 etc., and its programmable controller 2. The computer and control software 1 modules are connected to each other, one end of the silicon controlled rectifier 5 is connected to the input end of the programmable controller 2, and the main control furnace temperature thermocouple 8 is connected between the programmable controller 2 and the heating chamber 13 and the over-temperature control thermocouple 9 are connected to each other, an output end of the programmable controller 2 is connected with the input end of the heating chamber 13 through a digital signal output (D2) 11 line, and the output end of the heating chamber 13 is input through a digital signal (D1 ) 10 lines are connected with the input end of the programmable controller 2, one end of the PIRANI vacuum gauge display 3 is connected with the heating chamber 13, and its output end is connected with the input end of the programmable controller 2, and the thin-film vacuum gauge display 4 One end of the heating chamber is connected to the heating chamber 13, and its output end is connected to the input end of the programmable controller 2. The heat treatment workpiece 7 is placed in the heating chamber 13, and the heating chamber 13 and the quenching chamber 27 are connected as a whole, but there is a door in the middle to isolate them. .

所述的应用于低压渗碳热处理炉的动态控制系统的真空计至少有两种以上组成。The vacuum gauge used in the dynamic control system of the low-pressure carburizing heat treatment furnace has at least two or more components.

请参阅附图2、3、4所示,所述的应用于低压渗碳热处理炉的动态控制系统的加热室13的外部依次与真空计、真空阀14、真空泵15、真空泵马达16与真空泵马达的变频控制器17相互串接;渗剂储存钢瓶21依次与调压阀20、渗剂控制阀19及加热元件18相互串接,PIRANI真空计22与加热元件18相互连接,薄膜式真空计23与加热元件18相互连接,冲压管线(N2)25与淬火室27相互连接,淬火室真空系统与淬火室27相互连接,在淬火室27的一侧为淬火室前门28,淬火室27内壁一侧设有油槽搅拌30,其中间设有淬火升降台29。Please refer to accompanying drawing 2,3, shown in 4, the outside of described heating chamber 13 of the dynamic control system that is applied to low-pressure carburizing heat treatment furnace is successively connected with vacuum gauge, vacuum valve 14, vacuum pump 15, vacuum pump motor 16 and vacuum pump motor The frequency conversion controllers 17 are connected in series; the osmotic agent storage cylinder 21 is connected in series with the pressure regulating valve 20, the osmotic agent control valve 19 and the heating element 18 in sequence, the PIRANI vacuum gauge 22 is connected to the heating element 18, and the thin film vacuum gauge 23 It is connected with the heating element 18, the stamping pipeline (N2) 25 is connected with the quenching chamber 27, and the vacuum system of the quenching chamber is connected with the quenching chamber 27. On one side of the quenching chamber 27 is the front door 28 of the quenching chamber, and on the side of the inner wall of the quenching chamber 27 An oil tank stirring 30 is provided, and a quenching lifting platform 29 is arranged in the middle.

一种应用于低压渗碳热处理炉的动态控制系统的热处理制程方法的具体工作步骤是:The specific working steps of a heat treatment process method applied to a dynamic control system of a low-pressure carburizing heat treatment furnace are:

步骤1.工件7送入加热室13Step 1. The workpiece 7 is sent into the heating chamber 13

工件7备妥后,淬火室前门28及加热室前门24打开,直接送入加热室13;After the workpiece 7 is ready, the front door 28 of the quenching chamber and the front door 24 of the heating chamber are opened, and are directly sent into the heating chamber 13;

步骤2.抽真空Step 2. Vacuum

真空系统的真空阀14及淬火室真空系统26打开,开始抽真空,真空泵马达的变频器17设定在正常供电频率,例如:中国地区50HZ,美国为60HZ;The vacuum valve 14 of the vacuum system and the vacuum system 26 of the quenching chamber are opened to start vacuuming, and the frequency converter 17 of the vacuum pump motor is set at the normal power supply frequency, for example: 50HZ in China and 60HZ in the United States;

步骤3.加热运行Step 3. Heat Run

当真空度达1torr或小于1torr后,开始加热,并且真空泵15持续运行;When the vacuum reaches 1torr or less than 1torr, start heating, and the vacuum pump 15 continues to run;

步骤4.持续均热Step 4. Continue soaking

温度抵达渗碳温度后,持续运行均热程序直到工件温度均匀;After the temperature reaches the carburizing temperature, continue to run the soaking program until the workpiece temperature is uniform;

步骤5.变频器工作Step 5. Inverter working

进入渗碳制程后,根据制程,变频器将频率降至正常频率之60%-5%,真空泵15维持小抽吸量;After entering the carburizing process, according to the process, the frequency converter will reduce the frequency to 60%-5% of the normal frequency, and the vacuum pump 15 will maintain a small suction volume;

步骤6.注入渗碳材料Step 6. Inject carburizing material

渗碳剂控制阀19打开,开始注入一定量的渗碳材料;Carburizing agent control valve 19 is opened, begins to inject a certain amount of carburizing material;

步骤7.设定值Step 7. Set the value

当炉内压力至设定值时,利用变频器控制真空泵15的抽吸量,并将炉压维持在设定值;When the pressure in the furnace reaches the set value, use the frequency converter to control the suction volume of the vacuum pump 15, and maintain the furnace pressure at the set value;

步骤8.真空计显示器工作Step 8. Vacuum Gauge Display Working

当炉内气体进行渗碳反映时,PIRANI真空计显示器(V1)3及薄膜式真空计显示器(V2)4开始出现不同的读数,当PIRANI真空计显示器(V1)3/薄膜式真空计显示器(V2)4比值为一定时,变频器将频率调整为正常供电频率,以最快时间将真空度抽至最高;When the gas in the furnace is carburized, the PIRANI vacuum gauge display (V1) 3 and the thin-film vacuum gauge display (V2) 4 begin to show different readings. When the PIRANI vacuum gauge display (V1) 3/thin-film vacuum gauge display ( When the V2)4 ratio is constant, the inverter will adjust the frequency to the normal power supply frequency, and pump the vacuum to the highest in the fastest time;

步骤9.重复执行Step 9. Repeat execution

停留一段时间进行扩散后,重复步骤5、6、7、8的制程;After staying for a period of time for diffusion, repeat the process of steps 5, 6, 7, and 8;

步骤10.自动控制Step 10. Automatic Control

步骤9重复的次数及每次停留扩散时间,皆由计算机根据渗碳要求,自动控制其次数及时间长短;The number of repetitions of step 9 and the time of each residence and diffusion are automatically controlled by the computer according to the carburizing requirements;

步骤11.降温Step 11. Cool down

当渗碳及扩散的阶段完成,便开始进行降温;When the carburizing and diffusion stages are completed, the cooling begins;

步骤12.工件搬入Step 12. Workpiece loading

当温度降至淬火温度时,加热室13前门打开,工件7搬入淬火窒27;When the temperature dropped to the quenching temperature, the front door of the heating chamber 13 was opened, and the workpiece 7 was moved into the quenching block 27;

步骤13.规定压力Step 13. Specified pressure

工件7送至淬火升降台29,关上加热室前门24,注入冲压管线(N2)25,直到规定压力;The workpiece 7 is sent to the quenching lifting platform 29, the front door 24 of the heating chamber is closed, and the stamping pipeline (N2) 25 is injected until the specified pressure;

步骤14.淬火行程Step 14. Quenching Stroke

淬火升降台29浸入油槽内,进行淬火行程。The quenching lift table 29 is immersed in the oil tank to carry out the quenching stroke.

所述的应用于低压渗碳热处理炉的动态控制系统的热处理制程方法的计算机及控制软件利用输入的参数进行动态全程控制,在操作之前,预先输入以下的参数为:The computer and control software of the heat treatment process method applied to the dynamic control system of the low-pressure carburizing heat treatment furnace use the input parameters to perform dynamic full-range control. Before operation, the following parameters are pre-input:

a)、工件的材料;a), the material of the workpiece;

b)、工件之总表面积;b), the total surface area of the workpiece;

c)、渗碳层深度要求;c) Requirements for the depth of the carburized layer;

d)、表面含碳量要求;d), surface carbon content requirements;

e)、最高工作温度限制;e), the maximum working temperature limit;

f)、渗碳材料的种类;f), the type of carburizing material;

g)、电源的频率;g), the frequency of the power supply;

采用多参数输入计算机做为控制基础,使用两种以上的真空计,以真实反应炉内渗碳气体的化学变化。制程中,计算机根据已输入的各项参数,含有工件总表面积,层深要求,材料种类,最高设定温度等参数,并接受时时输入的温度值及两种以上的真空度值,立刻演算并作时时的动态控制,其控制机制,除了通过控制马达变频器来达成指挥真空泵15系统的必要抽吸量外,并由上述的多种参数,控制渗碳材料的注入量,注入时间及行程,反复多次直到渗碳层深。The multi-parameter input computer is used as the control basis, and more than two vacuum gauges are used to truly react the chemical changes of the carburizing gas in the furnace. During the manufacturing process, the computer calculates and calculates immediately based on the input parameters, including the total surface area of the workpiece, layer depth requirements, material type, maximum set temperature and other parameters, and accepts the input temperature value and more than two vacuum degree values. Dynamic control during operation, the control mechanism, in addition to controlling the motor inverter to achieve the necessary suction volume of the vacuum pump 15 system, and the above-mentioned various parameters to control the injection volume, injection time and stroke of the carburizing material, Repeat many times until the carburized layer is deep.

所述的应用于低压渗碳热处理炉的动态控制系统的热处理制程方法的计算机及控制软件利用输入的参数进行动态全程控制,其计算机利用输入的参数决定以下控制条件:The computer and control software of the heat treatment process method applied to the dynamic control system of the low-pressure carburizing heat treatment furnace use the input parameters to perform dynamic full-range control, and the computer uses the input parameters to determine the following control conditions:

a)、渗碳的压力;a), carburizing pressure;

b)、渗碳与扩散的时间。b), carburization and diffusion time.

渗碳初期,表面立刻建立很高炭量,表面以下含碳很低,碳迅速扩散,第一次之后的扩散时间逐渐拉长,至于完成每一段小渗碳的时间(为2秒-100秒),完全根据PIRANI真空计显示器(V1)3与薄膜式真空计显示器(V2)4的差值,即渗碳材料已完成渗碳作用,其有非常明显的优点如下:In the initial stage of carburizing, a high amount of carbon is immediately established on the surface, and the carbon content below the surface is very low, and the carbon diffuses rapidly. The diffusion time after the first time gradually elongates. As for the time to complete each small carburizing (2 seconds to 100 seconds ), completely according to the difference between the PIRANI vacuum gauge display (V1) 3 and the thin-film vacuum gauge display (V2) 4, that is, the carburizing material has completed carburizing, which has very obvious advantages as follows:

(1)、炉内工件所有面积,时时接受到同样的碳势,所以渗碳速度完全相同,深孔尤其明显;(1) All areas of the workpiece in the furnace receive the same carbon potential all the time, so the carburizing speed is exactly the same, especially for deep holes;

(2)、新鲜的渗碳材料在炉内完成反应后立刻排出,所以不致于在炉内形成积碳;(2) The fresh carburizing material is discharged immediately after the reaction in the furnace is completed, so it will not form carbon deposits in the furnace;

(3)、渗碳可计算机精确的控制,渗层可非长精确且均匀;(3) Carburizing can be precisely controlled by computer, and the carburizing layer can be long, accurate and uniform;

(4)、装载量可大幅提高;(4), the loading capacity can be greatly increased;

(5)、全自动控制,没有人为失误。(5) Fully automatic control without human error.

本发明的设备规格:Equipment specification of the present invention:

(1)、二室式油淬渗碳热处理炉;(1), two-chamber oil quenching carburizing heat treatment furnace;

(2)、加热室有效尺寸:1200MM×760MM×800MM;(2) The effective size of the heating chamber: 1200MM×760MM×800MM;

(3)、加热室容积:8.0立方米;(3), heating chamber volume: 8.0 cubic meters;

(4)、真空系统:机械真空泵300M3/HR,鲁氏真空泵2000M3/HR(4), vacuum system: mechanical vacuum pump 300M3/HR, Lushi vacuum pump 2000M3/HR

本发明的工件尺寸:The workpiece size of the present invention:

1.S15C钢板:52MM×52MM×3MM      80件1. S15C steel plate: 52MM×52MM×3MM 80 pieces

2.SCM 420钢棒:直径40MM×65MM    10件2. SCM 420 steel rod: diameter 40MM×65MM 10 pieces

本发明的第一次测试结果:有效渗碳层0.6~0.68mm,炉内情况良好,没有积碳。The first test result of the present invention: the effective carburized layer is 0.6~0.68mm, the condition in the furnace is good, and there is no carbon deposit.

本发明的第二次测试结果:有效渗碳层0.9~0.95mm,炉内情况良好,没有积碳。The second test result of the present invention: the effective carburized layer is 0.9-0.95mm, the condition in the furnace is good, and there is no carbon deposit.

本发明的真空计工作原理说明:The working principle of the vacuum gauge of the present invention is explained:

(1)、PIRANI GAUGE(1) PIRANI GAUGE

派拉尼真空计是采用气体冷却FILAMENT时,产生惠斯登电路不平衡,而测出气体之多少,即真空度之数值。因气体之重量及冷却率不同,所以必须以已知的一种气体,预设真空表的参数,以计算真空度。When the Pirani vacuum gauge is used to cool the FILAMENT with gas, the Wheatstone circuit is unbalanced, and the amount of gas measured is the value of the vacuum degree. Because the weight and cooling rate of the gas are different, a known gas must be used to preset the parameters of the vacuum gauge to calculate the vacuum degree.

(2)薄膜式真空计(2) Thin film vacuum gauge

薄膜式真空计是利用气体分子碰撞运动,产生的压力,其行为近于理想气体状态,其压力与气体摩耳数有关,与气体种类无关。The thin-film vacuum gauge uses the collision motion of gas molecules to generate pressure, and its behavior is close to the ideal gas state. The pressure is related to the number of moles of gas, and has nothing to do with the type of gas.

PV=NRTPV=NRT

P:气体压力P: gas pressure

V:炉体容积V: Furnace volume

N:气体摩耳数N: number of moles of gas

R:常数R: constant

T:温度T: temperature

本发明真空计的特点说明:The feature description of the vacuum gauge of the present invention:

(1)、气氛的均匀性(1), the uniformity of the atmosphere

当渗碳开始时,真空泵15抽量降至很小,所以渗碳材料可迅速的建立均匀的渗碳气氛,由于抽吸量很小所以炉内不会因大力抽吸,产生绕动而不均匀,并且因为间断性定量注入,所以渗碳材料可以大幅降低。另外,抽气的时机,完全是根据炉内气体反应状况,所以是在可控的状态下进行真空渗碳。When the carburizing starts, the pumping capacity of the vacuum pump 15 is reduced to a very small level, so the carburizing material can quickly establish a uniform carburizing atmosphere. Because the pumping capacity is very small, the furnace will not revolve around due to strong suction. Uniform, and because of the intermittent quantitative injection, the carburizing material can be greatly reduced. In addition, the timing of pumping air is completely based on the gas reaction conditions in the furnace, so vacuum carburizing is carried out under a controllable state.

所以它的优点非常明显为:So its advantages are very obvious:

1)、炉内气氛更均匀,渗碳均匀度可大幅提升;1) The atmosphere in the furnace is more uniform, and the carburizing uniformity can be greatly improved;

2)、可增加工件装载量;2), can increase the workpiece loading capacity;

3)、在可控的状态下,渗层深度可以完全掌握;3) In a controllable state, the depth of the seepage layer can be fully grasped;

4)、大量减少渗碳材料耗量,并大幅减少炉内及真空系统的积碳及污染;4), greatly reduce the consumption of carburizing materials, and greatly reduce the carbon deposition and pollution in the furnace and vacuum system;

(2)、计算机产生制造工艺,并且动态全程控制(2), the computer generates the manufacturing process, and the dynamic whole process control

操作之前,工程师已预先输入以下的参数Before operation, the engineer has pre-entered the following parameters

1)、工件之材料;1), the material of the workpiece;

2)、工件之总面积;2), the total area of the workpiece;

3)、渗碳层深要求;3) Requirements for carburizing layer depth;

4)、表面含碳要求;4), surface carbon requirements;

5)、最高工作温度限制;5), the maximum working temperature limit;

6)、渗碳材料之种类;6), the type of carburizing material;

7)、电源之频率;7), the frequency of the power supply;

根据以上的参数,计算机自动产生一个合适的工艺,在实际制程中,计算机根据时时输入的数据,对制程做修正或补偿,所以生产可以完全自动化,而且生产品质可以达到最佳。According to the above parameters, the computer automatically generates a suitable process. In the actual process, the computer corrects or compensates the process according to the data input from time to time, so the production can be fully automated and the production quality can reach the best.

Claims (4)

1、一种应用于低压渗碳热处理炉的动态控制装置,该装置有计算机及控制软件(1)、可编程控制器(2)、热电偶、真空计、电源(6)、工件(7)及淬火室(27),其特征在于:可编程控制器(2)、计算机及控制软件(1)模块相互连接,可控硅整流器(5)的一端与可编程控制器(2)的输入端相连接,可控硅整流器(5)的另一端与电源(6)的一端相连接,电源(6)的另一端与加热室(13)的输入端相连接,可编程控制器(2)与加热室(13)之间由主控炉温热电偶(8)及过温控制热电偶(9)相互连接,可编程控制器(2)的一输出端通过数位信号输出(11)线与加热室(13)的输入端相连接,可编程控制器(2)的一输出端通过数位信号输入(10)线与加热室(13)的输出端相连接,PIRANI真空计显示器(3)的一端通过真空计与加热室(13)相连接,其输出端与可编程控制器(2)的输入端相连接,薄膜式真空计显示器(4)的一端通过真空计与加热室(13)相连接,其输出端与可编程控制器(2)的输入端相连接,加热室(13)内安置有热处理工件(7),加热室(13)与淬火室(27)连为一体,中间有门隔离,其中:1. A dynamic control device applied to a low-pressure carburizing heat treatment furnace. The device has a computer and control software (1), a programmable controller (2), a thermocouple, a vacuum gauge, a power supply (6), and a workpiece (7) And quenching chamber (27), it is characterized in that: programmable controller (2), computer and control software (1) module are interconnected, one end of silicon controlled rectifier (5) and the input end of programmable controller (2) The other end of the silicon controlled rectifier (5) is connected with one end of the power supply (6), the other end of the power supply (6) is connected with the input end of the heating chamber (13), and the programmable controller (2) and The heating chamber (13) is connected to each other by the main control furnace temperature thermocouple (8) and the over-temperature control thermocouple (9), and an output terminal of the programmable controller (2) is connected with the digital signal output (11) line The input end of heating chamber (13) is connected, and an output end of programmable controller (2) is connected with the output end of heating chamber (13) by digital signal input (10) line, the PIRANI vacuum gauge display (3) One end is connected to the heating chamber (13) through a vacuum gauge, its output end is connected to the input end of the programmable controller (2), and one end of the thin-film vacuum gauge display (4) is connected to the heating chamber (13) through a vacuum gauge. connection, its output end is connected with the input end of the programmable controller (2), the heat treatment workpiece (7) is placed in the heating chamber (13), the heating chamber (13) is connected with the quenching chamber (27) as a whole, and there is door isolation, where: 加热室的外部依次与真空阀(14)、真空泵(15)、真空泵马达(16)与真空泵马达的变频控制器(17)相互串接,PIRANI真空计(22)与加热元件(18)相互连接,薄膜式真空计(23)与加热元件(18)相互连接。The outside of the heating chamber is connected in series with the vacuum valve (14), the vacuum pump (15), the vacuum pump motor (16) and the frequency conversion controller (17) of the vacuum pump motor, and the PIRANI vacuum gauge (22) is connected to the heating element (18) , the thin-film vacuum gauge (23) is connected to the heating element (18). 2、根据权利要求1所述的应用于低压渗碳热处理炉的动态控制装置,其特征在于:所述的真空计至少有两种以上组成。2. The dynamic control device applied to a low-pressure carburizing heat treatment furnace according to claim 1, characterized in that the vacuum gauge has at least two or more components. 3、一种应用于低压渗碳热处理炉的动态控制系统的热处理方法,该方法通过多参数输入计算机为控制基础,用两种以上的真空计反应炉内渗碳气体的化学变化,通过控制马达变频器来达成指挥真空泵系统的必要抽吸量,拉地完成计算机及控制软件模快的工作,其中:3. A heat treatment method applied to the dynamic control system of a low-pressure carburizing heat treatment furnace. The method uses multi-parameter input to the computer as the control basis, uses more than two vacuum gauges to react the chemical changes of the carburizing gas in the furnace, and controls the motor The frequency converter is used to achieve the necessary suction volume to command the vacuum pump system, and to complete the fast work of the computer and control software, among which: 输入计算机的参数包括两种方式:渗碳过程中实时测得的参数以及在操作之前预先输入的参数,包括:a)、工件的材料;b)、工件之总表面积;c)、渗碳层深度要求;d)、表面含碳量要求;e)、最高工作温度限制;f)、渗碳材料的种类;g)、电源的频率,其特征在于:该方法具体工作步骤是:The parameters input into the computer include two ways: the parameters measured in real time during the carburizing process and the parameters input before operation, including: a), the material of the workpiece; b), the total surface area of the workpiece; c), the carburized layer Depth requirement; d), surface carbon content requirement; e), maximum operating temperature limit; f), type of carburizing material; g), frequency of power supply, it is characterized in that: the specific working steps of this method are: 步骤1.工件送入加热室Step 1. The workpiece is sent into the heating chamber 工件备妥后,淬火室前门及加热室前门打开,直接送入加热室;After the workpiece is ready, the front door of the quenching chamber and the front door of the heating chamber are opened, and it is directly sent into the heating chamber; 步骤2.抽真空Step 2. Vacuum 真空系统的真空阀及淬火室真空系统打开,开始抽真空,真空泵马达变频器设定在正常供电频率;The vacuum valve of the vacuum system and the vacuum system of the quenching chamber are opened to start vacuuming, and the frequency converter of the vacuum pump motor is set at the normal power supply frequency; 步骤3.加热运行Step 3. Heat Run 当真空度达1torr或小于1torr后,开始加热,并且真空泵持续运行;When the vacuum reaches 1torr or less than 1torr, start heating, and the vacuum pump continues to run; 步骤4.持续均热Step 4. Continue soaking 温度抵达渗碳温度后,持续运行均热程序直到工件温度均匀;After the temperature reaches the carburizing temperature, continue to run the soaking program until the workpiece temperature is uniform; 步骤5.变频器工作Step 5. Inverter working 进入渗碳制程后,根据制程,变频器将频率降至正常频率之60%-5%,真空泵维持小抽吸量;After entering the carburizing process, according to the process, the frequency converter will reduce the frequency to 60%-5% of the normal frequency, and the vacuum pump will maintain a small suction volume; 步骤6.注入渗碳材料Step 6. Inject carburizing material 渗碳剂控制阀打开,开始注入一定量的渗碳材料;The carburizing agent control valve is opened and a certain amount of carburizing material is injected; 步骤7.设定值Step 7. Set the value 当炉内压力至设定值时,利用变频器控制真空泵的抽吸量,并将炉压维持在设定值;When the pressure in the furnace reaches the set value, use the frequency converter to control the suction volume of the vacuum pump and maintain the furnace pressure at the set value; 步骤8.真空计显示器工作Step 8. Vacuum Gauge Display Working 当炉内气体进行渗碳反映时,PIRANI真空计显示器V1及薄膜式真空计显示器V2开始出现不同的读数,当PIRANI真空计显示器V1/薄膜式真空计显示器V2比值为一定时,变频器将频率调整为正常供电频率,抽真空;When the gas in the furnace undergoes carburizing reaction, PIRANI vacuum gauge display V1 and film vacuum gauge display V2 begin to show different readings. When the ratio of PIRANI vacuum gauge display V1/film vacuum gauge display V2 is constant, the frequency converter will Adjust to normal power supply frequency, vacuumize; 步骤9.重复执行Step 9. Repeat execution 停留一段时间进行扩散后,重复步骤5、6、7、8的制程;After staying for a period of time for diffusion, repeat the process of steps 5, 6, 7, and 8; 步骤10.自动控制Step 10. Automatic Control 步骤9重复的次数及每次停留扩散时间,由计算机根据渗碳要求,自动控制其次数及时间长短;The number of repetitions of step 9 and the time of each residence and diffusion are automatically controlled by the computer according to the carburizing requirements; 步骤11.降温Step 11. Cool down 当渗碳及扩散的阶段完成,开始进行降温;When the carburizing and diffusion stages are completed, the cooling begins; 步骤12.工件搬入Step 12. Workpiece loading 当温度降至淬火温度时,加热室前门打开,工件搬入淬火窒;When the temperature drops to the quenching temperature, the front door of the heating chamber is opened, and the workpiece is moved into the quenching chamber; 步骤13.规定压力Step 13. Specified pressure 工件送至淬火升降台,关上加热室前门,将氮气N2通过冲压管线注入加热室,直到规定压力;Send the workpiece to the quenching lifting table, close the front door of the heating chamber, and inject nitrogen N2 into the heating chamber through the stamping pipeline until the specified pressure; 步骤14.淬火行程Step 14. Quenching Stroke 淬火升降台浸入油槽内,进行淬火行程。The quenching lifting platform is immersed in the oil tank to perform the quenching stroke. 4、根据权利要求3所述的应用于低压渗碳热处理炉的动态控制系统的热处理制程方法,其特征在于:所述的计算机及控制软件利用输入的参数进行动态全程控制,其计算机利用输入的参数决定以下控制条件:4. The heat treatment process method applied to the dynamic control system of a low-pressure carburizing heat treatment furnace according to claim 3, characterized in that: the computer and control software use the input parameters to perform dynamic full-range control, and the computer uses the input parameters The parameters determine the following control conditions: a)、渗碳的压力;a), carburizing pressure; b)、渗碳与扩散的时间。b), carburization and diffusion time.
CNB2004100163700A 2004-02-17 2004-02-17 Dynamic control system for low-pressure carburating heat treament furnace Expired - Fee Related CN1302146C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2004100163700A CN1302146C (en) 2004-02-17 2004-02-17 Dynamic control system for low-pressure carburating heat treament furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2004100163700A CN1302146C (en) 2004-02-17 2004-02-17 Dynamic control system for low-pressure carburating heat treament furnace

Publications (2)

Publication Number Publication Date
CN1560317A CN1560317A (en) 2005-01-05
CN1302146C true CN1302146C (en) 2007-02-28

Family

ID=34440450

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2004100163700A Expired - Fee Related CN1302146C (en) 2004-02-17 2004-02-17 Dynamic control system for low-pressure carburating heat treament furnace

Country Status (1)

Country Link
CN (1) CN1302146C (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4929657B2 (en) 2005-09-21 2012-05-09 株式会社Ihi Carburizing treatment apparatus and method
CN102063110B (en) * 2010-12-03 2012-07-18 上海交通大学 Control system of carbon intensity distribution of low-pressure carburized layer and control method thereof
CN103186151B (en) * 2011-12-31 2015-05-20 江苏丰东热技术股份有限公司 Heating furnace control system
CN106319435A (en) * 2015-07-07 2017-01-11 财团法人金属工业研究发展中心 Control method of carburizing heat treatment
CN106200543A (en) * 2016-08-17 2016-12-07 江苏丰东热技术股份有限公司 A kind of carbon-potential control method of gas carburizing heating furnace
CN110923676B (en) * 2019-11-19 2021-12-24 有研国晶辉新材料有限公司 Annealing equipment and process for multispectral zinc sulfide window
CN111536803B (en) * 2020-05-08 2022-04-01 北京汇磁粉体材料有限公司 Precise vacuum atmosphere heat treatment furnace with precise control
CN113755790B (en) * 2021-10-11 2024-03-22 江苏丰东热技术有限公司 Composite carburizing process and equipment

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1184510A (en) * 1995-03-29 1998-06-10 株式会社日本H Vacuum carburizing method, equipment and carburized products
WO2003048405A1 (en) * 2001-11-30 2003-06-12 Koyo Thermo Systems Co., Ltd. Method and apparatus for vacuum heat treatment

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1184510A (en) * 1995-03-29 1998-06-10 株式会社日本H Vacuum carburizing method, equipment and carburized products
WO2003048405A1 (en) * 2001-11-30 2003-06-12 Koyo Thermo Systems Co., Ltd. Method and apparatus for vacuum heat treatment

Also Published As

Publication number Publication date
CN1560317A (en) 2005-01-05

Similar Documents

Publication Publication Date Title
CN1302146C (en) Dynamic control system for low-pressure carburating heat treament furnace
CN1180119C (en) Cementation process and apparatus
CN1235665C (en) Method for Separating Oxygen by Composite Ceramic Membrane
CN1256755C (en) Substrate processing device and processing method
CN1908563A (en) Reduced-pressure drying apparatus
CN100350142C (en) Air-fuel ratio control apparatus for an internal combustion engine
CN1883074A (en) Fuel cell producing method and apparatus
CN101079199A (en) Gas turbine output learning circuit and combustion control device for gas turbine
CN101032008A (en) Semiconductor manufacturing device, flow correction method and program for semiconductor manufacturing device
CN1549871A (en) Vacuum heat treatment method and device
CN1739072A (en) Flow control method for clustering fluid and flow control device for clustering fluid
CN1834408A (en) Turbine starting controller and turbine starting control method
CN1701878A (en) Die-casting device and vacuum process
CN85109012A (en) Mainly be used as preparation method who stops the grafted ethylene copolymer of the additive of precipitation of paraffin in the crude oil and the composition that contains said crude oil and additive
CN1035528A (en) Carbon steel wire is heat-treated to the method and apparatus of high-quality pearlitic structure
CN1826492A (en) gas supply device
CN1209410C (en) Crosslinkable elastomer composition
CN1108541C (en) Corrosion inhibitor stripping liquid control device
CN1873914A (en) Substrate processing method, substrate processing program and storage medium
CN1270358C (en) Oxide film forming method
CN1444546A (en) Glass base material manufacturing device and glass base material manufacturing method
CN101050054A (en) Vacuum deshydroxy method for quartz glass cell
CN1934679A (en) Method and apparatus for forming silicon dots
CN1468821A (en) Flame polishing apparatus and method for glass container
CN1054778A (en) Novel type fluorubber based on vinylidene fluoride, R 1216 and tetrafluoroethylene

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070228

Termination date: 20110217