WO2015003654A1 - Prebake process and system for water-based painting without a middle coat - Google Patents

Prebake process and system for water-based painting without a middle coat Download PDF

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Publication number
WO2015003654A1
WO2015003654A1 PCT/CN2014/082056 CN2014082056W WO2015003654A1 WO 2015003654 A1 WO2015003654 A1 WO 2015003654A1 CN 2014082056 W CN2014082056 W CN 2014082056W WO 2015003654 A1 WO2015003654 A1 WO 2015003654A1
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Prior art keywords
heating
section
air
temperature
heating section
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PCT/CN2014/082056
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French (fr)
Chinese (zh)
Inventor
李晓琳
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安徽江淮汽车股份有限公司
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Priority claimed from CN201320416267.XU external-priority patent/CN203494747U/en
Priority claimed from CN201310294683.1A external-priority patent/CN103331244B/en
Application filed by 安徽江淮汽车股份有限公司 filed Critical 安徽江淮汽车股份有限公司
Priority to BR112016001095A priority Critical patent/BR112016001095A2/en
Publication of WO2015003654A1 publication Critical patent/WO2015003654A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
    • B05D3/02Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by baking
    • B05D3/0218Pretreatment, e.g. heating the substrate
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D3/00Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
    • B05D3/04Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by exposure to gases
    • B05D3/0406Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by exposure to gases the gas being air
    • B05D3/0413Heating with air

Definitions

  • the invention relates to the field of automobile painting, and particularly relates to a pre-baking process and a pre-drying system in an aqueous medium-free coating process. Background technique
  • 3C2B 3C stands for three coats, which are middle coat, top coat and cover light
  • 2B stands for two drying processes, namely, medium coat drying and top coat drying. Dry, including pre-drying of the intermediate coating and pre-drying of the topcoat.
  • 3C2B production process has a very mature experience, but its disadvantage is that the coating line is long and achieves maximum process reliability and meets all quality requirements at the expense of high cost.
  • the pre-drying process generally uses a two-stage heating and drying method, the heating temperature is controlled at 60 ⁇ 5 °C, and the tuyere wind speed is controlled at 6-10 m/s, heating time. It is l-2min; the heating temperature is controlled at 80 ⁇ 5 degrees Celsius, the tuyere wind speed is not less than 10m/s, and the heating time is 2.5-3min.
  • the ratio of the heating period to the heating of the second stage is generally controlled at about 1:2, which means that the heating from the heating stage to the heating of the second stage requires rapid temperature rise.
  • the object of the present invention is to overcome the above disadvantages, and to provide a pre-baking process which is advantageous for improving the pre-bake quality and the drying effect in the water-free intermediate coating, and provides a pre-drying process for realizing the pre-drying process.
  • a simple pre-drying system is to overcome the above disadvantages, and to provide a pre-baking process which is advantageous for improving the pre-bake quality and the drying effect in the water-free intermediate coating, and provides a pre-drying process for realizing the pre-drying process.
  • the present invention provides the following technical solutions:
  • An aqueous free intermediate coating pre-drying process comprising the following steps:
  • the gas seal is performed before heating for a period of time, and the gas seal temperature is 60-80 ° C;
  • Heating for a period the temperature is 70-80 ° C, the wind speed is 3-5 m / s, the heating time is 3-4 min; the heating is two, the temperature is 90-100 ° C, the wind speed is 10-14 m / s, the heating time is 3 -4min; after two stages of heating, the gas seal is performed at a gas seal temperature of 80-100 °C;
  • the heating section and the heating section ensure an absolute humidity of 10-15 g/kg.
  • the strong cold section has a temperature of 20 ° C and a wind speed of 16-20 m / s.
  • the heating is at a temperature of 75 ° C and the heating at a temperature of 90 ° C.
  • An aqueous medium-free coating pre-drying system comprising: a pre-drying chamber; a conveying system for conveying the workpiece to the pre-drying chamber; a heating system for supplying air to the pre-drying chamber; In the direction, the pre-drying chamber is arranged with an inlet air curtain, a heating section, a heating section, an outlet air curtain, and a strong cooling chamber, wherein the length of the heating section and the length of the heating section satisfy the following mathematical expression:
  • the ratio of the length of the heating section to the length of the heating section is 1:1.
  • the length of the heating section and the length of the heating section should also satisfy the following mathematical expression:
  • the heating system comprises a heating box for providing a circulating wind for the heating section and the inlet air curtain, a two-stage heating box for providing a circulating wind for the heating two sections and the outlet air curtain, and A cold air box that provides a cold air in a strong cold room.
  • the one-stage heating box comprises a fresh air valve, a filter, a surface cooler, a burner and a circulation fan, the wind passing through the fresh air valve, the filter, the air cooler, the burner and the After the circulation fan enters the heating section and the inlet air curtain;
  • the two-stage heating tank includes a circulation fan, a filter and a burner, and the wind from the heating section passes through the filter, the burner and The circulating fan enters the heating second section and the outlet air curtain;
  • the cold air box comprises a blower, an exhaust fan, a filter and a surface cooler, and the wind passes through the filter, the inlet fan, the strong The cold chamber and the exhaust fan realize air exchange with the outdoor.
  • a vehicle body manufactured by the above-described process and a vehicle using the vehicle body are provided.
  • a better pre-baking effect is obtained by controlling the temperature, time, and wind speed, and the appearance quality of the paint film on the surface of the workpiece is better.
  • heating time ratio of the heating section to the heating section is set to 1 : 1, which is advantageous for the sufficient evaporation of water and the gentle rise of the heating rate.
  • the heating temperature is 75 ° C, and the heating temperature is 90 ° C, which is higher than the set temperature of the conventional heating section and the heating section, but the temperature difference is small, and the heating temperature is close to the gas sealing temperature before the heating, heating The temperature of the second stage is close to the air sealing temperature thereafter, so that the higher the drying speed is ensured, the temperature rise is more stable, and defects such as pinholes are reduced.
  • the pre-drying system of the invention has a simple structure and can meet the above process requirements.
  • Figure 1 is a schematic view of the water-free intermediate coating pre-drying system of the present invention
  • Figure 2 is a graph showing the body temperature during the passage of the body through the pre-drying system of Figure 1.
  • the mark in the above figure shows: pre-drying chamber 1, heating system 2, one-stage heating box 21, two-stage heating box 22, and cold air box 23.
  • Table 1 shows the process and process requirements for using a conventional pre-baking process in a conventional aqueous coating process. It can be seen from Table 1 that the heating period is shorter than the heating period, generally the ratio of the heating period to the heating period is 1:2, and the heating time in the heating section and the heating section is generally not More than 4min. This results in a shorter heating time during heating and a shorter overall heating time, and the degree of moisture elimination in the paint film is not satisfactory because of the thick wet film thickness in the water-free intermediate coating.
  • the temperature difference between the heating section and the heating section is relatively large (generally, the temperature is set to 60 ° C in the heating section, and the temperature is set to 80 ° C in the heating section, and the temperature difference between the two sections generally reaches 20 °C), that is to say, the temperature rises from heating to the second stage of heating, and the speed is increased rapidly, so that defects such as pinholes are easily caused. Heating a higher wind speed is also not conducive to ensuring the quality of the paint film containing more moisture.
  • Table 2 shows the pre-drying process in accordance with the present invention.
  • the air seal is used for air sealing before heating for a period of time to ensure stable operation of the heating section.
  • the gas seal temperature is set to 60-80 ° C, and the workpiece entering the heating section is preheated.
  • the workpiece enters a heating process, setting the heating temperature to 70-80 ° C, the wind speed to 3-5 m / s, and the heating time to 3-4 min. Comparing with Table 1, it can be seen that the heating time of the heating section becomes longer, so that most of the moisture on the surface of the workpiece can be taken away during the heating period, and the wind speed of the tuyere is lowered, and the surface quality of the paint film is better.
  • the heating temperature is 90-100 ° C
  • the wind speed is 10-14 m / s
  • the heating time is 3-4 min.
  • the heating time of the heating section is also After being extended, the paint film is further dried. Although increasing the wind speed relative to heating is beneficial to increase the drying speed of the paint film, the wind speed should not be too large, otherwise the film quality will still be affected. Select 10-14m/s. It is suitable.
  • the air seal is used for air sealing, and the gas sealing temperature is 80-100 ° C, which is close to the temperature of the second heating stage.
  • the heating time becomes longer in the whole process, preferably at least 6.5min, and the temperature change is relatively gentle, by the temperature, the heating time and
  • the comprehensive control of the wind speed achieves better film quality and thus the appearance quality of the workpiece is better.
  • the heating time ratio of the heating section to the heating section is 1:1, and the requirement of the dry moisture requirement can be met.
  • the shortest time is now, and labor productivity is high.
  • the heating temperature is 75 ° C
  • the heating temperature is 90 ° C
  • the temperature is higher than the traditional process, the temperature difference is small, the drying water efficiency is high, and the temperature difference is gentle.
  • the workpiece After leaving the gas seal, the workpiece enters the strong cold section and reduces the surface temperature of the workpiece to 35 °C in preparation for the next step of the water-free intermediate coating process.
  • the strong cold section is carried out at a temperature of 20 ° C and a wind speed of 16-20 m/s. During the above treatment, heating one section and the heating section need to ensure an absolute humidity of 10-15 g/kg.
  • Comparative data on the appearance quality of the workpiece obtained by pre-baking are respectively performed using the parameters in Table 1 and Table 2, and other parameters are the same. It can be seen from Table 3 that the surface quality obtained by the pre-baking process according to the present invention is superior to the conventional one for the three different color paints in terms of length, short wave, gloss and vividness of the horizontal and vertical planes.
  • the pre-baking process, especially for white, does not meet the requirements in terms of vividness, and the pre-baking process of the present invention can meet the requirements.
  • heating one section and heating two sections means a time step, but in the following description, heating one section and heating two sections means the space physics of the pre-drying chamber. component.
  • an embodiment of the present invention provides an aqueous medium-free coating pre-drying system, comprising: pre-baking A dry chamber 1, a heating system 2, and a delivery system (not shown) that transports the workpiece to the pre-drying chamber.
  • the heating system 2 supplies air to the pre-drying chamber 1 to achieve the process requirements of the present invention in each section of the pre-drying chamber.
  • the pre-drying chamber 1 After the workpiece is carried by the conveying system, after the previous process of pre-drying is completed, the pre-drying chamber 1 enters and moves therein in the advancing direction of the workpiece indicated by the arrow in the figure. In the advancing direction of the workpiece, the pre-drying chamber 1 is sequentially arranged with an inlet air curtain, a heating section, a heating section, an outlet air curtain and a strong cooling chamber, and in order to satisfy the heating time of the process of the invention, heating a section and the heating
  • the length of the second segment should satisfy the following mathematical expression:
  • the time elapsed during the heating of one section and heating of the second section is 1:1, since the workpiece is advanced at the conveying system, it means that the time during which the workpiece is heated in the heating section and the heating section is also 1:1.
  • the length of the heating section and the length of the heating section should also satisfy the following equation:
  • the heating system 2 includes a section of heating tanks 21 for providing a circulating air for heating a section and an inlet air curtain, a two-stage heating tank 22 for providing circulating air for heating the two sections and the outlet air curtain, and a cold bellows 23 for supplying cold air to the forced cooling chamber.
  • a section of the heating box 21 heats the external fresh air and sends it to the inlet air curtain to provide a gas seal, and feeds the heating section to make the temperature of the air in the heating section reach the process requirement.
  • the two-stage heating box 22 further heats and heats the air in the second stage of heating to reach the requirements of the heating two-stage process, and provides a gas seal to the outlet air curtain.
  • the cold bellows 23 completes the heat exchange between the refrigerating chamber and the outside, thereby cooling the workpiece in the refrigerating chamber.
  • the fresh air from the outside passes through the fresh air valve, filter, air cooler and burner in the heating chamber 21 to reach the required temperature, and then enters the heating section and the inlet air curtain through the circulation fan.
  • the temperature from the heated section passes through the filter and burner in the two-stage heating tank 22, and the temperature is further increased, and the circulating fan enters the heating second section and the outlet air curtain.
  • the outdoor wind passes through the filter in the cold air box 23, enters the strong cold chamber through the inlet fan, and the air in the strong cold chamber exchanges heat with the workpiece, and then exchanges air with the outdoor through the exhaust fan.
  • the heating system 1 can also utilize other heating and cooling systems such as central air conditioning. After the workpiece leaves the forced cooling chamber, enter the transition section to prepare for the next process.
  • FIG. 2 is a view showing the temperature probe detection at different positions of the vehicle body in the process of the pre-drying system in the pre-drying room in the process of the pre-drying system of the embodiment of the present invention.
  • the appearance quality of the body paint film obtained in the process is given in Table 3 and will not be described here.
  • the appearance quality of the car body is improved, and accordingly, the overall appearance quality of the car will be significantly improved.

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  • Coating Apparatus (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

Provided is a prebake process for water-based painting without a middle coat, comprising the following steps: before a first heating stage, gas sealing at a temperature of 60-80°C; first heating stage at temperature of 70-80°C, wind velocity of 3-5 m/s, and heating time of 3-4 minutes; second heating stage at temperature of 90-100°C, wind velocity of 10-14 m/s, and heating time of 3-4 minutes; after second heating stage, gas sealing at a temperature of 80-100°C; a forced cooling stage in which workpiece surface temperature is reduced to ≤35°C; the first and second heating stages ensure an absolute humidity of 10-15 g/kg. Also provided are a prebake system for implementing the described process, a vehicle body manufactured using the process, and an automobile having the vehicle body. The process significantly improves the appearance of a workpiece after water-based painting without a middle coat.

Description

水性免中涂涂装预烘干工艺及系统  Water-based free intermediate coating pre-drying process and system
技术领域  Technical field
本发明涉及汽车涂装领域, 具体涉及一种在水性免中涂涂装工艺中的 预烘干工艺及预烘干系统 。 背景技术  The invention relates to the field of automobile painting, and particularly relates to a pre-baking process and a pre-drying system in an aqueous medium-free coating process. Background technique
由于国家对环保要求不断提高, 越来越多的汽车制造商选择使用水性 漆涂装。 目前应用较多的水性漆工艺是传统的 3C2B工艺, 其中 3C代表三 涂层, 分别是中涂、 面漆和罩光, 2B代表两道烘干工序, 分别是中涂烘干 和面漆烘干, 其中含中涂预烘干和面漆预烘干。 3C2B生产工艺具有很成熟 的使用经验, 但它的缺点是, 涂装生产线长, 是以高成本为代价来实现最 大的工艺可靠性和满足所有的质量要求。  As the country's environmental requirements continue to increase, more and more car manufacturers choose to use water-based paint. At present, the water-based paint process with many applications is the traditional 3C2B process, in which 3C stands for three coats, which are middle coat, top coat and cover light, and 2B stands for two drying processes, namely, medium coat drying and top coat drying. Dry, including pre-drying of the intermediate coating and pre-drying of the topcoat. The 3C2B production process has a very mature experience, but its disadvantage is that the coating line is long and achieves maximum process reliability and meets all quality requirements at the expense of high cost.
在 2011年第十四卷第七期的 《现代涂料与涂装》 , 作者为邢文平、 葛 菲、 皮沁, 名称为 "汽车涂装水性免中涂工艺的应用探讨" 的文章中, 介 绍了水性 B 1B2工艺流程, 其中公开了预烘干条件为 60至 80°C, 时间为 3-5min, 并对 B 1B2工艺进行了验证,其中并未涉及预烘干条件对于涂装效 果的影响。 在 2012年第 6期的 《电镀与涂饰》 第 31卷, 作者为邢汶平、 葛菲、 邱昌盛, 名称为 "水性免中涂涂装工艺研究" 的文章中, 对水性免 中涂涂装工艺, 以 B 1B2 工艺为例进行了技术效果、 影响因素、 存在问题 的介绍。 但该文在探讨中间闪干流平时间的影响时, 在预烘干过程中选择 了 4.5min和 7min两个时长进行试险, 给出了不同的闪干流平时间对颜色 和鲜映性基本无影响的结论, 而并未深入探讨预烘干温度、 时间等综合因 素对工件外观质量的影响。 在实际的水性免中涂涂装工艺中, 预烘干工艺 一般釆用两段式加热烘干方式, 加热一段温度控制在 60 ± 5 °C, 风口风速 控制在 6-10m/s, 加热时间为 l-2min; 加热二段温度控制在 80 ± 5摄氏度, 风口风速不小于 10m/s, 加热时间为 2.5-3min。 在实际生产中, 一般加热一 段与加热二段的时间比控制在 1 :2 左右, 这就意味着从加热一段到加热二 段需要快速升温。 但实际上, 釆用水性免中涂涂装工艺后, 在预烘干前的 湿膜膜厚较大, 基本会增加一倍以上, 快速升温会导致针孔等质量缺陷, 而且传统的水性预烘干系统的预烘干时间总和大约为 3-4min, 烘干时间过 短, 效果不佳, 不利于预烘干后下一阶段的工件处理。 依据上述条件进行 的预烘干工艺, 某些外观质量参数甚至不能达到标准要求。 发明内容 In the "Modern Coatings and Coatings" of the 14th issue of the 14th volume of 2011, the authors are Xing Wenping, Ge Fei, Pi Wei, the article entitled "Application of water-based coating process for automotive coating", introduced The aqueous B 1B2 process flow, in which the pre-baking conditions are 60 to 80 ° C, the time is 3-5 min, and the B 1B2 process is verified, which does not involve the influence of pre-drying conditions on the coating effect. . In the sixth issue of 2012, Electroplating and Finishing, Volume 31, the authors are Xing Wenping, Ge Fei, Qiu Changsheng, the article titled "Water-based Exemption Coating Process Research", for water-free intermediate coating The installation process, taking the B 1B2 process as an example, introduced the technical effects, influencing factors, and existing problems. However, when discussing the influence of the intermediate flashing and leveling time, the two periods of 4.5min and 7min were selected in the pre-drying process for the test, and the different flashing and leveling time were basically no color and vividness. The conclusion of the influence, but did not deeply explore the influence of the comprehensive factors such as pre-baking temperature and time on the appearance quality of the workpiece. In the actual water-free intermediate coating process, the pre-drying process generally uses a two-stage heating and drying method, the heating temperature is controlled at 60 ± 5 °C, and the tuyere wind speed is controlled at 6-10 m/s, heating time. It is l-2min; the heating temperature is controlled at 80 ± 5 degrees Celsius, the tuyere wind speed is not less than 10m/s, and the heating time is 2.5-3min. In actual production, the ratio of the heating period to the heating of the second stage is generally controlled at about 1:2, which means that the heating from the heating stage to the heating of the second stage requires rapid temperature rise. But in fact, after the water-repellent free-coating process, before pre-drying The wet film thickness is larger, which will more than double, and the rapid heating will lead to pinholes and other quality defects. Moreover, the pre-drying time of the traditional aqueous pre-drying system is about 3-4 minutes, and the drying time is too short. The effect is not good, which is not conducive to the next stage of workpiece processing after pre-drying. According to the pre-drying process carried out under the above conditions, some appearance quality parameters may not even meet the standard requirements. Summary of the invention
本发明的目的是克服上述缺点, 提出一种有利于在水性免中涂涂装中 提高预烘干质量、 烘干效果更好的预烘干工艺, 并提供一种实现此预烘干 工艺的结构简单的预烘干系统。  The object of the present invention is to overcome the above disadvantages, and to provide a pre-baking process which is advantageous for improving the pre-bake quality and the drying effect in the water-free intermediate coating, and provides a pre-drying process for realizing the pre-drying process. A simple pre-drying system.
为实现上述目的, 本发明提供了如下技术方案:  To achieve the above object, the present invention provides the following technical solutions:
一种水性免中涂涂装预烘干工艺, 包括的步骤有:  An aqueous free intermediate coating pre-drying process, comprising the following steps:
在加热一段前进行气封, 气封温度为 60-80°C ;  The gas seal is performed before heating for a period of time, and the gas seal temperature is 60-80 ° C;
加热一段, 温度为 70-80°C, 风速为 3-5m/s, 加热时间为 3-4min; 加热二段, 温度为 90-100°C, 风速为 10-14m/s, 加热时间为 3-4min; 在加热二段后进行气封, 气封温度为 80-100 °C ;  Heating for a period, the temperature is 70-80 ° C, the wind speed is 3-5 m / s, the heating time is 3-4 min; the heating is two, the temperature is 90-100 ° C, the wind speed is 10-14 m / s, the heating time is 3 -4min; after two stages of heating, the gas seal is performed at a gas seal temperature of 80-100 °C;
强冷段, 将工件表面温度降低至 35 °C ;  Strong cold section, reduce the surface temperature of the workpiece to 35 °C;
其中, 所述加热一段和所述加热二段保证绝对湿度为 10-15g/kg。  Wherein, the heating section and the heating section ensure an absolute humidity of 10-15 g/kg.
所述加热一段的加热时间与所述加热二段的加热时间的和至
Figure imgf000004_0001
The sum of the heating time of the heating section and the heating time of the heating section
Figure imgf000004_0001
优选地, 所述强冷段的温度为 20°C, 风速为 16-20m/s。  Preferably, the strong cold section has a temperature of 20 ° C and a wind speed of 16-20 m / s.
优选地, 所述加热一段温度为 75 °C, 所述加热二段温度为 90 °C。 一种水性免中涂涂装预烘干系统, 包括: 预烘干室; 向所述预烘干室 输送工件的输送系统; 为所述预烘干室供风的加热系统; 在工件的前进方 向上, 所述预烘干室依次布置有入口风幕、 加热一段、 加热二段、 出口风 幕、 强冷室, 所述加热一段与所述加热二段的长度满足以下数学表达式: Preferably, the heating is at a temperature of 75 ° C and the heating at a temperature of 90 ° C. An aqueous medium-free coating pre-drying system, comprising: a pre-drying chamber; a conveying system for conveying the workpiece to the pre-drying chamber; a heating system for supplying air to the pre-drying chamber; In the direction, the pre-drying chamber is arranged with an inlet air curtain, a heating section, a heating section, an outlet air curtain, and a strong cooling chamber, wherein the length of the heating section and the length of the heating section satisfy the following mathematical expression:
Sl=vti; S2=vt2; 3min < ti < 4min; 3min < t2 < 4min; Sl=vti; S2=vt 2 ; 3min < ti <4min; 3min < t 2 <4min;
其中, S I为加热一段的长度, 单位为 m; S2为加热二段的长度, 单位 为 m; V为所述输送系统上的工件前进速度, 单位为 m/min, ^、 t2分别为 工件在加热一段、 加热二段所经历的时间。 Wherein, SI is the length of the heating section, the unit is m; S2 is the length of the heating two sections, the unit is m; V is the advancement speed of the workpiece on the conveying system, the unit is m/min, ^, t 2 are respectively The time it takes for the workpiece to heat up for a period of time and heat for two stages.
优选地, 所述加热一段与所述加热二段的长度比为 1 :1。  Preferably, the ratio of the length of the heating section to the length of the heating section is 1:1.
优选地, 所述加热一段与所述加热二段的长度还应当满足以下数学表 达式: Preferably, the length of the heating section and the length of the heating section should also satisfy the following mathematical expression:
6.5 mm。  6.5 mm.
v  v
优选地, 所述加热系统包括为所述加热一段和所述入口风幕提供循环 风的一段加热箱、 为所述加热二段和所述出口风幕提供循环风的二段加热 箱和为所述强冷室提供冷风的冷风箱。  Preferably, the heating system comprises a heating box for providing a circulating wind for the heating section and the inlet air curtain, a two-stage heating box for providing a circulating wind for the heating two sections and the outlet air curtain, and A cold air box that provides a cold air in a strong cold room.
优选地, 所述一段加热箱包括新风阀、 过滤器、 表冷器、 燃烧器和循 环风机, 风经过所述新风阀、 所述过滤器、 所述表冷器、 所述燃烧器和所 述循环风机后进入所述加热一段和所述入口风幕; 所述二段加热箱包括循 环风机、 过滤器和燃烧器, 来自于所述加热一段的风经过所述过滤器、 所 述燃烧器和所述循环风机后进入所述加热二段和所述出口风幕; 所述冷风 箱包括送风机、 排风机、 过滤器和表冷器, 风经所述过滤器、 所述进风机、 所述强冷室、 所述排风机实现与室外的空气交换。  Preferably, the one-stage heating box comprises a fresh air valve, a filter, a surface cooler, a burner and a circulation fan, the wind passing through the fresh air valve, the filter, the air cooler, the burner and the After the circulation fan enters the heating section and the inlet air curtain; the two-stage heating tank includes a circulation fan, a filter and a burner, and the wind from the heating section passes through the filter, the burner and The circulating fan enters the heating second section and the outlet air curtain; the cold air box comprises a blower, an exhaust fan, a filter and a surface cooler, and the wind passes through the filter, the inlet fan, the strong The cold chamber and the exhaust fan realize air exchange with the outdoor.
釆用上所述的工艺制造的车身及釆用所述车身的汽车。  A vehicle body manufactured by the above-described process and a vehicle using the vehicle body.
在本发明的预烘干工艺中, 通过对温度、 时间、 风速的控制, 获得了 更好的预烘干效果, 工件表面漆膜外观质量更好。  In the pre-baking process of the present invention, a better pre-baking effect is obtained by controlling the temperature, time, and wind speed, and the appearance quality of the paint film on the surface of the workpiece is better.
进一步地, 将加热一段与加热二段的加热时间比设定为 1 : 1, 有利于 水分充分蒸发和加热速度的平緩上升。  Further, setting the heating time ratio of the heating section to the heating section is set to 1 : 1, which is advantageous for the sufficient evaporation of water and the gentle rise of the heating rate.
进一步地, 加热一段温度为 75 °C, 加热二段温度为 90°C, 较传统加热 一段和加热二段的设定温度高, 但温差小, 加热一段温度接近其前的气封 温度, 加热二段温度接近其后的气封温度, 因此在确保了较高的烘干速度 的同时, 使得温度上升更加平稳, 减少了针孔等缺陷的出现。  Further, the heating temperature is 75 ° C, and the heating temperature is 90 ° C, which is higher than the set temperature of the conventional heating section and the heating section, but the temperature difference is small, and the heating temperature is close to the gas sealing temperature before the heating, heating The temperature of the second stage is close to the air sealing temperature thereafter, so that the higher the drying speed is ensured, the temperature rise is more stable, and defects such as pinholes are reduced.
本发明的预烘干系统结构简单, 能够满足上述工艺要求。 说明书附图  The pre-drying system of the invention has a simple structure and can meet the above process requirements. Instruction sheet
图 1是本发明的水性免中涂涂装预烘干系统原理图;  Figure 1 is a schematic view of the water-free intermediate coating pre-drying system of the present invention;
图 2是车身通过图 1中的预烘干系统过程中车身温度曲线图。 上图中标记说明: 预烘干室 1、 加热系统 2、 一段加热箱 21、 二段加 热箱 22、 冷风箱 23。 具体实施方式 Figure 2 is a graph showing the body temperature during the passage of the body through the pre-drying system of Figure 1. The mark in the above figure shows: pre-drying chamber 1, heating system 2, one-stage heating box 21, two-stage heating box 22, and cold air box 23. detailed description
接下来将结合附图对本发明的具体实施方式做进一步详细说明。 表 1  Specific embodiments of the present invention will be further described in detail below with reference to the accompanying drawings. Table 1
Figure imgf000006_0001
Figure imgf000006_0001
表 1示出了在传统水性涂装工艺中釆用传统的预烘干工艺的工序和工 艺要求。 由表 1可见, 加热一段的时间较加热二段的时间短, 一般将加热 一段与加热二段的时间比设定为 1 :2,并且在加热一段与加热二段中的加热 时间总和一般不超过 4min。 这就造成了在加热一段的加热时间较短, 整体 加热时间也较短, 而由于水性免中涂涂装中的湿膜厚度较厚, 因此漆膜中 的水分消除程度并不能满足要求。 再加上加热一段与加热二段之间的温度 差较大(一般会在加热一段将温度设定为 60°C,而在加热二段设定为 80°C, 两段温度差一般达到 20°C ) , 也就是说加热一段到加热二段的温度升高速 度较快, 因此容易造成针孔等缺陷。 而加热一段较高的风速也不利于保证 含较多水分的漆膜的质量。 表 2 Table 1 shows the process and process requirements for using a conventional pre-baking process in a conventional aqueous coating process. It can be seen from Table 1 that the heating period is shorter than the heating period, generally the ratio of the heating period to the heating period is 1:2, and the heating time in the heating section and the heating section is generally not More than 4min. This results in a shorter heating time during heating and a shorter overall heating time, and the degree of moisture elimination in the paint film is not satisfactory because of the thick wet film thickness in the water-free intermediate coating. In addition, the temperature difference between the heating section and the heating section is relatively large (generally, the temperature is set to 60 ° C in the heating section, and the temperature is set to 80 ° C in the heating section, and the temperature difference between the two sections generally reaches 20 °C), that is to say, the temperature rises from heating to the second stage of heating, and the speed is increased rapidly, so that defects such as pinholes are easily caused. Heating a higher wind speed is also not conducive to ensuring the quality of the paint film containing more moisture. Table 2
Figure imgf000007_0001
Figure imgf000007_0001
表 2表明了根据本发明的预烘干工艺过程。 在本发明中, 在加热一段 前利用风幕进行气封, 以保证加热一段的工作状况稳定。 并且, 气封温度 设定为 60-80°C, 对进入加热一段的工件进行预热。 接下来, 工件进入加热 一段处理, 设定加热温度为 70-80°C, 风速为 3-5m/s, 加热时间为 3-4min。 与表 1对比可见, 加热一段的加热时间变长, 这样在加热一段能够带走工 件表面大部分水分, 同时风口风速降低, 漆膜表面质量更好。 经过加热一 段的加热后, 工件进入加热二段, 加热温度为 90-100°C, 风速为 10-14m/s, 加热时间为 3-4min, 与表 1对比可见, 加热二段的加热时间也被延长, 漆 膜被进一步干燥, 虽然此时相对于加热一段提高风速有利于提高漆膜的干 燥速度, 但风速仍不宜过大, 否则仍然会对漆膜质量造成影响, 选择 10-14m/s 是合适的。 在加热二段后利用风幕进行气封, 气封温度为 80-100 °C , 接近加热二段的温度。 由上述可知, 从工件经气封进入加热一 段、 加热二段到经气封结束加热, 整个过程中加热时间变长, 优选至少达 到 6.5min, 同时温度变化较为平緩, 通过对温度、 加热时间和风速的综合 控制, 获得了更好的漆膜质量, 从而工件外观质量更好。 其中, 优选加热 一段与加热二段的加热时间比为 1 : 1,在能够满足干燥水分要求的前提下实 现了时间的最短, 劳动生产率高。 优选加热一段温度为 75 °C, 加热二段温 度为 90°C, 相对于传统工艺设定的温度高, 温差小, 干燥水分效率高, 温 差变化平緩。 在离开气封后, 工件进入强冷段, 将工件表面温度降低至 35 °C, 为水性免中涂涂装的下一步工序做准备。 优选强冷段是在温度为 20 °C , 风速为 16-20m/s的条件下进行。 在上述处理过程中, 加热一段和所 述加热二段需要保证绝对湿度为 10-15g/kg。 Table 2 shows the pre-drying process in accordance with the present invention. In the present invention, the air seal is used for air sealing before heating for a period of time to ensure stable operation of the heating section. Moreover, the gas seal temperature is set to 60-80 ° C, and the workpiece entering the heating section is preheated. Next, the workpiece enters a heating process, setting the heating temperature to 70-80 ° C, the wind speed to 3-5 m / s, and the heating time to 3-4 min. Comparing with Table 1, it can be seen that the heating time of the heating section becomes longer, so that most of the moisture on the surface of the workpiece can be taken away during the heating period, and the wind speed of the tuyere is lowered, and the surface quality of the paint film is better. After heating for a period of time, the workpiece enters the heating stage, the heating temperature is 90-100 ° C, the wind speed is 10-14 m / s, and the heating time is 3-4 min. Compared with Table 1, the heating time of the heating section is also After being extended, the paint film is further dried. Although increasing the wind speed relative to heating is beneficial to increase the drying speed of the paint film, the wind speed should not be too large, otherwise the film quality will still be affected. Select 10-14m/s. It is suitable. After heating the second stage, the air seal is used for air sealing, and the gas sealing temperature is 80-100 ° C, which is close to the temperature of the second heating stage. It can be seen from the above that from the workpiece through the gas seal into the heating section, heating the second section to the end of the gas seal heating, the heating time becomes longer in the whole process, preferably at least 6.5min, and the temperature change is relatively gentle, by the temperature, the heating time and The comprehensive control of the wind speed achieves better film quality and thus the appearance quality of the workpiece is better. Wherein, it is preferred that the heating time ratio of the heating section to the heating section is 1:1, and the requirement of the dry moisture requirement can be met. The shortest time is now, and labor productivity is high. Preferably, the heating temperature is 75 ° C, the heating temperature is 90 ° C, the temperature is higher than the traditional process, the temperature difference is small, the drying water efficiency is high, and the temperature difference is gentle. After leaving the gas seal, the workpiece enters the strong cold section and reduces the surface temperature of the workpiece to 35 °C in preparation for the next step of the water-free intermediate coating process. Preferably, the strong cold section is carried out at a temperature of 20 ° C and a wind speed of 16-20 m/s. During the above treatment, heating one section and the heating section need to ensure an absolute humidity of 10-15 g/kg.
表 3  table 3
Figure imgf000008_0001
Figure imgf000008_0001
件进行预烘干所获得的工件外观质量的对比数据。 其中, 传统预烘干工艺 与本发明预烘干工艺分别釆用表 1、 表 2 中的参数进行, 其它参数相同。 由表 3可见, 针对三种不同颜色的色漆, 在水平面和垂直面的长、 短波, 光泽、 鲜映性三个方面, 根据本发明的预烘干工艺所获得的表面质量整体 优于传统预烘干工艺, 尤其是对于白色, 传统工艺在鲜映性方面并不能满 足要求, 而本发明的预烘干工艺能够满足要求。 Comparative data on the appearance quality of the workpiece obtained by pre-baking. Wherein, the conventional pre-drying process and the pre-drying process of the present invention are respectively performed using the parameters in Table 1 and Table 2, and other parameters are the same. It can be seen from Table 3 that the surface quality obtained by the pre-baking process according to the present invention is superior to the conventional one for the three different color paints in terms of length, short wave, gloss and vividness of the horizontal and vertical planes. The pre-baking process, especially for white, does not meet the requirements in terms of vividness, and the pre-baking process of the present invention can meet the requirements.
本领域普通技术人员应当理解, 在以上描述中, 加热一段、 加热二段 表示的是时间上的工序步骤, 但在以下描述中, 加热一段、 加热二段表示 的是预烘干室的空间物理组成部分。 参考图 1, 为实现本发明的预烘干工 艺, 本发明的实施例提供了一种水性免中涂涂装预烘干系统, 包括: 预烘 干室 1、 加热系统 2和向预烘干室输送工件的输送系统 (未示出) 。 其中, 加热系统 2为预烘干室 1供风以使预烘干室内各段达到本发明的工艺要求。 工件在输送系统的承载下, 在完成预烘干上一道工序后, 在图中箭头所示 的工件的前进方向上进入预烘干室 1并在其中运动。在工件的前进方向上, 预烘干室 1依次布置有入口风幕、 加热一段、 加热二段、 出口风幕和强冷 室, 并且为了满足本发明工艺的加热时间, 加热一段与所述加热二段的长 度应当满足以下数学表达式: It will be understood by those skilled in the art that in the above description, heating one section and heating two sections means a time step, but in the following description, heating one section and heating two sections means the space physics of the pre-drying chamber. component. Referring to FIG. 1, in order to realize the pre-baking process of the present invention, an embodiment of the present invention provides an aqueous medium-free coating pre-drying system, comprising: pre-baking A dry chamber 1, a heating system 2, and a delivery system (not shown) that transports the workpiece to the pre-drying chamber. Wherein, the heating system 2 supplies air to the pre-drying chamber 1 to achieve the process requirements of the present invention in each section of the pre-drying chamber. After the workpiece is carried by the conveying system, after the previous process of pre-drying is completed, the pre-drying chamber 1 enters and moves therein in the advancing direction of the workpiece indicated by the arrow in the figure. In the advancing direction of the workpiece, the pre-drying chamber 1 is sequentially arranged with an inlet air curtain, a heating section, a heating section, an outlet air curtain and a strong cooling chamber, and in order to satisfy the heating time of the process of the invention, heating a section and the heating The length of the second segment should satisfy the following mathematical expression:
Sl=vti; S2=vt2; 3min < ti < 4min; 3min < t2 < 4min; Sl=vti; S2=vt 2 ; 3min < ti <4min; 3min < t 2 <4min;
其中, S I为加热一段的长度, 单位为 m; S2为加热二段的长度, 单位 为 m; V为所述输送系统上的工件前进速度, 单位为 m/min, ^、 t2分别为 工件在加热一段、 加热二段所经历的时间。 优选加热一段与加热二段的长 度比为 1 : 1, 由于工件是在输送系统上勾速前进的, 因此意味着工件在加热 一段与加热二段中所加热的时间比也为 1 : 1。优选加热一段与加热二段的长 度还应当满足以下等式: Wherein, the SI is heated for a length, in units of m; S2 is a two-stage heating of length, in m; V is the velocity of the advancing workpiece transport system, the unit is m / min, ^, t 2 respectively workpiece The time elapsed during the heating of one section and heating of the second section. Preferably, the length ratio of the heating section to the heating section is 1:1, since the workpiece is advanced at the conveying system, it means that the time during which the workpiece is heated in the heating section and the heating section is also 1:1. Preferably, the length of the heating section and the length of the heating section should also satisfy the following equation:
^^^6.5 min , 即工件在加热一段和加热二段中经历的时间不少于 ^^^6.5 min, that is, the time the workpiece has been in the heating section and the heating section is not less than
V V
6.5min。  6.5min.
加热系统 2包括为加热一段和入口风幕提供循环风的一段加热箱 21、 为加热二段和出口风幕提供循环风的二段加热箱 22 和为强冷室提供冷风 的冷风箱 23。 一段加热箱 21 将外部新风加热后送入入口风幕提供气封, 并送入加热一段使加热一段中的空气温度达到工艺要求。二段加热箱 22对 加热二段中的空气进行进一步加热升温, 达到加热二段工艺要求, 并且向 出口风幕送风提供气封。 冷风箱 23完成制冷室与外界的热交换, 从而为制 冷室中的工件降温。 外界的新风经过一段加热箱 21中的新风阀、 过滤器、 表冷器、 燃烧器后达到所需温度, 然后通过循环风机进入加热一段和入口 风幕。 来自于加热一段的风经过二段加热箱 22中的过滤器、 燃烧器后温度 进一步升高, 经循环风机进入加热二段和出口风幕。 室外风经冷风箱 23中 的过滤器, 经进风机进入强冷室, 强冷室中的空气与工件进行热交换后, 经排风机实现与室外的空气交换。 通过控制循环风机、 进风机和排风机的 运转, 既能够控制预烘干室内各部分的风口风速。 当然, 本领域普通技术 人员能够很容易地想象, 加热系统 1也能够釆用其它例如中央空调式的加 热、 制冷系统。 在工件离开强冷室后, 进入过渡段为下一道工序做准备。 The heating system 2 includes a section of heating tanks 21 for providing a circulating air for heating a section and an inlet air curtain, a two-stage heating tank 22 for providing circulating air for heating the two sections and the outlet air curtain, and a cold bellows 23 for supplying cold air to the forced cooling chamber. A section of the heating box 21 heats the external fresh air and sends it to the inlet air curtain to provide a gas seal, and feeds the heating section to make the temperature of the air in the heating section reach the process requirement. The two-stage heating box 22 further heats and heats the air in the second stage of heating to reach the requirements of the heating two-stage process, and provides a gas seal to the outlet air curtain. The cold bellows 23 completes the heat exchange between the refrigerating chamber and the outside, thereby cooling the workpiece in the refrigerating chamber. The fresh air from the outside passes through the fresh air valve, filter, air cooler and burner in the heating chamber 21 to reach the required temperature, and then enters the heating section and the inlet air curtain through the circulation fan. The temperature from the heated section passes through the filter and burner in the two-stage heating tank 22, and the temperature is further increased, and the circulating fan enters the heating second section and the outlet air curtain. The outdoor wind passes through the filter in the cold air box 23, enters the strong cold chamber through the inlet fan, and the air in the strong cold chamber exchanges heat with the workpiece, and then exchanges air with the outdoor through the exhaust fan. By controlling the operation of the circulating fan, the inlet fan and the exhaust fan, it is possible to control the tuyere wind speed of each part of the pre-drying chamber. Of course, the prior art It can be easily imagined by the personnel that the heating system 1 can also utilize other heating and cooling systems such as central air conditioning. After the workpiece leaves the forced cooling chamber, enter the transition section to prepare for the next process.
图 2示出的是车身在经过本发明的实施例的预烘干系统的过程中, 在 预烘干室内的预烘干条件满足表 2的工艺要求条件下, 车身不同位置处的 温度探头检测到的车身温度曲线。 车身漆膜在该过程中所获得的外观质量 在表 3 中已给出, 在此不再赘述。 车身外观质量得到提高, 相应地, 汽车 的整车外观质量也会得到明显改善。  2 is a view showing the temperature probe detection at different positions of the vehicle body in the process of the pre-drying system in the pre-drying room in the process of the pre-drying system of the embodiment of the present invention. The body temperature curve to the arrival. The appearance quality of the body paint film obtained in the process is given in Table 3 and will not be described here. The appearance quality of the car body is improved, and accordingly, the overall appearance quality of the car will be significantly improved.
虽然本发明是结合以上实施例进行描述的, 但本发明并不限定于上述 实施例。 本领域普通技术人员能够容易地对其进行修改和变化, 但并不离 开本发明的实质构思和范围。  Although the invention has been described in connection with the above embodiments, the invention is not limited to the embodiments described above. A person skilled in the art can easily modify and change the present invention without departing from the spirit and scope of the invention.

Claims

权 利 要 求 Rights request
1. 一种水性免中涂涂装预烘干工艺, 其特征在于, 包括的步骤有: 在加热一段前进行气封, 气封温度为 60-80°C ; 1. A water-based mid-coat-free pre-drying process, characterized in that it includes the following steps: air sealing before heating for a period of time, and the air sealing temperature is 60-80°C;
加热一段, 温度为 70-80°C, 风速为 3-5m/s, 加热时间为 3-4min; 加热二段, 温度为 90-100°C, 风速为 10-14m/s, 加热时间为 3-4min; 在加热二段后进行气封, 气封温度为 80-100 °C ; In the first heating section, the temperature is 70-80°C, the wind speed is 3-5m/s, and the heating time is 3-4min; in the second heating section, the temperature is 90-100°C, the wind speed is 10-14m/s, and the heating time is 3 -4min; Carry out air sealing after the second heating stage, the air sealing temperature is 80-100 °C;
强冷段, 将工件表面温度降低至 35 °C ; The strong cooling section reduces the surface temperature of the workpiece to 35 °C;
其中, 所述加热一段和所述加热二段保证绝对湿度为 10-15g/kg。 Among them, the first heating stage and the second heating stage ensure that the absolute humidity is 10-15g/kg.
2. 根据权利要求 1所述的工艺, 其特征在于, 所述加热一段的加热时 间与所述加热二段的加热时间的和至少达到 6.5min。 2. The process according to claim 1, characterized in that the sum of the heating time of the first heating stage and the heating time of the second heating stage reaches at least 6.5 minutes.
3. 根据权利要求 1所述的工艺, 其特征在于, 所述加热一段与所述加 热二段的加热时间比为 1 : 1。 3. The process according to claim 1, characterized in that the heating time ratio between the first heating stage and the second heating stage is 1:1.
4. 根据权利要求 1 所述的工艺, 其特征在于, 所述强冷段的温度为 20 °C , 风速为 16-20m/s。 4. The process according to claim 1, characterized in that the temperature of the strong cooling section is 20°C, and the wind speed is 16-20m/s.
5. 根据权利要求 1至 4中的任一项所述的工艺, 其特征在于, 所述加 热一段温度为 75 °C, 所述加热二段温度为 90 °C。 5. The process according to any one of claims 1 to 4, characterized in that the temperature of the first heating stage is 75 °C, and the temperature of the second heating stage is 90 °C.
6. 一种水性免中涂涂装预烘干系统, 包括: 6. A water-based mid-coat-free coating pre-drying system, including:
预烘干室; Pre-drying room;
向所述预烘干室输送工件的输送系统; A conveying system for conveying workpieces to the pre-drying chamber;
为所述预烘干室供风的加热系统; A heating system that supplies air to the pre-drying chamber;
其特征在于, 在工件的前进方向上, 所述预烘干室依次布置有入口风 幕、 加热一段、 加热二段、 出口风幕、 强冷室, 所述加热一段与所述加热 二段的长度满足以下数学表达式: It is characterized in that, in the forward direction of the workpiece, the pre-drying chamber is sequentially arranged with an inlet air curtain, a first heating section, a second heating section, an outlet air curtain, and a forced cooling chamber. The first heating section and the second heating section are arranged in sequence. The length satisfies the following mathematical expression:
Sl=vti; S2=vt2; 3min < ti < 4min; 3min < t2 < 4min; Sl=vti; S2=vt 2 ; 3min < ti <4min; 3min < t 2 <4min;
其中, S I为加热一段的长度, 单位为 m; S2为加热二段的长度, 单位 为 m; V为所述输送系统上的工件前进速度, 单位为 m/min, ^、 t2分别为 工件在加热一段、 加热二段所经历的时间; Among them, SI is the length of the first heating section, the unit is m; S2 is the length of the second heating section, the unit is m; V is the forward speed of the workpiece on the conveying system, the unit is m/min, ^ and t 2 are the workpiece respectively The time spent in the first heating stage and the second heating stage;
所述入口风幕提供温度为 60-80°C的气封,所述加热系统为所述预烘干 室供风以使所述加热一段温度为 70-80°C风速为 3-5m/s,并使所述加热二段 温度为 90-100°C, 风速为 10-14m/s, 所述出口风幕提供 80-100 °C的气封, 所述加热一段和所述加热二段保证绝对湿度为 10- 15g/kg。 The inlet air curtain provides an air seal with a temperature of 60-80°C, and the heating system is the pre-drying The room supplies air so that the temperature of the first heating section is 70-80°C and the wind speed is 3-5m/s, and the temperature of the second heating section is 90-100°C and the wind speed is 10-14m/s. The outlet The air curtain provides an air seal of 80-100°C, and the first heating section and the second heating section ensure an absolute humidity of 10-15g/kg.
7. 根据权利要求 6所述的系统, 其特征在于, 所述加热一段与所述加 热二段的长度比为 1 : 1。 7. The system according to claim 6, characterized in that the length ratio of the first heating section to the second heating section is 1:1.
8. 根据权利要求 6所述的系统, 其特征在于, 所述加热一段与所述加 热二段的长度还应当满足以下数学表达式: 8. The system according to claim 6, characterized in that the lengths of the first heating section and the second heating section should also satisfy the following mathematical expression:
^6.5 mm ^6.5 mm
V V
9. 根据权利要求 6至 8中的任一项所述的系统, 其特征在于, 所述加 热系统包括为所述加热一段和所述入口风幕提供循环风的一段加热箱、 为 所述加热二段和所述出口风幕提供循环风的二段加热箱和为所述强冷室提 供冷风的冷风箱, 所述一段加热箱包括新风阀、 过滤器、 表冷器、 燃烧器 和循环风机, 风经过所述新风阀、 所述过滤器、 所述表冷器、 所述燃烧器 和所述循环风机后进入所述加热一段和所述入口风幕; 所述二段加热箱包 括循环风机、 过滤器和燃烧器, 来自于所述加热一段的风经过所述过滤器、 所述燃烧器和所述循环风机后进入所述加热二段和所述出口风幕; 所述冷 风箱包括送风机、 排风机、 过滤器和表冷器, 风经所述过滤器、 所述进风 机、 所述强冷室、 所述排风机实现与室外的空气交换。 9. The system according to any one of claims 6 to 8, characterized in that, the heating system includes a section of heating box that provides circulating air for the heating section and the inlet air curtain. The second section and the outlet air curtain provide a second section heating box for circulating air and a cold air box that provides cold air for the forced cooling room. The first section heating box includes a fresh air valve, a filter, a surface cooler, a burner and a circulating fan. , the air passes through the fresh air valve, the filter, the surface cooler, the burner and the circulating fan and then enters the first heating section and the inlet air curtain; the second section heating box includes a circulating fan , filter and burner, the wind from the first heating section passes through the filter, the burner and the circulation fan and then enters the second heating section and the outlet air curtain; the cold air box includes an air blower , exhaust fan, filter and surface cooler, the air passes through the filter, the air inlet fan, the forced cooling chamber, and the exhaust fan to achieve air exchange with the outdoors.
10. 一种车身, 其特征在于, 所述车身釆用如权利要求 1至 5 中的任 一项所述的工艺制造。 10. A vehicle body, characterized in that the vehicle body is manufactured using the process described in any one of claims 1 to 5.
11. 一种汽车, 其特征在于, 其特征在于, 所述汽车釆用如权利要求 10所述的车身。 11. An automobile, characterized in that, the automobile adopts a body as claimed in claim 10.
PCT/CN2014/082056 2013-07-12 2014-07-11 Prebake process and system for water-based painting without a middle coat WO2015003654A1 (en)

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CN201310294683.1A CN103331244B (en) 2013-07-12 2013-07-12 Aqueous floating-coating-free coating prebaking technology and system

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