TWI827478B - Clean system and clean method for a steel strip - Google Patents
Clean system and clean method for a steel strip Download PDFInfo
- Publication number
- TWI827478B TWI827478B TW112108388A TW112108388A TWI827478B TW I827478 B TWI827478 B TW I827478B TW 112108388 A TW112108388 A TW 112108388A TW 112108388 A TW112108388 A TW 112108388A TW I827478 B TWI827478 B TW I827478B
- Authority
- TW
- Taiwan
- Prior art keywords
- cleaning
- steel strip
- water
- replenishment amount
- water replenishment
- Prior art date
Links
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 219
- 239000010959 steel Substances 0.000 title claims abstract description 219
- 238000000034 method Methods 0.000 title claims abstract description 35
- 238000004140 cleaning Methods 0.000 claims abstract description 335
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 238
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims abstract description 95
- 239000007921 spray Substances 0.000 claims description 39
- 238000004364 calculation method Methods 0.000 claims description 12
- 239000012141 concentrate Substances 0.000 abstract 1
- 239000002253 acid Substances 0.000 description 22
- 238000005554 pickling Methods 0.000 description 8
- 230000036571 hydration Effects 0.000 description 7
- 238000006703 hydration reaction Methods 0.000 description 7
- 238000003860 storage Methods 0.000 description 4
- 230000032258 transport Effects 0.000 description 4
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 239000010960 cold rolled steel Substances 0.000 description 1
- 238000005097 cold rolling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hcl hcl Chemical compound Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Images
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
Description
本發明是有關於一種鋼帶清洗系統與鋼帶清洗方法,特別是有關於針對酸洗後鋼帶的清洗系統與鋼帶清洗方法。The present invention relates to a steel strip cleaning system and a steel strip cleaning method, in particular to a cleaning system and a steel strip cleaning method for pickled steel strips.
酸洗製程是生產冷軋鋼帶的重要製程。一般而言,酸洗製程是用以處理鋼帶上的氧化鐵皮,以使得鋼帶的表面適於冷軋處理。在進行酸洗製程後,需要對鋼帶進行清洗,以去除鋼帶上的酸液。The pickling process is an important process for producing cold-rolled steel strips. Generally speaking, the pickling process is used to treat the iron oxide scale on the steel strip to make the surface of the steel strip suitable for cold rolling. After the pickling process, the steel strip needs to be cleaned to remove the acid on the steel strip.
現行的酸洗液清洗製程通常利用複數個串聯的清洗槽來進行。例如,當鋼帶被輸送穿過這些清洗槽時,利用這些清洗槽中的水沖洗(例如,噴射式酸洗清洗槽)鋼帶來去除鋼帶上的酸液。當這些清洗槽進行補水時,這些清洗槽中的水係以梯度控制(cascade)的方式來進行補水。具體而言,水從最後一個清洗槽進入補充,然後溢流至最後第二個清洗槽,接著再溢流至最後第三個清洗槽。如此,依序溢流直到第一個清洗槽。The current pickling solution cleaning process usually uses a plurality of cleaning tanks connected in series. For example, when the steel strip is conveyed through these cleaning tanks, the steel strip is flushed (eg, a spray pickling cleaning tank) with water in these cleaning tanks to remove acid from the steel strip. When these cleaning tanks are replenished, the water systems in these cleaning tanks are replenished in a cascade manner. Specifically, water enters the replenishment tank from the last wash tank, then overflows to the second last wash tank, and then overflows to the third last wash tank. In this way, the overflow continues until the first cleaning tank.
然而,現行的鋼帶清洗機制仍常有補水量不足或過多的問題,故需要一種新的鋼帶清洗系統與鋼帶清洗方法來解決上述問題。However, the current steel belt cleaning mechanism still often suffers from insufficient or excessive water replenishment, so a new steel belt cleaning system and steel belt cleaning method are needed to solve the above problems.
本發明係提供一種鋼帶清洗系統與鋼帶清洗方法,其可精確地計算出補水量,以避免補水量不足或過多的問題。The invention provides a steel belt cleaning system and a steel belt cleaning method, which can accurately calculate the amount of water replenishment to avoid the problem of insufficient or excessive water replenishment.
根據本發明之一實施例,上述之鋼帶清洗系統包含:複數個清洗槽、輸送裝置、第一清洗槽氯離子濃度偵測計、最後清洗槽氯離子濃度偵測計、絞乾輥裝置、補水裝置以及電腦裝置。清洗槽裝有清洗用水,且清洗槽之間連接有複數個水管,以串接這些清洗槽。輸送裝置係設置於清洗槽上,其中輸送裝置用以根據一鋼帶清洗速度來輸送鋼帶來經過清洗槽,以利用清洗槽中的清洗用水來清洗鋼帶。第一清洗槽氯離子濃度偵測計係設置於上述清洗槽之一第一者中,以量測上述清洗槽之第一者之一第一清洗槽氯離子濃度值。最後清洗槽氯離子濃度偵測計係設置於上述清洗槽之最後一者中,以量測上述清洗槽之最後一者之一最後清洗槽氯離子濃度值。絞乾輥裝置係設置於上述清洗槽之最後一者與最後第二者之間,以於鋼帶進入清洗槽之最後一者之前,對鋼帶進行一絞乾步驟。補水裝置係用以提供清潔用水至上述清洗槽之最後一者。電腦裝置係電性連接至補水裝置、第一清洗槽氯離子濃度偵測計以及最後清洗槽氯離子濃度偵測計,並進行:獲得第一清洗槽氯離子濃度和最後清洗槽氯離子濃度;獲得鋼帶之一鋼帶厚度值以及一鋼帶寬度值;獲得鋼帶清洗速度之值;獲得絞乾輥裝置之一絞乾輥補償參數之值;進行補水量計算步驟,以根據第一清洗槽氯離子濃度、最後清洗槽氯離子濃度、鋼帶厚度值、鋼帶寬度值、絞乾輥補償參數之值以及鋼帶清洗速度之值來計算出補水量;以及根據補水量來產生一補水訊號,並將補水訊號輸出至補水裝置,以控制補水裝置來提供清潔用水至上述清洗槽之最後一者。According to an embodiment of the present invention, the above-mentioned steel belt cleaning system includes: a plurality of cleaning tanks, a conveying device, a first cleaning tank chloride ion concentration detector, a final cleaning tank chloride ion concentration detector, a wringing roller device, Hydration device and computer device. The cleaning tank is filled with cleaning water, and a plurality of water pipes are connected between the cleaning tanks to connect these cleaning tanks in series. The conveying device is arranged on the cleaning tank, wherein the conveying device is used to transport the steel belt through the cleaning tank according to a steel belt cleaning speed, so as to use the cleaning water in the cleaning tank to clean the steel strip. The first cleaning tank chloride ion concentration detector is installed in the first one of the above-mentioned cleaning tanks to measure the chloride ion concentration value of the first one of the above-mentioned cleaning tanks. The last cleaning tank chloride ion concentration detector is installed in the last one of the above-mentioned cleaning tanks to measure the chloride ion concentration value of the last one of the above-mentioned cleaning tanks. The wringing roller device is arranged between the last one and the second last one of the above-mentioned cleaning tanks to perform a wringing step on the steel strip before the steel strip enters the last one of the cleaning tanks. The water replenishing device is used to provide clean water to the last one of the above-mentioned cleaning tanks. The computer device is electrically connected to the water replenishing device, the chloride ion concentration detector of the first cleaning tank and the chloride ion concentration detector of the last cleaning tank, and performs the following steps: obtaining the chloride ion concentration of the first cleaning tank and the chloride ion concentration of the last cleaning tank; Obtain a steel strip thickness value and a steel strip width value; obtain the value of the steel belt cleaning speed; obtain the value of the wringing roller compensation parameter of the wringing roller device; perform the water replenishment amount calculation step to calculate the water replenishment amount according to the first cleaning The chloride ion concentration of the tank, the chloride ion concentration of the final cleaning tank, the steel strip thickness value, the steel strip width value, the value of the wringing roller compensation parameter and the value of the steel strip cleaning speed are used to calculate the water replenishment amount; and a replenishment water is generated according to the water replenishment amount. signal, and output the water replenishing signal to the water replenishing device to control the water replenishing device to provide clean water to the last one of the above-mentioned cleaning tanks.
在一些實施例中,補水量計算步驟係根據下列方程式來計算補水量: Q 4=(Q CSP+Q CL1+Q CL4+Q TH+Q WD)*R ref其中,Q 4為上述之補水量;Q CSP為根據鋼帶清洗速度所計算出之一速度相關補水量;Q CL1為根據第一清洗槽氯離子濃度所計算出之一第一清洗槽補水量;Q CL4為根據最後清洗槽氯離子濃度所計算出之一最後清洗槽補水量;Q TH為根據鋼帶厚度值所計算出之一厚度相關補水量;Q WD為根據鋼帶寬度值所計算出之一寬度相關補水量;R ref為絞乾輥補償參數之值。 In some embodiments, the water replenishment amount calculation step is to calculate the water replenishment amount according to the following equation: Q 4 =(Q CSP +Q CL1 +Q CL4 +Q TH +Q WD )*R ref where Q 4 is the above water replenishment amount ; Q CSP is a speed-related water replenishment amount calculated based on the steel strip cleaning speed; Q CL1 is a first cleaning tank water replenishment amount calculated based on the chloride ion concentration of the first cleaning tank; Q CL4 is a water replenishment amount based on the last cleaning tank chlorine The final cleaning tank water replenishment amount is calculated based on the ion concentration; Q TH is the thickness-related water replenishment amount calculated based on the steel strip thickness value; Q WD is the width-related water replenishment amount calculated based on the steel strip width value; R ref is the value of the compensation parameter of the wringing roller.
在一些實施例中,上述之鋼帶清洗系統更包含噴水裝置。噴水裝置係用以於鋼帶從上述清洗槽之該最後一者離開時,對鋼帶進行噴水。In some embodiments, the above-mentioned steel belt cleaning system further includes a water spray device. The water spray device is used to spray water on the steel strip when the steel strip leaves the last one of the above-mentioned cleaning tanks.
在一些實施例中,上述噴水裝置係根據一噴水量來對鋼帶進行噴水,上述補水量計算步驟係根據下列方程式來計算補水量: Q 4= Q C+(Q CSP+Q CL1+Q CL4+Q TH+Q WD)*R ref其中,Q 4為補水量;Q C為噴水裝置之該噴水量;Q CSP為根據鋼帶清洗速度所計算出之一速度相關補水量;Q CL1為根據第一清洗槽氯離子濃度所計算出之第一清洗槽補水量;Q CL4為根據最後清洗槽氯離子濃度所計算出之一最後清洗槽補水量;Q TH為根據鋼帶厚度值所計算出之一厚度相關補水量;Q WD為根據鋼帶寬度值所計算出之一寬度相關補水量;R ref為絞乾輥補償參數之值。 In some embodiments, the above-mentioned water spray device sprays water on the steel strip according to a water spray amount, and the above-mentioned water replenishment amount calculation step calculates the water replenishment amount according to the following equation: Q 4 = Q C +(Q CSP +Q CL1 +Q CL4 +Q TH +Q WD )*R ref Among them, Q 4 is the water replenishment amount; Q C is the water spray amount of the water spray device; Q CSP is the speed-related water replenishment amount calculated based on the steel strip cleaning speed; Q CL1 is the water replenishment amount calculated based on the steel strip cleaning speed. The water replenishment amount of the first cleaning tank is calculated based on the chloride ion concentration of the first cleaning tank; Q CL4 is the water replenishment amount of the last cleaning tank calculated based on the chloride ion concentration of the last cleaning tank; Q TH is the water replenishment amount of the last cleaning tank calculated based on the thickness of the steel strip is the thickness-related water replenishment amount; Q WD is the width-related water replenishment amount calculated based on the steel strip width value; R ref is the value of the wringing roller compensation parameter.
在一些實施例中,絞乾輥補償參數之值係根據絞乾輥裝置之乾摩擦係數計算而得。In some embodiments, the value of the wringing roller compensation parameter is calculated based on the dry friction coefficient of the wringing roller device.
根據本發明之一實施例,上述之鋼帶清洗方法係適用於上述之鋼帶清洗系統,且由上述之鋼帶清洗系統所執行。鋼帶清洗方法包含:提供複數個清洗槽,其中這些清洗槽裝有清洗用水,清洗槽之間連接有複數個水管,以串接清洗槽;根據一鋼帶清洗速度來利用一輸送裝置輸送一鋼帶,以使此鋼帶經過上述清洗槽,而利用清洗槽中的清洗用水來清洗鋼帶;利用第一清洗槽氯離子濃度偵測計來量測上述清洗槽之第一者之一第一清洗槽氯離子濃度值;利用一最後清洗槽氯離子濃度偵測計來量測上述清洗槽之第一者之一最後清洗槽氯離子濃度值;利用一絞乾輥裝置來對鋼帶進行一絞乾步驟,其中此絞乾輥裝置設置於上述清洗槽之最後一者與最後第二者之間;進行一補水量計算步驟,以根據第一清洗槽氯離子濃度、最後清洗槽氯離子濃度、鋼帶厚度值、鋼帶寬度值、絞乾輥裝置之一補償參數之值以及鋼帶清洗速度之值來計算出一補水量;以及根據此補水量來產生一補水訊號,並將水訊號輸出至一補水裝置,以控制此補水裝置來提供清潔用水至上述清洗槽之最後一者。According to an embodiment of the present invention, the above-mentioned steel belt cleaning method is applicable to the above-mentioned steel belt cleaning system, and is executed by the above-mentioned steel belt cleaning system. The steel belt cleaning method includes: providing a plurality of cleaning tanks, wherein these cleaning tanks are filled with cleaning water, and a plurality of water pipes are connected between the cleaning tanks to connect the cleaning tanks in series; using a conveying device to transport a steel belt according to the cleaning speed of the steel belt. Steel strip, so that the steel strip passes through the above-mentioned cleaning tank, and the cleaning water in the cleaning tank is used to clean the steel strip; the first cleaning tank chloride ion concentration detector is used to measure the first one of the above-mentioned cleaning tanks. A cleaning tank chloride ion concentration value; a final cleaning tank chloride ion concentration detector is used to measure the chloride ion concentration value of the first one of the above-mentioned cleaning tanks, the final cleaning tank; a wringing roller device is used to perform the steel strip A wringing step, wherein the wringing roller device is arranged between the last one and the second last one of the above-mentioned cleaning tanks; a step of calculating the amount of water replenishment is performed to calculate the chloride ion concentration in the first cleaning tank and the chloride ion concentration in the last cleaning tank. The concentration, steel strip thickness value, steel strip width value, the value of a compensation parameter of the wringing roller device and the value of the steel belt cleaning speed are used to calculate a water replenishment amount; and a water replenishment signal is generated based on this water replenishment amount, and the water is The signal is output to a water replenishing device to control the water replenishing device to provide clean water to the last one of the above-mentioned cleaning tanks.
在一些實施例中,上述鋼帶清洗方法中的補水量計算步驟係根據下列方程式來計算補水量: Q 4=(Q CSP+Q CL1+Q CL4+Q TH+Q WD)*R ref其中,Q 4為上述之補水量;Q CSP為根據鋼帶清洗速度所計算出之一速度相關補水量;Q CL1為根據第一清洗槽氯離子濃度所計算出之一第一清洗槽補水量;Q CL4為根據最後清洗槽氯離子濃度所計算出之一最後清洗槽補水量;Q TH為根據鋼帶厚度值所計算出之一厚度相關補水量;Q WD為根據鋼帶寬度值所計算出之一寬度相關補水量;R ref為絞乾輥補償參數之值。 In some embodiments, the water replenishment amount calculation step in the above steel strip cleaning method is to calculate the water replenishment amount according to the following equation: Q 4 =(Q CSP +Q CL1 +Q CL4 +Q TH +Q WD )*R ref where, Q 4 is the above-mentioned water replenishment amount; Q CSP is a speed-related water replenishment amount calculated based on the steel strip cleaning speed; Q CL1 is a first cleaning tank replenishment amount calculated based on the chloride ion concentration of the first cleaning tank; Q CL4 is the water replenishment amount of the final cleaning tank calculated based on the chloride ion concentration of the final cleaning tank; Q TH is the thickness-related water replenishment amount calculated based on the steel strip thickness value; Q WD is the water replenishment amount calculated based on the steel strip width value. A width-related water replenishment amount; R ref is the value of the wringing roller compensation parameter.
在一些實施例中,上述之鋼帶清洗方法更包含:當鋼帶從上述清洗槽之最後一者離開時,利用一噴水裝置來對鋼帶進行噴水。In some embodiments, the above-mentioned steel strip cleaning method further includes: when the steel strip leaves the last one of the above-mentioned cleaning tanks, using a water spray device to spray water on the steel strip.
在一些實施例中,上述噴水裝置係根據一噴水量來對鋼帶進行噴水,上述補水量計算步驟係根據下列方程式來計算補水量: Q 4= Q C+(Q CSP+Q CL1+Q CL4+Q TH+Q WD)*R ref其中,Q 4為補水量;Q C為噴水裝置之該噴水量;Q CSP為根據鋼帶清洗速度所計算出之一速度相關補水量;Q CL1為根據第一清洗槽氯離子濃度所計算出之第一清洗槽補水量;Q CL4為根據最後清洗槽氯離子濃度所計算出之一最後清洗槽補水量;Q TH為根據鋼帶厚度值所計算出之一厚度相關補水量;Q WD為根據鋼帶寬度值所計算出之一寬度相關補水量;R ref為絞乾輥補償參數之值。 In some embodiments, the above-mentioned water spray device sprays water on the steel strip according to a water spray amount, and the above-mentioned water replenishment amount calculation step calculates the water replenishment amount according to the following equation: Q 4 = Q C +(Q CSP +Q CL1 +Q CL4 +Q TH +Q WD )*R ref Among them, Q 4 is the water replenishment amount; Q C is the water spray amount of the water spray device; Q CSP is the speed-related water replenishment amount calculated based on the steel strip cleaning speed; Q CL1 is the water replenishment amount calculated based on the steel strip cleaning speed. The water replenishment amount of the first cleaning tank is calculated based on the chloride ion concentration of the first cleaning tank; Q CL4 is the water replenishment amount of the last cleaning tank calculated based on the chloride ion concentration of the last cleaning tank; Q TH is the water replenishment amount of the last cleaning tank calculated based on the thickness of the steel strip is the thickness-related water replenishment amount; Q WD is the width-related water replenishment amount calculated based on the steel strip width value; R ref is the value of the wringing roller compensation parameter.
在一些實施例中,絞乾輥補償參數之值係根據絞乾輥裝置之乾摩擦係數計算而得。In some embodiments, the value of the wringing roller compensation parameter is calculated based on the dry friction coefficient of the wringing roller device.
以下說明本發明的實施例。然而,可以理解的是,實施例提供許多可應用的概念,其可實施於各式各樣的特定內容中。所討論、揭示之實施例僅供說明,並非用以限定本發明之範圍。Examples of the present invention will be described below. It is to be appreciated, however, that the embodiments provide many applicable concepts that can be embodied in a wide variety of specific contexts. The embodiments discussed and disclosed are for illustration only and are not intended to limit the scope of the invention.
請同時參照圖1和圖2,圖1係繪示根據本發明實施例之鋼帶100的俯視圖,圖2係繪示根據本發明實施例之鋼帶清洗系統200的架構示意圖。鋼帶清洗系統200係適用於清洗鋼帶100,其中鋼帶100已經過酸洗製程處理,且具有酸液殘留。鋼帶清洗系統200包含複數個清洗槽211~214、輸送裝置220、第一清洗槽氯離子濃度偵測計230、最後清洗槽氯離子濃度偵測計240、絞乾輥裝置250、補水裝置260以及電腦裝置270。在本實施例中,鋼帶清洗系統200包含四個清洗槽211~214,四個清洗槽211~214之間以複數個水管串接,而達到梯度控制(cascade)補水的功能。清洗槽211~214裝有清洗用的水,在本實施例中,清洗用水為去離子水(deionized water),但本發明之實施例並不受限於此。Please refer to FIGS. 1 and 2 simultaneously. FIG. 1 is a top view of a
如圖1所示,輸送裝置220係用以輸送鋼帶100進入鋼帶清洗系統200,以對鋼帶100進行清洗,其中輸送裝置220係根據程控電腦設定的清洗速度來輸送鋼帶100,換句話說,輸送裝置220的輸送速度即為鋼帶的清洗速度。在本實施例中,輸送裝置220為複數個輸送輥,但本發明之實施例並不受限於此。As shown in Figure 1, the
當輸送裝置220輸送鋼帶100進入鋼帶清洗系統200時,鋼帶100會先經過上述清洗槽中的第一者,即清洗槽211,以利用清洗槽211中的水來清洗鋼帶100。然後,再依序經過清洗槽212和213,以利用清洗槽212和213來清洗。接著,經過上述清洗槽中的最後一者,即清洗槽214,以利用清洗槽211中的水來清洗鋼帶100。本實施例係使用四個清洗槽211~214來對鋼帶100進行四個階段的清洗,然而本發明之實施例並不受限於使用四個清洗槽。When the
當利用清洗槽211的水來對鋼帶100進行清洗時,鋼帶100上的酸液會被洗回清洗槽211中,如此清洗槽211中的酸液濃度會增加。類似地,當利用清洗槽212的水來對鋼帶100進行清洗時,鋼帶上的酸液會被洗回清洗槽212中,如此清洗槽212中的酸液濃度會增加;當利用清洗槽213的水來對鋼帶100進行清洗時,鋼帶100上的酸液會被洗回清洗槽213中,如此清洗槽213中的酸液濃度會增加;當利用清洗槽214的水來對鋼帶100進行清洗時,鋼帶上的酸液會被洗回清洗槽214中,如此清洗槽214中的酸液濃度會增加。由於鋼帶100係由清洗槽211、212、213和214依序清洗,故清洗槽211的酸液濃度會大於清洗槽212的酸液濃度,清洗槽212的酸液濃度會大於清洗槽213的酸液濃度,清洗槽213的酸液濃度會大於清洗槽214的酸液濃度。When the water in the
當清洗槽中的酸液濃度過多時,會使得鋼帶清洗系統200的清洗效果降低,因此需要對清洗槽211~214進行補水。例如,將乾淨的水補充至清洗槽214,再透過上述梯度控制的方式對清洗槽211~213進行補水。When the acid concentration in the cleaning tank is too high, the cleaning effect of the steel
考慮傳統酸鹼度計(PH計)容易受到清洗槽環境的影響而出現測量失準的問題,且對鋼帶製程影響較大的因素為氯離子濃度,本發明實施例採用氯離子濃度偵測計來取代傳統PH計。氯離子濃度偵測計係透過導電度測試來獲得清洗槽中的氯離子濃度。由於酸洗製程係採用鹽酸(HCl)來進行酸洗,故清洗槽中的氯離子濃度也可以代表清洗槽中的酸液濃度。在本實施例中,針對第一個清洗槽211和最後一個清洗槽214設置了第一清洗槽氯離子濃度偵測計230和最後清洗槽氯離子濃度偵測計240,以分別量測第一個清洗槽211和最後一個清洗槽214的氯離子濃度,並根據預設的氯離子濃度閥值來判斷出清洗槽中的酸液濃度是否過高。在本發明之實施例中,當第一個清洗槽211的濃度大於1600ppm和/或最後一個清洗槽214的氯離子濃度大於0ppm時,便會開始進行補水。然而,本發明之實施例並不受限於此。使用者可根據實際需求來調整氯離子濃度的閥值。Considering that traditional pH meters (PH meters) are easily affected by the cleaning tank environment and have measurement inaccuracies, and the factor that has a greater impact on the steel strip manufacturing process is the chloride ion concentration, the embodiment of the present invention uses a chloride ion concentration detection meter. Replace traditional pH meter. The chloride ion concentration detector uses conductivity testing to obtain the chloride ion concentration in the cleaning tank. Since the pickling process uses hydrochloric acid (HCl) for pickling, the chloride ion concentration in the cleaning tank can also represent the acid concentration in the cleaning tank. In this embodiment, a first cleaning tank chloride
在一些實施例中,為了避免前三個清洗槽211~213的酸水殘留在鋼帶100上,在最後一個清洗槽214與最後第二個清洗槽213之間設置有絞乾輥裝置250,以於鋼帶100進入最後一個清洗槽214之前,將鋼帶100上的殘餘酸水絞乾。絞乾輥裝置250可包含至少一對絞乾輥,在本實施例中,絞乾輥裝置250包含兩對絞乾輥,但本發明之實施例並不受限於此。另外,在一些實施例中,為了避免水槽之間的酸水互相影響,水槽之間也可都設有絞乾輥。In some embodiments, in order to prevent the acid water from the first three cleaning
在圖2中,電腦裝置270係用以計算補水量,並控制補水裝置260來對清洗槽214進行補水。在一些實施例中,電腦裝置270可為程控電腦,其係用以控制鋼帶清洗系統200中的各部件來對鋼帶100進行清洗。在一些實施例中,電腦裝置270可由程控電腦獨立出來,僅進行補水量計算步驟,並控制補水裝置260來對清洗槽214進行補水。In FIG. 2 , the
電腦裝置270可獲取第一清洗槽氯離子濃度(從第一清洗槽氯離子濃度偵測計230獲得)、最後清洗槽氯離子濃度(從最後清洗槽氯離子濃度偵測計240獲得)、鋼帶100之鋼帶厚度值以及鋼帶寬度值(由程控電腦提供)、鋼帶100之鋼帶清洗速度(由程控電腦提供)以及絞乾輥裝置250之補償參數(由程控電腦提供)。然後,再根據上述之第一清洗槽氯離子濃度、最後清洗槽氯離子濃度、鋼帶厚度值、鋼帶寬度值、絞乾輥補償參數之值以及鋼帶清洗速度之值(其單位為每分鐘公尺(m/hr)來計算出補水量。接著,再根據計算出的補水量輸出補水訊號至補水裝置260,以控制補水裝置來提供清潔用水至清洗槽214。在一些實施例中,電腦裝置270會先判斷清洗槽中的酸液濃度是否過高,再輸出補水訊號至補水裝置260。The
補水裝置260包含流量控制裝置261和閥門262。流量控制裝置261為一訊號處理器,其可接收電腦裝置270所提供的補水訊號,並據以控制閥門262來提供清潔用水至清洗槽214。The
在一些實施例中,電腦裝置270係根據下列方程式來計算出補水量:
Q
4=(Q
CSP+Q
CL1+Q
CL4+Q
TH+Q
WD)*R
ref(1)
其中,Q
4為電腦裝置270計算出的補水量,單位為每小時立方公尺(m
3/hr);Q
CSP為根據鋼帶清洗速度所計算出的速度相關補水量,單位為每小時立方公尺(m
3/hr);Q
CL1為根據第一清洗槽氯離子濃度所計算出的第一清洗槽補水量,單位為每小時立方公尺(m
3/hr);Q
CL4為根據最後清洗槽氯離子濃度所計算出的最後清洗槽補水量,單位為每小時立方公尺(m
3/hr);Q
TH為根據鋼帶厚度相關補水量,單位為每小時立方公尺(m
3/hr);Q
WD為根據鋼帶寬度值所計算出的鋼帶寬度相關補水量,單位為每小時立方公尺(m
3/hr);R
ref為絞乾輥補償參數之值,其由絞乾輥裝置250的開度和/或程控參數來決定。
In some embodiments, the
請同時參照圖3~7,其係繪示根據本發明實施例之補水參數與鋼帶清洗速度、第一清洗槽氯離子濃度、最後清洗槽氯離子濃度、鋼帶厚度值以及鋼帶寬度值的關係曲線,其中補水參數為補水量的參數。在本發明之實施例中,上述之補水量Q CSP、Q CL1、Q CL4、Q TH、Q WD係根據預設的補水曲線關係來計算獲得。例如,如圖3所示,補水量Q CSP的補水參數係隨著鋼帶清洗速度的增加而跟著增加。又例如,如圖4所示,當第一清洗槽氯離子濃度超過閥值時,補水量Q CL1的補水參數係隨著第一清洗槽氯離子濃度迅速增加。再例如,如圖5所示,當最後清洗槽氯離子濃度超過閥值時,補水量Q CL4的補水參數係隨著最後清洗槽氯離子濃度迅速增加,其中當最後清洗槽氯離子濃度的值接近1ppm時,補水參數的上升速度會下降。再例如,如圖6所示,當鋼帶厚度值超過預設厚度閥值(例如,1500)時,補水量Q TH的補水參數係隨著為鋼帶厚度值的增加而跟著減少。再例如,如圖7所示,當鋼帶寬度值超過預設寬度閥值(例如,15000)時,補水量Q WD的補水參數係隨著為鋼帶寬度值的增加而跟著增加。值一提的是,在鋼帶的清洗過程中,鋼帶寬度值和和厚度值都是固定的,而鋼帶清洗速度也大致為定值。 Please refer to Figures 3 to 7 at the same time, which illustrate water replenishment parameters and steel strip cleaning speed, chloride ion concentration in the first cleaning tank, chloride ion concentration in the last cleaning tank, steel strip thickness value and steel strip width value according to the embodiment of the present invention. The relationship curve, in which the water replenishment parameter is the parameter of the water replenishment amount. In the embodiment of the present invention, the above-mentioned water replenishment amounts Q CSP , Q CL1 , Q CL4 , Q TH , and Q WD are calculated according to the preset water replenishment curve relationship. For example, as shown in Figure 3, the water replenishment amount Q CSP 's water replenishment parameter increases with the increase of the steel strip cleaning speed. For another example, as shown in Figure 4, when the chloride ion concentration in the first cleaning tank exceeds the threshold, the water replenishment parameter Q CL1 increases rapidly with the chloride ion concentration in the first cleaning tank. For another example, as shown in Figure 5, when the chloride ion concentration in the last cleaning tank exceeds the threshold, the water replenishment parameter Q CL4 increases rapidly with the chloride ion concentration in the last cleaning tank. When the value of the chloride ion concentration in the last cleaning tank When it is close to 1ppm, the rising speed of hydration parameters will decrease. For another example, as shown in Figure 6, when the steel strip thickness exceeds the preset thickness threshold (for example, 1500), the water replenishment parameter Q TH decreases as the steel strip thickness increases. For another example, as shown in Figure 7, when the steel strip width value exceeds the preset width threshold (for example, 15000), the water replenishment parameter QWD increases as the steel strip width value increases. It is worth mentioning that during the cleaning process of the steel strip, the width and thickness of the steel strip are fixed, and the cleaning speed of the steel strip is also roughly fixed.
請再回到圖2,在鋼帶清洗系統200的出口處另設置有絞乾輥以及噴水裝置280。出口處的絞乾輥係用防止鋼帶清洗系統200所輸出的鋼帶100帶有過多的水分,而影響到後端製程。然而,絞乾輥可能會將鋼帶100絞得過乾而形成乾摩擦,使得鋼帶100產生瑕疵。為了防止乾摩擦,鋼帶清洗系統200設置有噴水裝置280來對鋼帶100進行噴水,以避免鋼帶100過於乾燥。噴水裝置280的噴水量也是由電腦裝置270計算而提供。如此,上式(1)可改寫為下式:
Q
4=Q
C+(Q
CSP+Q
CL1+Q
CL4+Q
TH+Q
WD)*R
ref(2)
其中,Q
C為噴水裝置280所提供的噴水量。
Please return to Figure 2. A wringing roller and a
請參照圖8,其係繪示根據本發明實施例之鋼帶清洗方法800的流程示意圖。鋼帶清洗方法800係適用於上述的鋼帶清洗系統200。在鋼帶清洗方法800中,首先進行步驟810,以提供上述之清洗槽211~214。然後,進行步驟820,以根據預設的鋼帶清洗速度來利用輸送裝置220輸送鋼帶100,以使鋼帶100經過清洗槽211~214,而利用清洗槽211~214中的清洗用水來清洗鋼帶100。在清洗的過程中,可利用絞乾輥裝置250來對鋼帶100進行絞乾步驟。接著,進行步驟830,以利用第一清洗槽氯離子濃度偵測計230來量測第一個清洗槽211之一第一清洗槽氯離子濃度值,以及利用最後清洗槽氯離子濃度偵測計240,來量測最後一個清洗槽214之一最後清洗槽氯離子濃度值。然後,進行步驟840,以根據第一清洗槽氯離子濃度、最後清洗槽氯離子濃度、鋼帶厚度值、鋼帶寬度值、絞乾輥裝置之補償參數之值以及鋼帶清洗速度之值來計算出補水量。接著,進行步驟850,根據計算出的補水量來產生補水訊號,並將補水訊號輸出至補水裝置260,以控制補水裝置260來提供清潔用水至最後一個清洗槽214。Please refer to FIG. 8 , which is a schematic flow chart of a steel
由上述說明可知本發明實施例之鋼帶清洗系統200與鋼帶清洗方法800採用了第一清洗槽氯離子濃度、最後清洗槽氯離子濃度、鋼帶厚度值、鋼帶寬度值、絞乾輥裝置之補償參數值以及鋼帶清洗速度來計算清洗槽的補充水量,故本發明實施例之鋼帶清洗系統200與鋼帶清洗方法800可較先前技術更為準確地對清洗槽進行補水,避免補水量不足或過多的問題。From the above description, it can be seen that the steel
雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明的精神和範圍內,當可作些許的更動與潤飾,故本發明的保護範圍當視後附的申請專利範圍所界定者為準。Although the present invention has been disclosed above through embodiments, they are not intended to limit the present invention. Anyone with ordinary knowledge in the technical field may make some modifications and modifications without departing from the spirit and scope of the present invention. Therefore, The protection scope of the present invention shall be determined by the appended patent application scope.
100:鋼帶
200:鋼帶清洗系統
211~214:清洗槽
220:輸送裝置
230:第一清洗槽氯離子濃度偵測計
240:最後清洗槽氯離子濃度偵測計
250:絞乾輥裝置
260:補水裝置
261:流量控制裝置
262:閥門
270:電腦裝置
280:噴水裝置
800:鋼帶清洗方法
810~850:步驟100:Steel strip
200: Steel
[圖1] 係繪示根據本發明實施例之鋼帶的俯視圖。 [圖2] 係繪示根據本發明實施例之鋼帶清洗系統的架構示意圖。 [圖3]至[圖7]係繪示根據本發明實施例之補水參數與鋼帶清洗速度、第一清洗槽氯離子濃度、最後清洗槽氯離子濃度、鋼帶厚度值以及鋼帶寬度值的關係曲線。 [圖8] 係繪示根據本發明實施例之鋼帶清洗方法的流程示意圖。 [Fig. 1] is a top view of a steel strip according to an embodiment of the present invention. [Fig. 2] is a schematic structural diagram of a steel belt cleaning system according to an embodiment of the present invention. [Figure 3] to [Figure 7] illustrate the water replenishment parameters and steel strip cleaning speed, chloride ion concentration in the first cleaning tank, chloride ion concentration in the last cleaning tank, steel strip thickness value and steel strip width value according to the embodiment of the present invention. relationship curve. [Fig. 8] is a schematic flowchart illustrating a steel strip cleaning method according to an embodiment of the present invention.
國內寄存資訊(請依寄存機構、日期、號碼順序註記) 無 國外寄存資訊(請依寄存國家、機構、日期、號碼順序註記) 無 Domestic storage information (please note in order of storage institution, date and number) without Overseas storage information (please note in order of storage country, institution, date, and number) without
200:鋼帶清洗系統 200: Steel belt cleaning system
211~214:清洗槽 211~214: Cleaning tank
230:第一清洗槽氯離子濃度偵測計 230: Chloride ion concentration detector in the first cleaning tank
240:最後清洗槽氯離子濃度偵測計 240: Chloride ion concentration detector for final cleaning tank
250:絞乾輥裝置 250: Wringing roller device
260:補水裝置 260:Hydration device
261:流量控制裝置 261:Flow control device
262:閥門 262:Valve
270:電腦裝置 270:Computer device
280:噴水裝置 280:Water spray device
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW112108388A TWI827478B (en) | 2023-03-08 | 2023-03-08 | Clean system and clean method for a steel strip |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW112108388A TWI827478B (en) | 2023-03-08 | 2023-03-08 | Clean system and clean method for a steel strip |
Publications (1)
Publication Number | Publication Date |
---|---|
TWI827478B true TWI827478B (en) | 2023-12-21 |
Family
ID=90053536
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW112108388A TWI827478B (en) | 2023-03-08 | 2023-03-08 | Clean system and clean method for a steel strip |
Country Status (1)
Country | Link |
---|---|
TW (1) | TWI827478B (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007031791A (en) * | 2005-07-28 | 2007-02-08 | Nisshin Steel Co Ltd | Cleaning method for pickled steel strip in continuous pickling treatment line and cleaning apparatus |
KR100953138B1 (en) * | 2005-02-26 | 2010-04-16 | 에스엠에스 지마크 악티엔게젤샤프트 | Method and device for cleaning a metal strip |
CN104117510A (en) * | 2013-04-27 | 2014-10-29 | 宝山钢铁股份有限公司 | Device and method for cleaning surface of silicon steel |
-
2023
- 2023-03-08 TW TW112108388A patent/TWI827478B/en active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100953138B1 (en) * | 2005-02-26 | 2010-04-16 | 에스엠에스 지마크 악티엔게젤샤프트 | Method and device for cleaning a metal strip |
JP2007031791A (en) * | 2005-07-28 | 2007-02-08 | Nisshin Steel Co Ltd | Cleaning method for pickled steel strip in continuous pickling treatment line and cleaning apparatus |
CN104117510A (en) * | 2013-04-27 | 2014-10-29 | 宝山钢铁股份有限公司 | Device and method for cleaning surface of silicon steel |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR100527788B1 (en) | Continuous Pickling Method and Continuous Pickling Device | |
JP3074366B2 (en) | Processing equipment | |
US5472516A (en) | Process and apparatus for semiconductor device fabrication | |
JP3374844B2 (en) | Acid concentration measurement and automatic control method and device | |
KR102135000B1 (en) | Substrate treating device and substrate treating method | |
TWI827478B (en) | Clean system and clean method for a steel strip | |
US6494961B2 (en) | Method of controlling solution concentration in strip cleaning line | |
TWI679696B (en) | Substrate processing device and substrate processing method | |
JP2003277998A (en) | Plating apparatus, and method for controlling plating solution using the same | |
WO2022074814A1 (en) | Analysis system and management system, and analysis method and analysis program | |
KR101518640B1 (en) | Method for determining input flow of fresh acid in pickling process | |
JP6290691B2 (en) | Method for determining the amount of pickling solution input | |
JP2020087985A (en) | Substrate processing apparatus and substrate processing method | |
JP3626360B2 (en) | Substrate processing apparatus and method | |
CN215865787U (en) | Automatic detection mechanism for squeezing roller between pickling tanks | |
JP2003342764A (en) | Pickling device and pickling method | |
JPH0754175A (en) | Method for controlling acid concentration of pickling equipment for steel strip | |
JPH01215990A (en) | Method for controlling acid concentration of pickling tank and circulation tank | |
JP2020072189A (en) | Substrate processing apparatus | |
JP3710676B2 (en) | Substrate processing method and substrate processing apparatus | |
JP3819668B2 (en) | Substrate processing method and substrate processing apparatus | |
JP2005248272A (en) | Method for controlling concentration of hydrofluoric acid in nitric-hydrofluoric acid pickling liquid for stainless steel strip | |
JPS5814836A (en) | Controlling method for correction of oxidation by testing of test piece in automatic developing machine | |
JPH08160629A (en) | Developing device for photosensitive lithographic printing plate | |
JPH052951B2 (en) |