TWI626978B - Fluid filter abnormality detecting method and fluid filter abnormality detecting system - Google Patents

Fluid filter abnormality detecting method and fluid filter abnormality detecting system Download PDF

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TWI626978B
TWI626978B TW105135537A TW105135537A TWI626978B TW I626978 B TWI626978 B TW I626978B TW 105135537 A TW105135537 A TW 105135537A TW 105135537 A TW105135537 A TW 105135537A TW I626978 B TWI626978 B TW I626978B
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fluid
fluid filter
filter
pressure difference
impurity
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TW201817487A (en
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程聖傑
顧詠元
林克衛
姜嘉瑞
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財團法人車輛研究測試中心
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Abstract

本發明提供一種流體濾清器異常偵測方法,其係藉綜合判斷流體濾清器之幾何型態、流體之物理特性、流體濾清器之孔隙率、雜質密度、測量得到之流體流量及壓力差而建立流體濾清器之一運作模型,並透過此運作模型測得流體濾清器內之初始雜質累積量。再者,本發明更透過卡爾曼估測器取得流體濾清器內之雜質於一估測時間之雜質累積量,並將此雜質累積量與一預設值比對,藉此判斷流體濾清器是否運作異常。藉此,本發明之流體濾清器異常偵測方法透過實驗證明具有高的準確度。 The invention provides a fluid filter abnormality detecting method, which comprehensively judges the geometry of the fluid filter, the physical properties of the fluid, the porosity of the fluid filter, the impurity density, the measured fluid flow rate and the pressure Poorly, an operational model of the fluid filter is established, and the initial impurity accumulation in the fluid filter is measured through the operational model. Furthermore, the present invention further obtains the impurity accumulation amount of the impurity in the fluid filter at an estimated time through the Kalman estimator, and compares the accumulated amount of the impurity with a preset value, thereby judging the fluid filtration. Whether the device is operating abnormally. Thereby, the fluid filter abnormality detecting method of the present invention proves to have high accuracy through experiments.

Description

流體濾清器異常偵測方法及流體濾清器異常偵測系統 Fluid filter abnormality detecting method and fluid filter abnormality detecting system

本發明係關於一種流體濾清器異常偵測方法及流體濾清器異常偵測系統;更特別言之,本發明係關於一種同時結合流體流量偵測及流體濾清器之壓力差偵測,而可動態預測雜質累積量之流體濾清器異常偵測方法及流體濾清器異常偵測系統。 The present invention relates to a fluid filter anomaly detection method and a fluid filter anomaly detection system; more particularly, the present invention relates to a pressure difference detection that simultaneously combines fluid flow detection and fluid filter. The fluid filter anomaly detection method and the fluid filter anomaly detection system capable of dynamically predicting the accumulation of impurities.

一般而言,流體濾清器係作為過濾雜質之用,依照其使用類型大致可區分為液體濾清器及氣體濾清器等。於一車輛載具中,通常配備有例如空氣濾清器、機油濾清器、燃油濾清器、自動變速箱油濾清器及室內空調濾清器等多種流體濾清器。目前基於環保節能需求,柴油車輛日益受到重視;而柴油車輛之驅動引擎,係使用電控共軌式柴油噴射系統,其需具備高噴油壓力及高霧化效果;因此,對於燃油濾清器的過濾精度與效率具有高度重視與要求,是故燃油濾清器扮演重要角色。燃油濾清器主要用途係為過濾燃油系統內部雜質,而燃油 系統內部雜質可能來自加油站油品本身的品質純度、加油站的油槽清潔度以及車輛油箱因長期使用的溶出物質等。 In general, fluid filters are used for filtering impurities, and can be roughly classified into liquid filters and gas filters depending on the type of use. In a vehicle vehicle, a plurality of fluid filters such as an air cleaner, an oil filter, a fuel filter, an automatic transmission oil filter, and an indoor air conditioner filter are usually provided. At present, based on environmental protection and energy saving demand, diesel vehicles are receiving more and more attention; while diesel engine driving engines use electronically controlled common rail diesel injection systems, which require high injection pressure and high atomization effect; therefore, for fuel filters The filtration accuracy and efficiency are highly valued and required, so the fuel filter plays an important role. The main purpose of the fuel filter is to filter the internal impurities of the fuel system, while the fuel Impurities in the system may come from the quality purity of the gas station itself, the cleanliness of the tank at the gas station, and the dissolution of the vehicle's fuel tank due to long-term use.

大致而言,流體濾清器係藉由其濾材(濾芯)進行過濾。由於雜質將隨時間而累積,流體濾清器將隨使用時間增長而逐漸阻塞,此將影響油路流量及油品品質。因此,車廠均建議車主定期更換流體濾清器。但由於各車輛載具之行車狀況、使用油品種類、品質及使用環境皆有所差異,提高流體濾清器阻塞時間點預測之困難度,過早更換則造成保養成本增加,過晚更換則導致故障風險提高。 In general, a fluid filter is filtered by its filter material (filter element). As the impurities will accumulate over time, the fluid filter will gradually block as the time of use increases, which will affect the oil flow and oil quality. Therefore, the car manufacturer recommends that the owner change the fluid filter regularly. However, due to differences in driving conditions, oil types, quality and usage environment of each vehicle, it is difficult to predict the timing of fluid filter blocking. Premature replacement will result in increased maintenance costs. This leads to an increased risk of failure.

習知技術係透過判斷流體濾清器流體入口與流體出口壓力差的改變,判斷濾芯阻塞壓差點,並啟動預警機制提醒使用者。上述方式於流體流量穩定狀態下可獲得良好結果。然而,車輛載具行駛為動態,此造成流體流量的不穩定變化,而使壓力差亦無法穩定;壓力差不穩定將使預警機制啟動時機無法準確確定。 The prior art technique determines the filter block pressure difference point by judging the change of the fluid filter fluid inlet and the fluid outlet pressure difference, and initiates an early warning mechanism to alert the user. The above method can obtain good results in a steady state of fluid flow. However, the vehicle vehicle travels dynamically, which causes an unstable change in fluid flow, and the pressure difference cannot be stabilized; the unstable pressure difference will make the timing of the early warning mechanism unable to be accurately determined.

因此,流體濾清器需要更精確的判斷更換時機,適時提醒車主更換新品,確保車輛載具於最佳效率與安全條件下行駛。 Therefore, the fluid filter needs to be more accurate in judging the timing of replacement, promptly reminding the owner to replace the new product, and ensuring that the vehicle is driven under optimal efficiency and safety conditions.

基於上述,市場期待發展一種能準確判斷流體濾清器是否運作異常之方法及系統,並可即時通知使用者更換新品時機的新技術,且其技術重要性也逐漸提高。 Based on the above, the market expects to develop a method and system that can accurately determine whether the fluid filter is operating abnormally, and can immediately notify the user of new technology for replacing the new product timing, and its technical importance is gradually improved.

本發明係提供一種流體濾清器異常偵測方法。依 據測得之流體流量及壓力差,並一併考量流體濾清器之幾何型態、流體之物理特性、流體濾清器之孔隙率及雜質密度等參數、建立流體濾清器之運作模型。由此運作模型可取得流體濾清器內之雜質累積量,並透過卡爾曼估測器可預測雜質累積量隨時間之變化。藉此,本發明的流體濾清器異常偵測方法具有高的準確率。 The invention provides a fluid filter anomaly detection method. according to According to the measured fluid flow and pressure difference, together with the geometry of the fluid filter, the physical properties of the fluid, the porosity of the fluid filter and the impurity density, the operational model of the fluid filter is established. The operating model can obtain the accumulation of impurities in the fluid filter and predict the change of impurity accumulation over time through the Kalman estimator. Thereby, the fluid filter abnormality detecting method of the present invention has high accuracy.

為達上述目的,於一實施例中,本發明提供一流體濾清器異常偵測方法,其步驟包含:偵測一流體濾清器內之一流體之一流量;偵測流體濾清器內之一壓力差;依據流體濾清器之幾何型態、流體之物理特性、流體濾清器之孔隙率、一雜質密度、流量及壓力差建立流體濾清器之一運作模型;透過運作模型取得一初始雜質累積量;透過一卡爾曼估測器,依據初始雜質累積量及一初始壓力差,估測流體濾清器內之雜質隨時間累積之一變化狀態;依據變化狀態取得流體濾清器內之雜質於一估測時間之一雜質累積量,並將雜質累積量與一預設值比對,以便判斷流體濾清器是否運作異常。 To achieve the above objective, in one embodiment, the present invention provides a fluid filter anomaly detection method, the method comprising: detecting a flow of a fluid in a fluid filter; detecting a fluid filter One pressure difference; establishes a working model of the fluid filter according to the geometry of the fluid filter, the physical properties of the fluid, the porosity of the fluid filter, an impurity density, the flow rate and the pressure difference; An initial impurity accumulation amount; through a Kalman estimator, estimating a state of accumulation of impurities in the fluid filter over time according to an initial impurity accumulation amount and an initial pressure difference; obtaining a fluid filter according to the change state The impurity inside is used to estimate the amount of impurity accumulation in one time, and the impurity accumulation amount is compared with a preset value to determine whether the fluid filter operates abnormally.

上述流體濾清器異常偵測方法中,流體可為一燃油、一機油或一自動變速箱油。壓力差為流體流經流體濾清器之一流體入口及流體濾清器之一流體出口所形成之壓力差值,且壓力差包含一空殼壓力差、一濾芯壓力差以及一雜質壓力差。 In the above fluid filter abnormality detecting method, the fluid may be a fuel oil, an oil or an automatic transmission oil. The pressure difference is a pressure difference formed by the fluid flowing through one of the fluid inlet of the fluid filter and one of the fluid outlets of the fluid filter, and the pressure difference includes a void pressure difference, a filter pressure difference, and an impurity pressure difference.

上述流體濾清器異常偵測方法中,流體濾清器之孔隙率包含一空殼孔隙率、一濾芯孔隙率以及一雜質孔隙率。流體濾清器之幾何型態包含流體濾清器之一截面積、一空殼厚度、一濾芯厚度以及一雜質厚度。流體之物理特性包含流體之 一黏滯係數。 In the above fluid filter abnormality detecting method, the porosity of the fluid filter includes a void porosity, a filter porosity, and an impurity porosity. The geometry of the fluid filter includes a cross-sectional area of the fluid filter, a void thickness, a filter thickness, and an impurity thickness. The physical properties of the fluid include fluid A viscosity coefficient.

上述流體濾清器異常偵測方法中,流體濾清器之運作模型係可以下列關係式表示: 其中m為空氣濾清器內之雜質累積量,△P為壓力差,μ為流體黏滯係數,Q為流體之流量,A為流體濾清器之截面積,κ b 為空殼孔隙率,κ f 為濾芯孔隙率,κ p 為雜質孔隙率,ρ p 為雜質密度,L b 為空殼厚度,L f 為濾芯厚度。空殼孔隙率κ b 可透過對複數組流量之數值進行二次線性迴歸而得到。 In the above fluid filter anomaly detection method, the operational model of the fluid filter can be expressed by the following relationship: Where m is the cumulative amount of impurities in the air filter, Δ P is the pressure difference, μ is the fluid viscosity coefficient, Q is the flow rate of the fluid, A is the cross-sectional area of the fluid filter, and κ b is the porosity of the empty shell. κ f is the filter core porosity, κ p is the impurity porosity, ρ p is the impurity density, L b is the empty shell thickness, and L f is the filter core thickness. The porosity of the shell κ b can be obtained by quadratic linear regression of the values of the complex array flow.

上述之流體濾清器異常偵測方法中,於判斷流體濾清器運作異常後,可發出一警示音、一警示光或一警示訊息。 In the above fluid filter abnormality detecting method, after the fluid filter is abnormally operated, a warning sound, a warning light or a warning message may be issued.

於另一實施例中,本發明提供一種流體濾清器異常偵測系統,其包含一流體濾清器、一流量偵測器、一壓差偵測器、一分析器、一卡爾曼估測器以及一處理器。流體濾清器內流動有一流體。流量偵測器係偵測流體之一流量;壓差偵測器係偵測流體濾清器內之一壓力差。分析器係依據流體濾清器之幾何型態、流體之物理特性、流體濾清器之孔隙率、一雜質密度、流量及壓力差建立流體濾清器之一運作模型,並透過運作模型取得一初始雜質累積量。卡爾曼估測器係依據初始雜質累積量及一初始壓力差,估測流體濾清器內之雜質隨時間累積之一變化狀態。處理器係依據變化狀態取得流體濾清器內之雜質於一估測時間之一雜質累積量,並將雜質累積量與一預設值比對,以便判斷流體濾清器是否運作異常。 In another embodiment, the present invention provides a fluid filter anomaly detection system including a fluid filter, a flow detector, a differential pressure detector, an analyzer, and a Kalman estimation. And a processor. A fluid flows through the fluid filter. The flow detector detects the flow of one of the fluids; the differential pressure detector detects a pressure difference within the fluid filter. The analyzer establishes an operational model of the fluid filter based on the geometry of the fluid filter, the physical properties of the fluid, the porosity of the fluid filter, an impurity density, the flow rate, and the pressure difference, and obtains a model through the operational model. Initial impurity accumulation. The Kalman estimator estimates the state of accumulation of impurities in the fluid filter over time based on the initial impurity accumulation and an initial pressure difference. The processor obtains an impurity accumulation amount of the impurity in the fluid filter at an estimated time according to the change state, and compares the impurity accumulation amount with a preset value to determine whether the fluid filter operates abnormally.

上述流體濾清器異常偵測系統中,流體可為一燃油、一機油或一自動變速箱油。壓力差包含一空殼壓力差、一濾芯壓力差以及一雜質壓力差。另外,流體濾清器係可配置於一航海載具、一陸行載具或一飛行載具。 In the above fluid filter abnormality detecting system, the fluid may be a fuel oil, an oil or an automatic transmission oil. The pressure difference includes a shell pressure difference, a filter pressure difference, and an impurity pressure difference. Additionally, the fluid filter can be disposed on a marine vehicle, a land vehicle, or a flying vehicle.

上述流體濾清器異常偵測系統中,流體濾清器之運作模型係可以下列關係式表示: 其中m為空氣濾清器內之雜質累積量,△P為壓力差,μ為流體黏滯係數,Q為流體之流量,A為流體濾清器之截面積,κ b 為空殼孔隙率,κ f 為濾芯孔隙率,κ p 為雜質孔隙率,ρ p 為雜質密度,L b 為空殼厚度,L f 為濾芯厚度。 In the above fluid filter anomaly detection system, the operational model of the fluid filter can be expressed by the following relationship: Where m is the cumulative amount of impurities in the air filter, Δ P is the pressure difference, μ is the fluid viscosity coefficient, Q is the flow rate of the fluid, A is the cross-sectional area of the fluid filter, and κ b is the porosity of the empty shell. κ f is the filter core porosity, κ p is the impurity porosity, ρ p is the impurity density, L b is the empty shell thickness, and L f is the filter core thickness.

S101~S106‧‧‧步驟 S101~S106‧‧‧Steps

100‧‧‧流體濾清器 100‧‧‧Fluid filter

110‧‧‧濾芯 110‧‧‧ filter

120‧‧‧空殼 120‧‧‧ empty shell

130‧‧‧單向閥 130‧‧‧check valve

130a‧‧‧流體入口 130a‧‧‧ fluid inlet

130b‧‧‧流體出口 130b‧‧‧Fluid outlet

130c‧‧‧環形通道 130c‧‧‧ annular passage

200‧‧‧流量偵測器 200‧‧‧Flow detector

300‧‧‧壓差偵測器 300‧‧‧ Differential Pressure Detector

400‧‧‧分析器 400‧‧‧Analyzer

500‧‧‧卡爾曼估測器 500‧‧‧Kalman estimator

600‧‧‧處理器 600‧‧‧ processor

F‧‧‧流體 F‧‧‧ fluid

第1圖係繪示依據本發明一實施例之流體濾清器異常偵測方法流程示意圖;第2圖係繪示依據本發明一實施例之流體濾清器異常偵測系統示意圖;第3圖係繪示第2圖中之流體濾清器運作狀態示意圖;第4圖係繪示於本發明一實施例中,使用卡爾曼估測器預估流體濾清器內之雜質隨時間累積之變化狀態示意圖;第5A圖係繪示於一流體(油品D100)中,預測與實際壓力差隨流體流量之變化圖; 第5B圖係繪示於另一流體(油品B100)中,預測與實際壓力差隨流體流量之變化圖;第6圖係繪示於一含有雜質之流體(油品B20)中,預測與實際壓力差隨流體流量之變化圖;第7圖係繪示於流體流量2l/min條件下,模擬雜質累積量由1g到6g時,預測與實際壓力差隨時間變化圖;第8圖係繪示於流體流量2l/min條件下,模擬雜質累積量由1g到6g時,預測與實際雜質累積量隨時間變化圖;第9圖係繪示於流體流量2l/min條件下,模擬雜質累積量由1g到6g時,預測與實際之雜質濃度隨時間變化圖;以及第10圖係繪示於流體流量2l/min條件下,模擬雜質累積量由1g到6g時,預測與實際雜質累積量之誤差變化圖。 1 is a flow chart showing a fluid filter abnormality detecting method according to an embodiment of the present invention; and FIG. 2 is a schematic view showing a fluid filter abnormality detecting system according to an embodiment of the present invention; FIG. 4 is a schematic diagram showing the operation state of the fluid filter in FIG. 2; FIG. 4 is a schematic diagram of estimating the accumulation of impurities in the fluid filter over time using a Kalman estimator. State diagram; Figure 5A is a plot of the predicted and actual pressure difference as a function of fluid flow in a fluid (oil D100); Figure 5B is shown in another fluid (oil B100), the predicted and actual pressure difference as a function of fluid flow; Figure 6 is shown in a fluid containing impurities (oil B20), prediction and Figure 5 shows the change of the actual pressure difference with the fluid flow rate; Figure 7 shows the change of the predicted and actual pressure difference with time when the simulated impurity accumulation is from 1g to 6g under the condition of fluid flow rate 2l/min; It is shown in the case of fluid flow rate 2l/min, when the simulated impurity accumulation amount is from 1g to 6g, the predicted and actual impurity accumulation amount changes with time; the ninth figure shows the simulated impurity accumulation amount under the condition of fluid flow rate 2l/min. From 1g to 6g, the predicted and actual impurity concentration changes with time; and Figure 10 is shown in the fluid flow rate of 2l / min, the simulated impurity accumulation from 1g to 6g, the predicted and actual impurity accumulation Error change graph.

以下將參照圖式說明本發明之複數個實施例。為明確說明起見,許多實務上的細節將在以下敘述中一併說明。然而,應瞭解到,這些實務上的細節不應用以限制本發明。也就是說,在本發明部分實施例中,這些實務上的細節是非必要的。此外,為簡化圖式起見,一些習知慣用的結構與元件在圖式中將以簡單示意的方式繪示之。 Hereinafter, a plurality of embodiments of the present invention will be described with reference to the drawings. For the sake of clarity, many practical details will be explained in the following description. However, it should be understood that these practical details are not intended to limit the invention. That is, in some embodiments of the invention, these practical details are not necessary. In addition, some of the conventional structures and elements are shown in the drawings in a simplified schematic manner in order to simplify the drawings.

請參照第1圖,其係繪示依據本發明一實施例之流體濾清器異常偵測方法流程示意圖。本發明所提出的流體濾清器異常偵測方法大致包含下列步驟。 Please refer to FIG. 1 , which is a flow chart showing a method for detecting an abnormality of a fluid filter according to an embodiment of the invention. The fluid filter anomaly detection method proposed by the present invention generally comprises the following steps.

步驟S101,偵測一流體濾清器內之一流體之一流量。 Step S101, detecting a flow rate of one of the fluids in the fluid filter.

步驟S102,偵測此流體濾清器內之一壓力差。 Step S102, detecting a pressure difference in the fluid filter.

步驟S103,依據此流體濾清器之幾何型態、流體之物理特性、此流體濾清器之孔隙率、雜質密度、流量及壓力差建立此流體濾清器之一運作模型。 Step S103, establishing an operational model of the fluid filter according to the geometry of the fluid filter, the physical properties of the fluid, the porosity of the fluid filter, the impurity density, the flow rate, and the pressure difference.

步驟S104,透過運作模型取得一初始雜質累積量。 In step S104, an initial impurity accumulation amount is obtained through the operation model.

步驟S105,透過一卡爾曼估測器,依據初始雜質累積量及一初始壓力差,估測此流體濾清器內之雜質隨時間累積之一變化狀態。 Step S105, estimating, by a Kalman estimator, a state of change of impurities in the fluid filter over time according to an initial impurity accumulation amount and an initial pressure difference.

步驟S106,依據變化狀態取得此流體濾清器內之雜質於一估測時間之一雜質累積量,並將雜質累積量與一預設值比對,以便判斷此流體濾清器是否運作異常。 Step S106: Obtain an impurity accumulation amount of the impurity in the fluid filter at an estimated time according to the change state, and compare the impurity accumulation amount with a preset value to determine whether the fluid filter operates abnormally.

於一例中,本發明提供運行上述流體濾清器異常偵測方法之一流體濾清器異常偵測系統。請一併參照第2圖及第3圖。第2圖係繪示依據本發明一實施例之流體濾清器系統示意圖;第3圖係繪示第2圖中之流體濾清器100運作示意圖。流體濾清器異常偵測系統大致包含一流體濾清器100、一壓差偵測器200以及一流量偵測器300、一分析器400、一卡爾曼估測器500以及一處理器600。 In one example, the present invention provides a fluid filter anomaly detection system that operates one of the fluid filter anomaly detection methods described above. Please refer to Figure 2 and Figure 3 together. 2 is a schematic view showing a fluid filter system according to an embodiment of the present invention; and FIG. 3 is a schematic view showing the operation of the fluid filter 100 in FIG. The fluid filter anomaly detection system generally includes a fluid filter 100, a differential pressure detector 200 and a flow detector 300, an analyzer 400, a Kalman estimator 500, and a processor 600.

流體濾清器100之運作,大致而言,如第3圖所示,流體F進入單向閥130之流體入口130a,並為濾芯110所過濾。基於此實施例,濾芯110為圓柱狀對稱,因此流體F亦部 分通過環形通道130c而流入濾芯110,以便使流體F得到完整過濾效果。過濾後,流體F由單向閥130之流體出口130b流出。 Operation of Fluid Filter 100, generally, as shown in Figure 3, fluid F enters fluid inlet 130a of one-way valve 130 and is filtered by filter element 110. Based on this embodiment, the filter element 110 is cylindrically symmetrical, so the fluid F is also part The flow passes through the annular passage 130c into the filter element 110 to provide a complete filtering effect for the fluid F. After filtration, the fluid F flows out of the fluid outlet 130b of the one-way valve 130.

流量偵測器300用以測得流體濾清器100內流體F之流量。一般而言,若為一車輛載具,流量偵測器300於車輛載具出廠時即已裝配,無須額外加裝,可節省額外成本。另外,除汽、機車等陸行載具外,流體濾清器100亦可配置於航海載具或飛行載具中。 The flow detector 300 is used to measure the flow of the fluid F in the fluid filter 100. In general, if it is a vehicle carrier, the traffic detector 300 is assembled when the vehicle carrier is shipped from the factory, and no additional installation is required, which can save additional cost. In addition, the fluid filter 100 may be disposed in a marine carrier or a flight carrier in addition to a land vehicle such as a steam or a locomotive.

壓差偵測器200則用以測得流體濾清器100內之壓力差。此壓力差係為流體F通過流體入口130a,再由流體出口130b流出所形成之壓力差值。 The differential pressure detector 200 is used to measure the pressure difference within the fluid filter 100. This pressure difference is the difference in pressure formed by the fluid F passing through the fluid inlet 130a and then flowing out of the fluid outlet 130b.

分析器400係用以同時接收流體F之流量及壓力差,並另外取得流體濾清器100之幾何型態、流體F之物理特性、流體濾清器100之孔隙率、雜質密度等參數以建立流體濾清器100之運作模型。分析器400於建立流體濾清器100之運作模型後,可依據實際狀況取得一初始雜質累積量。 The analyzer 400 is configured to simultaneously receive the flow rate and the pressure difference of the fluid F, and additionally obtain the parameters of the geometry of the fluid filter 100, the physical characteristics of the fluid F, the porosity of the fluid filter 100, the impurity density, and the like to establish The operational model of the fluid filter 100. After the analyzer 400 establishes the operational model of the fluid filter 100, an initial amount of accumulated impurities can be obtained according to actual conditions.

卡爾曼估測器500依據初始雜質累積量及一初始壓力差,估測流體濾清器100內之雜質隨時間累積之一變化狀態。 The Kalman estimator 500 estimates a state in which the impurities in the fluid filter 100 accumulate over time based on the initial impurity accumulation amount and an initial pressure difference.

處理器600依據變化狀態取得流體濾清器100內之雜質於一估測時間之一雜質累積量,並將此雜質累積量與一預設值比對,以便判斷流體濾清器100是否運作異常。於一例中,當雜質累積量超過預設值後,則判斷流體濾清器100運作異常,並發出一警示音、一警示光或一警示訊息以提醒使用者。 The processor 600 obtains an impurity accumulation amount of the impurity in the fluid filter 100 at an estimated time according to the change state, and compares the impurity accumulation amount with a preset value to determine whether the fluid filter 100 operates abnormally. . In one example, when the accumulated amount of impurities exceeds a preset value, it is determined that the fluid filter 100 is abnormally operated, and a warning sound, a warning light or a warning message is issued to remind the user.

上述分析器400、處理器600等,皆指具有邏輯運算功能之電腦裝置,其並具有非暫態之儲存媒介以便儲存運算所需之軟體程式。於其他可能例中,分析器400及處理器600可整合為一多功能電腦裝置或一整合晶片以便精簡體積。 The analyzer 400, the processor 600, and the like all refer to a computer device having a logical operation function, and has a non-transitory storage medium for storing software programs required for the operation. In other possible instances, analyzer 400 and processor 600 can be integrated into a multi-function computer device or an integrated chip to streamline the volume.

上述之流體F,可為一燃油、一機油或一自動變速箱油。於可能實施例中,其餘須經由流體濾清器100過濾之其餘油品種類亦有可能應用於本發明之方法及系統。 The fluid F described above may be a fuel oil, an oil or an automatic transmission fluid. In other embodiments, the remaining oil species that must be filtered via fluid filter 100 are also potentially applicable to the methods and systems of the present invention.

另需提及的是,上述壓力差係包含一空殼壓力差、一濾芯壓力差以及一雜質壓力差。上述流體濾清器之孔隙率係包含一空殼孔隙率、一濾芯孔隙率以及一雜質孔隙率。上述流體濾清器之幾何型態包含流體濾清器之一截面積、一空殼厚度、一濾芯厚度以及一雜質厚度;而上述流體之物理特性包含流體之一黏滯係數。 It should also be mentioned that the above pressure difference comprises a shell pressure difference, a filter element pressure difference and an impurity pressure difference. The porosity of the fluid filter comprises an empty shell porosity, a filter core porosity, and an impurity porosity. The geometry of the fluid filter includes a cross-sectional area of the fluid filter, a void thickness, a filter thickness, and an impurity thickness; and the physical properties of the fluid include a viscosity coefficient of the fluid.

以下續再詳細說明上述各參數之意義,及如何建立流體濾清器之運作模型。首先,假設流體F流經流體濾清器100時,符合下列關係式:△P=△P box +△P filter +△P P (1); 其中,m為流體濾清器內之雜質累積量,△P為壓力差,μ為流體黏滯係數,Q為流體之流量,A為流體濾清器之截面積,κ b 為空殼孔隙率,κ f 為濾芯孔隙率,κ p 為雜質孔隙率,ρ p 為雜質密度,L b 為空殼厚度,L f 為濾芯厚度,L P 為雜質厚度,△P box 為空殼壓力差,△P filter 濾芯壓力差,△P P 為雜質壓力差。 The meaning of each of the above parameters will be described in detail below, and how to establish an operational model of the fluid filter. First, assuming that the fluid F flows through the fluid filter 100, the following relationship is satisfied: Δ P = Δ P box + Δ P filter + Δ P P (1); Where m is the cumulative amount of impurities in the fluid filter, Δ P is the pressure difference, μ is the fluid viscosity coefficient, Q is the flow rate of the fluid, A is the cross-sectional area of the fluid filter, and κ b is the porosity of the shell κ f is the filter porosity, κ p is the impurity porosity, ρ p is the impurity density, L b is the empty shell thickness, L f is the filter thickness, L P is the impurity thickness, Δ P box is the empty shell pressure difference, △ P filter filter pressure difference, △ P P is the impurity pressure difference.

結合上述式(1)至式(5),可得到: Combining the above formulas (1) to (5), we can obtain:

上述式(6)即為流體濾清器100之運作模型,亦即,利用流體濾清器100內之雜質累積量m表示流體濾清器100運作時,流體濾清器100內雜質累積之狀態。需再說明的是,由於流體F係同時流經流體濾清器100之空殼120以及濾芯110而形成雜質累積,故需同時考量空殼狀態、濾芯狀態以及雜質累積狀態三種情況下的不同參數,故有空殼孔隙率κ b ,濾芯孔隙率κ f ,雜質孔隙率κ p ,空殼厚度L b ,濾芯厚度L f ,雜質厚度L P ,空殼壓力差△P box ,濾芯壓力差△P filter ,以及雜質壓力差△P P 的綜合考量。 The above formula (6) is the operational model of the fluid filter 100, that is, the state of accumulation of impurities in the fluid filter 100 when the fluid filter 100 is operated by the impurity accumulation amount m in the fluid filter 100. . It should be noted that since the fluid F flows through the empty shell 120 of the fluid filter 100 and the filter element 110 to form impurities, it is necessary to consider different parameters of the empty shell state, the filter state, and the impurity accumulation state. Therefore, there is void porosity κ b , filter porosity κ f , impurity porosity κ p , empty shell thickness L b , filter thickness L f , impurity thickness L P , empty shell pressure difference Δ P box , filter pressure difference △ P filter , and a comprehensive consideration of the impurity pressure difference Δ P P .

另需提及,由於開孔或與開孔連通的孔隙方能允許流體進入,故將開孔所占體積與材料總體積之比值定義為孔隙率(porosity)。孔隙率愈高,則流體含量愈高,故孔隙率為評估流體表現一重要參數。空殼孔隙率κ b 一般為流體濾清器100供應廠商所提供,若未提供時,本發明提出一方法,係可 透過對複數組流體F流量之數值進行二次線性迴歸而得到△P box =f(Q),再透過式(2)得到空殼孔隙率κ b 。亦即,流體F流量之變化將影響空殼壓力差△P box 之變化,而流體F流量與壓力差變化符合二次線性方程式的關係。濾芯孔隙率κ f 及雜質孔隙率κ p 可透過類似的方式,再結合上述式(3)及式(4)而得到。 It should also be mentioned that since the opening or the pore communicating with the opening allows fluid to enter, the ratio of the volume occupied by the opening to the total volume of the material is defined as porosity. The higher the porosity, the higher the fluid content, so the porosity is an important parameter for evaluating fluid performance. The void porosity κ b is generally provided by the fluid filter 100 supplier. If not provided, the present invention proposes a method for obtaining a Δ P box by performing a quadratic linear regression on the value of the F-flow of the complex array fluid. = f ( Q ), and then the void porosity κ b is obtained by the formula (2). That is, the change of the fluid F flow rate will affect the change of the empty shell pressure difference Δ P box , and the change of the fluid F flow rate and the pressure difference conforms to the relationship of the quadratic linear equation. The filter core porosity κ f and the impurity porosity κ p can be obtained in a similar manner by combining the above formulas (3) and (4).

上述透過式(6),可得到初始雜質累積量。然而,為能估測於某一估測時間時之雜質累積量,需引入一預估之方法。請續參照第4圖。第4圖係繪示於本發明一實施例中,使用卡爾曼估測器500預估流體濾清器內之雜質隨時間累積之變化狀態示意圖。 The above-mentioned transmission formula (6) can obtain the initial impurity accumulation amount. However, in order to estimate the amount of impurities accumulated at a certain estimated time, an estimation method needs to be introduced. Please continue to refer to Figure 4. 4 is a schematic diagram showing the state of change of impurities accumulated in a fluid filter over time using a Kalman estimator 500 in an embodiment of the present invention.

於第4圖中,將透過式(6)所得到之初始雜質累積量及測得之一初始壓力差,代入卡爾曼估測器500中。接續,依序進行:計算Jacobian矩陣、預先估計狀態方程式、預先估計誤差協方差、計算Jacobian矩陣、計算卡爾曼增益、已測量值更新預先估計狀態、更新誤差協方差矩陣等步驟,並將更新後的預先估計狀態及更新後的誤差協方差矩陣代入原預先估計狀態方程式及預先估計誤差協方差中,進行重複步驟。藉此,即可得到流體濾清器100內之雜質隨時間累積之變化狀態。 In Fig. 4, the initial impurity accumulation amount obtained by the equation (6) and the measured initial pressure difference are substituted into the Kalman estimator 500. Continuation, sequential: Calculate the Jacobian matrix, pre-estimate the state equation, pre-estimate the error covariance, calculate the Jacobian matrix, calculate the Kalman gain, update the pre-estimated state of the measured value, update the error covariance matrix, etc., and update The pre-estimated state and the updated error covariance matrix are substituted into the original pre-estimated state equation and the pre-estimated error covariance, and the repeating steps are performed. Thereby, the state in which the impurities in the fluid filter 100 are accumulated over time can be obtained.

請續參照第5A圖及第5B圖。第5A圖係繪示於一流體(油品D100)中,預測與實際壓力差隨流體流量之變化圖;第5B圖係繪示於另一流體(油品B100)中,預測與實際壓力差隨流體流量之變化圖。由第5A圖及第5B圖,可以看出本發明對複數組流體F流量之數值進行二次線性迴歸的方式,所模擬出的空殼壓力差△P box 隨流體流量之變化,與所測出之實際 空殼壓力差△P box 隨流體流量之變化相當吻合,且可適用於不同種類的流體,具有廣泛應用性。 Please continue to refer to Figures 5A and 5B. Figure 5A is shown in a fluid (oil D100), the predicted and actual pressure difference as a function of fluid flow; Figure 5B is shown in another fluid (oil B100), the predicted and actual pressure difference A graph of changes with fluid flow. 5B by the first and second FIG. 5A, the present invention can be seen that a plurality of sets of values of the secondary fluid flow F linear regression manner, the shell of the simulated differential pressure △ P box with the fluid flow rate variation, and the measured The actual empty shell pressure difference Δ P box is quite consistent with the change of fluid flow rate, and can be applied to different kinds of fluids, and has wide applicability.

請續參照第6圖。第6圖係繪示於一含有雜質之流體(油品B20)中,預測與實際壓力差隨流體流量之變化圖。由第6圖,可知本發明所提出對複數組流體F流量之數值進行二次線性迴歸以求得壓力差的方法,除可應用於不同種類的流體F外,亦可應用於存在有濾芯及雜質累積的狀態。如第6圖所示,壓力差△P係包含對空殼壓力差△P box ,濾芯壓力差△P filter ,以及雜質壓力差△P P 的綜合考量。更詳細而言,壓力差△P係為空殼壓力差△P box 、濾芯壓力差△P filter 以及雜質壓力差△P P 的總和。由第6圖中,可看出模擬與實際壓力差△P隨流體流量之變化曲線相當吻合。 Please continue to refer to Figure 6. Figure 6 is a graph showing the predicted and actual pressure difference as a function of fluid flow in a fluid containing impurities (oil B20). From Fig. 6, it can be seen that the method for quadratic linear regression of the value of the flow rate of the complex array fluid F to obtain the pressure difference is applicable to the presence of the filter element and The state of accumulation of impurities. As shown in Fig. 6, the pressure difference Δ P includes a comprehensive consideration of the pressure difference Δ P box , the filter pressure difference Δ P filter , and the impurity pressure difference Δ P P . More specifically, the pressure difference Δ P is the sum of the empty case pressure difference Δ P box , the filter element pressure difference Δ P filter , and the impurity pressure difference Δ P P . In FIG. 6, it can be seen the difference between simulation and actual pressure △ P of the fluid flow rate variation curve with good agreement.

請參照以下表一,其係列示不同種類之流體F(油品)於不同狀態(含雜質累積或不含雜質累積)及不同流體F流量下,模擬與實際壓力差△P的誤差百分比。可看到誤差皆在10%內。 Please refer to Table 1 below. The series shows the error percentage of the simulated and actual pressure difference Δ P for different types of fluid F (oil) in different states (including accumulation of impurities or no accumulation of impurities) and different fluid F flow rates. It can be seen that the error is within 10%.

請續參照第7圖至第10圖。第7圖係繪示於流體流量2l/min條件下,模擬添加雜質由1g到6g時,預測與實際壓力差隨時間變化圖;第8圖係繪示於流體流量2l/min條件下,模擬添加雜質由1g到6g時,預測與實際雜質累積量隨時間變化圖;第9圖係繪示於流體流量2l/min條件下,模擬添加雜質由1g到6g時,預測與實際之雜質濃度隨時間變化圖;第10圖係繪示於流體流量2l/min條件下,模擬添加雜質由1g到6g時,預測與實際雜質累積量之誤差變化圖。 Please continue to refer to Figures 7 through 10. Fig. 7 is a graph showing the predicted and actual pressure difference with time when the simulated impurity is added from 1g to 6g under the condition of fluid flow rate of 2l/min; Fig. 8 is shown in the case of fluid flow rate of 2l/min, simulation When the impurity is added from 1g to 6g, the predicted and actual impurity accumulation amount changes with time; the ninth figure is shown in the fluid flow rate of 2l/min, when the simulated impurity is added from 1g to 6g, the predicted and actual impurity concentration The time change graph; Fig. 10 is a graph showing the error variation between the predicted and actual impurity accumulation amount when the simulated impurity is added from 1g to 6g under the condition of fluid flow rate of 2l/min.

藉由本發明所建立流體濾清器100之運作模型,再結合卡爾曼估測器500的運用,可對雜質累積量隨時間之變化進行準確之預估。為說明本發明之流體濾清器異常偵測方法的準確性,以人工添加雜質1g到6g的方式,模擬由1g到6g的雜質累積量。於第7圖中,可看到壓力差隨雜質累積量而逐漸上升,最終收斂於雜質累積量為6g時。於第8圖中,顯示透過卡爾曼估測器500的估測,所預估出的雜質累積量隨時間的變化與實際雜質添加量隨時間的變化相當吻合。最後透過第10圖的總結,可發現利用本發明的流體濾清器異常偵測方法所預估之雜質累積量隨時間的變化與實際雜質添加量隨時間的變化的誤差不超過10%,具有相當高的準確度。 With the operational model of the fluid filter 100 established by the present invention, combined with the application of the Kalman estimator 500, accurate estimation of the accumulation of impurities over time can be made. To illustrate the accuracy of the fluid filter anomaly detection method of the present invention, the amount of impurities accumulated from 1 g to 6 g was simulated by manually adding impurities of 1 g to 6 g. In Fig. 7, it can be seen that the pressure difference gradually increases with the amount of accumulated impurities, and finally converges when the accumulated amount of impurities is 6 g. In Fig. 8, showing the estimation by the Kalman estimator 500, the estimated change in the amount of impurities accumulated over time coincides with the change in the amount of actual impurities added over time. Finally, through the summary of FIG. 10, it can be found that the error of the cumulative amount of impurities predicted by the fluid filter abnormality detecting method of the present invention with time and the change of the actual impurity addition amount with time does not exceed 10%. Quite high accuracy.

綜上,本發明所揭露的流體濾清器異常偵測方法中,透過量測流體流量及壓力差,建立流體濾清器之運作模型,再配合卡爾曼估測器的預估,可準確得到雜質累積量對時間的變化,並以雜質累積量判斷是否需更換新的流體濾清器。藉此,消除習知僅以量測壓力差作為判斷基準所產生的不穩定因素,有效提高本發明流體濾清器異常偵測系統的判斷準確率。 In summary, in the fluid filter abnormality detecting method disclosed in the present invention, by measuring the fluid flow rate and the pressure difference, the operation model of the fluid filter is established, and the estimation of the Kalman estimator can be accurately obtained. The change in the amount of impurities accumulated over time, and the amount of impurities accumulated to determine whether a new fluid filter needs to be replaced. Thereby, the instability factor which is only known by measuring the pressure difference as a criterion for judgment is eliminated, and the judgment accuracy of the fluid filter abnormality detecting system of the present invention is effectively improved.

雖然本發明已以實施方式揭露如上,然其並非用以限定本發明,因此本發明之保護範圍當視後附之申請專利範圍所界定者為準。 While the invention has been described above by way of example, the invention is not intended to be limited thereby, the scope of the invention is defined by the scope of the appended claims.

Claims (10)

一種流體濾清器異常偵測方法,其包含:偵測一流體濾清器內之一流體之一流量;偵測該流體濾清器內之一壓力差;依據該流體濾清器之幾何型態、該流體之物理特性、該流體濾清器之孔隙率、一雜質密度、該流量及該壓力差建立該流體濾清器之一運作模型;透過該運作模型取得一初始雜質累積量;透過一卡爾曼估測器,依據該初始雜質累積量及一初始壓力差,估測該流體濾清器內之雜質隨時間累積之一變化狀態;依據該變化狀態取得該流體濾清器內之雜質於一估測時間之一雜質累積量,並將該雜質累積量與一預設值比對,以便判斷該流體濾清器是否運作異常;其中該流體濾清器之該運作模型係可以下列關係式表示: 其中m為空氣濾清器內之雜質累積量,△P為壓力差,μ為流體黏滯係數,Q為流體之流量,A為流體濾清器之截面積,κ b 為空殼孔隙率,κ f 為濾芯孔隙率,κ p 為雜質孔隙率,ρ p 為雜質密度,L b 為空殼厚度,L f 為濾芯厚度。 A method for detecting an abnormality of a fluid filter, comprising: detecting a flow rate of a fluid in a fluid filter; detecting a pressure difference in the fluid filter; and determining a geometry of the fluid filter State, the physical properties of the fluid, the porosity of the fluid filter, an impurity density, the flow rate, and the pressure difference establish an operational model of the fluid filter; an initial impurity accumulation is obtained through the operational model; a Kalman estimator, estimating the state of accumulation of impurities in the fluid filter over time according to the initial impurity accumulation amount and an initial pressure difference; obtaining impurities in the fluid filter according to the change state Estimating the amount of impurities accumulated in one time, and comparing the accumulated amount of impurities with a preset value to determine whether the fluid filter operates abnormally; wherein the operational model of the fluid filter can have the following relationship Expression: Where m is the cumulative amount of impurities in the air filter, Δ P is the pressure difference, μ is the fluid viscosity coefficient, Q is the flow rate of the fluid, A is the cross-sectional area of the fluid filter, and κ b is the porosity of the empty shell. κ f is the filter core porosity, κ p is the impurity porosity, ρ p is the impurity density, L b is the empty shell thickness, and L f is the filter core thickness. 如申請專利範圍第1項所述之流體濾清器異常偵測方法,其中該流體為一燃油、一機油或一自動變速箱 油。 The fluid filter abnormality detecting method according to claim 1, wherein the fluid is a fuel oil, an oil or an automatic transmission. oil. 如申請專利範圍第1項所述之流體濾清器異常偵測方法,其中該壓力差為該流體流經該流體濾清器之一流體入口及該流體濾清器之一流體出口所形成之一壓力差值。 The fluid filter abnormality detecting method according to claim 1, wherein the pressure difference is formed by the fluid flowing through one of the fluid inlet of the fluid filter and one of the fluid outlets of the fluid filter. A pressure difference. 如申請專利範圍第3項所述之流體濾清器異常偵測方法,其中該壓力差包含一空殼壓力差、一濾芯壓力差以及一雜質壓力差。 The fluid filter abnormality detecting method according to claim 3, wherein the pressure difference comprises a shell pressure difference, a filter element pressure difference, and an impurity pressure difference. 如申請專利範圍第1項所述之流體濾清器異常偵測方法,其中於判斷該流體濾清器運作異常後,發出一警示音、一警示光或一警示訊息。 The method for detecting an abnormality of a fluid filter according to the first aspect of the invention, wherein after the fluid filter is abnormally operated, a warning sound, a warning light or a warning message is issued. 如申請專利範圍第1項所述之流體濾清器異常偵測方法,其中空殼孔隙率κ b 可透過對複數組該流量之數值進行二次線性迴歸而得到。 The method for detecting an abnormality of a fluid filter according to claim 1, wherein the void porosity κ b is obtained by performing a quadratic linear regression on the value of the complex array. 一種流體濾清器異常偵測系統,其包含:一流體濾清器,其內流動一流體;一流量偵測器,其係偵測該流體之一流量;一壓差偵測器,其係偵測該流體濾清器內之一壓力差;一分析器,其係依據該流體濾清器之幾何型態、該流體之物理特性、該流體濾清器之孔隙率、一雜質密度、該流量 及該壓力差建立該流體濾清器之一運作模型,並透過該運作模型取得一初始雜質累積量;一卡爾曼估測器,其係依據該初始雜質累積量及一初始壓力差,估測該流體濾清器內之雜質隨時間累積之一變化狀態;以及一處理器,其係依據該變化狀態取得該流體濾清器內之雜質於一估測時間之一雜質累積量,並將該雜質累積量與一預設值比對,以便判斷該流體濾清器是否運作異常;其中該流體濾清器之該運作模型係可以下列關係式表示: 其中m為空氣濾清器內之雜質累積量,△P為壓力差,μ為流體黏滯係數,Q為流體之流量,A為流體濾清器之截面積,κ b 為空殼孔隙率,κ f 為濾芯孔隙率,κ p 為雜質孔隙率,ρ p 為雜質密度,L b 為空殼厚度,L f 為濾芯厚度。 A fluid filter anomaly detection system includes: a fluid filter in which a fluid flows; a flow detector that detects a flow of the fluid; and a differential pressure detector Detecting a pressure difference in the fluid filter; an analyzer depending on the geometry of the fluid filter, the physical properties of the fluid, the porosity of the fluid filter, an impurity density, The flow rate and the pressure difference establish an operational model of the fluid filter, and an initial impurity accumulation amount is obtained through the operation model; a Kalman estimator is estimated based on the initial impurity accumulation amount and an initial pressure difference Detecting a change state of impurities in the fluid filter over time; and a processor for obtaining an impurity accumulation amount of the impurity in the fluid filter at an estimated time according to the change state, and The accumulated amount of impurities is compared with a predetermined value to determine whether the fluid filter operates abnormally; wherein the operational model of the fluid filter can be expressed by the following relationship: Where m is the cumulative amount of impurities in the air filter, Δ P is the pressure difference, μ is the fluid viscosity coefficient, Q is the flow rate of the fluid, A is the cross-sectional area of the fluid filter, and κ b is the porosity of the empty shell. κ f is the filter core porosity, κ p is the impurity porosity, ρ p is the impurity density, L b is the empty shell thickness, and L f is the filter core thickness. 如申請專利範圍第7項所述之流體濾清器異常偵測系統,其中該流體為一燃油、一機油或一自動變速箱油。 The fluid filter anomaly detection system of claim 7, wherein the fluid is a fuel oil, an oil or an automatic transmission fluid. 如申請專利範圍第7項所述之流體濾清器異常偵測系統,其中該壓力差包含一空殼壓力差、一濾芯壓力差以及一雜質壓力差。 The fluid filter abnormality detecting system of claim 7, wherein the pressure difference comprises a void pressure difference, a filter element pressure difference, and an impurity pressure difference. 如申請專利範圍第7項所述之流體濾清器異常偵測系統,其中該流體濾清器係配置於一航海載具、一陸行載具或一飛行載具。 The fluid filter anomaly detection system of claim 7, wherein the fluid filter is disposed on a marine vehicle, a land vehicle or a flight vehicle.
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US20060259273A1 (en) * 2005-05-11 2006-11-16 Hamilton Sundstrand Corporation Filter monitoring system
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