TWI741490B - Control system and control method - Google Patents
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- TWI741490B TWI741490B TW109102866A TW109102866A TWI741490B TW I741490 B TWI741490 B TW I741490B TW 109102866 A TW109102866 A TW 109102866A TW 109102866 A TW109102866 A TW 109102866A TW I741490 B TWI741490 B TW I741490B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/02—Circuit arrangements for generating control signals
- F02D41/021—Introducing corrections for particular conditions exterior to the engine
- F02D41/0235—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
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- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2006—Periodically heating or cooling catalytic reactors, e.g. at cold starting or overheating
- F01N3/2013—Periodically heating or cooling catalytic reactors, e.g. at cold starting or overheating using electric or magnetic heating means
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- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2066—Selective catalytic reduction [SCR]
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- F02D41/024—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus to increase temperature of the exhaust gas treating apparatus
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- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/16—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being an electric heater, i.e. a resistance heater
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- F01N2610/02—Adding substances to exhaust gases the substance being ammonia or urea
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- F02D41/0025—Controlling engines characterised by use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
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- Y02T10/12—Improving ICE efficiencies
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
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Abstract
Description
相關申請之交互參照 Cross-reference of related applications
本申請案主張2019年1月29日提交的16/260,507之優先權及權益,其為2017年3月2日提交的美國專利申請案第15/447,942號之部份接續申請案,該專利申請案主張2016年3月2日提交的美國臨時申請案第62/302,482號之優先權及權益,該等申請案之內容被以引用的方式全部併入本文中。 This application claims the priority and rights of 16/260,507 filed on January 29, 2019, which is a partial continuation of the U.S. Patent Application No. 15/447,942 filed on March 2, 2017. The patent application The case claims the priority and rights of U.S. Provisional Application No. 62/302,482 filed on March 2, 2016, and the contents of these applications are fully incorporated herein by reference.
發明領域 Field of invention
本揭露內容係關於用於流體流應用之加熱及感測系統,該等應用例如,車輛排氣系統,諸如,柴油排氣及後處理系統。 This disclosure relates to heating and sensing systems for fluid flow applications, such as vehicle exhaust systems, such as diesel exhaust and aftertreatment systems.
發明背景 Background of the invention
此章節中之敘述僅提供與本揭露內容有關之背景資訊,且可不構成先前技術。 The description in this chapter only provides background information related to the content of this disclosure, and does not constitute prior art.
歸因於諸如振動及熱循環之嚴苛環境狀況,諸如引擎之排氣系統的瞬時流體流應用中之實體感測器之使用係挑戰性的。一種已知溫度感測器包括在熱電偶套管內部之一礦物絕緣式感測器,熱電偶套管則焊接至留持一管狀元件之一支撐托架。遺憾地,此設計花費大量時間來達到穩定性,且高振動環境可導致實體感測器之損壞。 Due to harsh environmental conditions such as vibration and thermal cycling, the use of physical sensors in transient fluid flow applications such as the exhaust system of an engine is challenging. A known temperature sensor includes a mineral insulated sensor inside a thermowell, which is welded to a support bracket that holds a tubular element. Unfortunately, this design takes a lot of time to achieve stability, and a high vibration environment can cause damage to the physical sensor.
實體感測器亦呈現許多應用中的實際電阻性元件溫度之一些不確 定性,且結果,在加熱器功率之設計中常應用大的安全裕度。因此,供實體感測器使用之加熱器通常提供較低瓦特密度,此允許以較大加熱器大小及成本為代價帶來的較低之損壞加熱器之風險(在更多電阻性元件表面區域上散佈之相同加熱器功率)。 The physical sensor also exhibits some inaccuracy of the actual resistive element temperature in many applications Qualitative, and as a result, a large safety margin is often used in the design of heater power. Therefore, heaters for physical sensors generally provide lower watt density, which allows a lower risk of damage to the heater at the expense of larger heater size and cost (in more resistive element surface area) The same heater power distributed on the above).
此外,已知技術使用來自熱控制迴路中之外部感測器的開/關控制或PID控制。外部感測器具有自在其電線與感測器輸出端之間的熱電阻之固有延遲。任一外部感測器增大了組件故障模式之可能性,且設定至總體系統之任一機械支座之限制。 In addition, the known technology uses on/off control or PID control from an external sensor in the thermal control loop. The external sensor has an inherent delay from the thermal resistance between its wire and the output of the sensor. Any external sensor increases the possibility of component failure mode and is set to the limit of any mechanical support of the overall system.
流體流系統中的加熱器之一個應用為車輛排氣,其耦接至一內燃機以輔助減少至大氣內的各種氣體及其他污染物排放之不良釋放。此等排氣系統典型地包括各種後處理裝置,諸如,柴油顆粒過濾器(DPF)、催化轉化器、選擇性催化還原(SCR)、柴油氧化催化劑(DOC)、稀油氮氧化物捕集器(LNT)、氨逃逸催化劑或重組器,外加其他。DPF、催化轉化器及SCR捕獲廢氣中之一氧化碳(CO)、氧化氮(NOx)、顆粒物(PM)及未燃燒之烴(HC)。加熱器可經週期性或在一預定時間啟動以增大排氣溫度,且啟動催化劑及/或燃燒已在排氣系統中捕獲之顆粒物或未燃燒之烴。 One application of heaters in fluid flow systems is vehicle exhaust, which is coupled to an internal combustion engine to assist in reducing the undesirable release of various gases and other pollutants into the atmosphere. These exhaust systems typically include various aftertreatment devices, such as diesel particulate filters (DPF), catalytic converters, selective catalytic reduction (SCR), diesel oxidation catalysts (DOC), lean oil nitrogen oxide traps (LNT), ammonia escape catalyst or reformer, plus others. DPF, catalytic converter and SCR capture carbon monoxide (CO), nitrogen oxide (NOx), particulate matter (PM) and unburned hydrocarbons (HC) in exhaust gas. The heater may be activated periodically or at a predetermined time to increase the exhaust gas temperature, and activate the catalyst and/or burn particulate matter or unburned hydrocarbons that have been trapped in the exhaust system.
加熱器通常安裝於排氣管或諸如排氣系統之容器的組件中。該等加熱器可包括在排氣管內之多個加熱元件,且典型地經控制至相同目標溫度以提供相同熱量輸出。然而,由於不同操作狀況(諸如,來自鄰近加熱元件之不同熱輻射,及流過加熱元件的不同溫度之廢氣),典型地出現溫度梯度。舉例而言,下游加熱元件通常具有比上游元件高的溫度,此係因為下游加熱元件曝露於具有已由上游加熱元件加熱之一較高溫度的流體。此外,中間加熱元件接收來自鄰近上游及下游加熱元件之較多熱輻射。 The heater is usually installed in an exhaust pipe or a component such as a container of an exhaust system. The heaters may include multiple heating elements in the exhaust pipe, and are typically controlled to the same target temperature to provide the same heat output. However, due to different operating conditions (such as different heat radiation from adjacent heating elements, and different temperatures of exhaust gas flowing through the heating elements), temperature gradients typically occur. For example, the downstream heating element usually has a higher temperature than the upstream element because the downstream heating element is exposed to a fluid having a higher temperature that has been heated by the upstream heating element. In addition, the intermediate heating element receives more heat radiation from adjacent upstream and downstream heating elements.
加熱器之壽命取決於處於最嚴苛加熱狀況下且將首先出故障的加 熱元件之壽命。在不知曉哪一加熱元件將首先出故障之情況下,難以預測加熱器之壽命。為了改良所有加熱元件之可靠性,加熱器典型地經設計成按一安全係數操作以避免加熱元件中之任一者之故障。因此,處於不太嚴苛加熱狀況下之加熱元件典型地經操作以產生低於其最大可用加熱輸出許多之一熱輸出。 The life of the heater depends on the heater that is under the most severe heating conditions and will fail first. The life of the thermal element. Without knowing which heating element will fail first, it is difficult to predict the life of the heater. In order to improve the reliability of all heating elements, heaters are typically designed to operate with a safety factor to avoid failure of any one of the heating elements. Therefore, heating elements under less severe heating conditions are typically operated to produce a heat output that is much lower than their maximum available heating output.
發明概要 Summary of the invention
以一個形式,提供一種用於一排氣系統之一加熱系統之控制系統。該控制系統包括安置於一排放流體流路徑中之至少一個電加熱器,及適於接收至少一個輸入之一控制裝置。該至少一個輸入係選自由以下各者組成之群組:沿著該排放流體流路徑之溫度讀數、交流發電機功率、交流發電機電流、交流發電機電壓、電池功率、電池電流、電池電壓、電池電荷狀態、進氣口空氣節流閥(IAT)及排氣節流閥(EAT)構型、廢氣再循環(EGR)、排放流體流之質量流率、NH3逃逸、該至少一個電加熱器之電阻溫度係數(TCR)特性、交流發電機速度、引擎速度、後處理組件之老化狀態、引擎之老化狀態、老化降級特性、柴油排氣流體(DEF)之配量率、DEF之溫度、後處理系統之NH3儲存狀況、注入計時延遲、氣缸關斷、可變閥操縱、渦輪增壓器旁路、進氣預加熱、缸內次後噴、環境溫度、環境溫度及其組合。該控制裝置可操作以基於該至少一個輸入調變至該至少一個電加熱器之功率,使得隨著該至少一個輸入而變,一不同加熱輸出由該至少一個電加熱器提供,且該至少一個電加熱器在該排氣系統之操作期間提供一連續可變加熱輸出。 In one form, a control system for a heating system of an exhaust system is provided. The control system includes at least one electric heater arranged in a discharge fluid flow path, and a control device adapted to receive at least one input. The at least one input is selected from the group consisting of: temperature readings along the discharge fluid flow path, alternator power, alternator current, alternator voltage, battery power, battery current, battery voltage, Battery state of charge, intake air throttle (IAT) and exhaust throttle (EAT) configurations, exhaust gas recirculation (EGR), mass flow rate of exhaust fluid flow, NH 3 escape, the at least one electric heating The temperature coefficient of resistance (TCR) characteristics, alternator speed, engine speed, aging status of post-processing components, engine aging status, aging degradation characteristics, dosing rate of diesel exhaust fluid (DEF), DEF temperature, NH 3 storage status, injection timing delay, cylinder shut-off, variable valve operation, turbocharger bypass, intake air preheating, post-injection in the cylinder, ambient temperature, ambient temperature and their combinations in the aftertreatment system. The control device is operable to modulate the power to the at least one electric heater based on the at least one input, so that as the at least one input changes, a different heating output is provided by the at least one electric heater, and the at least one The electric heater provides a continuously variable heating output during the operation of the exhaust system.
自本文中提供之描述,另外應用領域將變得顯而易見。應理解,描述及具體實例僅意欲用於說明之目的,且並不意欲限制本揭露內容之範疇。 From the description provided in this article, additional application areas will become apparent. It should be understood that the description and specific examples are only intended for illustrative purposes, and are not intended to limit the scope of the disclosure.
10:引擎系統 10: Engine system
12:柴油機 12: Diesel engine
14:交流發電機 14: Alternator
16:渦輪增壓器 16: turbocharger
18:排氣後處理系統 18: Exhaust aftertreatment system
20:加熱系統 20: heating system
22:柴油氧化催化劑(DOC) 22: Diesel oxidation catalyst (DOC)
24:柴油顆粒過濾器(DPF) 24: Diesel Particulate Filter (DPF)
26:選擇性催化還原裝置(SCR) 26: Selective Catalytic Reduction (SCR)
27:尿素水溶液注入器 27: Urea aqueous solution injector
28:加熱器總成 28: heater assembly
30:加熱器控制模組 30: Heater control module
31:控制裝置 31: control device
32:上游排氣管道 32: Upstream exhaust pipe
34:中間排氣管道 34: Intermediate exhaust pipe
36:下游排氣管道 36: Downstream exhaust pipe
40:管狀加熱器,加熱器 40: Tubular heater, heater
42:電阻性加熱元件 42: Resistive heating element
44:外殼,加熱器外殼 44: Shell, heater shell
46:絕緣材料 46: Insulation material
48:預定演算法 48: scheduled algorithm
50:電力接腳 50: Power pin
52:密封件 52: Seal
60:電力開關 60: Power switch
62:控制器 62: Controller
64:質量流限制表 64: Mass flow limit table
66:功率輸出限制裝置 66: Power output limiting device
100:預測具有安置於用於加熱流體之一加熱系統中之一加熱器的一流體流系統中之至少一個位置之溫度之方法 100: Method for predicting the temperature of at least one location in a fluid flow system with a heater in a heating system for heating fluid
110~140,210~240:步驟 110~140,210~240: steps
200:預測在安置於一流體流系統中用於加熱流體之一加熱器系統中的多個電阻性加熱元件中之各者後之出口溫度之另一方法 200: Another method for predicting the outlet temperature after each of the multiple resistive heating elements in a heater system that is placed in a fluid flow system for heating fluid
為了可很好地理解本揭露內容,現將藉由實例描述其各種形式, 對隨附圖式進行參看,其中:圖1為應用本揭露內容之原理的一柴油引擎及排氣後處理系統之示意圖;圖2為根據先前技術的一管狀加熱器構造之橫截面圖;圖3為繪示根據本揭露內容之教示的一流體流系統中之一系列組件之示意圖;圖4為繪示根據本揭露內容之教示的預測具有一加熱器之一流體流系統中的至少一個位置之溫度之方法之流程圖;圖5為繪示根據本揭露內容之教示的預測在安置於一流體流系統中之一加熱器系統中之多個電阻性加熱元件中之各者後的出口溫度之方法之流程圖;且圖6為根據本揭露內容之教示構造的一加熱器控制模組之方塊圖。 In order to better understand the content of this disclosure, various forms will be described with examples. Refer to the accompanying drawings, in which: Fig. 1 is a schematic diagram of a diesel engine and exhaust gas aftertreatment system applying the principles of the present disclosure; Fig. 2 is a cross-sectional view of a tubular heater structure according to the prior art; 3 is a schematic diagram showing a series of components in a fluid flow system according to the teachings of the present disclosure; FIG. 4 is a diagram showing at least one position in a fluid flow system predicted to have a heater according to the teachings of the present disclosure The flow chart of the temperature method; FIG. 5 is a diagram showing the outlet temperature of each of a plurality of resistive heating elements placed in a heater system in a fluid flow system predicted according to the teachings of the present disclosure The flow chart of the method; and FIG. 6 is a block diagram of a heater control module constructed according to the teachings of the present disclosure.
本文中描述之圖式僅係用於繪示目的,且並不意欲以任何方式來限制本揭露內容之範疇。 The drawings described in this article are for illustration purposes only, and are not intended to limit the scope of the disclosure in any way.
較佳實施例之詳細說明 Detailed description of the preferred embodiment
以下描述在本質上僅為例示性的,且決不意欲限制本揭露內容、其應用或用途。亦應理解,在不更改本揭露內容之原理之情況下可以不同次序執行一方法內之步驟。 The following description is merely illustrative in nature, and is in no way intended to limit the content of the disclosure, its application, or use. It should also be understood that the steps in a method can be executed in a different order without changing the principle of the content of the disclosure.
參看圖1,一例示性引擎系統10大體包括一柴油機12、一交流發電機14(或在一些應用中,發電機)、一渦輪增壓器16及一排氣後處理系統18。該排氣後處理系統18安置於渦輪增壓器16下游,用於在將來自柴油機12之廢氣釋放至大氣前處理該等廢氣。該排氣後處理系統18可包括一或多個額外組件、裝置或系統,其可操作以進一步處理排放流體流以達成一所要的結果。在圖1之實例
中,該排氣後處理系統18包括一加熱系統20、一柴油氧化催化劑(DOC)22、一柴油顆粒過濾器(DPF)24及一選擇性催化還原裝置(SCR)26。該排氣後處理系統18包括:一上游排氣管道32,其在其中接納一加熱器總成28;一中間排氣管道34,在其中提供DOC 22及DPF 24;及一下游排氣管道36,在其中安置SCR 26。
Referring to FIG. 1, an
應理解,本文中繪示及描述之引擎系統10僅為例示性,且因此可包括諸如NOx吸收器或氨氧化催化劑(外加其他)之其他組件,同時可不使用諸如DOC 22、DPF 24及SCR之其他組件。另外,雖然展示了一柴油機12,但應理解,本揭露內容之教示亦適用於汽油機及其他流體流應用。因此,不應將柴油機應用解釋為限制本揭露內容之範疇。此等變化應被解釋為屬於本揭露內容之範疇。
It should be understood that the
加熱系統20包括安置於DOC 22上游之一加熱器總成28,及用於控制加熱器總成28之操作之一加熱器控制模組30。加熱器總成28可包括一或多個電加熱器,其中各電加熱器包括至少一個電阻性加熱元件。加熱器總成28安置於一排放流體流路徑內,以便在操作期間加熱流體流。加熱器控制模組30典型地包括一控制裝置,其適於接收來自加熱器總成28之輸入。控制加熱器總成28之操作之實例可包括接通及關斷加熱器總成,調變至作為一單一單元之加熱器總成28的功率,及/或調變至單獨子組件(諸如,若可用,個別或成群組之電阻性加熱元件)之功率,及其組合。
The
在一個形式中,加熱器控制模組30包括一控制裝置。該控制裝置與加熱器總成28之至少一個電加熱器通信。該控制裝置適於接收至少一個輸入,包括但不限於排放流體流、排放流體流之質量速度、在至少一個電加熱器上游之流動溫度、在至少一個電加熱器下游之流動溫度、輸入到至少一個電加熱器之功率、自加熱系統之物理特性得出之參數及其組合。該至少一個電加熱器可為適合於加熱排放流體之任一加熱器。實例電加熱器包括但不限於帶式加熱器、裸線電阻性加熱元件、纜線加熱器、筒式加熱器、分層加熱器、電熱絲
加熱器、管狀加熱器及其組合。以實例說明,物理特性可包括電阻絲直徑、MgO(絕緣)厚度、外殼厚度、傳導率、構造之材料之比熱及密度、熱傳遞係數及加熱器及流體管道之輻射率,外加其他幾何及應用有關之資訊。
In one form, the
圖1之系統包括安置於加熱器總成28下游之DOC 22、DOC 22充當催化劑來氧化廢氣中之一氧化碳及任何未燃燒烴。此外,DOC 22將一氧化氮(NO)轉換成二氧化氮(NO2)。DPF 24安置於DOC 22下游,以輔助自廢氣移除柴油顆粒物(PM)或煙灰。SCR 26安置於DPF 24下游,且藉助於催化劑,將氧化氮(NOx)轉換成氮(N2)及水。尿素水溶液注入器27安置於DPF 24下游且SCR 26上游,用於將尿素水溶液注入至廢氣流內。當將尿素水溶液用作SCR 26中之還原劑時,將NOx還原成N2、H2O及CO2。
The system of Fig. 1 includes a
在本揭露內容之一個形式中,來自以上描述之引擎系統10的資料在數學模型中用來不使用實體感測器預測各種溫度,包括加熱器溫度、排氣入口溫度及排氣出口溫度,外加其他。此等模型已經開發用於瞬時及非瞬時系統兩者,且適用於多種加熱器類型及流體流應用。因此,管狀加熱器及引擎排氣的本文中提供之各種形式不應被解釋為限制本揭露內容之範疇。另外,對「加熱器外殼」溫度之具體參考僅為例示性,且計算之溫度可針對諸如帶式加熱器、裸線電阻性加熱元件、纜線加熱器、筒式加熱器、分層加熱器、電熱絲加熱器或管狀加熱器外加其他的任一類型之加熱器之任一組件。「分層加熱器」先前已在美國專利第7,196,295號中定義,該專利與本申請案係共同轉讓的且其內容被以引用的方式全部併入本文中。
In one form of this disclosure, the data from the
參看圖2,一管狀加熱器用作在加熱器總成28中使用之一實例加熱器類型,且經繪示且大體由參考數字40指示。管狀加熱器40包含安置於一外殼44內之一電阻性加熱元件42,及安置於其間之一絕緣材料46,諸如,以實例說明,緻密氧化鎂(MgO)。管狀加熱器40亦可包括電力接腳50及密封件52。
Referring to FIG. 2, a tubular heater is used as an example heater type used in the
本揭露內容提供一種控制系統及一種控制一電加熱器之方法,該電加熱器通常包括使用輸入(諸如,質量流或流動速率、在加熱器上游或下游之流動溫度、加熱器功率輸入及自系統之物理特性得出之任何參數)之一裝置/設備,以接著基於此等輸入調變至加熱器之功率。為了取決於一組已知變數來計算系統之值,本文中揭露多種方式。應理解,此等方程僅為例示性,且不應被解釋為限制本揭露內容之範疇。 The present disclosure provides a control system and a method for controlling an electric heater. The electric heater usually includes input (such as mass flow or flow rate, flow temperature upstream or downstream of the heater, heater power input, and auto Any parameter derived from the physical characteristics of the system) is a device/equipment to then modulate the power to the heater based on these inputs. In order to calculate the value of the system depending on a set of known variables, various methods are disclosed in this article. It should be understood that these equations are only illustrative, and should not be construed as limiting the scope of the disclosure.
舉例而言,為了在諸如如上闡述之柴油排氣之應用中不使用實體感測器計算外殼44之溫度,針對多種加熱器組配,使用質量流率、入口溫度及送至加熱器40之功率,連同熱傳遞方程。在一個形式中,使用以下方程式1計算外殼44之溫度(Ts):
其中:Ac=加熱器橫截面積;As=外殼面積;C=基於雷諾數(Re)及以下展示之表1的第一常數;C2=基於加熱器元件之數目的偏差;D=加熱器元件直徑;K=空氣之熱導率;kW=總加熱器功率;M燃料=燃料之質量流率;M入口=入口質量空氣流動(MAF)速率; m=基於雷諾數(Re)及以下展示之表1的第二常數;Pr=在氣體溫度下取得的空氣之卜朗特數;Prs=在外殼溫度下取得的空氣之卜朗特數;ST=元件之間的橫向距離;T出口=加熱器出口溫度;及μ=空氣之黏度。 Among them: Ac = heater cross-sectional area; As = housing area; C = based on Reynolds number (Re) and the first constant shown in Table 1 below; C 2 = deviation based on the number of heater elements; D = heater Element diameter; K = thermal conductivity of air; kW = total heater power; M fuel = mass flow rate of fuel; M inlet = inlet mass air flow (MAF) rate; m = display based on Reynolds number (Re) and below The second constant in Table 1; P r = the Bront number of air obtained at the gas temperature; Pr s = the Bront number of air obtained at the case temperature; S T = the lateral distance between components; T outlet = heater outlet temperature; and μ = air viscosity.
ReD,max=針對一給定直徑及速度最大值之雷諾數;NL=元件之數目;及C2=當評估元件1時,使用NL=1;當評估6個元件時,NL開始於0.7,且隨著分析各元件,增大至0.92。 Re D,max = Reynolds number for a given diameter and maximum speed; N L = number of elements; and C 2 = When evaluating element 1, use N L =1; when evaluating 6 elements, N L It starts at 0.7 and increases to 0.92 as each component is analyzed.
另外,在此方程式1中,尚未併有輻射效應,然而,當保持處於本揭露內容之範疇內時可併有輻射效應。 In addition, in this equation 1, there is no radiation effect yet, but it can be combined while staying within the scope of this disclosure.
除了加熱器外殼44溫度之外,可計算/模型化在流體流動流(見圖3)內之每一元件後的出口溫度,因此減少了對於額外溫度感測器之需求。在一個形式中,根據以下方程式2計算出口溫度:
其中:As=外殼表面積;Cp=在恆定壓力下的空氣之比熱;h=對流熱傳遞係數;=質量流率;T出口,1=在加熱元件1後之出口溫度;T入口,1=加熱元件1之入口溫度;及Ts=外殼溫度。 Among them: A s = surface area of the shell; C p = specific heat of air under constant pressure; h = convective heat transfer coefficient; = Mass flow rate; T outlet, 1 = outlet temperature after heating element 1; T inlet, 1 = inlet temperature of heating element 1; and T s = shell temperature.
因此,使用方程式2,可貫穿流體流系統不使用實體感測器來預測溫度。作為再一優勢,歸因於與實體感測器相關聯之滯後時間,且尤其在瞬時系統中,使用如本文中闡述之方程式導致較快回應時間。較好準確度及較快回應時間亦允許使用在較高溫度下操作之加熱器,因此提供改良之效能且減小安全裕度。此外,實體感測器之故障模式由本揭露內容移除。
Therefore, using
因為方程式1係針對穩態,所以再一下面之方程式用於如本文中揭露之虛擬感測,即,方程式3:
其中:Ac=加熱器橫截面積; As=外殼面積;C=基於雷諾數(Re)及表1之常數;C2=基於加熱器元件之數目的偏差;Cp=在恆定壓力下的空氣之比熱;D=加熱器元件直徑;K=空氣之熱導率;M燃料=燃料之質量流率;M入口=入口質量空氣流動(MAF)速率;m=基於雷諾數(Re)及表1之常數;=質量流率;Pr=在氣體溫度下取得的空氣之卜朗特數;Prs=在外殼溫度下取得的空氣之卜朗特數;ST=元件之間的橫向距離;T入口=加熱器入口溫度;T出口=加熱器出口溫度;及μ=空氣之黏度。 Among them: Ac = heater cross-sectional area; As = housing area; C = constant based on Reynolds number (Re) and Table 1; C 2 = deviation based on the number of heater elements; C p = air under constant pressure The specific heat; D = heater element diameter; K = thermal conductivity of air; M fuel = mass flow rate of fuel; M inlet = inlet mass air flow (MAF) rate; m = based on Reynolds number (Re) and Table 1 The constant = Mass flow rate; Pr=Brand number of air obtained at gas temperature; Pr s =Brand number of air obtained at shell temperature; S T = lateral distance between elements; T inlet = heating The inlet temperature of the heater; T outlet = the heater outlet temperature; and μ = the viscosity of the air.
通常,為了不限於本文中揭露之具體方程式,Ts由使用設定點、質量流及入口溫度之輸入的方程組判定以計算系統溫度。 Generally, in order not to be limited to the specific equations disclosed in this article, T s is determined by the input equation set using the set point, mass flow, and inlet temperature to calculate the system temperature.
本揭露內容進一步提供加熱器40之預測性/前攝性控制。舉例而言,可將諸如轉矩需求、踏板位置及增大之歧管絕對壓力(MAP)/增壓/引擎計時之系統資料轉換至質量流率,接著可將質量流率提供至控制系統以在需要功率時之前判定所要的加熱器功率,而非依賴於對實體感測器之延遲之回應。
The present disclosure further provides predictive/proactive control of the
本揭露內容之一個變化考量根據方程式4之輻射效應:Q=ε.σ.v f (T h +T se ) 方程式4 A variation of the content of this disclosure considers the radiation effect according to Equation 4: Q=ε. σ. v f ( T h + T se ) Equation 4
其中:Q=輻射密度;Th=絕對加熱器溫度;Tse=絕對感測器溫度;Vf=視角因數(撞擊感測器的加熱器輻射之部分);ε=輻射率;及σ=斯蒂芬-波滋曼常數。 Among them: Q = radiation density; T h = absolute heater temperature; T se = absolute sensor temperature; V f = viewing angle factor (the part of the heater radiation that strikes the sensor); ε = emissivity; and σ = Stephen-Bozeman constant.
此外,加熱器可經充分數學量化,使得可自質量空氣流動(MAF)速率、加熱器入口溫度及施加之功率判定包含加熱器的所有材料之系統頻率回應。加熱器對改變引擎及排氣狀況或一般系統破壞之頻率回應可減少,從而允許加熱器具有較快回饋回應。此接著改良對加熱器元件溫度之控制,從而隨著減小了溫度波動,允許加熱器具有較高瓦特密度(每單位長度之瓦特數、每單位面積之瓦特數或每單位體積之瓦特數)及較好耐久性。可將系統表示簡化成控制微處理器可按減小之精力來利用之一形式。另外,本揭露內容可將相對複雜之數學過程簡化成表格形式,以減少處理能力及定義之預期狀態。應理解,可使用獲得質量流率之多種方法,諸如,以實例說明,MAP及組合入口空氣質量流與燃料消耗。因此,如本文中使用,術語「質量流」應被解釋為包括獲得質量空氣流之此等及其他方法。 In addition, the heater can be fully mathematically quantified so that the system frequency response of all materials including the heater can be determined from the mass air flow (MAF) rate, heater inlet temperature, and applied power. The frequency response of the heater to changes in the engine and exhaust conditions or general system damage can be reduced, allowing the heater to have a faster feedback response. This then improves the control of the heater element temperature, which allows the heater to have a higher watt density (watts per unit length, watts per unit area, or watts per unit volume) as temperature fluctuations are reduced. And better durability. The system representation can be simplified into a form that the control microprocessor can use with reduced effort. In addition, the content of this disclosure can simplify the relatively complex mathematical process into a tabular form, so as to reduce the processing capacity and the expected state of the definition. It should be understood that a variety of methods for obtaining mass flow rate can be used, such as, to illustrate, MAP and combined inlet air mass flow and fuel consumption. Therefore, as used herein, the term "mass flow" should be interpreted to include these and other methods of obtaining mass air flow.
通常,本揭露內容取得來自多種裝置(諸如,以實例說明,引擎、排氣裝置、電力及加熱器)之輸入,執行各種演算法,且接著產生輸出,諸如,實際功率消耗、排氣溫度、加熱器溫度、診斷及排放質量流。引擎輸入/參數可包括排氣溫度及排放流;且加熱器輸入/參數可包括加熱器功率、幾何尺寸及係數。系統模型可包括加熱器模型、電線溫度及外殼溫度及至少一個控制演算法。 該等輸出可接著包括排氣溫度、排放流及診斷。 Generally, the present disclosure takes input from various devices (such as, by way of example, engine, exhaust device, electric power, and heater), executes various algorithms, and then generates output, such as actual power consumption, exhaust temperature, Heater temperature, diagnosis and emission mass flow. Engine inputs/parameters may include exhaust temperature and exhaust flow; and heater inputs/parameters may include heater power, geometric dimensions and coefficients. The system model may include a heater model, wire temperature and housing temperature, and at least one control algorithm. These outputs can then include exhaust temperature, exhaust flow, and diagnostics.
在再一形式中,虛擬感測系統在一診斷模式中用以比較加熱器40之一回應與一已知施加功率以判定總排氣後處理系統18是否正劣化、具有降低之效率,或在排氣後處理系統18中是否存在缺陷。此外,虛擬感測系統可允許移除催化劑入口溫度感測器,因此減少總排氣後處理系統18之成本且降低複雜性。若催化劑入口溫度感測器保持在排氣後處理系統18中,則可將其輸出與由虛擬感測系統提供的計算/預測之加熱器出口溫度比較,且其間之任何不匹配可觸發引擎控制單元(ECU)內之一診斷故障碼。此外,本揭露內容之虛擬感測器系統可與一基於模型之設計(例如,Simulink)整合以改良瞬時效能,且允許加熱器系統之更好特性化。此外,一基於模型之設計可基於不同於如本文中使用之柴油排氣應用之一具體應用來調整虛擬感測器系統之參數/特性化。
In yet another form, the virtual sensing system is used in a diagnostic mode to compare a response of the
虛擬感測器系統之使用進一步減少了知曉實際電阻性元件(例如,電線)溫度之不確定性,且允許減小安全裕度、增大之瓦特密度及較小之加熱器表面積,因此導致更高效且成本較少之加熱器。 The use of the virtual sensor system further reduces the uncertainty of knowing the temperature of the actual resistive element (for example, wires), and allows for reduced safety margins, increased watt density, and smaller heater surface area, thus leading to more Efficient and less costly heater.
如本文中揭露之控制系統亦可藉由電阻性加熱元件(諸如,電阻絲)之一計算之或虛擬溫度控制至加熱器之功率。對已被以引用的方式併入本文中之題為「Advanced Two-Wire Heater System for Transient Systems」之同在申請中之申請案進行參考。在諸如管狀加熱器之一些應用中,藉由虛擬電線溫度進行之控制克服了絕緣件及外殼之熱惰性。此導致電線上之較少溫度變化,其改良可靠性。此方法亦減小了電源上之循環負載,從而允許更平衡之功率傳遞及電源上之較少應變。 The control system as disclosed herein can also control the power to the heater by calculating or virtual temperature by one of the resistive heating elements (such as a resistance wire). Reference is made to the application in the same application titled "Advanced Two-Wire Heater System for Transient Systems" which has been incorporated herein by reference. In some applications such as tubular heaters, the control of the temperature of the virtual wire overcomes the thermal inertia of the insulation and the housing. This results in less temperature changes on the wires, which improves reliability. This method also reduces the cyclic load on the power supply, thereby allowing more balanced power transfer and less strain on the power supply.
本揭露內容進一步提供一引擎系統10,其包括用於控制如前描述之排氣系統之加熱系統的一控制系統。該控制裝置適於接收選自由引擎參數、排氣參數、電力輸出、加熱器參數組成之群組的引擎輸入,且該裝置可操作以
產生選自由功率消耗、排氣溫度、加熱器溫度、診斷、排放質量流率及其組合組成之群組的輸出。該控制系統進一步可操作以診斷劣化的引擎系統組件。在此實例中,控制系統與一引擎控制單元通信,且適於當一判定之參數與一預設定參數不匹配時觸發一診斷故障碼。
The present disclosure further provides an
參看圖4,本揭露內容進一步包括一種預測具有安置於用於加熱流體之一加熱系統中之一加熱器的一流體流系統中之至少一個位置之溫度之方法100。該方法包括獲得流體流系統之流體流之質量流率110、獲得加熱器之流體出口溫度及流體入口溫度中之至少一者120、獲得提供至加熱器之功率130,及基於流體流系統之一模型及獲得之質量流率及流體出口及入口溫度計算在至少一個位置處之溫度140。該至少一個位置可在該加熱總成之至少一個電加熱器之一加熱元件上。該模型可包括如上文先前描述之溫度預測模型。該過程可進一步與一基於模型之設計整合。
Referring to FIG. 4, the present disclosure further includes a
參看圖5,本揭露內容進一步提供預測在安置於一流體流系統中用於加熱流體之一加熱器系統中的多個電阻性加熱元件中之各者後之出口溫度之另一方法200。該方法包括獲得流體流系統之流體流之質量流率210、獲得至至少一個電阻性加熱元件之流體入口溫度220、獲得提供至各電阻性加熱元件之功率及流體流系統之使輸入至各電阻性加熱元件之功率與轉移至流體流之功率有關的特性230,及基於流體流系統之一模型計算出口溫度240。
Referring to FIG. 5, the present disclosure further provides another
如本文中使用,術語「模型」應被解釋為意謂一方程式或一方程組、表示在各種操作狀況下之參數之值的值之一表格、一演算法、一電腦程式或一電腦指令集、一信號調節裝置或基於預測/計劃/未來狀況修改控制之變數(例如,至加熱器之功率)之任一其他裝置,其中預測/計劃係基於先驗與現場量測之組合。 As used herein, the term "model" should be interpreted as meaning a program or a system of equations, a table of values representing the values of parameters under various operating conditions, an algorithm, a computer program, or a computer instruction set , A signal conditioning device or any other device that modifies controlled variables (for example, the power to the heater) based on prediction/planning/future conditions, where the prediction/planning is based on a combination of a priori and field measurements.
因此,本文中已揭露多種不同形式之加熱器、感測器、控制系統 及有關裝置及方法,用於在流體流系統中使用。不同形式中之許多者可相互組合,且亦可包括具體針對如本文中闡述之資料、方程式及組配之額外特徵。此等變化應被解釋為屬於本揭露內容之範疇。 Therefore, many different forms of heaters, sensors, and control systems have been disclosed in this article. And related devices and methods for use in fluid flow systems. Many of the different forms can be combined with each other, and can also include additional features specific to the data, equations, and combinations as described herein. These changes should be interpreted as belonging to the scope of this disclosure.
參看圖6,結合圖1,如先前指出,加熱器控制模組30可經組配以控制加熱器總成28之操作及調變至加熱器總成28之功率。在本實施例中,加熱器控制模組30可與引擎12整合或通信,以允許處理排氣後處理系統18中之廢氣,而不危害燃料效率或對燃料效率具有較少干擾。
Referring to FIG. 6, in conjunction with FIG. 1, as previously indicated, the
在用於排氣系統之先前技術加熱系統中,可僅基於排氣系統之狀況(諸如,廢氣之溫度)來啟動加熱器,而不考慮引擎及電池之狀況。此控制可危害燃料效率。舉例而言,當在車輛操作取決於來自電池組之能量的電荷耗盡或EV模式中操作車輛時,在此狀態中致動加熱器引起對功率之增大需求。若電荷之電池狀態低,則對功率之此增大需求可使車輛自電荷耗盡模式切換至引擎運轉模式,藉此不良地增大燃料消耗。 In the prior art heating system used in the exhaust system, the heater can be activated based only on the condition of the exhaust system (such as the temperature of the exhaust gas) without considering the condition of the engine and the battery. This control can compromise fuel efficiency. For example, when the vehicle is operated in a charge exhaustion or EV mode where the operation of the vehicle depends on energy from the battery pack, actuating the heater in this state causes an increased demand for power. If the state of the charged battery is low, this increased demand for power can switch the vehicle from the charge depletion mode to the engine operation mode, thereby undesirably increasing fuel consumption.
因此,用於排氣後處理系統18的加熱系統20之加熱器控制模組30可經組配以按減少來自排氣後處理系統18之排放同時考慮燃料效率之一方式來控制加熱器總成28之一或多個電加熱器。加熱器總成28之一或多個電加熱器安置於一排放流體流路徑中。加熱器控制模組30包括一控制裝置31,其經組配以接收關於引擎、電池、交流發電機、加熱器、排氣後處理系統18之後處理組件之狀況的至少一個輸入以及沿著排氣後處理系統18之排放流體流路徑之溫度,及因此調變至加熱器總成28之功率。
Therefore, the
當至少一個輸入為引擎有關狀況時,該引擎有關狀況可由一預定或所要的溫度分佈表示。該至少一個輸入亦可關於電池、交流發電機、加熱器、排氣後處理系統18之後處理組件之狀況。因此,該至少一個輸入可選自由以下各者組成之群組:沿著該排放流體流路徑之溫度讀數、交流發電機功率、交流
發電機電流、交流發電機電壓、電池功率、電池電流、電池電壓、電池電荷狀態(SOC)、進氣口空氣節流閥(IAT)及排氣節流閥(EAT)構型、廢氣再循環(EGR)、排放流體流之質量流率、NH3逃逸、電加熱器之電阻溫度係數(TCR)特性、交流發電機速度、引擎速度、後處理組件之老化狀態、引擎之老化狀態、老化降級特性、柴油排氣流體(DEF)之配量率、DEF之溫度、後處理系統之NH3儲存狀況、注入計時延遲、氣缸關斷、可變閥操縱、渦輪增壓器旁路、進氣預加熱、缸內次後噴、環境溫度及其組合。基於至少一個輸入,控制裝置31可操作以連續或按一預定間隔調變及調整至加熱器總成28之功率。隨著該至少一個輸入而變,不同功率/加熱輸出由加熱器總成28提供以加熱排氣後處理系統18中之廢氣。
When at least one input is an engine-related condition, the engine-related condition can be represented by a predetermined or desired temperature distribution. The at least one input may also be related to the condition of the battery, the alternator, the heater, and the post-processing components of the exhaust gas after-
在多個輸入當中,組件之老化狀態指組件之時間及溫度歷史。IAT-EAT分佈可包括溫度-質量流分佈、溫度-引擎速度分佈、溫度-引擎速度分佈、溫度-負載分佈或溫度-引擎狀況分佈。所有此等分佈具有基於引擎狀況之不同溫度目標。加熱器總成28之一或多個電加熱器可包括一或多個電阻性元件。控制裝置31可基於電阻性元件之計算之溫度來調變至加熱器總成28之功率。
Among multiple inputs, the aging state of the component refers to the time and temperature history of the component. The IAT-EAT distribution may include temperature-mass flow distribution, temperature-engine speed distribution, temperature-engine speed distribution, temperature-load distribution, or temperature-engine condition distribution. All these distributions have different temperature targets based on engine conditions. One or more of the electric heaters of the
作為一實例,當至少一個輸入包括沿著排放流體流路徑之溫度讀數時,該等溫度讀數係相對於一臨限值,以調整或修改加熱器總成28之輸出,使得由該加熱器總成28提供低於及高於該臨限值之不同功率輸出。在一個實例中,該等溫度讀數可為選擇性催化還原(SCR)裝置26之入口溫度。當SCR入口溫度低於臨限值時,加熱器總成28提供一較高功率輸出。當SCR入口溫度高於臨限值時,加熱器總成28提供一較低功率輸出。較高功率輸出包括功率增大之量值及/或速率之增大。
As an example, when at least one input includes temperature readings along the discharge fluid flow path, the temperature readings are relative to a threshold value to adjust or modify the output of the
控制裝置31可包括一電力開關60、一控制器62、一質量流限制表64及一功率輸出限制裝置66。控制器62可為一PID控制器、一預測性回饋控制器、一基於模型之控制器或可控制加熱器功率輸出的此項技術中已知之任一控
制器。
The
當諸如溫度讀數之至少一個輸入高於臨限值時,控制器62可用以基於溫度讀數控制加熱器功率。然而,當溫度讀數低於臨限值且需要較高加熱器功率輸出或快速加熱時,控制裝置31可繞過或越過控制器62,且使用質量流限制表64及功率輸出限制裝置66提供加熱器功率。該至少一個輸入經不斷地或定期監視。當該至少一個輸入已增大以達到臨限值時,可將加熱器總成28之控制切換至具有極限之PID控制。替代地,加熱器總成28之控制可基於一預定演算法48。
When at least one input such as a temperature reading is higher than a threshold value, the
在冷排氣狀況期間改良NOx轉換可達成最佳燃料節省。當排氣裝置冷時,在冷排氣狀況期間之較快加熱可改良NOx轉換,藉此允許引擎在排氣裝置稍後變得較暖時在相對較低溫度下運轉,以節省燃料。在冷排氣狀況期間的較快加熱可藉由提高送至加熱器之功率以提供更多熱量來達成。提前燃料注入計時亦可改良燃料節省。因此,可修改引擎校準以當需要較多熱量時連同加熱器總成28之操作一起供應額外熱量。
Improved NOx conversion during cold exhaust conditions can achieve the best fuel savings. When the exhaust device is cold, faster heating during cold exhaust conditions can improve the NOx conversion, thereby allowing the engine to run at a relatively lower temperature when the exhaust device later becomes warmer to save fuel. Faster heating during cold exhaust conditions can be achieved by increasing the power sent to the heater to provide more heat. Advance fuel injection timing can also improve fuel economy. Therefore, the engine calibration can be modified to supply additional heat along with the operation of the
在冷排氣狀況期間使用之燃料典型地為總燃料使用之一較小部分。藉由使用比當排氣溫度低時典型地所需要多之燃料,可達成較快加熱,藉此達成較好之NOx轉換。在冷排氣狀況期間的較好之NOx轉換實現當排氣裝置稍後變得較暖時的減少之NOx轉換。因此,當排氣裝置較暖時用於NOx轉換之溫度可降低以減少燃料消耗。當排氣裝置較暖時,加熱器功率亦可最小化。 The fuel used during cold exhaust conditions is typically a small part of the total fuel use. By using more fuel than is typically required when the exhaust gas temperature is lower, faster heating can be achieved, thereby achieving better NOx conversion. Better NOx conversion during cold exhaust conditions achieves reduced NOx conversion when the exhaust device later becomes warmer. Therefore, when the exhaust device is warmer, the temperature for NOx conversion can be lowered to reduce fuel consumption. When the exhaust device is warm, the heater power can also be minimized.
當使用附加燃料達成在冷排氣狀況期間之快速加熱時,在當引擎在一相對較低溫度下運轉時之隨後較暖排氣狀況期間,節省燃料。結果,在冷排氣狀況期間使用之附加燃料係藉由在隨後變暖排氣狀況期間降低溫度(及因此燃料消耗)來補償。雖然此策略將增大在隨後較暖排氣狀況期間之NOx排放,但NOx排放之量將仍然在根據政府法規之受控制範圍內。此燃料節省策略之效應 可藉由組合用於快速加熱(諸如,用於燃料注入之推遲之計時)之引擎加熱、多個注入與注入壓力來進一步增強。 When additional fuel is used to achieve rapid heating during cold exhaust conditions, fuel is saved during subsequent warmer exhaust conditions when the engine is running at a relatively low temperature. As a result, the additional fuel used during cold exhaust conditions is compensated by lowering the temperature (and therefore fuel consumption) during subsequent warming exhaust conditions. Although this strategy will increase NOx emissions during subsequent warmer exhaust conditions, the amount of NOx emissions will still be within the control range according to government regulations. The effect of this fuel saving strategy It can be further enhanced by combining engine heating for rapid heating (such as delayed timing for fuel injection), multiple injections, and injection pressures.
為了減少在低負載操作期間之燃料消耗,使用基於狀況之設定點替代單一固定設定點來更密切地匹配所要的基於引擎狀況之溫度分佈。換言之,所要的設定點隨引擎狀況而變化。 In order to reduce fuel consumption during low load operation, a condition-based set point is used instead of a single fixed set point to more closely match the desired temperature distribution based on engine conditions. In other words, the desired set point varies with engine conditions.
在另一實例中,該至少一個輸入可包括電池電流或電流電荷狀態。在此情況中,當電池電荷狀態低於一臨限值時,加熱器功率受到限制。因此,可基於引擎/交流發電機速度或基於電壓隨時間之改變來將加熱器總成28控制為受到限制。
In another example, the at least one input may include battery current or current state of charge. In this case, when the state of charge of the battery is below a threshold, the heater power is limited. Therefore, the
當在SCR裝置26中注入過多氨時或當SCR溫度增加且NH3儲存容量減小時,發生NH3逃逸。當至少一個輸入包括NH3逃逸時,加熱器功率在NH3逃逸超過一臨限值時較低,且當NH3逃逸低於該臨限值時較高。
When too much ammonia is injected into the
可使用控制裝置31之電力開關60來控制至加熱器總成28之功率。電力開關60可使脈衝式電流/電力供應至加熱器總成28。電力係脈衝式的,以控制至加熱器總成28之電流供應。當電流為脈衝式,使用電壓及平均電流來計算至加熱器總成28之功率。藉由使用脈衝式電力連同功率量測,與關於排放質量流之資訊組合,質量流限制表64及演算法48可用以保護加熱器總成28,且可使加熱器總成28較小。
The
總之,加熱器總成28經控制以考慮燃料效率對排氣後處理系統18中之廢氣提供加熱。因此,按提供更精確熱控制以當經由最佳化保存燃料時符合排放要求之一方式來操作加熱器總成28。加熱器總成28可基於至少一個輸入低於還是高於一臨限值不同地控制,或可在多個加熱模式中不同地控制。該至少一個輸入包括關於引擎之狀況、電池之狀況、交流發電機之狀況、後處理組件之狀況及加熱器之狀況的參數,以及排氣後處理系統之溫度。該等多個加熱
模式係基於引擎、電池、交流發電機、後處理組件、加熱器之狀況,以及排氣後處理系統之溫度。
In summary, the
加熱器功率基於功率量測及基於工作循環而受到限制,以減少燃料消耗。藉由限制加熱器功率,避免了特別在大體較低引擎速度及負載之時期間將廢氣加熱至一單一設定點。藉由限制加熱器功率,避免了將車輛自EV模式切換至引擎運轉模式(其中交流發電機對電池再充電)。功率限制隨質量流(或基於引擎之映射)變化。加熱器總成28亦可用來管理NH3儲存,藉此控制NH3逃逸。基於功率量測(在引擎、交流發電機、電池等之情況中)控制加熱器總成28之溫度。此外,為了保存燃料,溫度設定點在不同引擎狀況下變化。結果,可更高效地使用燃料,同時可在一範圍內控制NOx排放以符合政府法規。
The heater power is limited based on the power measurement and based on the duty cycle to reduce fuel consumption. By limiting the heater power, it is avoided that the exhaust gas is heated to a single set point, especially during periods of generally lower engine speed and load. By limiting the heater power, switching the vehicle from the EV mode to the engine operation mode (in which the alternator recharges the battery) is avoided. The power limit varies with the mass flow (or engine-based mapping). The
本揭露內容之描述在本質上僅為例示性,且因此,不脫離本揭露內容之實質的變化意欲在本揭露內容之範疇內。不應將此等變化看作脫離本揭露內容之精神及範疇。 The description of the content of the disclosure is merely illustrative in nature, and therefore, changes that do not deviate from the essence of the content of the disclosure are intended to be within the scope of the content of the disclosure. Such changes should not be regarded as departing from the spirit and scope of the content of this disclosure.
10:引擎系統 10: Engine system
12:柴油機 12: Diesel engine
14:交流發電機 14: Alternator
16:渦輪增壓器 16: turbocharger
18:排氣後處理系統 18: Exhaust aftertreatment system
20:加熱系統 20: heating system
22:柴油氧化催化劑(DOC) 22: Diesel oxidation catalyst (DOC)
24:柴油顆粒過濾器(DPF) 24: Diesel Particulate Filter (DPF)
26:選擇性催化還原裝置(SCR) 26: Selective Catalytic Reduction (SCR)
27:尿素水溶液注入器 27: Urea aqueous solution injector
28:加熱器總成 28: heater assembly
30:加熱器控制模組 30: Heater control module
32:上游排氣管道 32: Upstream exhaust pipe
34:中間排氣管道 34: Intermediate exhaust pipe
36:下游排氣管道 36: Downstream exhaust pipe
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