Agent-Based Computer-Aided Process Engineering
ERP术语(最好用)

A字母
AR
应收帐款
AP
应付帐款
ATP---available to promise
可供销售量
AMT---Advanced Manufacturing Technology
先进制造技术
AVL—Approved Vendor List
认可供应商名单
ASVL—Approved Service Vendor List
作业现场库存
firm-planned order
确定定单
firm-planned time fence
确定计划时单
feature
特征件
forward scheduling
顺排计划
favorable variance
有利差异
finite forward scheduling
有限顺排计划
finite loading
backflushing
反冲法
business plan
经营规划
batch process
批流程
bottleneck
瓶颈资源(工序)
back order
脱期定单
backlog
拖欠定单
bucketless system
无时段系统
C字母
CR--------Contract Review
合同审核
COS
销售成本(成品)
计划评审技术
ploicy and procedure
工作准则与工作规程
planned order receipts
计划产出量
planned order
计划定单
planned capacity
中科院SCI期刊分区表-控制类2014

Subcategory ISSN Abbreviated Journal Title中科院分区2013年10月发布Total CitesSYSTEMS (自动化与控制系统)0278-0046IEEE T IND ELECTRON1区 17404 (自动化与控制系统)1532-4435J MACH LEARN RES1区 6024 (自动化与控制系统)1551-3203IEEE T IND INFORM2区 969 (自动化与控制系统)1083-4419IEEE T SYST MAN CY B2区 5821 (自动化与控制系统)1083-4435IEEE-ASME T MECH2区 2878 (自动化与控制系统)0005-1098AUTOMATICA2区 15500 (自动化与控制系统)0018-9286IEEE T AUTOMAT CONTR2区 23664 (自动化与控制系统)1070-9932IEEE ROBOT AUTOM MAG2区 1163 (自动化与控制系统)0016-0032J FRANKLIN I2区 2276 (自动化与控制系统)1066-033X IEEE CONTR SYST MAG2区 2254 (自动化与控制系统)0169-7439CHEMOMETR INTELL LAB2区 4880 (自动化与控制系统)1063-6536IEEE T CONTR SYST T2区 4147 (自动化与控制系统)0886-9383ISA Transactions2区 2658 (自动化与控制系统)1049-8923INT J ROBUST NONLIN2区 2213 (自动化与控制系统)0959-1524J PROCESS CONTR2区 2881 (自动化与控制系统)1751-8644IET CONTROL THEORY A3区 1967 (自动化与控制系统)1751-570X NONLINEAR ANAL-HYBRI3区 535 (自动化与控制系统)1545-5955IEEE T AUTOM SCI ENG3区 871 (自动化与控制系统)0967-0661CONTROL ENG PRACT3区 3413 (自动化与控制系统)0167-6911SYST CONTROL LETT3区 4239 (自动化与控制系统)0952-1976ENG APPL ARTIF INTEL3区 2085 (自动化与控制系统)1562-2479INT J FUZZY SYST3区 284 (自动化与控制系统)1561-8625ASIAN J CONTROL3区 853 (自动化与控制系统)0363-0129SIAM J CONTROL OPTIM3区 4590 (自动化与控制系统)0020-7721INT J SYST SCI3区 1996 (自动化与控制系统)0957-4158MECHATRONICS3区 1681 (自动化与控制系统)1367-5788ANNU REV CONTROL3区 662 (自动化与控制系统)1292-8119ESAIM CONTR OPTIM CA3区 608 (自动化与控制系统)0947-3580EUR J CONTROL4区 636 (自动化与控制系统)0890-6327INT J ADAPT CONTROL4区 809 (自动化与控制系统)0268-3768INT J ADV MANUF TECH4区 7187 (自动化与控制系统)0921-8890ROBOT AUTON SYST4区 1807 (自动化与控制系统)0143-2087OPTIM CONTR APPL MET4区 411 (自动化与控制系统)0020-7179INT J CONTROL4区 4282 (自动化与控制系统)1641-876X INT J AP MAT COM-POL4区 562 (自动化与控制系统)1598-6446INT J CONTROL AUTOM4区 774 (自动化与控制系统)1387-2532AUTON AGENT MULTI-AG4区 500 (自动化与控制系统)0022-0434J DYN SYST-T ASME4区 2738 (自动化与控制系统)0265-0754IMA J MATH CONTROL I4区 303 (自动化与控制系统)0332-7353MODEL IDENT CONTROL4区 170 (自动化与控制系统)0924-6703DISCRETE EVENT DYN S4区 292 (自动化与控制系统)0959-6518P I MECH ENG I-J SYS4区 567 (自动化与控制系统)1392-124X INF TECHNOL CONTROL4区 125 (自动化与控制系统)0142-3312T I MEAS CONTROL4区 272 (自动化与控制系统)0144-5154ASSEMBLY AUTOM4区 252 (自动化与控制系统)1220-1766STUD INFORM CONTROL4区 145 (自动化与控制系统)0826-8185INT J ROBOT AUTOM4区 199 (自动化与控制系统)1079-2724J DYN CONTROL SYST4区 239 (自动化与控制系统)1841-9836INT J COMPUT COMMUN4区 175 (自动化与控制系统)0932-4194MATH CONTROL SIGNAL4区 515(自动化与控制系统)1004-4132J SYST ENG ELECTRON4区 357 (自动化与控制系统)1697-7912REV IBEROAM AUTOM IN4区 50 (自动化与控制系统)0005-1144AUTOMATIKA4区 48 (自动化与控制系统)0020-2940MEAS CONTROL-UK4区 183 (自动化与控制系统)0178-2312AT-AUTOM4区 160 (自动化与控制系统)1454-8658CONTROL ENG APPL INF4区 40 (自动化与控制系统)0005-1179AUTOMAT REM CONTR+4区 812 COMPUTER SCIENCE, ARTIFICIAL(自动化与控制系统)1064-2315J AUTOMAT INFORM SCI4区 41 INTELLIGENCE 计算机科学、人工智COMPUTER SCIENCE,能1392-124X INF TECHNOL CONTROL4区 125 CYBERNETICS 计算机科学、控制论1083-4419IEEE T SYST MAN CY B1区 5821计算机科学、控制论1094-6977IEEE T SYST MAN CY C2区 2037计算机科学、控制论0737-0024HUM-COMPUT INTERACT2区 851计算机科学、控制论1083-4427IEEE T SYST MAN CY A2区 2785计算机科学、控制论0340-1200BIOL CYBERN3区 4557计算机科学、控制论0924-1868USER MODEL USER-ADAP3区 437计算机科学、控制论1071-5819INT J HUM-COMPUT ST3区 2062计算机科学、控制论1939-1412IEEE T HAPTICS3区 140计算机科学、控制论1073-0516ACM T COMPUT-HUM INT3区 537计算机科学、控制论0953-5438INTERACT COMPUT3区 850计算机科学、控制论1044-7318INT J HUM-COMPUT INT4区 619计算机科学、控制论0932-8092MACH VISION APPL4区 839计算机科学、控制论1054-7460PRESENCE-TELEOP VIRT4区 1068计算机科学、控制论0196-9722CYBERNET SYST4区 453计算机科学、控制论0144-929X BEHAV INFORM TECHNOL4区 802计算机科学、控制论1783-7677J MULTIMODAL USER IN4区 42计算机科学、控制论0332-7353MODEL IDENT CONTROL4区 170计算机科学、控制论0023-5954KYBERNETIKA4区 536计算机科学、控制论1615-5289UNIVERSAL ACCESS INF4区 188计算机科学、控制论0368-492X KYBERNETES4区 462 COMPUTER SCIENCE,计算机科学、控制论1064-2307J COMPUT SYS SC INT+4区 177 INFORMATION SYSTEMS计算机科学、信息系统1392-124X INF TECHNOL CONTROL4区 125 ENGINEERING, AEROSPACE工程、航空航天0376-0421PROG AEROSP SCI1区 1296工程、航空航天0018-9251IEEE T AERO ELEC SYS2区 5915工程、航空航天0731-5090J GUID CONTROL DYNAM2区 4539工程、航空航天0001-1452AIAA J2区 10686工程、航空航天0376-4265ESA BULL-EUR SPACE2区 780工程、航空航天1270-9638AEROSP SCI TECHNOL3区 918工程、航空航天0893-1321J AEROSPACE ENG3区 434工程、航空航天0748-4658J PROPUL POWER3区 2340工程、航空航天0094-5765ACTA ASTRONAUT3区 2040工程、航空航天0021-9142J ASTRONAUT SCI3区 561工程、航空航天0021-8669J AIRCRAFT3区 2646工程、航空航天1475-472X INT J AEROACOUST3区 190工程、航空航天1756-8293INT J MICRO AIR VEH3区 56工程、航空航天1542-0973INT J SATELL COMM N4区 181工程、航空航天0002-8711J AM HELICOPTER SOC4区 377工程、航空航天0022-4650J SPACECRAFT ROCKETS4区 1593工程、航空航天1748-8842AIRCR ENG AEROSP TEC4区 180工程、航空航天1000-9361CHINESE J AERONAUT4区 334工程、航空航天0954-4100P I MECH ENG G-J AER4区 514工程、航空航天0885-8985IEEE AERO EL SYS MAG4区 471工程、航空航天0001-9240AERONAUT J4区 502工程、航空航天0334-0082INT J TURBO JET ENG4区 76工程、航空航天0549-3811T JPN SOC AERONAUT S4区 126工程、航空航天0010-9525COSMIC RES+4区 332工程、航空航天1940-3151J AEROS COMP INF COM4区 93工程、航空航天0740-722X AEROSPACE AM4区 63工程、航空航天0971-1600J SPACECR TECHNOL4区 11 ENGINEERING, ELECTRICAL &ELECTRONIC 工程、电气与电子1751-8644IET CONTROL THEORY A3区 1967工程、电气与电子0967-0661CONTROL ENG PRACT3区 3413工程、电气与电子0890-6327INT J ADAPT CONTROL3区 809工程、电气与电子0932-4194MATH CONTROL SIGNAL4区 515IF 2012-20135-YearImpactFactorImmediacyIndexArticlesCited Half-life5.165 5.078 0.943 470 4.23.424.284 0.168 119 73.381 3.191 0.88 92 2.63.236 3.949 0.439 132 6.33.135 3.386 0.545 121 5.52.9193.944 0.292 391 7.22.7183.411 0.374 364>10.02.4843.097 0.216 37 6.10000000000 2.418 2.457 0.454 1854.62.372 4.329 0.462 26>10.02.291 2.432 0.253 154 9.52 2.62 0.34 153 6.91.937 1.935 0.212 66 9.51.92.255 0.559 118 5.31.8052.285 0.2 180 6.60000000000 1.717 2.04 0.182 3023.31.685 1.513 0.409 22 3.31.674 1.859 0.306 72 3.91.6692.033 0.165 127 7.71.6672.054 0.218 1709.69999999999 1.625 1.947 0.253 154 5.11.506 1.185 0.246 57 3.31.411 1.36 0.201 164 4.21.379 1.885 0.232 138>10.01.305 1.504 0.246 195 6.51.3 1.599 0.239 109 6.60000000000 1.2892.973 0.571 28 5.81.282 1.1 0.132 53 71.25 1.052 0.487 39 7.91.219 1.334 0.323 65 61.205 1.423 0.107 633 51.156 1.615 0.2 135 6.51.062 1.074 0.116 437.10000000000 1.008 1.289 0.084 154>10.01.008 1.146 0.173 75 5.10.953 0.898 0.13 154 3.50.79 1.41 0.242 33 6.70.758 1.182 0.182 121>10.00.741 0.596 0.065 318.30000000000 0.714 0.75 0.167 129.30000000000 0.711 0.99 0.15 20 90.667 0.8 0.177 113 5.10.667 0.560 38 3.40.656 0.886 0.04 75 5.50.603 0.5710 35 6.70.554 0.149 47 3.80.494 0.545 0.306 36 5.60000000000 0.462 0.569 0.276 298.69999999999 0.441 0.436 0.06 84 40.417 0.968 0.222 18>10.00.384 0.344 0.034 116 3.90.375 0.242 0.023 430.349 0.061 330.29 0.4250 24 6.70.284 0.274 0.014 74 50.2020 400.192 0.226 0.042 191>10.00.0380 850.667 0.560 38 3.43.236 3.949 0.439 132 6.32.5483.105 0.151 152 5.60000000000 2.25 3.039 0.667 12>10.02.183 2.44 0.465 127 6.10000000000 2.067 1.938 0.373 51>10.01.6 2 1.867 158.80000000000 1.4152.003 0.117 60 8.11.393 1.5 0.083 362.81.179 1.368 0.094 32 8.51.158 1.493 0.075 407.10000000000 1.131 1.284 0.133 60 7.41.103 1.42 0.143 84 7.41.04 1.112 0.091 33>10.00.973 0.814 0.237 38 80.856 1 0.188 808.30000000000 0.833 0.6 0.061 330.714 0.75 0.167 129.30000000000 0.619 0.548 0.054 74 9.60.532 0.065 31 5.40.318 0.37 0.05 121 60.249 0.242 0.078 64 4.60.667 0.560 38 3.42.3963.795 0.038 269.30000000000 1.299 1.767 0.214 257>10.01.27 1.474 0.097 185 9.91.08 1.301 0.164 256>10.01.064 1.447 0.5 16 9.90.873 1.022 0.139 108 6.90.778 0.854 0.162 68 7.30.717 0.936 0.09 145 9.10.701 0.664 0.155 245 6.30.697 0.677>10.00.632 0.701 0.076 2109.30000000000 0.627 0.139 36 5.90.562 1.041 0.235 170.535 0.635 0.19 21 8.10.514 0.571 0.071 28>10.00.489 0.707 0.075 120>10.00.441 0.348 0.023 43 6.90.438 0.584 0.054 112 4.10.4 0.663 0.036 112 5.10.343 0.456 0.037 54 8.1 0.311 0.469 0.015 65 8.6 0.261 0.2140 270.259 0.292 0.149 47 6.4 0.244 0.275 0.019 53>10.00.2140 120.048 0.048 0.008 1190.034 0.1111.7172.04 0.182 3023.3 1.669 2.033 0.165 127 7.7 1.219 1.334 0.323 65 6 0.417 0.968 0.222 18>10.0。
企业EPR

ERP(enterprise resource planning )企业资源计划系统,是指建立在信息技术基础上,以系统化的管理思想,为企业决策层及员工提供决策运行手段的管理平台。
ERP的专业词汇1safety stock安全库存safety lead time 安全提前期ERP的专业词汇2Office Automation (OA)办公自动化carrying cost保管费closed-loop MRP 闭环MRP(MRP=manufacturing resource planning 制造资源规划)ERP的专业词汇3standard cost system 标准成本体系resupply order 补库单unfavorable/adverse variance 不利差异concurrent engnineering 并行工程ERP的专业词汇4financial accounting 财务会计financial entity 财务实体vloume variance 产量差异prodcut data management (PDM)产品数据管理系统ERP专业词汇5shop floor control 车间作业控制shop order, work order车间定单cost roll-up 成本滚动计算法costed BOM 成品物料单(BOM=bill of materials材料单)yield 成品率ERP专业词汇5group technology 成组技术repetitive manufacturing 重复式生产rough-cut capacity planning (RCCP) 粗能力计划move time, transit time 传递时间ERP专业词汇6group technology 成组技术repetitive manufacturing 重复式生产rough-cut capacity planning (RCCP) 粗能力计划move time, transit time 传递时间ERP专业词汇7Deming circle 戴明环back scheduling 倒排计划wait time 等待时间low-level code 低层码electronic date interchange 电子数据交换(EDI) ERP专业词汇8order point system 订货点法acquisition cost, ordering cost 订货费make-to-order 订货生产(MTO)assemble-to-order 订货组装(ATO)fixed period requirements 定期用量法ERP专业词汇9独立需求independent demand短缺损失cost of stockout额定能力rated capacity反查物料单where-used list反冲法backflushingERP专业词汇10非规范化管理informal system废品率scrap分布式控制系统distributed control system (DCS) 分布式MRP distributed MRP (DMRP)分销资源计划distribution resource planning (DRP) 分销需求计划distribution requirements planning ERP专业词汇11供方计划员vendor scheduler, supplier scheduler 供应链supply chain供应链管理supply chain management (SCM)供应链合作伙伴关系supply chain partnership (SCP) ERP专业词汇12工效学ergonomics工艺线路routing工作流work flow工作日历shop calendar工作中心work center工作准则与工作规程policy and procedureERP专业词汇13固定批量法fixed order quantity(FOQ)固定资产fixed assets关键过程域key process areas (KPA)关键工作中心critical work center关键路径法critical path method(CPM)ERP专业词汇14管理会计management accounting管理信息系统management information system (MIS)规范化管理系统formal system后勤保证体系logistics呼叫中心computer telephony integration (CTI)ERP专业词汇15会议室模拟conference room pilot汇总物料清单summarized BOM基本组件feature计划产出量planned order receipts计划定单planned order计划接收量scheduled receiptsERP专业词汇16计划能力planned capacity计划评审技术program evaluation research technology (PERT)计划期planning horizon计划时界planned time fence (PTF)计划投入量planned order releases计划物料单planning BOMERP专业词汇17季节储备seasonal stock计算机辅助工艺设计computer-aided process planning (CAPP)计算机辅助软件工程computer-aided software engineering (CASE)计算机辅助设计computer-aided design (CAD)计算机辅助制造computer-aided Manufacturing (CAM)计算机集成制造系统computer integrated manufacturing system (CIMS) ERP专业词汇18机群式布置车间job shop加工时间run time价值链value chain间接费分配overhead apportionment/allocation间接费率overhead rate, burden factor, absorption rate建议成本proposed cost净改变法net changeERP专业词汇19经济订货f法economic order quantity (EOQ)经济订货周期Economic Order Interval (EOI)紧迫系数critical ratio净需求net requirement净需求计算netting精益生产lean production经营规划business plan决策支持系统decision support system (DSS)ERP专业词汇20开支差异spending variance, expenditure variance可供销售量available to promise (ATP)客户关系管理customer relationship management (CRM)客户机服务器client server客户交货提前期customer delivery leadtime可选件option库存inventory库存(资金)周转次数inventory turnover / turns快速换模法single-minute exchange of dies (SMED)ERP专业词汇21累计提前期cumulative lead time离散型生产discrete manufacturing例外管理法management by exception连续流程continous process领料提货单picking list流动负债current liabilities流动资产current assetsERP专业词汇22毛需求gross requirements美国生产与库存管理协会American Production and Inventory Control Society, Inc. (APICS) 面向客户制造管理系统Customer Oriented Manufacturing Management System (COMMS) 敏捷制造Agile manufacturing模块化物料单modular BOM模拟成本simulated cost母件parent itemERP专业词汇23能力成熟度模型capability maturity model (CMM)能力利用水平capacity level能力管理capacity management能力需求计划capacity requirements planning帕拉图原理Pare to Principle排队时间queue time派工单dispatch timeERP专业词汇24配套出售件kitting批量规则lot sizing批量库存lot size inventory批流程batch process偏置天数days offset瓶颈资源bottleneckERP专业词汇25其它应收款other receivables企业资源计划enterprise resource planning (ERP)请购单requisition全面质量管理total quality management(TQM)确认订单firm-planned order确认计划需求时界firm-planned time fenceERP专业词汇26人力资源管理human resouce management (HRM)人力资源计划human resouce planning (HRP)柔性制造系统flexible manufacturing system (FMS)设计物料清单engineering BOM生产周期production cycle成产和决策管理信息系统production and decision information system (PADIS) 生产作业控制production activity controlERP专业词汇27时段time bucket时界time fence时区time zone所有者权益owner's equity顺排计划forward scheduling缩减率shrinkage缩排式物料清单indented BOMERP专业词汇28提前期lead time提前期偏置lead time offset投入/产出控制input/output control囤积库存hedge inventory脱期定单back order拖欠定单backlog未结定单open orderERP专业词汇29物料material, item物料管理material management物料核定机构material review board物料经理material manager物料可用量material available物料清单bill of materials物料需求计划material requirements planning (MRP)物料主文件material master, item masterERP专业词汇30无形资产intangible assets无时段系统bucketless system无限排负荷infinite loading下达定单released order现货生产make to stock (MTS)现金cash on hand先进制造技术advanced manufacturing technology相关需求件dependent demand销售力量自动化sales force automation销售与运作规划sales and operations planningERP专业词汇31虚拟企业Virtual Enterprise (VE) or virtual organization 虚拟件phantom需求管理dmand management需求时界demand time fence (DTF)需求周期demand cycle需求能力required capacity循环盘点cycle counting业绩评价performance measurement银行存款cash on bankERP专业词汇32应付票据notes payable应付帐款accounts payable应收票据notes receivable应收帐款accounts receivable应用服务外包application service provider (ASP)因需定量法lot-for-lot应用模拟live pilotERP专业词汇33优化生产技术optimized production technology (OPT) 优先级priority有限能力计划finite capacity scheduling (FCS)有限排负荷finite loading有限顺排finite forward scheduling预计可用库存量projected available balance预期储备anticipation inventory原型测试prototyping约束理论theory of constraints (TOC)ERP专业词汇34在途库存transportation inventory制造物料清单manufacturing BOM制造执行系统manufacturing executive system (MES) 周期定量法period order quantity (POQ)主生产计划master production planning (MPS)主生产计划员master scheduler专项生产engineer to order (ETO)总提前期total lead time。
表示计算机辅助工程的英文缩写

表示计算机辅助工程的英文缩写Computer-Aided Engineering (CAE) is a term commonly used to refer to the application of computer software and tools in the field of engineering. It encompasses a wide range of disciplines, including mechanical, electrical, civil, and chemical engineering, among others. CAE plays a crucial role in the design, analysis, and optimization of various engineering systems and processes. In this article, we will explore the significance of CAE and its impact on the engineering industry.One of the key advantages of CAE is its ability to simulate and model complex engineering problems. By using advanced software and algorithms, engineers can create virtual prototypes and test them under different conditions. This allows for a more efficient and cost-effective design process, as it reduces the need for physical prototypes and extensive testing. Additionally, CAE enables engineers to identify potential issues and make necessary modifications before the actual production or construction phase, saving both time and resources.Another important aspect of CAE is its contribution to the analysis and optimization of engineering systems. Through the use of computational methods, engineers can evaluate the performance of various components and systems, such as stress analysis, fluid dynamics, and thermal management. This enables them to identify potential weaknesses or areas for improvement, leading to enhanced designs and increased efficiency. Moreover, CAE facilitates the exploration of different design alternatives and the evaluation of their impact on performance, allowing engineers to make informed decisions based on data-driven analysis.Furthermore, CAE plays a significant role in the field of manufacturing. It enables engineers to simulate and optimize manufacturing processes, such as casting, molding, and machining. By analyzing factors such as material properties, tooling, and process parameters, CAE helps in improving product quality, reducing production costs, and minimizing waste. It also aids in the identification of potential manufacturing issues, such as part distortion or tool wear, allowing for timely adjustments and improvements.In addition to design and analysis, CAE is also utilized in the field of virtual testing and validation. Engineers can simulate and evaluate the performance of products under various operating conditions, such as structural integrity, durability, and safety. This helps in ensuring that products meet the required standards and regulations before they are manufactured or deployed. Virtual testing also allows for the identification of potential failure modes and the optimization of product performance, leading to enhanced reliability and customer satisfaction.The use of CAE has revolutionized the engineering industry, providing engineers with powerful tools and capabilities to tackle complex problems. It has significantly reduced the time and cost associated with traditional design and testing methods, while improving overall product quality and performance. Moreover, CAE has enabled engineers to explore innovative design concepts and push the boundaries of engineering possibilities.In conclusion, Computer-Aided Engineering (CAE) is an essential component of modern engineering practices. Its ability to simulate, analyze, and optimize engineering systems has revolutionized the design and manufacturing processes. By leveraging advanced software andcomputational methods, engineers can enhance product performance, reduce costs, and improve overall efficiency. CAE has undoubtedly become an indispensable tool in the field of engineering, enabling engineers to push the boundaries of innovation and deliver cutting-edge solutions.。
Unit 4-计算机专业英语(第2版)-邱晓红-清华大学出版社

Unit Four Software Engineering 软件过程Text A Software processes软件过程A software process is a set of activities that leads to the production of a software product.一个软件过程是一组引发软件产品生产的活动。
These activities may involve the development of software from scratch in a standard programming language like Java or C.这些活动刻画了软件使用像Java或C这样的标准编程语言从头开始的一步步的开发过程。
Increasingly, however,new software is developed by extending and modifying existing systems and by configuring and integrating off-the-shelf software or system components.然而,现在越来越多的软件是通过在旧软件基础上修改或通过配置和集成现成软件或系统组件而形成。
Software processes are complex and, like all intellectual and creative processes, rely on people making decisions and judgements.软件过程是复杂的,像所有智力过程一样,它依赖于人的判断。
Because of the need for judgement and creativity, attempts to automate software processes have met with limited success.因而需要判断和创造力,软件过程自动化的尝试只获得了有限的成功。
Integrated process design instruction

Computers and Chemical Engineering26(2002)295–306Integrated process design instructionD.R.Lewin a,*,W.D.Seider b,J.D.Seader ca Chemical Engineering Department,Technion,Israel Institute of Technology,Haifa32000,Israelb Chemical Engineering Department,Uni6ersity of Pennsyl6ania,Philadelphia,PA19104,USAc Chemical and Fuels Engineering Department,Uni6ersity of Utah,Salt Lake City,UT84112,USAReceived21August2000;received in revised form2January2001;accepted2January2001AbstractAs chemical engineering education moves into the new millennium,it is incumbent on educators to provide a modern curriculum for process design,yet mindful of the limited time for instruction that is available.This paper addresses three key components of a chemical engineering curriculum that prepare undergraduates to be effective process designers in industry:(a)a structured approach relying on fundamentals,integrated with instruction in the competent use of process simulators;(b)a balance between heuristic and algorithmic approaches;and(c)instruction in the integration of design and control.It is argued that these components should be included in an integrated fashion,with much of the material appearing gradually during the delivery of core courses,taking full advantage of computing capability and multimedia support for self-paced instruction.In this paper,each of the features is discussed in detail and demonstrated for the design of a typical process.©2002Elsevier Science Ltd.All rights reserved.Keywords:Process design instruction;Heuristic and algorithmic approaches;Chemical process simulators;Interaction of design and control; Multimedia and web-based instruction/locate/compchemeng1.IntroductionInstruction of chemical engineers should reflect the challenges they face in industry.Young chemical engi-neers are required to assimilate rapidly new and emerg-ing technologies to react in aflexible manner to shorter production cycles and strict quality regulations.They are expected to improve product quality while at the same time reduce operating costs and environmental impact,improve operability,minimize waste produc-tion,and eliminate possible hazards.It is incumbent on chemical engineering educators to provide a modern curriculum for process design instruction that addresses these needs while being mindful of the limited time available.Thefirst issue involves the concept of a structured core curriculum that focuses on fundamentals as a basis for design.Typically,design is taught in the senior year and involves the integration and assimilation of core course material as dictated by the needs of a design project.Section2describes how the core course se-quence has impact on the needs of instruction in design. Furthermore,we discuss the need for students to sup-port their developing knowledge of engineering funda-mentals in general,and more specifically their design activity,by mastering the use of a commercial simulator to a high level of competence.We suggest that adopting self-paced methods relying on multimedia tutorials, which assist the students in preparing simulations of processflowsheets,can support this effort.In the sec-ond issue,which is discussed in Section3,it is postu-lated that the teaching of design itself should strike a balance between heuristic and algorithmic approaches. While heuristics lay the foundations for acquiring the experience necessary to carry out practical process cre-ation and equipment design,the importance of the latter is to ensure the generation of optimal designs. The last issue is the importance of dealing with interac-tions between the design and control of chemical pro-cesses when learning to prepare process designs.In Section4,the current state of the art in the integration of process design and process control is reviewed with*Corresponding author.Tel.:+972-4-829-2006;fax:+972-4-823-0476;http://tx.technion.ac.il/ dlewin/pse.htm.E-mail address:dlewin@tx.technion.ac.il(D.R.Lewin).0098-1354/02/$-see front matter©2002Elsevier Science Ltd.All rights reserved. PII:S0098-1354(01)00747-5D.R.Lewin et al./Computers and Chemical Engineering26(2002)295–306 296particular emphasis on its impact on the education of undergraduates.Several textbooks are available to support a senior course in process design.The traditional textbooks focus on either hierarchical design relying on back-of-the-envelope calculations(Douglas,1988),or on de-tailed equipment design,costing,and economics (Ulrich,1984;Peters&Timmerhaus,1991).Of the more recent texts(Smith,1995;Woods,1995;Turton, Bailie,Whiting,&Shaeiwitz,1997;Biegler,Grossmann, &Westerberg,1997),only Seider,Seader,and Lewin (1999)additionally provide detailed support on the use of simulators,with an explicit treatment of the interac-tion of design and control.In this paper,it is an objective to discuss our view of several key aspects of how computer-aided process design can be taught to chemical engineering under-graduates.This topic has been treated previously by a number of chemical engineering educators,starting with Westerberg(1971),and with more recent treat-ments by Turton and Bailie(1992),Cameron,Douglas, and Lee(1994),Shaeiwitz,Whiting,and Velegol(1996), Bell(1996),Rockstraw,Eakman,Nabours,and Bellner (1997),Counce,Holmes,Edwards,Perilloux,and Reimer(1997).It is not intended in this article to provide a comprehensive coverage of instruction in process design with emphasis on the advantages and disadvantages of alternative approaches.Rather,it is our purpose to extend some old ideas and introduce some new ones that we have tested with our students.2.A structured approach relying on fundamentals Before discussing the building blocks that are an integral part of the toolbox of a process designer,a brief mention of the educational approach that we advocate is in order.We thereforefirst discuss the particular skills that need to be fostered,and the frame of reference used to define goals for the student, couched in terms of educational objectives.cational approach ad6ocatedAn important goal of the undergraduate curriculum in chemical engineering is to develop the integration, design,and evaluation capabilities of the student.As shown in Fig.1,Bloom(1956),characterized the six cognitive levels in the hierarchy:Knowledge Comprehension Application Analysis Synthesis Evaluation.The cognitive skills at the highest level are synthesis and evaluation,which rely on comprehen-sion,application,and analysis capabilities in the knowl-edge domain,and are consequently the most difficult and challenging to teach.However,to prepare under-graduates to be effective designers in industry,it is important to ensure an adequate coverage of these higher-level skills,rather than limit their education to one based on just knowledge,comprehension,applica-tion,and analysis.To achieve the desired coverage in a cost-effective manner,it is important to define instruc-tional objectives in each undergraduate course in a manner such that the six skills are covered by the senior year.Note that Bloom’s taxonomy has been applied in chemical engineering by Fogler and LeBlanc(1995), Fogler(1999),Felder and Rousseau(2000).The focus of the learning activity is placed on the accomplishments expected from the student through the formulation of course goals in terms of instructional objectives.The key is to provide material that increases the abilities of the students,with the emphasis being on what the student is able to achieve rather than merely what he or she is aware of or understands.As an example of a possible approach,the instructional objec-tives for a typical course on process design might be: On completion of this course,the student should be able to:Carry out a detailed steady-state simulation of a chemical process using a process simulator(e.g. HYSYS)and interpret the results.Synthesize a network of heat exchangers for a chemi-cal process such that the maximum energy is recov-ered or the minimum number of exchangers is used. Synthesize a train of separation units.Suggest reasonable process control configurations us-ing qualitative methods.Formulate and sol6e a small-scale process optimiza-tion problem using a process simulator(e.g. HYSYS).E6aluate process alternatives at various levels:single units,complete plants,and the conglomerate level.Fig.1.Bloom’s taxonomy of educational objectives(Bloom,1956).D.R.Lewin et al./Computers and Chemical Engineering26(2002)295–306297Exercise judgment in the selection of physical prop-erty correlations for design.It is noted that these objectives focus on the profi-ciency in required skills expected from the student. Clearly,a precondition for exhibiting these skills is that the student understands the underlying material.Fur-thermore,it is our experience that students feel more comfortable with clearly defined objectives that quan-tify what is expected of them.2.2.The design project and process simulator as means to integrate process knowledgeA designer must have a working knowledge of math-ematics,chemical and physical technology,biotechnol-ogy,materials science,and economics,which are the building blocks used by the design engineer.This knowledge is developed in a structured fashion in the core chemical engineering courses.It is advantageous to develop the capabilities of the students with a process simulator,in conjunction with the core course materi-als,as will be discussed shortly.The integration skills of the students are developed through their solution of industrially-relevant design case studies.During the design project,teams of students are expected to call upon diverse aspects of their working knowledge to carry out an integrated process design,determining its feasibility with respect to environmental impact,safety, controllability,and economics.In so doing,the student designer integrates previously acquired knowledge in the engineering disciplines,as well as management skills.Due to the problem scale,this inevitably involves the use of a process simulator to formulate and solve the material and energy balances,with phase and chem-ical equilibrium,chemical kinetics,etc.and to size process equipment for cost estimation.Familiarity and competence in the use of a simulator permit the student to quickly develop a base-case design,which is verified against process and thermodynamic data.The availabil-ity of a reliable process model allows the design team to assess rapidly the economic potential for alternative designs,as well as to derive optimal operating condi-tions using optimization methods that incorporate eco-nomics.Moreover,competence in the use of the simulator allows process evaluation to go beyond eco-nomics alone;controllability and operability can be assessed using dynamic simulation,while some simula-tors automatically provide information to help deter-mine the environmental impact of each of the product streams.Process simulators are an indivisible part of modern practice in chemical process design.This has been true for some time in the petrochemicals,bulk andfine chemicals industry,and is rapidly becoming true in biotechnology and microelectronics manufacturing.The routine use of the process simulator in industry implies that chemical engineering graduates should be com-petent to utilize these tools in the analysis,synthesis, and evaluation of process designs.Once students have learned to use simulators intelligently and critically, they appreciate how easy it is to incorporate data and perform routine calculations,and master effective ap-proaches to building up knowledge about a process.As discussed next,the level of simulation skills required of the students completing industrial-scale design prob-lems imply sufficient exposure to the use of simulators during the core courses.e of the simulator in core courses:opportunities and challengesThe high level of competence in the use of simulation expected of the students in the design project relies on their having obtained exposure to simulation in parallel with the core courses.One way to accomplish this is to require students to solve at least one exercise involving the use of simulators as part of each core course. Indeed,recent articles by Russell and Orbey(1993), Bailie,Shaeiwitz,and Whiting(1994)discuss the addi-tion of design projects in the sophomore and junior years.Table1provides a typical simulator-based exer-cise for core courses in the chemical engineering cur-riculum.Adoption of such a sequence goes far in preparing students to use a simulator in solving large-scale problems in the senior design course.With the wide availability of commercial process simulators to educators,the working knowledge of mathematics, chemical and physical technology,and economics can be put to effective use in solving meaningful problems, starting in the sophomore course on material and en-ergy balances,by solving various parts of a complete process with a process simulator.The third author of this paper recalls vividly his experience as a junior when taking thefirst course in chemical engineering,based on material in Chemical Process Principles—Part1—Ma-terial and Energy Balances(Hougen&Watson,1943). The instructorfirst covered the fundamentals in Chap-ters1–9,with application to and homework exercises for small closed-end problems.The last2weeks of the course were spent on Chapter10,which involved mate-rial and energy balance calculations by hand for a complete process.Although the calculations were te-dious and very time consuming,students developed an appreciation of what chemical engineering was all about and a desire to proceed to the next level of instruction.Today,the tediousness and time-consuming aspect of process calculations can be eliminated and some time can be spent on teaching synthesis and evaluation skills, even in the sophomore year.The material and energyD.R.Lewin et al./Computers and Chemical Engineering26(2002)295–306298Table1Core course sequence and typical exercises using simulatorsCourse ObjectivesExerciseAnalysis of methanol synthesis loopMass and Convergence of material and energy balances for processes with recycle energy and purge streamsbalances Analysis of sensitivity to degrees-of-freedomSelection of economically optimal operating conditionsHeat-integrated toluene dehydroalkylationHeat transfer Designing a heat exchanger for vaporizingfluid(computing temperatureapproaches)(see Fig.1(d))Optimal selection of heat-transfer area,weighing reduced energy demandsin furnace against increased cost of exchangerAvoidance of temperature crossoversThermodynamics Constructing T–x–y diagrams for Impact of estimation method on the accuracy of thermodynamicproperties,including K-values and enthalpies.alcohol–water systemsSimulation of a depropanizer column Impact of design variables(e.g.number of ideal trays,feed tray location) Separationprocesses on performance of the columnImpact of selection of degrees of freedom on attaining columnspecificationsDifficulties in converging multicomponent,multistage separation models Dynamics and control of a binary distillationDynamics and Learning to set up a dynamic simulationcontrol column Definition of controlled and manipulated variables and the installationand tuning of control loopsTesting the dynamic resiliency of the columnProcess design Optimization of a multi-draw column Learning to use the simulator to set up and solve an optimizationproblemObserving the importance of selecting the appropriate manipulatedvariables for optimizationObserving the impact of process constraintsbalance course is taught in the sophomore year,using textbooks such as Himmelblau(1996),Felder and Rousseau(2000).Both of these books cover essentially the same fundamentals as presented in the Hougen and Watson textbook.In addition,Himmelblau(in Chapter 6)and Felder and Rousseau(in Chapter10)cover the solution of material and energy balances for continu-ous,steady-state processes with a process simulator. Both texts leave to the instructor the choice of a process simulator and instruction on how to use it,so unless he or she is knowledgeable in the use of computer-aided process simulation programs,it is probable that this material will not be covered.In Chapters12and13of Felder and Rousseau,two fairly complex processes are described and problems given for making material and energy balances,as well as other chemical engineering calculations.Calculations for the methanol synthesis process in Chapter13are particularly suitable for the use of a process simulator and serve as an excellent introduction in the sophomore year to process design. The use of a process simulator in the sophomore year introduces the student to the importance of being famil-iar with a large number of chemical species;the use of physical properties such as density,vapor pressure, specific heat,enthalpy,and K-values;the ease of chang-ing units;the ease of drawing processflow diagrams with systematic ways of numbering streams and equip-ment units;and methods of handling recycle.If students are introduced to the use of a process simulator in the sophomore year,their skill in using simulators can be further enhanced in the junior year in courses influid mechanics,heat transfer,separations, thermodynamics,and reaction engineering.The course influid mechanics can include simulator calculations of pipeline pressure drop,sieve-tray pressure drop,and power requirements of pumps,compressors,and tur-bines.The study of heat exchangers in the heat transfer course can include the detailed design of a heat ex-changer,including considerations of the complex varia-tion of the temperature driving force,temperature crossover violations,and prediction of bubble and dew points for multicomponent mixtures.Process simulators are quite useful in the solution thermodynamics course because the tedious calcula-tions of activity coefficients,K-values,bubble and dew points,vapor–liquid equilibria,liquid–liquid equi-libria,and data correlation are readily carried out,and property graphs and tables are easily prepared.When a process simulator is used in a thermodynamics course, less time need be spent on the myriad of equations thatD.R.Lewin et al./Computers and Chemical Engineering26(2002)295–306299appear in the textbooks and more time can be spent in solving practical problems that demonstrate the impor-tance of thermodynamics to students.Regrettably,the use of a process simulator in a solution thermodynam-ics course does not appear to be considered in the leading textbooks on the subject.Instead these text-books either provide their own computer programs for computing physical properties or suggest the use of popular numerical-method programs.Thus,the oppor-tunity to integrate the important lessons learned in the solution thermodynamics course for the later benefit of the capstone design course is often missed.The se-parations course can profit greatly from the use of process simulators to solve both binary and multicom-ponent,multistage separation operations such as distil-lation,absorption,stripping,and liquid–liquid extraction.It is suggested that less time be spent on graphical methods that are limited to binary and ternary mixtures,with more time spent on multicompo-nent separations that are readily handled by process simulators.The reactor-engineering course also affords an excel-lent opportunity to tackle practical problems in reactor design after completing instruction on the ideal plug-flow and CSTR ing an enthalpy datum of the elements(rather than the compounds),simulators readily handle reactor energy balances without the need to supply heat of reaction information.Simulators also readily compute chemical or simultaneous chemical and physical equilibrium using either the equilibrium-con-stant method for specified stoichiometry or the mini-mization of free energy method for specified product chemicals.Activity coefficients can be taken into ac-count and complex kinetic expressions can be specified. Here too,the use of process simulators to design chem-ical reactors appears to be ignored in the leading text-books on chemical reaction engineering.As discussed by de Nevers and Seader(1992),the use of process simulators prior to the senior design course provides students with an opportunity to develop a critical attitude towards chemical process calculations. They cite a problem involving the condensation and subsequent single-stageflash separation at100psia of a vapor mixture of ammonia and water,initially at290F and250psia.The studentfirst solves this problem graphically using an enthalpy–concentration diagram. The result,which is considered to be reasonably accu-rate,is a vapor of\99wt.%ammonia and a liquid of about68wt.%ammonia at a temperature of about80 F.The student then solves the problem numerically with a process simulation program.He or she is re-quired to select at least four different pairs of K-value and enthalpy correlations for comparison with the graphical solution.Many students are shocked by the widely varying results.For example,with one set of four pairs of correlations,theflash temperature ranges from−91.2to83.4°F with an average of0.5F.From then on,students pay careful attention to the selection of correlations for physical properties.The educational importance of discussing errors is also presented by Whiting(1987,1991).Students who have used process simulators through-out the chemical engineering curriculum are in a posi-tion in the senior design course to concentrate their efforts on synthesis and evaluation aspects of process design.Instructors can devote more time to instruction in the synthesis of heat-exchanger systems using pinch analysis,the synthesis of nearly-and non-ideal separa-tion trains,second-law analysis,economic evaluation, optimization,waste minimization,safety,environmen-tal impact,and controllability.During the senior design project,teams of students are better prepared to call upon diverse aspects of their working knowledge to carry out an integrated process design and determine its feasibility from all aspects,not just economics.2.4.Effecti6e instruction in process simulation:the role of self-paced approachesThe quality of training may be enhanced,and in-struction resources used more efficiently,through the use of multimedia and web-based approaches.Such self-paced methods of training undergraduates allow them to obtain the details they need to use the simula-tors effectively,saving instructors class time,as well as time answering detailed questions as the students use simulators to make calculations.In a typical situation, when creating a base-case design,students can use the examples in the multimedia tutorials to learn how to obtain physical property estimates,heats of reaction,flame temperatures,and phase distributions.Then,stu-dents can learn to create a reactor section,using the simulators to perform routine material and energy bal-ances,and in some cases kinetic calculations,to size the reactor.Next,they can create a separation section, which often involves multicomponent,multistage distil-lation-type calculations(Seader&Henley,1998),which almost always leads to the addition of recycle streams. Using the coverage of process simulators in the multi-media tutorials accompanying the textbook by Seider et al.(1999),the instructor needs only to review the highlights of simulator usage in class.This invariably leaves time for the discussion of more advanced issues. Furthermore,through installation of the multimedia materials on the web,students gain access to the mate-rial from remote locations.Our experience is that the response of students to self-paced multimedia instruc-tion has been very positive.D .R .Lewin et al ./Computers and Chemical Engineering 26(2002)295–3063003.A balance between heuristic and algorithmic approachesThe teaching of design should strike a balance be-tween heuristic and algorithmic approaches.Since de-sign invariably involves signi ficant designer intervention,it is important to teach both heuristics as well as computer-aided algorithmic methods.The for-mer lay the foundations for acquiring the experience necessary to carry out practical process design,while the latter is critical to ensure the generation of optimal designs.Process synthesis is generally introduced first by ex-ample and by instructing students to rely on heuristics (Douglas,1988).These heuristic rules are important in that they provide a framework for workable designs,based on easy to understand rules of thumb (Walas,1988).For example,consider the synthesis of a process to hydrodealkylate toluene using a number of heuristic rules,which lead to the sequence of flow diagrams shown in Fig.2(Seider et al.,1999).It is noted in Fig.2(a)that an undesirable side-reaction to biphenyl ac-companies the principal reaction,and the conversion of toluene is incomplete.The selection of the reactions conditions is motivated by a desire to minimize the production of the unwanted side-product,while maxi-mizing the yield.The reaction conditions lead to the distribution of chemicals shown in Fig.2(b),in which unreacted toluene and hydrogen are recovered by in-stallation of two material recycle streams.The two reaction products (benzene and biphenyl)are removed from the unreacted toluene and hydrogen by installa-tion of a separation section.One possible arrangement consists of the flash vessel and three distillation columns shown in Fig.2(c).It is noted that heuristics dictate that column operating pressures should be se-lected to allow the usage of cooling water whenever possible.Finally,Fig.2(d)shows a possible instantia-tion of task integration,in which a preheater is installed to supply much of the heat duty required to bring the reactor feed to the high temperature that favors the primary reaction,by exchange with the hot reactor products,which need to be cooled.This arrangement signi ficantly reduces the heat duty required in the furnace.As the heuristic ideas are mastered,the students should be directed to computer-aided algorithmic ap-proaches that assist them in the generation of better designs.Several algorithmic approaches,which have great practical value,should be presented.These in-clude heuristic and evolutionary synthesis of nearly ideal vapor –liquid separation sequences (Seader &Westerberg,1977),synthesis of separation systems for non-ideal liquid mixtures (Malone &Doherty,1995),the application of second -law analysis (Seider et al.,1999)to identify opportunities for improved energyFig.2.The evolution of the flowsheet for a process to hydrodealkylate toluene.D.R.Lewin et al./Computers and Chemical Engineering26(2002)295–306301Fig.2.(Continued)D.R.Lewin et al./Computers and Chemical Engineering26(2002)295–306 302utilization,and the application of methods to compute heat recovery targets(Linnhoff&Hindmarsh,1983), and to assist in the design of optimal or near-optimal heat-exchanger networks(Smith,1995).For example, the following algorithmic approaches can refine the design in Fig.2(c):pare the separation sequence in the base-casedesign to alternative sequences by branch-and-bound search.2.Check the utility requirements against the thermo-dynamic MER(maximum energy recovery)target using the temperature-interval or graphical meth-ods.Then,a mixed-integer non-linear program (MINLP)can be implemented to derive an optimal design for implementation.There may be additional opportunities for energy savings.For example,a number of alternative heat-integration configura-tions can be considered for the column sequence proposed in Fig.2(c).In these configurations,the heat of condensation in a column operating at high pressure is used to supply the heat of vaporization in a column operating at a lower pressure,requiring careful selection of column operating pressures to ensure sufficient temperature driving forces.In se-lecting between these alternatives,the economic benefits need to be weighed against their impact on the operability of the process,as discussed next. 4.Integration of design and controlTraditionally,plant controllability and operability has been considered late in the design process,often leading to poorly performing chemical plants.The in-disputable fact that design decisions invariably impact the process controllability and resiliency to disturbances and uncertainties is driving modern design methods to handleflowsheet controllability in an integrated fash-ion.Several recent articles,including Rhinehart,Na-tarajan,and Anderson(1995),Edgar(1997),stress the need to integrate process control with process design. The model of an industrial chemical process for study-ing process control technology presented by Downs and Vogel(1993)has proved to be very valuable in helping to bridge the gap.Morari and Perkins(1995)stress the importance of steady-state and dynamic analysis in the determination of controllability.Perkins(2000)cites the need for educators to develop a systematic process systems approach that considers design,operation and control.Lewin(1999)describes the state-of-the-art and suggests that two alternative approaches,controllability and resiliency(C&R)screening methods and integrated design and control,can ensure that chemical plants meet design specifications.While C&R analysis is used for screening early in the design process,the integrated design and control approaches can be applied to fully optimize and integrate the design of the process and its operation.Lewin focuses on three critical aspects that are predicted to characterize future activity in inte-grated design and control:1.The quantitative assessment of chemical processcontrollability and resiliency has generated consider-able interest,both academically and in industry.The vendors of commercial simulation software equate controllability assessment with dynamic simulation, and ultimately,plant-wide operability and control-lability needs to be verified using this tool.However, it is more important to initiate C&R diagnosis with-out this expensive and engineering-intensive activity.It has been shown that controllability analysis re-duces the alternatives early in the design process (Perkins&Walsh,1994;Weitz&Lewin,1996;Solovyev&Lewin,2000).The challenge to the vendors is to build these tools directly into their simulation software.2.Approaches for integrated design and control areimportant for improving afinal design(Bansal, Mohideen,Perkins,&Pistikopoulos,1998).To ef-fectively use a MINLP,it is necessary to develop methods to prune the network of configurations evaluated by the MINLP solver.The commonly used heuristic approach for MINLP network pruning can be replaced by adopting C&R analysis.3.The training of chemical engineers,who should betaught to view design and control as an integrated activity,is a precondition to the future advancement of thisfield(Seider et al.,1999;Luyben,Tyreus,& Luyben,1999).To this end,both the fundamentals of process dynamics and control,and the impact of design on control,should be covered adequately in the undergraduate curriculum.The concern here is the need to bridge the gap between traditional pro-cess control courses,which emphasize theory,and applications to actual processes.As an illustration,consider potential control prob-lems in theflowsheet in Fig.2(d),and their resolution by adopting C&R diagnosis during the design process: 1.Impact of recycle:The positive feedback loops asso-ciated with the material recycles in theflowsheet can amplify feed disturbances.Careful controllability assessment indicates that the control configuration needs to account for the dynamic interaction be-tween the process units.More specifically,to elimi-nate the disturbance amplification caused by the material recycles,it is recommended that theflow rate of the recycle streams be controlled,either directly or indirectly by manipulating the purge stream.2.Impact of heat-integration:The loss of degrees-of-freedom associated with heat integration may cause the quality of control to deteriorate,depending on the configuration selected.。
外企常用英文简写说明
生产制造管理中常用英文单词A/D/V Analysis/Development/Validation 分析/发展/验证AA Approve Architecture 审批体系ACD Actual Completion Date 实际完成日期ALBS Assembly Line Balance System 装配线平衡系统 ANDON 暗灯(安腾灯)AP Advanced Purchasing 提前采购API Advanced Product Information 先进的产品信息 APQP Advanced Product Quality Planning 先期产品质量策划 ATT Actual Tact Time 实际单件工时BIQ Building in Quality 制造质量BIW Body In White 白车身BOD Bill of Design 设计清单BOE Bill of Equipment 设备清单BOL Bill of Logistic 装载清单BOM Bill of Material 原料清单BOP Bill of Process 过程清单BPD Business Plant Deployment 业务计划实施CAD Computer-Aided Design 计算机辅助设计CAE Computer-Aided Engineering 计算机辅助工程(软件) CARE Customer Acceptance & Review Evaluation用户接受度和审查评估 CAS Concept Alternative Selection 概念可改变的选择 CIP Continue Improve Process 持续改进CIT Compartment Integration Team 隔间融合为组CKD Complete Knockdown 完全拆缷CMM Coordinate Measuring Machines 坐标测量仪CPV Cost per Vehicle 单车成本CR&W Controls/Robotics & Welding 控制/机器人技术和焊接 CS Contract Signing 合同签订CTD Cumulative Trauma Disadjust 累积性外伤失调CTS Component Technical Specification 零件技术规格CVIS Completed Vehicle Inspection Standards 整车检验标准 D/PFMEA Design/process failure mode & effects analysis设计/过程失效模式分析DAP Design Analysis Process 设计分析过程DES Design Center 设计中心DFA Design for Assembly 装配设计DOE Design Of Experiments 试验设计DOL Die Operation Line-Up 冲模业务排行DPV Defect per Vehicle 单车缺陷数DQV Design Quality Verification 设计质量验证DRE Design Release Engineer 设计发布工程师DRL Direct Run Loss 直行损失率DRR Direct Run Run 直行率DSC Decision Support Center 决策支持中心ECD Estimated Completion Date 计划完成日期EGM Engineering Group Manager 工程组经理ELPO Electrode position Primer 电极底漆ENG Engineering 工程技术、工程学EOA End of Acceleration 停止加速EPC&L Engineering Production Cntrol &Logistics 工程生产控制和后勤EQF Early Quality Feedback 早期质量反馈EWO Engineering Work Order 工程工作指令FA Final Approval 最终认可FE Functional Evaluation 功能评估FEDR Functional Evaluation Disposition Report 功能评估部署报告FFF Free Form Fabrication 自由形态制造FIN Financial 金融的FL 听FMEA Failure Mode and Effects Analysis 失效形式及结果分析 FPS Fixed Point Stop 定点停FTP File Transfer Protocol 文件传送协议FTQ First Time Quality 一次送检合格率GA General Assembly 总装GA Shop General Assembly Shop 总装车间Paint Shop 涂装车间Body Shop 车身车间Press Shop 冲压车间GCA Global Customer Audit 全球顾客评审GD&T Geometric Dimensioning & Tolerancing 几何尺寸及精度 GDS Global Delivery Survey 全球发运检查GM General Motors 通用汽车GMAP GM Asia Pacific 通用亚太GME General Motors Europe 通用汽车欧洲GMIO General Motors International Operations 通用汽车国际运作 GMIQ General Motors Initial Quality 通用汽车初始质量 GMPTG General Motors Powertrain Group 通用汽车动力组GMS Global Manufacturing System 通用全球制造系统GP General Procedure 通用程序GQTS Global Quality Tracking System 全球质量跟踪系统 GSB Global Strategy Board 全球战略部HVAC Heating, Ventilation ,and Air Conditioning 加热、通风及空调 I/P Instrument Panel 仪表板IC Initiate Charter 初始租约ICD Interface Control Document 界面控制文件IE Industrial Engineering 工业工程IEMA International Export Market Analysis 国际出口市场分析 ILRS Indirect Labor Reporting System 间接劳动报告系统 IO International Operations 国际业务IOM Inspection Operation Mathod 检验操作方法IOS Inspection Operation Summary 检验操作概要IPC International Product Center 国际产品中心 IPTV Incidents Per Thousand Vehicles 每千辆车的故障率 IQS Initial Quality Survey 初始质量调查IR Incident Report 事故报告ISP Integrated Scheduling Project 综合计划ITP Integrated Training Process 综合培训方法ITSD Interior Technical Specification Drawing 内部技术规范图IUVA International Uniform Vehicle Audit 国际统一车辆审核 JES Job Element Sheet 工作要素单JIS Job Issue Sheet 工作要素单JIT Just in Time 准时制JPH Job per hour 每小时工作量KCC Key Control Characteristics 关键控制特性KCDS Key Characteristics Designation System 关键特性标识系统KPC Key product Characteristic 关键产品特性LT Look at 看MFD Metal Fabrication Division 金属预制件区MFG Manufacturing Operations 制造过程MIC Marketing Information Center 市场信息中心MIE Manufacturing Integration Engineer 制造综合工程师 MKT Marketing 营销MLBS Material Labor Balance System 物化劳动平衡系统 MMSTS Manufacturing Major Subsystem TechnicalSpecifications 制造重要子系统技术说明书MNG Manufacturing Engineering 制造工程MPG Milford Proving Ground 试验场MPI Master Process Index 主程序索引MPL Master Parts List 主零件列表MPS Material Planning System 原料计划系统MRD Material Required Date 物料需求日期MSDS Material Safery Data Sheets 化学品安全数据单MSE Manufacturing System Engineer 制造系统工程MSS Market Segment Specification 市场分割规范MTBF Mean Time Between Failures 平均故障时间MTS Manufacturing Technical Specification 生产技术规范 MVSS Motor Vehicle Safety Standards 汽车发动机安全标准NAMA North American Market Analysis 北美市场分析NAO North American Operations 北美业务NAOC NAO Containerization NAO货柜运输NC Numerically Controlled 用数字控制NOA Notice of Authorization 授权书NSB NAO Strategy Board 北美业务部OED Organization and Employee Development 组织和员工发展 OSH Occupational Safety & Health 职业安全健康OSHA Occupational Safety & Health Act 职业安全与健康法案 OSHMS Occupational Safety & Health Management System 职业安全健康管理体系OSHS Occupational Safety & Health Standards 职业安全标准 PA Production Achievement 生产结果PAA Product Action Authorization 产品临时授权PAC Performance Assessment Committee 绩效评估委员会 PACE Program Assessment and Control Environment 项目评估和控制条件PAD Product Assembly Document 产品装配文件PARTS Part Readiness Tracking System 零件准备跟踪系统PC Problem Communication 问题信息PCL Production Control and Logistics 生产控制和支持PCM Process Control Manager 工艺控制负责人PCR Problem Communication Report 问题交流报告PDC Portfolio Development Center 证券发展中心PDM Product Data Management 产品资料管理PDS Product Description System 产品说明系统PDT Product Development Team 产品发展小组PED Production Engineering Department 产品工程部PEP Product Evaluation Program 产品评估程序PER Personnel 人员PET Program Execution Team 项目执行小组PGM Program Management 项目管理PI People Involement 人员参与PIMREP Project Incident Monitoring and ResolutionProcess 事故方案跟踪和解决过程PLP Production Launch Process 生产启动程序PMI Process Modeling Integration 加工建模一体化PMM Program Manufacturing Manager 项目制造经理PMR Product Manufacturability Requirements 产品制造能要求 PMT Product Management Team 产品车管理小组POMS Production Order Management System 产品指令管理小组 POP Point of Purchase 采购点PP Push - Pull 推拉Production Part Approval Process 生产零部件批准程序PPE 个人防护用品PPH Problems Per Hundred 百辆车缺陷数PPM Problems Per Million 百万辆车缺陷数PPS Practical Problem Solving 实际问题解决PR Performance Review 绩效评估PR/R Problem Reporting and Resolution 问题报告和解决 PRTS Problem Resolution and Tracking System 问题解决跟踪系统PSC Portfolio Strategy Council 部长职务策略委员会PST Plant Support Team 工厂支持小组PTO Primary Tryout 第一次试验PTR Production Trial Run 生产试运行PUR Purchasing 采购PVD Production Vehicle Development 生产汽车发展PVM Programmable Vehicle Model 可设计的汽车模型QA Quality Audit 质量评审QAP Quality Assessment Process 质量评估过程QBC Quality Build Concern 质量体系构建关系QC Quality Characteristic 质量特性QCOS Quality Control Operation Sheets 质量风险控制QE Quality Engineer 质量工程师QET Quality Engineering Team 质量工程小组QFD Quality Function Deployment 质量功能配置QRD Quality, Reliability,andDurability 质量、可靠性和耐久力QS Quality System 质量体系QUA Quality 质量RC Review Charter 评估特许RCD Required Completion Date 必须完成日期RFQ Request For Quotation 报价请求RGM Reliability Growth Management 可靠性增长小组RONA Return on Net Assets 净资产评估RPO Regular Production Option 正式产品选项RQA Routing Quality Assessment 程序安排质量评定RT&TM Rigorous Tracking and Throughout Managment 严格跟踪和全程管理SDC Strategic Decision Center 战略决策中心SF Styling Freeze 造型冻结SIL Single Issue List 单一问题清单SIP Stansardized Inspection Process 标准化检验过程SIU Summing It All Up 电子求和结束SL System Layouts 系统规划SLT Short Leading Team 缩短制造周期SMARTSMBP Synchronous Math-Based Process 理论同步过程SME Subject Matter Expert 主题专家SMT Systems Management Team 系统管理小组SNR 坏路实验Start of Production 生产启动Safe Operating Practice 安全操作规程SOR Statement of Requirements 技术要求SOS Standardization Operation Sheet 标准化工作操作单 SOW Statement of Work 工作说明SPA Shipping Priority Audit 发运优先级审计SPC Statistical Process Control 统计过程控制SPE Surface and Prototype Engineering 表面及原型工程 SPO Service Parts Operations 配件组织SPT Single Point Team 专一任务小组SQA Supplier Quality Assurance 供应商质量保证(供应商现场工程师)SQC Supplier Quality Control 供方质量控制SQD Supplier Quality Development 供应方质量开发SQE Supplier Quality Engineer 供方质量工程师SQIP Supplier Quality Improvement Process 供应商质量改进程序SSF Start of System Fill 系统填充SSLT Subsystem Leadership Team 子系统领导组SSTS Subsystem Technical Specification 技术参数子系统 STD Standardization 标准化STO Secondary Tryout 二级试验SUI 安全作业指导书SUW Standard Unit of Work 标准工作单位SWE Simulated Work Environment 模拟工作环境TAG Timing Analysis Group 定时分析组TBD To Be Determined 下决定TCS Traction Control System 牵引控制系统TDC Technology Development Centre 技术中心TDMF Text Data Management Facility 文本数据管理设备TG Tooling 工具TIMS Test Incident Management System 试验事件管理系统 TIR Test Incident Report 试验事件报告TMIE Total Manufacturing Integration Engineer 总的制造综合工程TOE Total Ownership Experience 总的物主体验TPM Total Production Maintenance 全员生产维护TSM Trade Study Methodology 贸易研究方法TT Tact Time 单件工时TVDE Total Vehicle Dimensional Engineer 整车外型尺寸工程师TVIE Total Vehicle Integration Engineer 整车综合工程师 TWS Tire and Wheel System 轮胎和车轮系统UAW United Auto Workers 班组UCL Uniform Criteria List 统一的标准表UDR Unverified Data Release 未经核对的资料发布UPC Uniform Parts Classification 统一零件分级VAE Vehicle Assembly Engineer 车辆装配工程师VAPIR Vehicle & Progress Integration Review Team 汽车发展综合评审小组VASTD Vehicle Assembly Standard Time Data 汽车数据标准时间数据VCD Vehicle Chief Designer 汽车首席设计师VCE Vehicle Chief Engineer 汽车总工程师VCRI Validation Cross-Reference Index 确认交叉引用索引 VDP Vehicle Development Process 汽车发展过程VDPP Vehicle Development Production Process 汽车发展生产过程VDR Verified Data Release 核实数据发布VDS Vehicle Description Summary 汽车描述概要VDT Vehicle Development Team 汽车发展组VDTO Vehicle Development Technical Operations 汽车发展技术工作VEC Vehicle Engineering Center 汽车工程中心VIE Vehicle Integration Engineer 汽车综合工程师VIN Vehicle Identification Number 车辆识别代码VIS Vehicle Information System 汽车信息系统VLE Vehicle Line Executive 总装线主管VLM Vehicle Launch Manager 汽车创办经理VMRR Vehicle and Manufacturing Requirements Review 汽车制造必要条件评审VOC Voice of Customer 顾客的意见VOD Voice of Design 设计意见VS Validation Station 确认站VSAS Vehicle Synthesis,Analysis,and Simulation 汽车综合、分析和仿真VSE Vehicle System Engineer 汽车系统工程师VTS Vehicle Technical Specification 汽车技术说明书WBBA Worldwide Benchmarking and Business Analysis 全球基准和商业分析WOT Wide Open Throttle 压制广泛开放WPO Work Place Organization 工作场地布置WWP Worldwide Purchasing 全球采购COMMWIP Correction 纠错浪费Overproduction 过量生产浪费Material Flow 过度物料移动浪费Motion 过度移动浪费Waiting 等待浪费Inventory 过度库存浪费Processing 过度加工浪费什么是TPM(Total Productive Maintenance)?Description:TPM是Total Productive Maintenance 第一个字母的,本意是"全员参与的生产保全",也翻译为"全员维护",即通过员工素质与设备效率的提高,使企业的体质得到根本改善。
FORD公司DV-PV培训教材
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DV & PV and PDSA
Vehicle整车
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Sub-System子系统
Design Verification at All Levels 所有级别上的设计验证
• Design Verification should occur at all levels with the emphasis being at the lower levels.
• 设计验证应该重点放在较低级别的情况 下在所有级别上进行。
Welcome
Design Verification and Production Validation 设计验证和生产确认
Ford Technical Education Program 福特技术培训项目
Global 8D
全球8D
Statistical Engineering
统计工程学
Reliability 可靠性
Systems “V” Model 系统V模型
• DV&PV is a requirements driven process • DV和PV 是一个需求驱动的过程 • DV&PV is best conducted in a systems
汽车行业专用英语词汇与常用缩写
专业英语词汇之DFL专用缩略英语词汇序号英文缩写英文全称中文含义1 1PITCH化率changing to 1 pitch 一个工位中所有零件与根据生产节拍算出的一个工位所需零件的比率2 3PL third-part logistics 第三方物流3 4M1E Man .Machine .Material .Method .Environment 人.机械.材料.方法.环境4 5S Seiri,Seiton,Seios,Seikets,Shitsuke(注:这是根据日语而来的,不是英文单词)整理.整顿.清扫.清洁.素养5 5W2H WHO(谁)、WHEN(何时)、WHER(在哪里)、WHAT(什么)、WHY(为什么)、HOW(如何)及HOW MUCH(多少)5W2H是品牌设计的基本方法,也是品牌必须解决的问题.5W2H包含了品牌从战略(WHO、WHY)到策略(WHAT、WHEN、WHER)直至战术(HOW)的完整运作系统,在加上另一个H----HOW MUCH(多少)即品牌预算,实际就是一个完整的品牌运作全案6 8D D1:Choose Team; D2:Describe; D3:Contain;D4:Root Cause;D5:Choose C.A. ;D6:ValidateC.A.; D7:Prevent recurr; D8:reward team团队的建立;问题的描述;抑制问题进一步发展;鉴别鉴别//说明根本原因;选择校正措施;执行执行//确认永久性校正措施;避免复发;奖励您的团队7 ABS Anti-skid Brake System 制动防抱死系统8 ACT Actual (试算)实际数9 A/C Account 帐户10 AM After planning Maintenance 事后保全11 AMS Assembly Manual Sheet 装配手册12 ANPQP ALliance New Product Quality Procedure 联合新产品质量程序13 APQP Advanced Product Quality Planning 产品质量先期策划14 AP Accounts Payable 应付账款15 AR Accounts Receivable 应收账款16 ASES Alliance Supplier Evaluation Standard 联合供应商评价标准17 A-VES Alliance Vehicle Evaluation System 联合车辆评价系统(雷诺-日产)18 ASAS-P Alliance Supplier Audit Standard-Production 雷诺/日产共同的对供应商量产阶段的品质保证体制、工程/产品监查基准19 ASG Alliance Supplier Guide 联合供应商指南20 BD Basic Design 基本设计21 BM Cost Bench Mark 成本标杆22 BOM Bill of Material 物料管理清单23 BP Business Plan 事业计划24 BP Basic Plan 基本构想25 BS Balance Sheet 资产负债表29 BS Brain Storm 头脑风暴法1 1 / / / 16 16 序号英文缩写 英文全称中文含义26 BT Business Trip 短期出差人员短期出差人员 27 BTBusiness Trial业务测试业务测试28 BUS A-VES Bus Alliance - Vehicle Evaluation System 客车联合车辆评价系统客车联合车辆评价系统 30 CAD Computer Aided Design计算机辅助设计计算机辅助设计 31 CAE Computer Aided Engineering 计算机辅助工程计算机辅助工程 32 CAPP Computer Aided Process Planning 计算机辅助工艺设计计算机辅助工艺设计 33 CAPEX Captal Expenditure 资本性支出资本性支出 34 CAR Countermeasure Request 对策要求对策要求 35 CBM Condition Based Maintenance状态基准保全状态基准保全 36 CBU Completely Build-up 完整整车进口完整整车进口 37 CC Career Coach职业指导员职业指导员 38 CCC(3C) China Compulsory Centification 中国强制认证中国强制认证 39 CCR Close Cycle Reduction缩短关账周期缩短关账周期40 CCR Concern & Countermeasure Recurrence 防止再发生对策报告书防止再发生对策报告书 41 CD Calendar Day日历日日历日42 CEMT Capital Expenditure Management Team 投资管理跨职能小组投资管理跨职能小组 43 CEO Chief Executive Officer 首席执行官首席执行官 44 CFO Chief Finance Officer 首席财务官首席财务官 45 CFS Cash Flow Statement 现金流量表现金流量表 46 CFT Cross-Functional Team 跨职能工作小组跨职能工作小组 47 CKD Completed Knocked Down 进口件组装进口件组装 48 CM Communication Management 通讯管理通讯管理 49CMSCash Management System现金管理系统现金管理系统50CM Component Marking组件标记,包括在产品上作出的任何标记,用于帮助识别产品。
计算机类SCI期刊及影响因子
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MODEL;0895-7177;1215;0.479;0.068;191;6.2; APPL INTELL;0924-669X;181;0.477;0.000;38;4.5;INT J NUMER METH FL;0271-2091;1940;0.476;0.068;177;8.1; ACM T DES AUTOMA T EL;1084-4309;139;0.475;0.067;15;4.6;J SUPERCOMPUT;0920-8542;161;0.474;0.133;60;4.6;ROBOT AUTON SYST;0921-8890;511;0.468;0.000;76;5.6;IEE PROC-SOFTW;1462-5970;72;0.466;0.045;22;;INT J COMPUT GEOM AP;0218-1959;190;0.463;0.000;21;6.6; COMPUT MUSIC J;0148-9267;238;0.459;0.167;18;>10.0;ASLIB PROC;0001-253X;112;0.456;0.000;35;4.4;COMPUT INFORM;1335-9150;46;0.456;0.000;4;;REAL-TIME IMAGING;1077-2014;143;0.455;0.028;36;5.2; INFORM PROCESS LETT;0020-0190;1680;0.4532006计算机类SCI期刊及影响因子2008-11-21 19:18Abbreviated Journal Title= =Impact= =FactorINT J COMPUT VISION= =6.085 ACM T INFORM SYST= =5.059 BIOINFORMA TICS= =4.894MIS QUART= =4.731IEEE T PATTERN ANAL= =4.306 ACM COMPUT SURV= =4.13ACM T GRAPHIC= =4.081J AM MED INFORM ASSN= =3.979 IEEE T EVOLUT COMPUT= =3.77 IEEE T MED IMAGING= =3.757 NEUROINFORMATICS= =3.541J CHEM INF MODEL= =3.423VLDB 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AbstractThis paper deals with the design process ofcomponent-based simulation. It relies on CAPE-OPEN interoperability standard. We firstpropose an ontology (named OntoCAPE) torepresent the domain knowledge. We thenintroduce an agent-based architecture to supportthe design of numerical simulation, with aconcrete implementation in the processsimulation domain.1.IntroductionObject-oriented programming, component software, and n-tier architectures are the current paradigm for Computer-Aided Process Engineering (CAPE) software development. Although there are other component-based architectures, the CAPE-OPEN interoperability architecture [Braunschweig 1999], based on object orientation and middleware, appears to be the dominant one, being adopted by a majority of players. CAPE-OPEN is now accepted as a standard for communication between simulation software components in process engineering. This leads to the availability of software components offered by leading vendors, research institutes, and specialized suppliers which enable the process industries to reach new quality and productivity levels in designing and operating their plants.The CAPE-OPEN standard facilitates new business models for process simulation software such as application service provision, and can be the foundation for web services in this domain. Our goal in the new COGents 1 IST project is to push this technology further by developing a1 COGents = CAPE-OPEN aGents. For more information see .new approach to "e-CAPE". We use cognitive agents to support the dynamic and opportunistic interoperability of CAPE-OPEN compliant process modeling components over the Internet. The result is an environment which provides automatic access to best-of-breed CAPE tools when required wherever situated.For this purpose the COGents project:•defines a framework allowing simulation components to be distributed and referenced on the Internet and intranets;•defines representations of requirements and services in form of an ontology of process modeling (named OntoCAPE) expressed in DAML+OIL, thus developing the CAPE-OPEN standards in the semantic and knowledge-based dimensions;•designs new facilities for supporting the dynamic matchmaking of modeling components with knowledge-intensive middleware agents;•demonstrates the concepts through advanced software prototypes and test cases;•shows how the framework can be applied to other areas of numerical simulation.This paper aims to present some aspects of COGents. It is organized as follows: Section 2 presents OntoCAPE. Section 3 introduces the proposed agent-based organization and Section 4 describes its implementation. Section 5 presents the related work.2.OntoCAPEIn order to allow dynamic and opportunistic interoperability of modeling components, we define knowledge-based representations of modeling requirements and services. These representations are in the form of an ontology of process modeling (technically expressed in an objectAgent-Based Computer-Aided Process EngineeringZahia Guessoum1, Othmane Nadjemi1,2, Bertrand Braunschweig2, Pascal Roux2, Aidong Yang 3,E. S. Fraga4, Iain D. Stalker4, Daniel Pinol 5, Manel Serra5, Didier Paen61 OASIS team, Laboratoire d'Informatique de Paris 6, Paris, France8, rue du Capitaine Scott, 75015 Paris (Zahia.Guessoum@lip6.fr)2 Institut Français du Pétrole, Technology, Computer Science and Applied Mathematics Department3 RWTH Lehrstuhl für ProzessTechnik, Aachen, Germany4 Department of Chemical Engineering, University College London, London UK5Aspen Technology, Barcelona, Spain6RSI - Réalisation en Systémique Industriellemodel), and of a corresponding language, OntoCAPE, implemented in DAML+OIL. This knowledge-based representation provides semantic content on top of CAPE-OPEN standard which is purely syntactic (i.e. consisting of specifications of input-output types allowing the technical interoperability of software components). This is the basis for a matchmaking process between user’s requirements and available services, therefore supporting opportunistic configuration of simulators.OntoCAPE is a conceptualization of process modeling, simulation and design which are the primary concern in COGents. It is used for the construction of the repositories of information characterizing Process Modeling Components (PMCs)which can be accessed by agents to perform process modeling. Furthermore, it is also a shared vocabulary used by the agents to understand the messages communicated to each other.Figure 1: Process modeling component From a technical point of view, there are several parts in OntoCAPE to formalize these functionalities. Software System is used to describe process modeling components and environments in term of supported interfaces, software/hardware requirements, selling/buying information, functionality, and usage limitation. Chemical Process System allows the definition of aspects like the realization; behavior and function of a plant being modeled (see Figure 1).Figure 2: Modeling Task SpecificationThe part of OntoCAPE that enables the formalization of the problem is Modeling Task specification. It expresses the various requirements to be fulfilled in a modeling task. The main elements of Modeling Task Specification are: the modeled objects, their properties able to be specified/evaluated, and the PME2in use (see Figure 2). 3.Multi-Agent OrganizationSeveral agent models have been proposed. Two main approaches can be distinguished: cognitive and reactive. In the cognitive approach, each agent contains a symbolic model of the outside world, about which it develops plans and makes decision in the traditional (symbolic) AI way. In the reactive approach, on the other hand, simple-minded agents react rapidly to asynchronous events without using complex reasoning.Figure 3: Minimal Multi-Agent Architecture In most existing agent-based systems, the organization is defined as a set of homogenous interacting agents which can be either reactive or cognitive. These homogeneous organizations are not suitable in the case of complex agent-based simulations. Thus, we propose a hybrid multi-agent architecture which combines reactive and cognitive agents. The problem is dynamically defined or adapted by the user to the situation.Figure 3 presents the minimum society of agents that we use to facilitate the design of numerical simulations. Several case studies have allowed to step forward the knowledge acquisition and design of this multi-agent organization: Automated design of Hydrodealkylation of Toluene (HDA) process [Douglas 1988], modeling the leacher unit in polyamide6 and synthesis of the HDA process.2PME (Process Modeling Environment): environments that support the construction of a process model.3.1Wrapper AgentsThese agents manage the interaction between the existing software and the other agents of COGents. They may be distributed on the Internet or intranets. Their functionalities are represented by services. Each Wrapper Agent holds therefore a set of services that can be provided to the other agents.The first step in COGents was the definition of these agents and the elaboration of a generic design and implementation approach. We associate a Wrapper Agent to each CAPE-OPEN component. Each Wrapper Agent provides the following services:•Request a dynamic connection to component.•Invoke operations on the component.•Query the properties of the component.•Set the parameters of the component.•Manage the state of the component.•Terminate the service.The CAPE-OPEN component-based Wrapper Agents are generic. They can be therefore provided with the library of the various CAPE-OPEN components.These agents are useful to control the simulation. However, other agents are useful to facilitate the design of a simulation. These agents are:•PME Wrapper: manages the interactions between a PME and the other agents. It allows 1) to observe the designer’s actions, 2) to change the model when needed, and 3) to provide helps to the designer.•Library Wrapper: manages the interactions between the agents and an existing local library of components.It has a description of all the components of the associated library; they are described by instantiating OntoCAPE classes. OntoCAPE and these instances are used to process the received requests from other agents.•Internet-Component Wrapper: manages the interactions between the agents and existing library of components on Internet. It is similar to the Library Wrapper agent but it does not use the same tools to communicate with the associated components.These wrapper agents are often reactive. Their goal is to respond to the requests of the other agents (i.e. Match-Maker). For example, the two last ones receive requests with some properties of components. They process the request and send the results to the sender of the request. These results are descriptions of the components that match the requirements of the sender.3.2Cognitive AgentsWe often consider that the simulation designer is an expert and the problem description is consistent. This designer can therefore define the model, and then find and select the suitable components to build his solution. This is not always true:•The user does not always have the model, he/she may have only a part of the model or the problem to solve (Inputs/outputs) without the associated model.•The library of components is now very large. So, it is not easy to select the suitable components.•The designer may need a component that is not provided in the library. He has therefore to look for these components on the Internet and/or intranets.•It is not easy to avoid inconsistency. The designer cannot learn all the component characteristics. So, the combination of some components may evolve some inconsistencies.•The problem description is not always consistent and the user can change or update this description at any moment. So, what is right at one moment might become incorrect later. For example, the user can decide to replace one component by two other components to improve the efficiency of his simulation.In this section, we propose examples of cognitive agents that seem very useful:•Personal Assistant Agent: manages the interaction between the system and the designer (user). For each designer there is an associated Personal Assistant Agent which has knowledge of its user preferences and skills with regards to the application. The role of the designer in COGents is to build a simulation. So, the Personal Assistant Agent interacts dynamically with the designer to define the problem or the model.Moreover, it can help novice designer to learn the PME.•MatchMaker: selects the components in the library of components (catalog) or on the Internet and/or intranets that match a given description of the problem or a task specification.•ModelingTaskManager: interacts with Personal Assistant Agent and uses OntoCAPE to define a consistent specification of the modeling task.•IntegrationManger: Manages the interaction between MatchMaker and PME Wrapper. It Provides extra support, when necessary, for the integration of components identified by the MatchMaker into the PME Wrapper. In particular, it translates the descriptions of selected components returned by the MatchMaker into a form usable by the PME Wrapper.Another category of cognitive agents allows to observe the execution of this organization to 1) detect run-time inconsistencies, 2) improve the efficiency of the simulator, 3) detect failures of the components, etc. These agents have not been studied yet.3.3Examples of interaction diagramsThis section describes two scenarios to illustrate the interactions between the various agents.Figure 4 presents an interaction diagram which illustrates the needed agent interactions to find a suitable component. The user builds a simulation through the PME. PME Wrapper sends the given task description to Personal Assistant Agent. This user has been identified as a non-novice user by Personal Assistant Agent. The latter sends therefore the given task description to Modeling Task Manager. The latter checks the consistency of this task description. If it is not consistent, it interacts with PME Wrapper to help the user to make it consistent. Otherwise, it sends a task specification to MatchMaker to select the components that match this modeling task specification. To find these components, MatchMaker needs to interact with Library Wrappers. If it has not their addresses, it sends an ask-all message to the Directory Facilitator (DF) asking for all the available components libraries. DF provides therefore the addresses of the wrapper agents of the available libraries. MatchMaker sends then a call for proposal message to all these wrappers. The latter perform some reasoning to find components that match the description and propose to MatchMaker these components. MatchMaker selects components that match the task specification and sends these components to Integration Manager. Finally, the new model is sent to PME Wrapper which integrates this new model in the flow sheet.Figure 5 describes an interaction diagram which illustrates the process modeling of a more complex task. The latter requires decomposition in elementary tasks. The first steps are similar to the previous example steps (see Figure 4). But in this example, MatchMaker fails to find suitable components. It sends therefore a request to Modeling Task Manager. The latter interact with the use to decompose the task and sends back the new elementary task specifications to MatchMaker. The latter tries then to find the suitable components for each task specification.Figure 4: Example of agent interactions to select a component.Figure 5: Example of agent interactions to decompose a task.4.ImplementationFigure 6: Architecture TechnologyThe various agents have been implemented with the platform DIMA [Guessoum and Briot 1999]. The latter provides a set of JAVA classes that have been reused to implement easily agents. The distribution of DIMA’s agents relies on the framework DarX3. DarX allows to distribute agent in a very transparent way. In DIMA, agents communicate by using FIPA ACL (Agent Communication Language) [FIPA 1998]. Figure 6 gives an overview of the realized architecture.To use OntoCAPE, DIMA has been enriched to provide agents with: 1) a DAML+Oil ontology and 2) an ontology reasoner (JTP –Java Theorem Prover- [Gleb 1999]). The message content can be described either in DQL (DAML Query Language) or KIF (Knowledge Interchange Format).5.Related WorkSeveral multi-agent systems have been proposed to support process engineering. A. Struthers [Struthers 1997] proposed an autonomous agent-based solution for the modeling of design processes. This solution is applied for organizing and managing a pressure relief and blowdown study.3 for more information, see http://www-src.lip6.fr/darx/R. Batres et al. [Batres et al., 1999] proposed an agent architecture for planning and control of a plant. These agents are based on the concept of controlled group unit (CGU) developed by Naka [Naka 1989].P. Tichy et al. [Tichy et al., 2002] proposed a 3-tier multi-agent architecture for planning and control of HAVC (Heating Ventilating and Air Conditioning) where the bottom level has physical connection to the hardware and it is responsible for local real-time control, the middle level contains smaller group of agents, and the top level maintains the overall goal of the system and gives strategic decisions.These various agent-based solutions and architectures propose interesting solutions to simulate and to control processes. However, they do not use agents to support process modeling. Moreover, some work has been done in the field of software agents on the Internet. For instance, RETSINA (Reusable Environment for Task-Structured Intelligent Networked Agents) has been successfully applied in several domains such as financial portfolio management, personalized web information management and k-buying auctions [Sycara et al., 2002]. The most important concept in RETSINA is the matchmaking process using middle agents (MatchMaker agents). The use of a matchmaking agent facilitates the search of agents, by advertising and requesting services. This idea is similar to the one used in COGents to select the suitable components.Steven C. Laufmann [Laufmann 1997] provides a good example of the use of wrapper agents to integrate legacy systems into a multi-agent architecture for enterprise applications (see also [Wooldridge et al., 2001]). The use of wrapper agents in COGents facilitates the integration and control of components.6.ConclusionThis paper presented a new approach to facilitate the design of process models. This solution combines several technologies and paradigms to represent this knowledge: components, ontology and agents. It aims to integrate, in the system, the knowledge of several experts.A prototype has been realized to validate the proposed ontology (OntoCAPE) and the proposed agent-based architecture. Several case studies are used to validate the generic agent-based organization and refine the agent knowledge. Our first experiments are based on a local library of components. The next step is the validation of this architecture with several kinds of component libraries (local, Internet, intranets) and its validation on a real world application.AcknowledgmentsProject COGents, Agent-Based Architecture For Numerical Simulation, funded by the European Community under the Information Society Technologies Program (IST), under contract IST-2001-34431.7.References[Batres et al., 1999] R. Batres, S. P. Asprey, T. Fuchino and Y. Naka. 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First International Workshop, AOSE 2000, Limerick, Ireland, June 10, 2000.。