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bluxwell铜虫 (初入文坛)
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[求助]
英译汉，急
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求助翻译下面内容，万分感激！ Comalco Alumina Refinery Located Gladstone,QLD Comalco-100% Rio Tinto Owned Stage One Announced October 2001-1.4Million tpa Came on-line September 2004 Rapidly approaching nameplate production rate Planned for 3 Stages-4.2 mtpa Australia’s Newest Alumina Refinery Presenters -Terry Snow : Process Control Superintendent -Jason Freyling : Process Control Engineer Presentation Overview Simulator-Cost Benefit -System Overview -Strategy for sustaining a simulator post commissioning -Cost/Benefit Analysis for 2005 -Application Case Study-Digestion Feed Pump Jump-Over -Application Case Study-7# Digestion Feed Pump -Lessons learnt Simulator – System Overview Developed by Honeywell as part of the CAR 1 construction project Estimated cost to commissioned (internal and external) ~A$4.5M Accepted by Management that Simulator paid for itself -For plant commissioning/start-up period -This is not relevant today (apart from credibility) Challenge-sustaining simulator post commissioning – can it be justified, how to do it System Benefits>System Sustaining Costs Training benefit diminishes over time* Support Costs need to diminish over time CAR Simulator Asset Intent – for lifetime of refinery Simulator Sustaining Strategy SWOT analysis – clearly identify costs and benefits – Formal annual C/B Maximize Benefits (not easily related to $ - really usage) -Number of operators trained -Number of control app’s tested (fast response to request) -Number of Procedures developed -Extend usage base (QA, Process Engineers) Minimize Costs (quantitative $) -Reduce effort required to resynch DCS (automation/tools) -Provide adequate simulator fidelity (qualitative assessment) -Provide adequate simulator scope (minimal effort for duplicated plant) -Labour substitution (right hourly rate for parts for parts of work) -Incremental Resynch + Full Resynch (at least 1 full per year per model) Console Training based Simulator System Simulator Training System Simulator Cost/Benefit Simulator Cost/Benefit – 2005 Costs (system, not training) - Internal Labour (1185 hrs) Resynch Trainer Support Documentation, Tool development - External Labour (305 hrs) Resynch Cap Project Tech Assist Train the trainer - License (HSE&SP) - Travel and Accom Total Cost ~$160,000 - 7 Full Resynchs - Multiple partial resynch’s - Resynch effort reduced from 120 hr to 20 hrs - Significant reduction in use of external labour Benefits (usage) - 21 operators trained 4 standard Boiler Tickets 2 Advanced Boiler Tickers - 4 Trainers trained - 7 Significant Process Control usages Liquor Filtration Master Sequence Dig . Feed Pump Cross-over Coal Mill 1A sequence abort Incorrect control action – Hydrate Flow Condensate Alarm rationalization Alternative design in Boilers to reduce RegPV’s Developed Standardized Work Practices for Calcination CRO’s Simulator Benefit Case Studies Digestion feed pump interlocks/trips - one of the refineries key safety controls - significant potential for equipment damage - significant potential for environmental incident Case 1: JPU Jump-over Case 2: 7th digestion slurry feed pump –swappable spare - simulator testing - verification of HPM Code - DCS testing - problems encountered CAR Digestion Trains Digester Feed Pumps Case 1: JPU Jump-Over Failure of 2 crank shafts in digestion slurry feed pumps of unit 1 Feeding one unit 1 digester from unit 2 feed pump Lost production due to having a whole unit down - flah tanks require that there be at least 2 trains on per unit Would involved leaving a unit offline for extended period Jump-over was in place for about 3 weeks ~7 days production From Decision to proceed to commissioning was 3days Pig Catching Station Case 1: Logic Connections Case 1: JPU Testing Procedure Using simulator , tested feasibility of jump-over from unit 1 train 1 to unit 2 train 1 - preliminary tests done to determine viability - unit start-ups and trips - was done in ~ 3 hrs Management decision to implement was late Wednesday afternoon Simulator configuration and logic on simulator configured late Thursday afternoon Testing of interlocks and control was done on the Friday morning Implementation and Testing on DCS done Friday afternoon Commission 11pm Saturday night 13 configuration changes, approximately 50 graphic modifications and 1 CL modification 24 trip/interlock tests to confirm logic connections Management sign off on risk based on quality of simulator testing Benefit: 14 days of 50% plant production Case 2: 7th Digestion Feed Pump CAR originally had 6 pump – 1 per train, no spare 7th – Spare that can operate in the duty of any of the other 6 Goal – reduce downtime of digestion trains because of pump availability Over 600 interlock tests carried out to prove logic Significant change to be done to an online plant All tests pre-done on simulator - prevent config errors on-line - only suitable platform to do large scale testing without plant impact No production loss associated with the logic changes Other forms of testing would have delayed the project – and cost production. The 7th pump was used 15 times in its 1st month of operation – significant production impact Case 2: Schedule DCS design meeting held early February - had to redesign all of the logic associated with the 6 existing pumps to allow for the interconnections to the digestion trains and the 7th pump Operations requirement for operator training by April - logic design had to be finalised quickly - simulator implementation completed on schedule. - decision made to test all control and interlock strategies in simulator - again completed before operator training 7th pump onsite late March 7th commissioned 1st week May Case 2: Logic Diagram Case 2: Modification Scope Unit based interlocks Will trip the whole digestion unit. 7th can be lined up to either of 2 units Train based interlocks Trips train when things like back pressure Hi. 7th can be lined up to any of 6 trains Pump based interlocks Some of the interlocks are in PLC and some in DCS. Feedfoward control signals Back pressure and feed tank levels Alarm strategies Contcutting of alarms on offline trains CL changes Decoding of PLC data Graphic modifications Status displays, operator displays Case 2: Implementation of Changes Large scale change - ~ 16000 lines of EB source involved in the change - ~ 150 HPM points - 7 existing graphics - 5 new graphics Built basic code in DCS for 1 of the pumps - didn’t impact on online trains Edit EB files to generate first pass of code for all of the pumps Loaded EB’s into the simulator Made modifications in the simulator as a result of testing Strict version control on EB source - EB files kept close to code in the simulator - not an automated process Pump Status Display Start Permissive Graphic Testing of Code – Simulator Example of Text Matrix Case 2: verification of code Ensuring code in DCS was what was tested in simulator Built a dummy set of simulator code from EB files Copied the actual simulator code from the simulator configuration Compared using CSDiff Reviewed and discrepancies so that the code to be loaded on DCS was the same as simulator code Implementation/Testing on DCS Changes on DCS had to be done when each digestion train was down Usually had between 1 hour and 1 day notice of when the pump would be down Repeated a similar set of interlock tests on pump after logic modifications on DCS Unit interlocks could only be tested if the whole unit was down. Approx 50 tests to be done on each train Tests took typically 2 hours to perform – production critical No surprises – no production loss because of delays fixing logic – due to pre-testing on simulator Problems Encountered 1 minor error detected in DCS code after implementation - forgot to re-setup an Automan block to allow external swiching Poit was not in scope of original changes 1 minor testing mistake on DCS - forgot to put an LIC back into PVAuto after testing. Overflowed a small amount of caustic Lessons Learnt Significant project and testing required. Simulator performed well for this task. - easy to reconfig when errors found -simulator model changes were fast, did not hold up project Simulator enabled comprehensive testing - not possible on real system with-out stressing plant or causing a production loss DCS implementation went well - no production loss during of DCS implementation - simulator eliminated live config changes to correct errors Simulator testing identified a line-up start permissive -preventing pump from starting when line-up isolations incorrect Verification difference in automan block (EXTSWOPT) was not part of original scope. Conclusion Simulator testing was a good way to implement project Simulator not just a training tool – even in a running plant Comprehensive testing of new code in a running plant is difficult Likely that logic errors would have been made without the comprehensive testing on the simulator |
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bluxwell
铜虫 (初入文坛)
- 应助: 0 (幼儿园)
- 金币: 166.5
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- 在线: 2.6小时
- 虫号: 475612
- 注册: 2007-12-07
- 性别: GG
- 专业: 矿物工程与物质分离科学
4楼2008-07-03 15:51:20
snipher950
木虫 (正式写手)
- 翻译EPI: 3
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- 帖子: 797
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- 虫号: 522854
- 注册: 2008-03-12
- 性别: MM
- 专业: 化工系统工程
2楼2008-07-03 08:07:55
snipher950
木虫 (正式写手)
- 翻译EPI: 3
- 应助: 2 (幼儿园)
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- 帖子: 797
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- 性别: MM
- 专业: 化工系统工程
★ ★ ★ ★ ★ ★ ★ ★ ★ ★
bluxwell(金币+10,VIP+0):翻译的比较用心，谢谢了。要是能全翻译了就好了。
bluxwell(金币+10,VIP+0):翻译的比较用心，谢谢了。要是能全翻译了就好了。
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再来两句： Rapidly approaching nameplate production rate 快速接近名牌产品 Planned for 3 Stages-4.2 mtpa 第三阶段计划年产4.2百万吨 Australia’s Newest Alumina Refinery 澳大利亚最新氧化铝精炼厂 Presenters 推荐者 -Terry Snow : Process Control Superintendent -Terry Snow：过程控制负责人 -Jason Freyling : Process Control Engineer -Jason Freyling：过程控制工程师 Presentation Overview 陈述的概要 Simulator-Cost Benefit 模拟器耗费的收益 -System Overview 系统概要 -Strategy for sustaining a simulator post commissioning 维持验收后运行模拟器的阶段 -Cost/Benefit Analysis for 2005 2005年成本/收益分析 -Application Case Study-Digestion Feed Pump Jump-Over 应用实例-消化给水泵 -Application Case Study-7# Digestion Feed Pump 应用实例-消化给水泵 -Lessons learnt 所学课程 Simulator – System Overview 模拟器-系统概要 |
3楼2008-07-03 08:30:30
google translate 翻译结果，差不多就知道所有的意思了，呵呵！
★ ★ ★ ★ ★ ★ ★ ★ ★ ★
bluxwell(金币+10,VIP+0):谢谢了，翻译的不是很准
bluxwell(金币+10,VIP+0):谢谢了，翻译的不是很准
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comalco氧化铝炼油厂 位于格拉德斯通，昆士兰 comalco - 100 ％ Rio Tinto的国有 阶段一宣布， 2001年10月- 1.4million的TPA 来到上线于2004年9月 迅速接近名牌产率 计划为3个阶段- 4.2 mtpa 澳洲最新的氧化铝提炼厂 主持人 -特里雪：过程控制总监 -贾森freyling ：过程控制工程师 概况介绍 模拟器-成本效益 -系统概述 -战略维持一个模拟器后，委托 -cost/benefit分析2005年 -应用案例研究消化进料泵跨越式 -应用案例研究- 7 ＃消化给水泵 -吸取的教训 模拟器-系统概述 霍尼韦尔公司研制的一部分，汽车一建设项目 估计费用为委托（内部和外部） ～一元4.5米 接受管理模拟器支付本身 -植物委托/初创时期 -这是不相关的今日（除了公信力） 挑战维持模拟器后，委托-可以是合理的，怎么做 系统效益> “系统维持费用 培训有利于削弱随着时间的推移* 支持费用有必要削弱随着时间的推移 汽车模拟器资产的意图-终身炼油厂 模拟器维持战略 SWOT分析-认清的成本和效益-正式的年度的C / b 最大利益（不容易与美元-真的使用） -营办商的数目受训 -数目控制应用程式的测试（快速反应要求） -一些程序开发 -延长使用基地（质量保证，工艺工程师） 费用减少到最低限度（定量元） -减少的努力，需要resynch区议会（自动化/工具） -提供足够的模拟器富达（定性评估） -提供足够的模拟器范围（最小的努力，为重复的植物） -劳工替代（右每小时收费为零件的部分工作） -增量resynch +充分resynch （至少1充分每人每年模型） 控制台基于培训 模拟器系统 模拟训练系统 模拟器成本/效益 模拟器成本/效益-2 005年 成本（制度，而不是培训） -内部劳动力（ 1 185小时） resynch 教练机支持 文件，工具开发 -外部劳动力（ 3 05小时） resynch 上限项目 技术协助 培训教员 -许可证（ H SE的＆ S P）的 -旅行和a ccom 总成本～ $ 160,000 -7充分r esynchs -多个局部r esynch的 -r esynch努力减少由1 20小时至2 0小时 -显着减少使用外部劳工 利益（使用） -训练有素的2 1家运营商 4标准的锅炉门票 2先进的锅炉代号 -4名教员受到了培训 -7显着的过程控制用法 酒过滤大师序 挖。给水泵跨超过 煤磨第1 A序列流产 不正确控制行动-水合物流 冷凝报警合理化 另类的设计在锅炉，以减少regpv的 制定了标准化工作的做法，焙烧所长， CRO的 模拟器受益的个案研究 消化进料泵联锁/人次 -一个炼油厂关键的安全控制 -具有很大的潜力，设备损坏 -具有很大的潜力，环境事件 案例1 ： jpu跨越式 案例2 ：第七消化料浆进料泵抽换备件 -模拟器测试 -核查H PM的代码 -区议会的测试 -遇到的问题 汽车消化列车 沼气池给水泵 案例1 ： jpu跨越式 失败的2曲柄轴在消化泥浆给水泵1号机组 饲1 1号机组沼气池，从2号机组给水泵 生产损失，由于有一个整体下跌 -f lah坦克需要有至少2列车上每单位 将所涉及的离开一个单位的离线延长服务时间内， 跨越式是在地方，约三周～ 7天内生产 从决定进行委托是三天 猪赶上站 案例1 ：逻辑连接 案例1 ： jpu测试程序 使用模拟器，测试的可行性，跳转-从1号机组列车1至2单元列车1 -初步测试，以确定是否可行 -单位初创公司和旅游 -是这样做～ 3小时 管理决定实施迟到周三下午 模拟器的配置和逻辑模拟器配置晚周四下午 测试联锁和控制是做对周五上午 实施和测试就区议会所做的星期五下午 委员会晚间11时星期六夜 13配置的变化，大约50个图形修改和一氯改性 24日之旅/联锁测试，以确认逻辑连接 管理签署的关于风险的基础上的质量模拟器测试 好处：在14天内的50 ％ ，植物生产 案例2 ：第七消化给水泵 汽车原本六泵-一％ ，火车，没有多余的 第七-备件，可以在运作的责任，任何其他6 目标-减少停机时间的消化列车，因为泵供货 超过600联锁进行的试验证明的逻辑 重大的改变做一个在线植物 所有测试前所做的模拟器 -防止错误配置上线 -只适合平台做大规模的测试，没有植物的影响 没有生产损失相关的逻辑变化 其他形式的测试将延迟项目-和生产成本。 第七届泵用的15倍，在其第一一个月的运作-重大生产的影响 案例2 ：附表 区议会的设计举行的会议2月上旬， -不得不重新设计所有的逻辑与6现有的水泵，以便相互联系，以消化火车和第七泵 行动的要求，操作人员培训4月 -逻辑设计要尽快敲定 -模拟器执行如期完成。 -作出的决定，以测试所有的控制和联锁的策略模拟器 -再次前完成，操作员培训 第七水泵站3月下旬 第七委托第一周可能 案例2 ：逻辑图 案例2 ：修改范围 单位基于联锁 将访问整个消化股。第七，可排队等候的任何2个单位 火车基于联锁 班列车，当事情想回压喜。第七，可排队等候的任何六列车 泵基于联锁 部分的联锁是在PLC和一些在DCS中。 feedfoward控制信号 回到压力和饲料坦克水平 报警战略 contcutting的警钟，对离线列车 氯离子的变化 解码PLC数据 图形修改 状态会显示，操作显示 案例2 ：执行的变化 大规模的改变 -～ 1 6000线的电子束源所涉及的变化 -～ 1 50点，高功率微波 -7现有的图形 -五月新的图形 兴建基本准则，在区议会为一的水泵 -没有影响，线上列车 编辑文件的电子束来产生首先通过代码为所有的水泵 加载电子束的进入模拟器 作出修改，在模拟器作为一个测试的结果 严格的版本控制，对电子束源 -电子束的文件保持着密切的代码在模拟器 -不是一个自动的过程 泵的状态显示器 开始，宽容的图形 测试代码-模拟器 例如文本矩阵 案例2 ：验证码 确保代码在DCS是什么测试，在模拟器 建立了一个虚拟的一套模拟器代码从电子束档案 复制的实际模拟器代码从模拟器配置 相比，使用csdiff 审查和差异，使代码加载在DCS上是一样的模拟器代码 实施/测试区议会 变化对区议会不得不做时，每个消化列车下跌 通常之间的1小时和1天通知时，泵将下降 反复一套类似的联锁试验，对泵逻辑修改后，就区议会 单位联锁只能测试如果整个股则下跌。 约50测试，以做到对每个列车 测试了，通常2小时演出-生产的关键 没有惊喜-没有生产损失，因为延误固定的逻辑-由于预测试对模拟器 遇到的问题 一小错误侦测码在DCS实施后 -忘了重新安装一a utoman座，以允许外部s wiching poit不是在原有的范围变化 一轻微的测试错误，就区议会 -忘了把一菱里克回p vauto后测试。溢出少量的苛性 吸取的教训 重大项目和测试要求。模拟器的表现良好，为完成这项任务。 -容易r econfig时，发现错误 -仿真模型的变化速度快，没有举行后续项目 模拟器启用了全面的测试， -不可能对真正的系统与淘汰，强调植物或造成的生产损失 区议会的执行情况，以及到 -没有生产损失在区议会的执行情况 -模拟器淘汰活配置的变化，以正确的错误 模拟器测试，确定了线的后续开始宽容 -防止泵从开始时，线的后续隔离不正确 核查的差异automan块（ extswopt ）没有参加原来的范围。 结论 模拟器测试是一个很好的方式，落实项目 模拟器不只是一个培训工具-即使是在运行的核电厂 全面的测试，新的代码在运行的核电厂是困难的 可能是逻辑错误，将已没有全面的测试，对模拟器 |
5楼2008-07-04 00:32:02