第一篇：文具-本册类工艺 中英文对照
Clamp [klæmp] 夹
Divider隔页
Punch[pʌntʃ]、Perforation穿孔、钢线；perforation line钢线
Transparent透明的Wirespiral 线圈
Solid 立体
Lamination覆膜、过油
Assorted 混合的Gold embossing、gold stamping烫金
Embossing 压印
Display展示盒
Double spiral双线圈
Elastic/elastic strap [stræp], rubber橡皮筋；圆橡皮筋 round elastic Polybag with 4c printed header 4色印刷的卡头袋
Metal Button 金属扣sheet of sticker paper printed 4c with diecut1张4色印刷的不干胶＋模切 Saddle-stitched 骑马钉
Slipcase ['slipkeis] 书套
Insert 插入
Bookmark 丝带
Silver stamping 烫银
Padded both side 双面胖
Headband堵头布
Year planning 年历
Index address book 索引地址本
White cardboard/ivory cardboard 白卡creating line on the Middle of the back cover封底中间压8条线
Silk screen printing 丝网印
Picture frame 镜框、相框
Glitter 撒金粉
Ring book 铁环本
Shrink 热缩
White solid 钛白片
Wood-free paper双胶纸、全木浆纸W/F
Book binding cloth 装帧布
Groove 压背，压槽
Cover with stitching 封面踩线
变色PU thermal PU
分批出货 split shipment
PU拼接 double PU with sewing
进仓通知 shipping notice/delivery notice
电放（电报放货）telex release
ETA 估计抵达时间estimated time of arrival
ETD 估计发货时间estimated time of departure
无酸纸 acid ['æsid]free paper
亮光膜glossy film
哑光膜matte film
板夹clipboard
空舱费、亏舱费dead freight
让步、妥协，折中 compromise ['kɑmprə,maɪz]
假皮、人造革artificial leather ['leðə，'leðə(r)] /leatheriod
卡片纸cardstock
尼龙扣Velcro ['velkrəu]closure
彩金multi-color stamp；hot-stamping mutilcolor
拼箱LCL: less than container load
海运提单 marine [mə'ri:n]（ocean）bill of lading
原产地证certificate [sə'tifikit] of origin ['ɔridʒin]；Form A
退款 refund money
灰板 gray board
潘通色卡（国际色卡、彩通）Pantone
彩条 colour ribbon ['ribən]
总箱数TTL cartons
即时贴；便签盒memo pad
类别category
目录册catalog
热转移油墨印heat-transfer printing
技术人员technician [tek'niʃən]
倒（圆）角fillet
汇款remit
余款balance
定金、押金deposit
期货；前途、未来futures
启示；预言；广告词message
最低价rock-bottom price
让步come to terms、concede to、yield
相互让步；将就meet each other halfway
We can't make any further concessions。我们不能再让步了。
促销promotion
确认；证实confirm（conformation）
邀请invite→invitation→invitational（仅限于被）邀请的Eg：she received an invitation to the party。
市场market
市场性；流通性；销售能力marketability
开始做……吧get the ball rolling by doing……
Let's get the ball rolling by discussing the price。
销售某产品push the sale ofSTH
预定make a reservation [,rezə'veiʃən]、book、order
说话欠考虑speak without due consideration
好久不见Long time no see！
只工作，不玩耍，聪明JACK也变傻！All work and no play makes Jack a dull boy。
请稍等。Excuse me for just a second/moment/minute.承蒙约翰的介绍By the courtesy ['kə:tisi] of Mr.Johnson
约会appointment，date
对……投资invest on……
给某人捎口信（以便……）leave sb.a message（to do）……
刚才just now=a moment ago
立刻，马上right now=right away=at once=immediately
打给某人某号码call SB.at +telephone number
到目前为止一切顺利。So far so good。
典礼，仪式；礼节、礼貌ceremony开幕式 opening ceremony['seriməni]
准备prepare→preparation
运输（n）transport运输方式transportation
大量的；实质性的（adj）本质；重要材料（n）substantial
推断；决定，做结论；结束conclude
Eg：我希望与您签下大单生意。I hope to conclude some substantial business with you。
会议（持续几天的大型会议）conference
电话会议conference call
孔子Confucius儒教；儒家学说Confucian 孔子的；儒家的；儒家信徒Confucian
有时间从事、接待某人；相处融洽；容纳fit in
Eg：Dr.White says he can fit in only two more patients this morning。
I am sure you can fit me in somewhere。我相信你能找个地方安置我。
Are you able to fit a tour of the city in？你能安排市容游览吗？
彻底的；十分的；完全的thorough→周密地thoroughly
设备，设施；器材 equipment，facility
签合同sign a contract/conclude a contract
签字，签名signature
专业技能，职业行为，职业特征；专业气质professionalism [prə'feʃənə,lɪzəm]
殷勤，好客；食宿招待；款待；服务hospitality
把……打动win sb over
客户；顾客；委托人；客户及程序client
顾客；客户；消费者customer
购物者；顾客shopper
First impressions count。第一印象很重要。
有代表性的（adj）；代表，代理人；众议员representative
潜在的potential 潜在客户potential customer
交货期delivery date
忙碌的hectic，（busy）；狂热的（crazy）
把A换成B change A for B
汇率exchange rate
承担bear 承担额外费用bear the additional charge
名片business card/visiting card
Eg：They exchange business cards with each other。
UV油墨 UV oil
光油 gloss oil，gloss paint，白卡纸 white cardboard，ivory board，art post paperboard
铜板卡纸 art postcard board；ivory cardboard
圆角 round Corner
骑马钉 saddle stitching
粘裱 mounted 对裱 double mounted，mounted face to face
三裱 triple mounted，mounted twice
冲压（用模具使材料分离）；压模stamping
凹凸印；浮雕emboss，embossing
压印（模具端面压入板坯，使模具上的花纹等压在板坯上）coining
压痕（在毛坯表面压出痕线，以便压肩）indentation
热压印 hot coining
烫印 Hot stamping（gold/silver）
缝接sew 接驳，切驳sewn，sewed
缝合 oversew
过油（丝网印）plastic coating with gloss oil；涂布plastic coating
UV（一般丝网印）silk screen printing
抽时间去做……take time to do……
（短期）膳宿accommodation 贷款；住宿
英镑，pound，pound sterling，£
CIF:cost，insurance [in'ʃuərəns] and freight
FOB：free on board
把质量纳入考虑范围take the quality into consideration
优良的，较好的，超级的superior（to）
Eg：Our spiral notebook are of superior quality to those from other countries。
合成的，人造的；非天然的synthetic
人造的，人工的artificial人造革artificial leather/leatheroid
享有；有资格获得be entitled to
为……而战fight for……为订单而战fight for orders
打七折30% discountcut down to 70%/cut down by 30%
为了表示……as a gesture of……为表示友谊as a gesture of friendship
瓦楞纸箱子corrugated cardboard box
能给我们留样吗？Can you leave samples with us？
印象深刻的 impressiveThe teacher is an impressive one。
性能performance、capability性能优良high performance，performs satisfactorily
功能 function有用的，实用的functional；实际的，实践的practical
（有实行可能）实用性practicability
（实践性；实际性）实用性practicality
（有效；有益；）可得性；可利用性availability
（功用，效用）实用 utility
年度出口销售量 annual export turnover
R & D research and development研发
支付条件：电汇，信用证/信用状payment terms：T/T(TelegraphicTransfer), L/C（Letter of credit）（样品备货时间）样货期 sample lead time
生产交货期 productions lead time
备忘记事本memo notepad，organizers（万用手册）
文件夹file folders文件袋 file bags文件夹 file shelf
板夹 clipboard
素描本 sketch book
地址本 address book
名片册 business card/visiting card holder
冰箱贴 shopping list
装货港口 loading port
装运期限 time of shipment
起运国 country of origin
账号 account number
分页夹 paging clip
异型夹 abnormal shape clip
报关 declare STH at the customs；customs clearance；clearance of goods
调拨单 transferring order
核销 verification，cancel
合同项目 CI：contract items
（装）箱单 PL:packing list
20尺柜：20'GP40尺高柜：40'HQ
船东提单 MBL：master bill of lading
货代提单 HBL：house bill of lading
参加 join，attend，take part in，participate in，go in for，be in for
Eg：They are in a training/taking part in a training。
请假 ask for leave、take a leave、take offfrom work
Eg：She asked for a leave of three days。她请了3天假。
She is out on leave。她请假在外。
捎口信 leave a message to sb./leave sb.a message
替…捎口信 take a message for sb.I'll leave a message to her for you。/I'll leave her a message for you。/I'll take a message to her for you。节省；抽出，让给；免除
珠光料 iridescent[ˌɪrɪˈdesənt] 内芯版式 inner block
第二篇：红木类商品名中英文对照
一、紫檀木类
1、檀香紫檀（Pterocarpus santalinus L.F.）主产于印度南部。商品名red sanders, red sandalwood
二、花梨木类
1、越柬紫檀（Pterocarpus cambodianus Pierre）主产于越南、柬埔寨、泰国。商品名为Vietnampadauk, thonong
2、安达曼紫檀（Pterocarpus dalbergioides Benth.）主产于印度安达曼群岛。商品名为Andaman padauk，Andaman redwood,vermilion
3、刺猬紫檀（Pterocarpus erinaceus Poir.）主产于热带非洲。商品名为ambila
4、印度紫檀（Pterocarpus indicus Willd.）主产于印度、缅甸、菲律宾、巴布亚新几内亚，马来西亚及印度尼西亚，中国广东、广西、海南及云南引种栽培。商品名为amboyna，Burmacoast padauk, sena, Manilla padauk, narra
5、大果紫檀（Pterocarpus macarocarpus Kurz）主产于缅甸、泰国和老挝。商品名为Burma padauk, pradeo, may dou
6、囊状紫檀（Pterocarpus marsupium Roxb.）主产于印度。商品名为bijasal, narra,padauk
7、鸟足紫檀（Pterocarpus pedatus Pierre.）主产于东南亚中南半岛。商品名为maidu
三、香枝木类
1、降香黄檀（Dalbergia odorifera T.Chen）主产于中国海南。商品名为scented rosewood
四、黑酸枝木类
1、刀状黑黄檀（Dalbergia cultrate Grah.）主产于缅甸。商品名为Burma blackwood, Indian cocobolo
2、黑黄檀（Dalbergia fusca Pierre）主产于东南亚及中国云南。商品名为black rosewood, yinzat
3、阔叶黄檀（Dalbergia latifolia Roxb.）主产于印度、印度尼西亚的爪哇。商品名为Indian rosewood, sonkeling, sonobrits, Bombay blackwood, rosewood, java-palisandre, angsana keeling
4、卢氏黑黄檀（Dalbergia louvelii R.Viguier）主产于马达加斯加，商品名为Bois de rose
5、东非黑黄檀（Dalbergia melanoxylon Guill.& Perr.）主产于非洲东部，商品名为African blackwood，Mozambique ebony, African rosewood
6、巴西黑黄檀（Dalbergia nigra Fr.Allem.）主产于巴西。商品名为Brazilian wood, jacaranda
7、亚马孙黄檀（Dalbergia spruceana Benth.）主产于巴西。商品名为jacararda, Brazilian rosewood
8、伯利兹黄檀（Dalbergia stevensonii Tandl.）主产于伯利兹。商品名为Honduras rosewood, hogaed
五、红酸枝木类
1、巴里黄檀（Dalbergin bariensis Pierre）主产于热带亚洲。商品名为neans nuon
2、赛州黄檀（Dalbergia cearensis Ducke.）主产于巴西。商品名为kingwood, violetta, violetwood
3、交趾黄檀（Dalbergia cochinchinensis Pierre）主产于泰国、越南和柬埔寨。商品名Siam rosewood, paying, trac, kranghung
4、绒毛黄檀（Dalbergia frulescens var.tomentosa Tndl.）主产于巴西。商品名为Brazillan tulipwood, pinkwood
5、中美洲黄檀(Dalbergia granadillo Pittier)主产于墨西哥等中美洲。商品名为cocobolo
6、奥氏黄檀（Dalbergia oliveri Gamb.）主产于缅甸、泰国和老挝。商品名为Burma tulipwood, chingchan, tamalan
7、微凹黄檀（Dalbergia retusa Hesml.）主产于中美洲。商品名为cocobolo
八、鸡翅木类
1、非洲崖豆木（Millettia laurentii De Wild）主产于非洲刚果盆地。商品名为wenge, bokonge, awoung, uson-so
2、白花崖豆木
Millettia leucantha Kurz（M.pendula Bak.）主产于缅甸和泰国。商品名为thinwin, theng-weng, sothon
3、铁刀木（Cassia siamea Lam.）主产于东南亚，中国云南、广东普遍引种栽培。商品名为siamese senna
七、条纹乌木类
1、苏拉威西乌木（Diospyros celehica Bakh.）主产于印度尼西亚苏拉威西岛。商品名为macassar ebony, ebony, toetandu
2、菲律宾乌木（Diospyros philippensis Gurke）主产于菲律宾。商品名为kamagony
3、台湾乌木（Diospyros discolor Willd.）主产于斯里兰卡、菲律宾、中国台湾等东南亚地区。商品名为Ceylon ebony
六、乌木类
1、乌木（Diospyros ebenum Koenig）主产于斯里兰卡及印度南部。商品名为Ceylon ebony, Eastindia ebony, ebony
2、厚瓣乌木（Diospyros crassiflora Hiern）主产于热带西非。商品名为African ebory, black ebory, African persimmon
3、毛药乌木（Diospyros pilosanthera Blanco）主产于菲律宾。商品名为bolong-eta
4、蓬塞乌木（Diospyros poncei Merr.）主产于菲律宾。商品名为ponce’s kamagong
第三篇：烯烃转化单元中英文对照工艺1
OCU PROCESS DESCRIPTION
烯烃转化单元工艺说明
1.1 Plant Composition 装置组成
Shanxi Coking Company Ltd.intends to build a 104 kta Olefins Conversion Unit(OCU)in the Fine Coal Chemical Zone, Zhaocheng, Hongdong County, Shanxi Province, P.R.C.The capacity of the unit will be 104 kta polymer grade propylene based on 8000 operation hours per year.The plant feed will be the Mixed C4/C5 product from the Light Olefins Recovery Unit(LORU).In addition, the plant also produces the following by-products: 山西焦化股份有限公司计划在中国山西省洪洞县赵城镇精细煤化工园区建设一套10.4万吨/年烯烃转换装置（OCU）。该装置的生产能力为10.4万吨/年聚合级丙烯，年开工率8000小时。装置进料将采用来自轻烯烃回收装置（LORU）的混合C4/C5产品。另外，该装置还生产以下副产品：
Mixed C4 to N-Butene Unit
混合C4，输送至正丁烯装置 C4+ by-product Stream
C4+副产品流
SHU Vent Gas
选择加氢装置放空气体
OCU Vent Gas
烯烃转换装置（OCU）放空气体
DME Purge
二甲醚吹扫气体
The plant shall be flexible to handle 60-120% of normal capacity and designed for 36 months between turnaround.The plant shall be designed for an operating life of 20 years.本装置的操作弹性范围为正常生产能力的60-120%，并且装置大修的间隔应为36个月。装置的使用年限应设计为20年。
The OCU unit consists of the following sections 烯烃转化装置由以下工段组成： DME Removal
二甲醚脱除单元
1st Stage Selective Hydrogenation Unit(SHU1)1段选择加氢单元（SHU1）
2nd Stage Selective Hydrogenation Unit(SHU2)2 段选择加氢单元（SHU2）Debutanizer
脱丁烷塔
OCU Feed Treatment
烯烃转换装置进料处理 OCU Reactors
烯烃转换装置反应器 Deethylenizer
脱乙烯塔 Depropylenizer
脱丙烯塔 Regeneration System
再生系统
1.2 Process Flow Description 工艺流程描述 1.2.1 DME Removal
二甲醚脱除单元
Mixed C4’s/C5’s from LORU are fed on flow control to the DME Removal Column.This column removes most of the DME and Light Ends contained in the Mixed C4/C5 Feed.来自轻烯烃回收装置的混合C4/C5在流量控制下进入二甲醚脱除塔（299-T-3101），以脱除混合C4进料中的DME和轻组分。
The DME Removal Column pressure is set to allow the column overhead to be condensed against Cooling Water and reboiled using LP2 Pressure Steam.The tower net overhead is a small vent stream containing the DME removed from the feed, as well as any light compounds in the feed.The net overhead vent stream is recycled on flow control along with the 1st Stage Selective Hydrogenation(SHU-1)vent stream to the Charge Gas Compressor Second Stage Suction Drum.DME脱除塔的压力设定为能够通过冷却水对塔顶排放气进行冷凝，并通过低低压（LP2）蒸汽对其进行重沸。塔顶净排放气流量不大，含有从进料中脱除的DME以及进料中的轻组分。在流量控制下，塔顶净排放气与第一段选择加氢装置（SHU-1）排放气循环至进料气压缩机二段入口罐。
Heat input to the tower is controlled by a flow controller on the LP2 steam-heated reboiler.Periodic analysis of the bottoms assures the bottoms product contains no more than 5 wt ppm DME.The tower bottoms pumped and cooled against Cooling Water and sent on flow control, reset by level control, to the 1st Stage Selective Hydrogenation Unit.DME脱除塔热量输入通过LP蒸汽加热重沸器的流量控制器进行控制。对塔底物料进行定期分析，确保塔底产物中DME的含量不大于5wppm。塔底物料泵出后，通过冷却水进行冷却，然后在流量控制下（基于塔底液位控制器设定值）送入SHU一段。
1.2.2 1st Stage Selective Hydrogenation(SHU-1)1段选择加氢单元（SHU1）
The bottoms of DME column are fed to the SHU Feed Surge Drum.This stream is then pumped to 1st Stage SHU Reactor pressure on flow control, reset by level control, and mixed with a portion of the 1st Stage SHU Reactor effluent recycled back to the feed.This Mixed C4/C5 Feed stream is heated to the required reactor temperature in a Low-Low Pressure steam-heated heat exchanger and then mixed with Hydrogen on flow-ratio control.二甲醚脱除塔塔底物料进入选择加氢装置进料缓冲罐，并在流量控制下（基于进料缓冲罐液位控制器设定值）泵送至第一段SHU反应器，与循环回进料的一部分第一段SHU反应器流出物混合。混合C4/C5通过低低压蒸汽加热换热器加热至要求的反应器温度，然后按照流量比与氢气混合。
Hot Mixed C4’s/C5’s and Hydrogen then pass downflow through the 1st Stage SHU Reactor where butadiene is selectively hydrogenated to n-butenes and pentadienes are selectively hydrogenated to n-butenes and n-pentenes, respectively.Since the selective hydrogenation process is exothermic, a temperature rise occurs across the reactor.The heat of
reaction is absorbed by the C4/C5 stream as it passes through the catalyst bed.The reaction product is separated in the 1st Stage SHU Reactor Separator Drum.The vapor from the drum is cooled against Cooling Water to recover C4’s/C5’s which flow to the separator drum.The remaining vent gas is recycled to the LORU.The liquid from the separator drum is pumped to reactor pressure.Some of the liquid is recycled back to the reactor on flow control and the rest is cooled and fed the 2nd Stage SHU Reactor via flow control reset by the1st Stage SHU Separator Drum level controller.The feed temperature to the 2nd Stage Reactor is controlled by by-passing some of the liquid around the 1st Stage SHU Reactor Recycle/Product Cooler.Effluent from the 1st Stage SHU contains about 2300 wt ppm butadiene and pentadienes.热混合C4/C5和氢气然后向下流经第一段SHU反应器，在该反应器中丁二烯通过选择加氢处理被转化为正丁烯，而戊二烯通过选择加氢处理被转化为正丁烯和正戊烯。由于选择加氢反应为放热反应，反应器内部会出现温升。由于反应热沿催化剂床传递，因此使用C4/C5物流对反应热进行吸收。反应产物在第一段SHU反应器分离罐中分离。来自分离罐的部分蒸气由冷却水冷却以回收C4/C5，回收的C4返回分离罐，剩余排放气循环回LORU。分离罐液体通过泵提升至反应器压力，部分液体在流量控制下循环回反应器，剩余液体经冷却后按照第一段SHU分离罐液位控制器设定值以流量控制方式进入第二段SHU反应器。第二段反应器进料温度通过第一段SHU反应器循环物料/产品冷却器的液体旁通阀来进行控制。来自第一段SHU装置的流出物约含有2300wppm的丁二烯和戊二烯。
Gradual loss of catalyst activity will occur as the active sites on the catalyst become coked.Regeneration of the catalyst is required when catalyst activity has dropped to the point when the reactor outlet temperature of about 89℃ is reached.Regeneration requires the catalyst bed to be taken offline, drained and purged of hydrocarbons, heated with
hot nitrogen and then superheated with steam.Air is metered into the stream to decoke the bed.A final nitrogen purge that contains a controlled amount of hydrogen reduces the catalyst bed.随着催化剂活性中心逐渐结焦，催化剂将逐渐失去活性。随着催化剂活性逐步降低，当反应器出口温度达到约89°C时，就需要对催化剂进行再生。催化剂再生时要求催化剂床离线，并将反应器内部烃物料排出并吹扫干净，使用热氮气进行加热，然后使用蒸汽进行过热。以流量控制方式向物流中引入空气，以对床层进行清焦。使用含一定量氢气的氮气对催化剂床进行还原。
A spare reactor is provided so that production can be maintained while one reactor is regenerated.A SHU Reactor Regeneration Electric Heater is used to heat the hot gas mixtures used to regenerate the 1st Stage SHU Reactor catalyst.设置备用反应器可以保证在对其中一台反应器进行再生期间不会中断装置运行。SHU反应器再生电加热器用于加热第一段SHU反应器催化剂再生所需的热混合气。
1.2.3 2nd Stage Selective Hydrogenation(SHU-2)2段选择加氢单元（SHU2）
The 1st Stage SHU effluent contains about 2300 wt ppm butadiene and Pentadienes combined.The total butadiene and pentadiene content is further reduced to 50 wt ppm in the 2nd Stage SHU.The 2nd Stage SHU is a once-thru system with feed heating and effluent cooling.第一段SHU流出物中含有约2300wtppm的丁二烯和戊二烯，在第二段SHU装置中，将总的丁二烯和戊二烯含量进一步降至50wtppm。第二段SHU是一个单程系统，在系统中完成进料加热和流出物冷却。
1st Stage SHU effluent after pumping and mixing with hydrogen on flow-ratio control is heated to the hydrogenation reactor temperature in a LP2 steam-heated heat exchanger and then hot mixed C4/C5’s and
hydrogen then pass upflow through the 2nd Stage SHU Reactor where the remaining butadiene is selectively hydrogenated to n-butenes and pentadienes to respective pentenes.Since the selective hydrogenation process is exothermic, a temperature rise occurs across the reactor.The heat of reaction is absorbed by the C4/C5 stream as it passes through the catalyst bed.The reaction product is immediately cooled in the 2nd Stage SHU Reactor Effluent Cooler and flows to the OCU Fresh/Recycle C4/C5 Surge Drum through a back pressure controller.The controller maintains the 2nd stage SHU Reactor in the liquid phase.将第一段SHU流出物泵出，并按照规定的流量比与氢气混合，然后通过LP2蒸汽加热换热器加热至加氢反应器温度。热混合C4/C5和氢气然后向上流经第二段SHU反应器，在该反应器中，剩余丁二烯通过选择加氢处理被转化为正丁烯，戊二稀转化为正戊烯。由于选择加氢反应为放热反应，反应器内部会出现温升。由于反应热沿催化剂床传递，因此使用C4/C5物流对反应热进行吸收。反应产物紧接着在第二段SHU反应器流出物冷却器中冷却，然后在背压控制器控制下进入OCU新鲜/循环C4/C5缓冲罐。该背压控制器用于使第二段SHU反应器中物料保持为液相。
Gradual loss of catalyst activity will occur as the active sites on the catalyst become coked.Regeneration of the catalyst is required when catalyst activity has dropped to the point when a reactor outlet temperature of about 89℃ is reached.Regeneration requires the catalyst bed to be taken offline, drained and purged of hydrocarbons, heated with hot nitrogen and then superheated with steam.Air is metered into the stream to decoke the bed.A final nitrogen purge that contains a controlled amount of hydrogen reduces the catalyst bed.随着催化剂活性中心逐渐结焦，催化剂将逐渐失去活性。随着催化剂活性逐步降低，当反应器出口温度达到约89°C时，就需要对催化剂进行再生。催化剂再生时要求催化剂床离线，并将反应器内部烃物料排出并吹
扫干净，使用热氮气进行加热，然后使用蒸汽进行过热。以流量控制方式向物流中引入空气，以对床层进行清焦。使用含一定量氢气的氮气对催化剂床进行还原。
No spare reactor is provided.When the 2nd Stage SHU Reactor requires regeneration the 1st stage SHU Reactor is temporarily run in less selective mode to reduce the butadiene and pentadiene content sufficient to feed the OCU.没有提供备用反应器。当需要对第二段SHU反应器进行再生时，应临时降低第一段SHU反应器的选择加氢性能，从而将丁二烯和戊二稀含量降至规定值，以向OCU装置进料。
A SHU Reactor Regeneration Electric Heater is used to heat the hot gas mixtures used to regenerate the 2nd Stage SHU Reactor catalyst.SHU反应器再生电加热器用于加热第二段SHU反应器催化剂再生所需的热混合气。
1.2.4 Debutanization
脱丁烷
The effluent from SHU-2 is sent to the debutanizer.This column removes C5 components to produce a Mixed C4 stream suitable for feed the OSBL N-butene Unit.来自二段选择加氢装置的流出物进入脱丁烷塔。该塔脱除C5组分以生产适合进入界区外正丁烯装置的混合C4产品流。
The debutanizer overhead is condensed by cooling water and reboiled by desuperheated LP2 pressure steam.A portion of the liquid from the debutanizer reflux drum is sent as reflux to the tower and the remaining liquid is taken as mixed C4 product, which is sent to OSBL.The bottoms C5 product is pumped and cooled to 40℃ by cooling water, before being sent to the OCT Fresh/Recycle C4/C5 Surge Drum.脱丁烷塔塔顶物经冷却水冷凝后通过减温较低压力蒸汽再煮沸。来自脱丁烷塔回流罐液体的一部分进入该塔作为回流，剩余液体抽出作为混合
C4产品输送到界区外。塔底C5产品经泵抽出后用冷却水冷却至40℃，然后输送至OCT新鲜/循环C4/C5缓冲罐。
1.2.5 OCT Reactor Feed Treatment
烯烃转换装置进料处理 The debutanizer overhead is combined with the Mixed C4 Raffinate from the N-Butene unit(OSBL)and the recycle C4/C5’s in the OCT Fresh/Recycle C4/C5 Surge Drum.The Mixed C4s/C5’s from this drum are pumped to the OCT reaction pressure and combined with Fresh and Recycle Ethylene, mixed in a static mixer to dissolve the Ethylene in the liquid C4/C5, then treated in the OCT Reactor Feed Treater.The operating pressure of the treater is such that the Mixed C4+C5/Ethylene feed is in liquid phase.脱丁烷塔塔顶物料与界区外正丁烯装置混合C4的抽余液及循环C4/C5在OCT新鲜/循环C4/C5缓冲罐中混合。来自该罐的混合C4/C5经泵提升至OCT反应器压力，并与新鲜和循环乙烯在静态混合器中混合，以使乙烯溶解在液体C4/C5中，然后在OCT反应器进料处理器中进行处理。处理器设计运行压力能够保证使混合C4+C5乙烯进料保持为液相。
The OCT Reactor Feed Treater is designed to remove trace potential catalyst temporary poisons in the Mixed C4+C5/Ethylene stream that could impair the OCT Reactor performance such as oxygenates, sulfur, alcohols, carbonyls, and/or water.There are two treaters provided in the system.One is normally in operation;while the other is in regeneration or on standby.The treater regeneration initially requires draining of the liquid inventory followed by regeneration using hot Nitrogen from the Regeneration Gas System plus a supplemental electric heater.The treater effluent passes through a filter to remove any adsorbent dust.OCT反应器进料处理器用于脱除C4+C5乙烯混合进料中的痕量催化剂毒物，如氧合物、羰基化合物、乙醇、硫化合物和/或水，以防止对OCT反应器运行性能造成影响。系统设置两台处理器：一台通常处于运行状态，另一台用于再生目的或作为备用处理器。在对处理器进行再生时，首先对处理器进行排液，然后采用来自再生气系统的热氮气和辅助电加热器进行再生。处理器流出物送入过滤器，以脱除任何吸附剂粉末。
1.2.6 OCU Reactors
烯烃转换装置反应器
In this section, the OCU Reactor feed is heated to the required reaction temperature, passed through the OCU Reactor and cooled prior to OCU reactor effluent fractionation.The main reactions that occur are ethylene plus 2-butene forming propylene and ethylene plus 2-pentene forming propylene plus 1-butene.Some byproducts, primarily C5 to C8 olefins, are also formed by side reactions.在本工段，将OCU反应器进料加热至要求的反应温度后送入OCU反应器，并且在将OCU反应器流出物送入精馏塔之前应先进行冷却。主要OCU反应是以乙烯和2-丁烯作为原料经反应生成丙烯以及乙烯和2-戊烯反应生成丙烯和1-丁烯。另外，也发生一些副反应，所生成的副产品主要为C5-C8烯烃。
The OCU reactor feed is vaporized and heated to the required OCU Reactor temperature in an OCT Reactor Feed/Effluent Exchanger followed by the OCT Reactor Feed Heater.The OCU reaction occurs in a fixed bed catalytic reactor.The OCU catalyst is a mixed catalyst bed comprised of magnesium oxide and tungsten oxide on silica.The reactions occurring are essentially isothermal.OCU反应器进料先由OCT反应器进料/流出物换热器进行汽化，然后再通过OCT反应器进料加热器加热至要求的OCU反应器温度。OCU反应在固定床催化反应器中进行。OCU催化剂为混合催化剂，由氧化镁和以硅藻土为载体的氧化钨制备而成。所有反应基本上均为等温反应。
Prior to entering the recovery section, the OCU Reactor effluent is cooled by interchange with reactor feed followed by the OCT Reactor Effluent Cooler against Cooling Water.在进入回收工段之前，OCU反应器流出物首先与OCU反应器进料进行换热，然后在OCT反应器流出物冷却器中通过冷却水进行冷却。
Regeneration of the OCU Reactor requires the catalyst bed to be taken offline, purged of hydrocarbons, and heated with hot Nitrogen.A nitrogen-air mixture is then fed to the reactor to decoke the bed.A nitrogen purge, which contains a controlled amount of hydrogen, reduces the catalyst bed.A high temperature Nitrogen desorption step follows to remove any traces of oxygen and water from the bed.Hot regeneration gases for the regeneration of the OCU Reactor are provided by the Regeneration Gas Heater.在对OCU反应器进行再生时需要使催化剂床离线、将烃物料吹扫干净、使用热氮气进行加热。然后，向OCU反应器注入氮气-空气混合气体以对床层进行清焦。使用含一定量氢气的氮气对催化剂床进行还原。随后进行热氮气解吸，以将催化剂床的痕量氧气和水分脱除。OCU反应器再生用高温再生气由再生气加热器提供。
1.2.7 Deethylenizer 脱乙烯塔
The OCU Reactor effluent is chilled by vaporizing a portion of the Recycle Ethylene in the Deethylenizer Feed Chiller.The chilled feed then flows to the Deethylenizer column.OCU反应器流出物通过在脱乙烯塔进料深冷器中对一部分循环乙烯进行汽化来实现冷却。然后，已冷却进料流入脱乙烯塔。
The Deethylenizer pressure is selected to recycle vent gas from the reflux drum and to allow the overhead to condense against-24℃ Propylene Refrigerant from the Propylene Refrigeration System of the LORU.A small vent gas stream containing Hydrogen, Methane, and Ethylene flows from the reflux drum on flow control to the LORU for recovery.10
脱乙烯塔设计压力能够对来自回流罐的排放气进行循环，并使用来自LORU装置丙烯制冷系统的-24°C丙烯冷剂对塔顶物料进行冷凝。一小股含有氢气、甲烷和乙烯的排放气以流量控制方式从回流罐流入LORU进行回收。
Fresh Ethylene liquid is fed to the Deethylenizer Reflux Drum.The bulk of the tower overhead is condensed against Propylene Refrigerant and sent to the Deethylenizer Reflux Drum.Liquid from the reflux drum is split, with a portion pumped to OCU Reactor Feed Treater pressure to supply Recycle Ethylene, and a portion pumped separately to supply tower reflux on flow control.The net Fresh plus Recycle Ethylene is pumped and sent to the Deethylenizer Feed Chiller on flow control.A portion of the Recycle Ethylene stream is vaporized in this heat exchanger.The rest bypasses the feed chiller on temperature control, in order to maintain the OCU Reactor feed in the liquid phase at the outlet of the OCU Reactor Feed Treater.The Recycle Ethylene stream then mixes with Fresh and Recycle C4’s/C5’s at the OCU Reactor Feed Treater Mixer and flows to the OCU Reactor Feed Treaters.新鲜乙烯液体送入脱乙烯塔回流罐。大量脱乙烯塔塔顶物料经丙烯冷剂冷凝后送入脱乙烯塔回流罐。脱乙烯塔回流罐中的液体分为两股：一股液体泵送至OCU反应器进料处理器作为循环乙烯，另外一股液体以流量控制方式泵送回脱乙烯塔作为回流。净新鲜乙烯和循环乙烯以流量控制方式泵送至脱乙烯塔进料深冷器。在脱乙烯塔进料深冷器中，一部分循环乙烯被汽化，而剩余循环乙烯以温度控制方式进入脱乙烯塔进料深冷器旁路，以确保将来自OCU反应器进料处理器出口的OCU反应器进料保持为液相。然后，循环乙烯通过OCU反应器进料处理器混合器与新鲜和循环C4、C5混合后流入OCU反应器进料处理器。
The tower is reboiled by LP2 Steam with the bottoms product flowing to the Depropylenizer on flow control, reset by level control.A temperature
controller is used to control the reboiler steam to maintain the proper bottoms specification.脱乙烯塔内物料通过LP2蒸汽进行重沸，塔底产品按照液位控制器设定值以流量控制方式流入脱丙烯塔。通过温度控制器对重沸器蒸汽流量进行控制，以确保塔底产品始终符合规格要求。
1.2.8 Depropylenizer
脱丙烯塔
The Depropylenizer separates the Deethylenizer bottoms into three products: 脱丙烯塔（299-T-3302）将脱乙烯塔塔底物料分离为三种产品： • Polymer Grade Propylene(overhead)聚合物级丙烯（塔顶产品）； • C4/C5 Recycle(side-draw)C4、C5循环物流（侧线抽出）； • C4+ byproduct(bottoms product)C4+副产品（塔底产品）The tower pressure is selected to condense the overhead against Cooling Water and reboil against LP2 Steam.The tower C4/C5 side-draw is cooled in a Cooling Water heat exchanger and recycled on flow control to mix with the Fresh C4/C5 feed in the OCT Fresh/Recycle C4/C5 Surge Drum.脱丙烯塔设计压力能够通过采用冷却水对塔顶产品进行冷凝，然后使用LP2蒸汽进行重沸。脱丙烯塔C4、C5侧线抽出物流通过冷却水换热器进行冷却，然后以流量控制方式循环回OCT新鲜/循环C4、C5缓冲罐，并与新鲜C4、C5进料混合。
The tower overhead is completely condensed and sent to the Depropylenizer Reflux Drum.The liquid from this drum is then pumped and split with a portion providing reflux, on flow control for the tower.The remainder of the liquid is the Polymer Grade Propylene Product and is sent to OSBL on flow control reset by level control.脱丙烯塔塔顶产品经完全冷凝后，送入脱丙烯塔回流罐。然后，将脱丙烯塔回流罐中的液体泵出并分为两股物流：一股液体以流量控制方式送
回脱丙烯塔作为回流，剩余液体作为聚合物级丙烯产品按照液位控制器设定值以流量控制方式送至界区外（OSBL）。
The tower bottoms product is C4+ by-product.It is cooled against cooling water and sent on flow control reset by level control to OSBL.脱丙烯塔塔底产品为C4副产品。该副产品按照液位控制器设定值以流量控制方式送至OSBL。
A temperature controller is used to control the reboiler steam rate to the Depropylenizer.通过温度控制器对自重沸器去脱丙烯塔的蒸汽流量进行控制。1.2.9 Regeneration System 再生系统
A treater Regeneration System is used to provide hot Regeneration Gas during the heating stage of regeneration and cold Regeneration Gas during the cooling stage of regeneration.处理器再生系统用于为每一再生加热阶段提供高温再生气以及为再生冷却阶段提供低温再生气。
1.2.9.1 Treater Regeneration 处理器再生
Hot nitrogen is supplied from the Regeneration Gas System to regenerate the OCU Reactor Feed Treaters.The Regeneration Nitrogen is supplied at the battery limits.Cold Regeneration Nitrogen is sent as cold Regeneration Nitrogen to treater when required.Hot Regeneration Nitrogen is first heated against HP steam in the Treater Regeneration Gas Steam Heater and further heated in the Treater Regeneration(electric)Gas Heater before flowing to the treater when required.由再生气系统提供热氮气，OCU反应器进料处理器进行再生。自界区提供再生氮气。低温再生氮气当需要时提供给OCU反应器进料处理器用作低温再生氮气。当要求向处理器引入高温再生氮气之前，应先通过处理器再生气体（电）加热器对高温再生氮气进行进一步加热。
The relative amounts of hot and cold Regeneration Nitrogen flow and temperature are controlled automatically to achieve complete regenerations within the required cycle times.Although the treaters are typically designed for a 48 hour adsorption cycle, they are typically designed for a 24 to 36 hour regeneration cycle.高温和低温再生氮气相对流量和温度采用自动控制方式，以确保在规定的再生周期内实现完全催化剂再生。尽管处理器吸附周期通常设计为48小时，但其再生周期通常设计为24到36小时。
Spent Regeneration Nitrogen returning from the treaters is cooled and sent to the Flare System.来自处理器的废再生氮气经冷却后送入火炬系统。1.2.9.2 C4/C5 Stripping System
C4/C5汽提系统
This system is a closed–loop process where the pressure is dependent on condensing C4’s/C5’s against Cooling Water.The system includes a C4/C5 Stripping Holding Drum, which is inventoried from the cooled 2nd Stage SHU Reactor effluent stream.Filling is controlled so that the rate is less than 5% of the forward flow from the 2nd Stage SHU Reactor effluent to avoid disturbing the OCU operation.In the first stage of regeneration, the butenes are pumped to sufficient pressure, vaporized in a LP2 Steam heater and superheated to about 120℃.The hot C4/C5 vapor is then sent to the OCU Reactor Feed Treaters on flow control where it strips the C4’s/C5’s trapped on the adsorbent pores(stripping/warm soak).The effluent vapor is then condensed in the C4/C5 Stripping Condenser against Cooling Water and collected in the C4/C5 Stripping Holding Drum.Pressure control on the C4/C5 Stripping Holding Drum allows for venting of non-condensables during this stripping/warm soak step.14
丁烯汽提系统为密闭回路系统，运行压力取决于通过冷却水对C4/C5 进行的冷凝。丁烯汽提系统包括一个C4/C5 汽提储罐，用于存储来自第二段SHU反应器的已冷却流出物。对去C4/C5 汽提储罐的进料流量进行控制，确保低于来自第二段SHU反应器流出物流量的5%，以避免影响OCU装置的正常运行。在第一阶段再生期间，通过泵将丁烯压力提升至足够高后经由LP2蒸汽加热器进行汽化，再过热至120℃。然后，以流量控制方式将C4/C5气体送入OCU反应器进料处理器，以将截留在吸附剂空隙中的C4/C5 汽提出来（汽提/温热浸泡）。汽提后的丁烯气体通过C4/C5 汽提冷凝器使用冷却水冷凝后收集至C4/C5 汽提储罐。对C4/C5 汽提储罐进行压力控制有助于在汽提/温热浸泡期间将不冷凝气排放出来。
When the stripping step is complete, the spent butenes/C5’s in the C4/C5 Stripping Holding Drum are drained by pumping on flow control to the drain drum of the regenerating treater.当完成汽提操作后，通过泵以流量控制方式将C4/C5汽提储罐中的废丁烯排入再生处理器排液罐。
第四篇：中英文对照A
《美国口语惯用法例句集粹》Ａ
A(Page 1-4)
1.about
1)
2)
3)
4)
5)
6)
7)I'd like to know what this is all about.我想知道这到底是怎么回事。How about a fish sandwich? 来一块鱼肉三明治怎么样？What about me? 我怎么样？I'm not about to go in that old house.我是不会进那幢旧房子的！Yes I remember that night.What about it? 是的，我记得那个晚上，那又怎样？What's this all about? 这到底是怎么回事？It's about time you showed up!差不多是你该露面的时候了。
2.above
1)
2)Above all, I want everything quiet.首要的是：我要一切保持安定。Tom thinks he's above hard work.汤姆认为自己没必要努力工作。
3.act
1)
2)
3)
4)
5)
6)Would you please act out what happened? 你能把发生的事演示一下吗？Watch Ricky.He sometimes likes to act up in class.注意里基，他又是喜欢在课堂上捣蛋。That profane comedian needs to clean up his act.那个爱说粗言秽语的喜剧演员应该净化一下自己的言行。We need to get our act together and come to see you.我们需要统一意见后来见你。The newspapers called the earthquake an act of God.报纸上称那次地震为天灾。Masa is a class act.玛莎是位杰出的女性。
4.action
1)
2)
3)
4)We're going to bring action against our debtors.我们打算控告我们的债务人。Did you see any action in yesterday's ballgame? 昨晚的棒球比赛中你看到有什么有趣的精彩场面吗？Our community is going to take action against the proposed waste dump.我地区要采取行动反对那项垃圾处理场的提案。Jim wants to go where the action is.吉姆想去有刺激性的地方。
5.advantage
1)
2)Our opponents have a height advantage on us.我们的对手在身高上比我们占有优势。Nobody likes to be taken advantage of.没有人喜欢被捉弄（或：被欺骗、利用）
6.after
1)
2)
3)
4)I think that girl is after you.我想那女孩是在追你。It looks like things are gonna work out after all.看起来事情终会解决的。This soft drink has a nasty aftertaste.这软饮料有种让人难受的余味。I see your point, but don't you think it's way after the fact.我明白你的意思，但你不觉
得这已是“事后诸葛亮”了吗？
7.again
1)I could go to Japan again and again.我可以一而再、再而三地去日本。（注：意指不会感到
厌倦）
8.age
1)
2)Would you please act your age!请你做事要有一个与自己年龄相称的样子。This is a “coming of age” movie.这是一部成人影片。
9.air
1)
2)
3)
4)
5)
6)
7)
8)
9)I need to go outside and get some air.我需要出去呼吸点新鲜空气。I don't know what's wrong, but can feel it in the air.虽然我不知道到底是出了什么差错，但我能隐隐约约感觉到。Mike was sad when they took his favorite program off the air.当迈克喜欢的节目被取消时，他感到很伤心。The sale of our house is still up in the air.我们的房子出勤率售一事还没有最后定下来。After winning the championship, I felt I could walk on air.获得冠军后，我飘飘欲仙。Your sister is such an airhead.你姐姐真是来个没有头脑的人。Janet Jackson's new song is getting lots of airplay.珍妮〃杰克逊的新歌到处都在不断地播放。That last time I took a plane, I got airsick.上次我乘飞机时晕机了。I hope there's no bad air between us.我希望我们之间的关系不要很别扭。
10.all
1)
2)
3)
4)
5)
6)
7)
8)
9)
10)
11)
12)
13)It's looks like we won't be going after all.看起来最后我们还是不能去。We've all but finished the project.我们已几乎完成了那个项目。All in all I'd say it's been a very productive day.总的来说，我认为这一天过得很充实。Let's go all-out and win this game!让我们尽全力来打赢这场比赛。We knew it was all over when we saw the building burst.当我们看见那座建筑突然起火时，我们知道一切全完了。We wish you all the best.我们大家祝福你一切如意。If it's all the same to you, I'd just as soon not go.如果这对你都是一回事的话，我就不想去了。They were running from the police like all get-out.他们以极快的速度逃脱警察的追赶。I didn't see them come in at all.我根本高没有发现他们的进来。Let's settle this matter once and for all.让我们来把这个问题一次性地彻底解决掉。Mark is an all-around athlete.马克是一个全能运动员。Did you get to play in the all-star game? 你入选全明星队的比赛了吗？He bloke the all-time record in the 100-meter run at his school.他打破了他所在的学校
100米跑的历史最高记录。
11.alley
1)Working on cars isn't up my alley.修理汽车不是我拿手的活儿。
12.alone
1)
2)I just wanna be left alone.我只是想一个人呆会儿。Can't you just leave well enough alone? 你不能少管一些闲事吗？
13.along
1)
2)You knew all along what was going on.你从一开始就知道所发生的事。Debbie doesn't get along with Steve.戴比和史蒂夫相处得不好。
1)
2)
3)
4)
5)Mr.Pak came here searching for the American dream.帕克先生来到这儿寻求他的“美国梦”。Some foreigners become Americanized while living in the U.S.一些外国人在美国居住时被美国化了。Not having any job freedom would be totally unAmerican.没有选择职业的自由是完全违背美国精神传统的。Bill is an all-American quarterback.比尔是全美（橄榄球）明星赛的四分卫队员。I just can't go on the American way.我无法适应美国方式。
15.animal
1)
2)Water-skiing really brings out the animal in Tom.滑水运动真正激发出了汤姆的活力与激情。The young actor emits a lot of animal magnetism on the screen.那个年轻演员在荧幕
上充分显示出他的性魅力。
16.answer
1)I called Emi but there was no answer.我给埃米打了电话，但是没人接。
17.apple
1)
2)
3)
4)
5)Have you ever been to the Big Apple? 你去过纽约吗？Do I sense an apple of discord between you two? 你问我有没有感觉出你们两人之间的不和，是吗？Heather is the apple of my eye.希瑟是我的掌上明珠。Rita likes to keep everything in apple-pie order.丽塔喜欢把一切都弄得井井有条。Dennis has always been an apple polisher.丹尼斯一直就是一个马屁精。
18.arm
1)
2)
3)
4)You don't have to twist my arm to get me to go with you.用不着你强迫我跟你走。My father is a hopeless armchair quarterback.我爸爸是一个没救了的纸上谈兵的人。The suspects are armed and dangerous.嫌疑犯带有武器，十分危险。Every spring the park is filled with lovers walking arm in arm.每到春天公园里到处都是
手挽手散步的恋人。
19.around
1)
2)Coach Johnson has been around for 30 years.约翰逊教练已有三十年的经验了。Someone is on duty here around-the-clock.有人在这里昼夜值班。
20.as
1)
2)
3)
4)
5)
6)It looks as if someone has already been here.看起来在人来过这里了。As for me, I'm going home.至于我，我准备回家。Marty is acting as if nothing happened.马蒂表现得像什么也没发生过一样。I want this room left as is.我希望这间房子保持原样。The changes will begin taking place as of tomorrow.变动从明天开始实施。Police are baffled as to the whereabouts of the kidnappers.警察局搜寻绑架者的工作受
挫。
1)
2)
3)
4)Our gas bill average about $50 a month.我们每个月的煤气费平均50美元。On the average, I'd say we eat chicken once a week.我们平均每周吃一次鸡肉。Kent describes himself as just an average Joe.肯特视自己为一名普通的美国人。On the average day, over 100,000 kids bring guns to school in the U.S.在美国平常日
子里，有100,000个孩子带手枪去上学。
22.away
1)
2)
3)
4)
5)What makes you think you're gonna get away with this? 是什么使你认为你可以免受处罚？I wish they'd do away with these complicated tax forms.我希望他们能费除掉这些复杂的税务表格。We're planning a weekend getaway for our anniversary.我们正在为庆祝我们的纪念日而安排一次周末的外出活动。Tom wants to run away from home.汤姆想从家里出逃。Dave and Kathy are going to steal away on vacation.戴夫和凯茜计划在假期里偷偷跑出
去。
第五篇：中英文对照
AEROFLEX “亚罗弗”保温 ALCO “艾科”自控 Alerton 雅利顿空调 Alfa laval阿法拉伐换热器 ARMSTRONG “阿姆斯壮”保温 AUX 奥克斯
BELIMO 瑞士“搏力谋”阀门 BERONOR西班牙“北诺尔”电加热器 BILTUR 意大利“百得”燃烧器 BOSIC “柏诚”自控 BROAD 远大
Burnham美国“博恩汉”锅炉 CALPEDA意大利“科沛达”水泵 CARLY 法国“嘉利”制冷配件 Carrier 开利 Chigo 志高
Cipriani 意大利斯普莱力
CLIMAVENETA意大利“克莱门特” Copeland“谷轮”压缩机 CYRUS意大利”赛诺思”自控 DAIKIN 大金空调
丹佛斯自控 Dorin “多菱”压缩机
DUNHAM-BUSH 顿汉布什空调制冷 DuPont美国“杜邦”制冷剂 Dwyer 美国德威尔 EBM “依必安”风机
ELIWELL意大利“伊力威”自控 Enfinilan 英国“英菲尼兰“阀门 EVAPCO美国“益美高”冷却设备 EVERY CONTROL意大利“美控” Erie 怡日
FRASCOLD 意大利“富士豪”压缩机 FRICO瑞典“弗瑞克”空气幕 FUJI “富士”变频器
FULTON 美国“富尔顿”锅炉 GENUIN “正野”风机 GREE 格力
GREENCOOL格林柯尔 GRUNDFOS “格兰富”水泵 Haier 海尔 Hisense 海信 HITACHI 日立
霍尼韦尔自控 Johnson 江森自控 Kelon 科龙
KRUGER瑞士“科禄格”风机 KU BA德国“库宝”冷风机 Liang Chi 良机冷却塔 LIEBERT 力博特空调 MARLEY “马利”冷却塔 Maneurop法国“美优乐”压缩机 McQuary 麦克维尔 Midea 美的 MITSUBISHI三菱
Munters 瑞典“蒙特”除湿机 Panasonic 松下 RANCO “宏高”自控
REFCOMP意大利“莱富康”压缩机 RIDGID 美国“里奇”工具 RUUD美国“路德”空调 RYODEN “菱电”冷却塔 SanKen “三垦”变频器 Samsung 三星 SANYO 三洋
ASWELL英国森威尔自控 Schneider 施耐德电气 SenseAir 瑞典“森尔”传感器 SIEMENS 西门子
SINKO ",28商机网;新晃“空调 SINRO “新菱”冷却塔 STAND “思探得”加湿器 SWEP 舒瑞普换热器 TECKA “台佳”空调 Tecumseh“泰康”压缩机 TRANE 特灵
TROX德国“妥思”风阀 VASALA芬兰“维萨拉”传感器 WILO德国“威乐”水泵 WITTLER 德国”威特”阀门 YORK 约克
ZENNER德国“真兰”计量
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