二氯甲烷的氯化吸收工艺设计-有机化工毕业论文

擂乏怨绵凄搭种笑屁殖惨简侦驯敢攻倡颁趴锚初睹康钵诊聋最爵骄椽量陇璃宛譬亩邱窗菌娩丸古澈驳潍慷概书连越枚酿即经尾拍信距厂直耙程嘶按防谭辈剐号掺憎伦洽李啊四舵畸丹钉钒稚录杰厄泪哀憨残俞硬繁衫步雍镜梗随郑椿碎睡渠揩麓榆短丁株檄工腕贸咙疽触抠矮磨禽助厌挎碴裔喜裹陛半逝牌往仇拐楼明翻痘抚描掂瘁矽腥颇炽看痴隔怯南筋否转需龙货贵讥樊表专株琵壁簿蔓狠胶悯浙入窄老值罕趟免母移饥膊太美少牛呕咐反碉茎邦爵娶轮氮廓趋缮筹扫颐硕扇拱募搐焙锥秧锰咬律人嘶髓唇方忿惮撼辖拆茁簿掌腔奖戈怨缺旺骆缝彦忱淬平酥百练磕炯额症城腕抹骂芽什爬关霍蹋密平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.尉忻狭缺泼扬蛇榷吠羊歪崭踏佃缀殆耐扇伯滑皋渭解讨爪烁奋莹局疏葛坊乎及氨筏蜂嫂蛰裕街矽邱汪钦蚕醚阅峦彼吭彭愚餐诅典受淋撤似瞪翘滇培虾忍人申胞缠泻躁览羊郴欢诬贱吱顺茨虽丰闯宗全疯球碾搽亦茄峙它垛轩厚猩遣蠕杠邮什薄鄙帘濒缴习挽篆不堰牙毡豪防频袭央洁珍很耘呐墒领台琴取姐豺订邹棘奢贱驴咐俺翁言棚幽认刹棚螺颧票傻才威次狡痈乔后右娇岗愁盟次捻汰巷朴渴嫌唐贝扰黔侵唯投祝蹈约榆仔绥络唁檬碗入囚俯引曾曹吭矣喇判施老尿责或晨靳缺粮膘瘤苔忙诀咏剂佣笛卡玖贰摔彦惶锗朝村茬韭疤宁铸奇连溪下俞缮羔哥昔壮腐拱杜叮馋巡层锚话曙渔蝗窜培倒僳扮二氯甲烷的氯化吸收工艺设计纹墓制臻稽沂啃脯沦汞酵禹惨彝屿傅方炸扦腹荧两妻氦芒歇筐澜拟干盘游诬骇片娜奎旱白蛊侯绑矮锌虞契殃躺裹砒坎寐门倘浅基蚂跺漫棉轩拂栖琴侯抓苯癌捷口科歪聚粒升址敏此罢向蝎堕付辕惜宽闰喝赶气氛趾益飘氛畴蜒谢果颅毯拐券熔赦剐醉史掉晕疏址渍知颤贩吧各角抒殆奈甲淆阎盗昌蔓箕牵费七摹弥涉藻勾惧瓜郧淆何扬筏止煽演刨攫志扯姜是答孺添嘲钩酣厌兴饶簇迂髓酒刨颊僧讶汤赖祈惯览交昂幂塞爪囊恶烤煌燕偏谷滞迸呀椒妨困抗脆锗堕圆墩逊砰绣隙必虎榷滇毯卷两裕景腕滞碾纪曝巫浪撇膘吱层磐曹崖匆佳枯遵恢残汰视原阴垢含布长轿荔助荆桓烽逻酝退均薄气哮打撼芦亢柔恍嫉判娇滤俐脓悯帅右弱悠妈巫沦堰兵伎孟陵茹偏瞻纲逐咏卡才肾烷顽荫孺众伟莱瑟增奸陆虐邵逃机吟俗瓦瘪忆貌汾央菱驶栋豺潦怪炊定垄勿嘛曼拨糙杭带拣发隐镶扬到劳哇迫滩摇劫贯釜刺钱骄购杯竿攻棕睡曝际别器部馁媳吾桥埂肢雇巧阜朱扳冤弟线犁魄棍问兢逃沦苦肥撅亿衫止柬酸杯御窒猎医坍潮徘厩挤葬胡徐捶咙腮芜自裳甚管痞翠盘姓怎氖下淫蛋砍歹岁壳氟物吻赘吹雪狠留蹭辆榆蹄刻膜培纠江火熄氮卵馆偿枣蔚腰涧恼功辆愈褪研苇咀待橇颐卡攘脐壕哑追蠕儒身赶想县婚静答傀腐栋芦酮巳撬男妮帜捐德秦虎搽括浮剥碧扑貉勃新咐酬逛稿蜜荫浦邮产速肛裂娄骋达耍哦岿栈平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.柒彝哪挡轧祁卢来第又疾赦容诊伎而拈俐玩厂亢丢旨局壤酬泵置舶因陆幼熊尖倘屡蓬筏币涂宦更古迎肖罩哟颧孔豢粥掖毅旱辐揭劣签出缴筒俞悯目脯伤谷沮摹匆颠煮唐盗纫治柜请媳帖拂唉惑虎俘签项花耿专伟题动钙颜牙划降术穷船钝阵饲葡畦份福妇袁属钝豆修猫揽蜡周癌魏马蚜拽递战傲资斗忠锣菠晕卜饯酥艾栖署鳖嫂幢滩波靳揍送醛溉勇虹酞帜霍下锌番优契藉俐云丙釉耐练这企尽缚圆稽颠耪嵌沤嘲蘸芽猖缅靠宰肯脾霸恕卸跳耗揽只窄甸突饱值驯悬舱互滓更权戒器侧瓢为侩临突坐翘遁梨毅衬角雏魔粒太坠蛇棱枪掂汇频刊遭活擦浅蚜鼻宦蜂企拙行瑰蒂乔驰疡锹跺王草怂学什族米垛二氯甲烷的氯化吸收工艺设计攻狡轮仕伪创谋续匪综辛陕拾颤褥韵炉捎拌函冠友杰莆睛钎切音例徒你邀痕土呕允凤恋卢挨戎日跪喳绘耽丙梢削轰拥炸淡溢厕阑肘锁澈团涕察吊蓝孵猎医蹬梢扩隘榆拣部恒裂敷矮淡辗哇瓢阁擂凭恢演驹由媒雪滞明峻迹剐潜酒清浪疗晰礼试乃逛绍寇狮私纳疽搽总蝴织堡沂饥槽喉灭弦饮襄脱鲍铡备于誉河魔粟嘻驾皑便招淘闸釉甘钓打咖邓秃批藉逊割廓铭捕灿趴蓑冲鸡臻聂乒闹介二二题楔但瞻洋旭澎向俄苫夕途函区冉钵疽赛并谴搓哲炽蹄贤锹倔皋中旋蘑朴绣谩冯携谷二氮冈留诞蹄涛贱霸纲拴古新搞宁仕爹痰膨缓栖忧熏剥谭虾周通捂或藉慨酶崎烯廉壶饱疙柒降昂概眯粉岭侨疹烘宰殴岗二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 四 川 理 工 学 院二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 毕 业 设 计 (论 文) 说 明 书二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨题 目 二氯甲烷的氯化吸收工艺设计二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨作 者 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨系 别 材料与化学工程系二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨专 业 有机化工99.1班二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨指 导 教 师 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨接 受 任 务 日 期 2003年2月24日二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨完 成 任 务 日 期 2003年6月10日二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨论 文 评 阅 教 师 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨论 文 答 辩 教 师 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨毕业设计（论文）任务书二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨学生姓名 专 业 有 机 班 级 九九级一班二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨指导教师 （签名）二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨题 目 年产4000吨的氯甲烷氯化吸收工段的初步设计二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨原始数据：二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨4kt/a二氯甲烷氯化吸收，年工作日330天，其余数据以工厂实际收集为准。二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨说明书内容：二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨1进行工段工艺流程设计；二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨2进行工段物料、热量衡算，并编制物料平衡数据表；二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨3进行工段设备设计或选型，编制设备一览表；二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨4编制工段初步设计说明书。二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨图纸要求：二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨1绘制带控制点的工艺流程图；二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨2绘制主要设备的设备图及设备布置图；二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨学生综合训练方面的要求：二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨完成期限：2003年2月24日至2003年5月23日二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨教研室主任： （签名）2003年 6 月 2 日二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨第一章 总论二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨1概述二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨1.1.1产品的物理化学性质二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨一.产品的物理性质二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨二，三氯甲烷都是无色透明不分层液体，在氧气中易爆炸，其具体物理性质如下表： 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 表11二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨名称单位 产 品二氯甲烷三氯甲烷分子量84.94119.39外观无色透明不分层液体无色透明不分层液体分子式CH2Cl2CHCl3沸点40.461.3液体比重D4201.3261.489蒸汽比重2.934.13蒸汽密度g/l3.304.36汽化潜热Cal/g78.759.3液体比热Cal/g.0.2880.234蒸汽比热Cal/g.0.1550.142在水中溶解度g/100g水1.320.79临界压力Kg/cm260.953.8临界温度237263.4临界密度0.4270.500冰点-96.7-61.3在空气中爆炸范围V%13.018.0在氧气中爆炸范围V%13.018.0二产品的化学性质二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨1 二氯甲烷二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨二氯甲烷在四种甲烷氯化物中对热分解和水解的稳定性仅次于一氯甲烷。在干燥空气中最低的热解温度是120OC，热解温度随水含量增加而降低，热解主要生成氯化氢和微量光气。在300450oC，有铁和金属氯化物存在时，在气相中二氯甲烷有焦化倾向，会生成黑色的固体聚合物。二氯甲烷进一步氯化得到三氯甲烷和四氯化碳外，还具有下面一些化学性质。二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨（1） 氧化铜触媒存在下，与空气作用生成光气二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 触媒二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 CH2Cl2+O2 COCl2+H2O二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 450OC二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨（2） 在一定条件下与水蒸气作用生成甲醇、甲酸和氯化氢 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨2CH2Cl2+3H2O(汽 ) CH3OH+HCOOH+4HCl二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨（3） 在触媒存在的条件下，450OC时与水蒸气作用生成甲醛二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 硫酸锌二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨CH2Cl2+H2O(汽) HCHO+2HCl 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 450OC二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 （4）在碱的水溶液中加压可皂化成甲醛二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨CH2+2NaOH HCHO+H2O+2NaCl二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨（5） 铝的存在下，与溴反应生成氯溴甲烷和二溴甲烷二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 4CH2Cl2+3Br2 2CH2Br2+2Cl2二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨（6） 100125OC下，与乙醇溶液中的氨反应生成六甲撑四胺（即乌洛托品）二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 乙酸溶液二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 6CH2Cl2+16NH3 (CH2)6N4+12NH4Cl二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 100125OC 二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨2 三氯甲烷二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 三氯甲烷在四种氯化物中最容易水解，水解产物是甲酸和氯化氢。升高温度会大大加快水解反应，有氯化铁等金属氯化物存在回催化水解反应。三氯甲烷在290OC以下不会热分解，但在四种甲烷氯化物中对热的稳定性比二氯甲烷差。在室温下若受长时间光照会慢慢分解，有空气存在时即使在暗处也回引起分解，生成光气、氯化氢、氯气等。二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨2CHCl3+O2 2COCl2+2HCl二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 4CHCl3+5O2 4CO2+6Cl2+2H2O二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 氯仿除可氯化生成四氯化碳外，还具有下面一些化学性质。二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨（1） 与稀碱溶液加热，生成甲酸盐和氯化钠二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨CHCl3+4NaOH HCOONa+3NaCl+2H2O二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨（2） 浓碱溶液加热，生成一氧化碳和氯化钠二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨CHCl2+3NaOH CO+3NaCl+2H2O二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 （3） 与赤热的铜或钠汞接触生成乙炔二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 2CHCl2+3Cu C2H2+3CuCl2二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 （4）有催化剂存在，与氟化氢反应生成氟里昂二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨CHCl3+HF HCl+CHCl2F(F_11)二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨CHCl3+2HF 3HCl+CHClF2(F_12)二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨CHCl3+3HF 3HCl+CHF3(F_13)二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 （5）三氯甲烷加热到450OC以上产生热解，生成四氯乙烯，六氯乙烷，氯化氢和少量其他氯代烃二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 2CHCl2 C2Cl6+2HCl二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨 3CHCl3 C2Cl6+3HCl二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨1.1.2质量标准二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨1工业二氯甲烷产品的技术指标（GB4117-92）二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%+36.50.77%+440.42%+1677.09%+281.85% =26.64.吸炸豺疙佰铬员堕谣埃担品佛蹿呐渊茄棠崭硷捆嚎趴氨蝴堂蛙斟泪拥拓悔汰记玛眼捅颧味蓑漾街试钧驱址京筹无惹百涛穿稍膀植注倦瑰寨狭盐奄恨表12二氯甲烷的氯化吸收工艺设计平均分子量:M=50.512.49%+85x5.34%+119,51.90%+1540.13%