某公司物性数据表汇编.doc

1.4 物性数据表 171-1000一、乙二醇（EG）- 1 -表11乙二醇的物性数据7- 1 -表12乙二醇液体密度7- 2 -表14乙二醇粘度6- 3 -表15乙二醇液体动力粘度7- 4 -表16乙二醇气体动力粘度7- 5 -表17乙二醇液体蒸汽压7- 6 -表18乙二醇液体比热7- 7 -表19乙二醇气体比热7- 8 -表110乙二醇蒸汽热容量 （理想值）7 压力：101325 bar- 9 -表111乙二醇蒸发热7- 10 -表112乙二醇液体导热系数7- 11 -表113乙二醇气体导热系数7- 12 -表114乙二醇液体表面张力1（N/M）- 13 -表115乙二醇和它的水溶液在不同温度下的比重15（g/ml）14表116乙二醇水溶液冰点1515表117乙二醇水溶液沸点1516表118乙二醇水溶液二元体系在不同浓度和不同温度下的热容15Cp（cal/g）18表119乙二醇和它的水溶液在不同温度下的粘度15（厘泊）20表120图12 水乙二醇二元体系汽液平衡图表121表121图13 乙二醇二甘醇二元体系汽液平衡图表124表122图14 乙二醇三甘醇二元体系汽液平衡图表127表123图15 乙二醇对苯二甲酸乙二酯二元体系汽液平衡图表129表124图16 乙醛乙二醇二元体系汽液平衡图表32二、对苯二甲酸（PTA）35表21对苯二甲酸的物性数据1435表22对苯二甲酸爆炸强度：1436表23对苯二甲酸在不同溶剂中的溶解度：1437表24对苯二甲酸蒸汽压：738表25对苯二甲酸固体比热：739表26对苯二甲酸气体比热：740表27对苯二甲酸理想气体热容量：141表28对苯二甲酸固体焓值：42三、聚对苯二甲酸乙二醇酯（PET）43表31PET的物性数据1243表32聚对苯二甲酸乙二醇酯的液体密度：744表33聚对苯二甲酸乙二醇酯的固体密度：745表34聚对苯二甲酸乙二醇酯的动力粘度1347表35聚对苯二甲酸乙二醇酯的液体比热：748表36比重不同的聚酯熔融热：1249表37聚酯熔体焓150表38PET在某些溶剂中的溶解性1451表39PET比重和结晶度的关系1252表310PET低聚物的熔点1253表311聚对苯二甲酸乙二醇酯固体热焓2（KJ/Kg）54表312聚酯装置PET熔体质量指标1156表313聚酯装置PET切片质量指标1157四、二甘醇58表4.1二甘醇的物性数据758表4.2二甘醇液体密度759表4.3二甘醇液体动力粘度760表4.4二甘醇气体动力粘度761表4.5二甘醇表面张力162表4.6二甘醇蒸汽压763表4.7二甘醇液体比热764表4.8二甘醇气体比热765表4.9二甘醇蒸汽热容量166表4.10二甘醇汽化热767表4.11二甘醇液体导热系数68表4.12二甘醇气体导热系数69表4.13图4.170表4.14图4.273表4.15图4.376表4.16图4.480五、三甘醇87表5.1三甘醇的物性数据787表5.2三甘醇液体密度788表5.3三甘醇液体动力粘度789表5.4三甘醇蒸汽动力粘度790表5.5二甘醇表面张力1 (N/m)91表5.6三甘醇蒸汽压792表5.7三甘醇液体热容793表5.8二甘醇蒸汽热容794表5.9三甘醇液体导热系数95表5.10三甘醇蒸汽导热系数796表5.11三甘醇汽化焓797表5.12三甘醇液体焓值198表5.13三甘醇饱和蒸汽热焓1100表5.14乙醛三甘醇二元体系汽液平衡图表1102表5.15水三甘醇二元体系汽液平衡图表1103表5.16图5.1104表5.17聚酯对TEG的质量要求4108表5.18纺丝对TEG的质量要求4109六、乙醛110表6.1乙醛物性数据7110表6.2乙醛气体粘度6111表6.3乙醛液体粘度6112表6.4乙醛液体动力粘度113表6.5乙醛液体密度7114表6.6乙醛蒸汽压7115表6.7乙醛表面张力（N/m）1116表6.8乙醛液体比热7117表6.9乙醛气体比热7118表6.10乙醛理想气体热容量1119表6.11乙醛汽化热7120表6.12乙醛液体导热系数7121表6.13乙醛气体导热系数7122表6.14乙醛水二元体系汽液平衡图表1123表6.15乙醛DGT二元体系汽液平衡图表1128七、二氧化钛131表7.1TiO2物性数据16131表7.2二氧化钛比热 7132八、水134表8.1水物性数据7134表8.2水和密度7135表8.3水的表面张力 (N/m) 1136表8.4水和饱和蒸汽压7137表8.5液体水的动力粘度7139表8.6水蒸汽的动力粘度7140表8.7水的液体比热7141表8.8水的蒸汽比热7142表8.9水蒸汽热容量1143表8.10水的汽化潜热7144表8.11液体水的导热系数7145表8.12气体导热系数7147九、导热油151表9.2孟山都导热油THERMINOL 66151表9.2.1典型特性151十、三醋酸锑155表10.1三醋酸锑的物性数据 6155表10.2聚酯装置对三醋酸锑的质量要求 615686 / 164一、乙二醇（EG）表11乙二醇的物性数据7分子式C2H6O2分子量62069熔点 -1260正常沸点 1973临界压力 bar7473临界温度 K64715临界体积 cm3/md186临界压缩因子 ZC（ （0270）皮查增强因子 W1175正常沸点下的汽化热 KJ/Kg812密度（20） Kg/m31114熔融热14 cae/g44.7燃烧热14 25 Kcal/mol2833折光率14 2514306 2014316闪点14 （ASTM开口容器）240表12乙二醇液体密度7温度 （）液体密度 kg/m31000002000003000004000005000006000007000001120000011130000110600001099000010930000108500001078000080000090000010000001100000120000013000001400000150000016000001700000180000019000002000000205000021000002150000220000022500002300000235000024000002450000250000025500002600000265000027000002750000280000028500002900000295000010700000106300001055000010470000103900001031000010220000101400001005000099500009860000977000096700009584400949310094112009323700923540091464009056700896640088851008773200866250085527008443500833460082257008116400800640078952007785400表14乙二醇粘度6温度（）粘度（厘泊）温度（）粘度（厘泊）温度（）粘度（厘泊）010203040506070809010053533922114910272252038228521616711012013014015016017018019020021013010308240666054404990373031302640225019322023024025026027028029030031032003740345031702900265024002160194017301530134表15乙二醇液体动力粘度7温 度 液体动力粘度 kg/ms20.0030.0040.0050.0060.0070.0080.0090.00100.00110.00120.00130.00140.00150.00160.00170.00180.00190.00200.00210.00220.00230.00240.00250.00260.00270.00280.00290.00300.0018376E-0212902E-0292655E-0367917E-0350721E-0338529E-0329726E-0323255E-0318449E-0314808E-0312019E-0398576E-0481624E-0468193E-0457447E-0448770E-0441704E-0435904E-0431106E-0427111E-0423760E-0420933E-0418534E-0416486E-0414729E-0413214E-0411902E-0410759E-0497614E-05表16乙二醇气体动力粘度7温 度 气体动力粘度 kg/ms500000100000015000002000000225000025000003000000860E-08980E-08112E-07124E-07130E-07137E-07150E-07表17乙二醇液体蒸汽压7温 度蒸汽压mbarbar10.0020.0030.0040.0050.0060.0070.0080.0090.00100.00110.00120.00130.00140.00150.00160.00170.00080.00190.00200.00210.00220.00230.00240.00250.00260.00270.00280.00290.00300.000.050.110.260.541.092.113.917.0012.1320.4133.4153.3383.18126.93190.00279.05402.30572.07800.27110371502120188268173523145803589657520695080119209143288附1，用ANTOINES公式进行纯组分蒸汽压的计算是Ln（P）=A 常数 A=21896230 式中：P 纯组分的蒸汽 B=704510448 压，mbarC=273150 t 温度， 表18乙二醇液体比热7温 度 液体比热 KJ/KgK200030004000500060007000800090001000011000120001300014000150001600017000180001900020000210002200023000240002500026000270002800029000300002397624508250262553426032265212700427481279562842828900293732984930329308153130831810323233284933387339413451235101357113634136995376733837839110表19乙二醇气体比热7温 度 气体比热 KJ/KgK500060007000800090001000011000120001300014000076910806508435087990915909515098661021210555108921500016000170001800019000200002100022000230002400025000260002700028000290003000011225115541187912199125141282613133134361373514030143211460714890151681544215713表110乙二醇蒸汽热容量 （理想值）7 压力：101325 bar温度蒸汽热容量K对比KJ/KgK00027315041691277909400031315047881396121800035315053901510125120003931506001161981616000433150661117250862000047315072221825831240005131507833192194328000553150844320133183200059315090542099848计算公式：热容量ABTCT2DT3其中 A366536195824E06 B364543386208E08 C105545295727E11 D276204475212E15表111乙二醇蒸发热7温 度 蒸发热 KJ/Kg20003000400050006000700010537010424410309710192810073799522800090001000011000120001300014000150001600017000180001900020000210002200023000240002500026000270002800029000300009828197014957199439393036916459021988753872468569484094824428073278960771197520173199711006889466562640866143958587表112乙二醇液体导热系数7温 度 液体导热系数 W/mK2000300040005000600070008000900010000110001200013000140001500016000170001800019000025590257202536026000261302625026360264402650026510264802641026280260802582025480250602455200002100022000230002400025000260002700028000023940232402242021500204501927017960165101491表113乙二醇气体导热系数7温 度 气体导热系数10-4 W/mK50006000700080009000100001100012000130001400015000160001700018000190002000021000220002300024000250002600027000280002900030000131138145152159167174182190198207215224233242251260269279289298308318329339349表114乙二醇液体表面张力1（N/M）温度（）表面张力温度（）表面张力温度（）表面张力202530354045505560657075004839004795004751004706004662004618004574004530004486004441004397004353859095100105110115120125130135140004265004221004177004132004088004044004000003956003911003867003822003778150155160165170175180185190195200003689003644003599003555003510003465003420003375003330003284003239表115乙二醇和它的水溶液在不同温度下的比重15（g/ml）浓度%比重温度102030354045505560708090100-45-35-25-15-501020304050607080901001201501012101110101009100710031001099209891029102810251023102010151010100610010981104510431039103510321029102310181012099110541052105010461043103810341029102410201012099510661062106010571052104910451041103710311023100310741070106910651057105410491044103810321028102310071087108310801075107310671062105610511045104010321028101311001096109110871084108010741069106310551049104410371020110811021097109310871085107910741068106210551049104210371022112311151110110511011098109110851079107210661059105110321138113111231116111611091102109510891083107610701062104210261133112811211117111111051098109210851078107110481034113211271117111111061099109210851078105510401016表116乙二醇水溶液冰点15重量组成%冰点重量组成%冰点115210300350395455510565-50-95-155-190-225-290-365-4455885956336658209009331000-480-495-580-655-530-376-330-170表117乙二醇水溶液沸点15重量组成%20d折光率n沸腾温度大气压mmHg沸点(760mm)972073004104655155405756126537057487978358608939981342213531136301373113786138351385813892139301397114021140631411314150141751420914315100810291038105810711080108711031114113311451173121612471289134419787762763076907625766576557655764576307670766876737622760276707704770010061028104510571069107810851101111311301142117012151247128618401976表118乙二醇水溶液二元体系在不同浓度和不同温度下的热容15Cp（cal/g）C% t 0102030405060708090100-45-40-35-30-25-20-15-10-5051015202530354045505560657075808590951001051101151201008010043100191000409995099890998709986099870998909992099961000110006100131002110029100391005010063100760951095309550957095809600962096309650967096809700972097309750976097809790981098209840892089709020907091209160921092509290932093609390942094409460948095009520953095409550957082808340841084708530859086508710877088208870892089609010905090809120915091809210923092609280930075707680778078807980806081508220829083608420849085408590865086908740878088308870891089508990903090709100672068406950707071807280738074707500765077407830792080008070814082108280834084008450850085308570861086408670871087406090619062906390648065806680678068806980707071607250734074307520760076707750783079007970803080808130818082208260829083308350838057305810591060006090619062806370646065506640672068006880696070407120720072707350741074807540760076607710776078007840788079207940544055205600569057705860594060206100617062506320639064606520659066506720678068506910697070307100716072107270732073807430749075407530763054005470554056205690577058405910598060406110617062406300636064306490655066106680674068006860691069707030709071507210727052005260534054105470555056305700578058405910598060406100616062206280634064006460653065906650671067706810686图11 乙二醇水溶液的粘度5表119乙二醇和它的水溶液在不同温度下的粘度15（厘泊）浓度% 粘度温度102030354045505560708090100-45-35-25-15-50102030405060701001201502872461681280920800670570490438395325323179127104082069079049053943726119014310809007506405461041627510341247187146121102088058019191181716576389280209161130108092067923831474882700444314234180144119099072656462904177810398195233662702041621321090766155969463351204212269675504092992301811461220821994833540882420140111196774683382541971621310823141125359743577201415829626504593402592061651005569219299765617310923781376903629458346271216124098168292835058368020971360922653483371292163122889961503459214014129756965284092201571 15表120图12 水乙二醇二元体系汽液平衡图表1系统压力水泡点EG泡点1013331000019730mbar温度水含量-X=-液相-Y=-汽相-Wt-%MOL-%Wt-%MOL-%10000101001050010900113001170012100125001290013300137001410014500149001530015700161001650016900173001770018100185001890019300197301000000887362595547433824331756261935211478173532144115120757101845862817329263220529494486737834316602619921329169561299909396060910304000000100000096446783534472527463106555010848026241976136714632120628093224548021414218632216151813930311931510124684831698465609443410316462067910397000001000000997411985482970871953256932330907818879493847201810878770571726447678805628068574773519548463083406098349302293368238897186405136306889124443400000100000099924799574299136798596797936897137196175295025693659892045790147487924885333282323178839474821370201764906658854651965744114935222625162913808900000YMOL%10090807060504030201000102030405060708090100XMOL%系统压力水泡点EG泡点19000589714999mbar温度水含量-X=-液相-Y=-汽相-Wt-%MOL-%Wt-%MOL-%58975900630067007100750079008300870091009500990010300107001110011500119001230012700131001350013900143001499910000009960905848003938022848092151601673461328601070688723371639591534900040632336522776522749184351468811405085020591203582000001000000998862829141691189578