简介：TheRMCtechnologydevelopedbyRIPPhasbeenappliedina1.5Mt/amediumpressurehydrocrackingunitatShanghaiPetrochemicalCompany.TheunitwassuccessfullyputonstreaminSeptember2002.CalibrationoftheperformanceofthecommercialunithasshownthattheRMCtechnologyhashigherhydrogenationactivityandselectivity,andhighqualityproductcanbeobtainedunderlowerreactiontemperature.Theheavynaphthawithlessthan0.5ppmofsulfurand58.5m%potentialaromaticcontentisagoodfeedstockforcatalyticreformingunit.Thedieselwithlessthan0.5ppmofsulfur,6.6m%aromaticsandcetaneratingof56isahigh-gradedieselfuel.Thehydrocrackedtailoilcontainingmorethan14m%hydrogenandmere1.7m%aromaticscouldbeusedasagoodfeedstockforsteamcrackingprocesstoproduceethylene.

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简介：ThekeyscienceandtechnologydevelopmentprojectofSINOPEC—thepilotscalestudyofsyngas-to-ethyleneglycolpackagetechnologyhaspassedtheexpertappraisalsponsoredbytheSINOPECScienceandTechnologyDivision.Thisprojectfacility,whichisjointlydevelopedbytheSINOPECShanghaiPetrochemicalResearchInstitute

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简介：The1,4-butanediol(BDO)/tetrahydrofuran(THF)projectconstructedbytheBlueStar(Nanjing)NewChemicalMa-terialsCo.,Ltd.adoptingawholepackageoftheworld'slatestpatentedtechnologywillcome

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简介：基于冷模型测试的结果，LPEC与新奇格子类型内幕在一个改革者为FCC催化剂的新生开发了一种技术以便加强在气体和固体之间的接触并且提高在regenerator.Testresults烧效率的焦炭表明了在与格子内幕装备的使流体化的床上的密度变化是相对同类的并且起泡的频率显然在邻近改革者墙的死了的使流体化的地区与明显的改进被减少，并且这台设备能在FCC改革者被用于催化剂的加强的新生。在在精炼厂A的0.8Mt/aRFCCU的这台设备的在工业上的应用显示了改革催化剂的碳含量从0.18%被归结为0.03%，并且烧的焦炭的数量被5%在改革者的烯释相节在改革者和某密度减小的主要的空中与明确的减小增加。

简介：Anewcontinuousprocessforpreparingmethanol-dieselemulsifiedfuelwithanImpingingStream-RotatingPackedBedisproposed.Thedropletsizeofdispersedphase(methanol)oftheemulsifiedfuelhasasignificanteffectonthecombustionofmethanol-dieselemulsifiedfuel.Inthispaper,themethanol-dieselemulsifiedfuelusesdieselasthecontinuousphaseandmethanolasthedispersedphase.TheSautermeandiameterofthedispersedphaseofmethanol-dieselemulsifiedfuelwascharacterizedwithmicrophotographyandarithmeticmethod.TheexperimentalresultshowedthattheSautermeandiameterofthedispersedphase,whichwasdecreasedwiththeaugmentationofthehighgravityfactor,liquidflowrateandemulsifierdosage,wasinverselyproportionaltothemethanolcontent.TheSautermeandiameterofthedispersedphasecanbecontrolledandadjustedintherangeof12—40μmthroughthechangeofoperatingconditions.ThecorrelativeexpressionsoftheSautermeandiameterofemulsifiedfuelwereobtainedandthecalculatedvaluesagreedwellwiththeexperimentalvalues.

简介：为在裂开的炉子试管由金属的CAS研究所发明了的蒸气的强迫的热传递的技术是成功地在SINOPEC系统以内适用并且被同意SINOPEC“s首先在2006在科技前进上分级奖品。

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简介：FiveChinaInventionPatentshavebeengrantedto'Plasmaprocessforcoal-basedacetylenetechnology'independentlydevelopedbytheXinjiangTianyeCompany,whichboastsagroupoftechnicalpatentsonitscoreprocessandequipment.Pyrolysisofcoaltomanufactureacetyleneinthermalplasmareactor,whichisbasedonthehigh-temperaturehydrogenplasma,enhancedchemicalaffinity,andthecharacteristicfeaturerelatingtotheclosecarbon/hydro-

简介：TheprocessformanufactureofDMEthroughreactiverectificationanditsassociatedequipmentandtechnologydevelopedbyShandongUniversityofScienceandTechnologyhasbeenrealizedincommercialscaleinthe50kt/ademon-

简介：TheR&Dproject'commercialtestofolefinisomerizationtechnologyforincreasingbutene-1output'jointlyundertakenbytheSINOPECShanghaiPetrochemicalResearchInstituteandtheZhongyuanPetrochemicalCompanyhadpassedthetechnicalappraisalsponsoredbytheScienceandTechnologyDevelopmentDivisionofSINOPECon

简介：ChinaLihuayiGrouphasselectedtheLPOxo~(SM)SELECTOR~(SM)(low-pressurebutanol/octanol)technologyjointlylicensedbyDowChemicalCompanyandDavyPro-cessTechnologyLimitedtobeusedonitsnew250kt/aunit.ThisunitislocatedinDongyingcity,Shandongprov-incewithadesigncapacityratedat140kt/aoctanol,85kt/an-butanoland24.4kt/aiso-butanol,andtheconstruc-tionofthisunitisexpectedtobecompletedby2010.

简介：催化py-rolysis-maximizing丙烯(TMP)技术独立地由中国石油大学(华东)的州的关键重油实验室开发了的二阶段的起床人的商业测试表明了在受到TMP之上的那大气的残油(AR)能超过18%完成丙烯收益，并且LPG，汽油和柴油机产量的和能接近83%。当重油的FCC或两重棉包线吸引了特殊注意最大化丙烯产量，在最近的年，这处理，因为常规催化裂开技术能仅仅在3%的范围贡献丙烯收益—5%。

简介：Thethird-generationtechnologyformanufacturingethylbenzenefromFCCoffgasdevelopedbyCASDalianInstituteofChemicalPhysics(DICP)hasbeentransferredtoPetroChinaJinxiRefining&ChemicalGeneralWorksandPetroChinaJinzhouBranchCompany,respectively,forconstructionofethylbenzeneunitsratedat60kt/aand80kt/a.DICPwillalsosignwithPetroChinaLinyuanPetrochemicalGeneralWorksandHainanrefinery,respectively,

简介：Thenewprocessforcatalyticrectification/hydrolysisofmethylacetatedevelopedbytheChemistryandChemicalEngineeringCollegeofFuzhouUniversityhasbeendissemi-natedandapplied.Thisprocessadoptsthenewintegratedtechnologyofcatalyticrectificationwhichnotonlyhastack-ledtheproblemoflowrateofhydrolysisofmethylacetateobtainedinthecourseofPVAmanufacture,butisalsobe-

简介：在分析hydrotreating催化的裂开联合处理的传统的残余的劣势以后，RIPP建议了集成与催化裂开对待的残余水疗院的一种双向联合技术叫了不推进的RICP再循环FCC在FCC单位内的重周期油(HCO)并且把HCO送到对待为并发地受到对待的水疗院的残余作为冲淡的油联合起来的残余水疗院在被用作FCC以前喂油。RICP技术能刺激与FCC轻精华的增加的收益一起通过HCO的利用对待反应的残余水疗院，导致提高的石油利用和精炼厂的经济好处。

简介：Theproductionunitusinganewprocessformanufactureof1,3-phenylenediaminedevelopedindependentlybytheQingdaoScienceandTechnologyUniversity(QSTU)hasbeensuccessfullyputonstreamattheShandongEkesenChemicalCompanywithitsproductioncapacityreaching10kt/aandalltechnicalindicatorscomplyingwith