% Exported from MKS Knowledge Base: MATLAB Export KB.mkskbd
% Exported by SYNAPSE 4.0, Core 327.0, Professional Edition
% Exported on Feb 27, 2024 at 20:18:20

% MKS Request Object
mksReq = MKSRequest;
mksReq.fileName = "MATLAB Export KB.mkskbd";
mksReq.processor = "SYNAPSE 4.0, Core 327.0, Professional Edition";
mksReq.type = "Get Values";
mksReq.date = "Feb 27, 2024 at 20:18:20";
mksReq.version = 2.0;

   % Entity Start: Levulinic acid
   mksEnt = MKSEntity;
   mksEnt.identifier = "Levulinic acid";
   mksEnt.entityType = "Chemical";

      % Property Start: Molecular Weight
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Molecular Weight";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 116.115;
         mksDtm.reference = "Mw: Definition [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:14 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Molecular Weight
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Melting Point
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Melting Point";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 277.796566028342;
         mksDtm.valueUnits = "K";
         mksDtm.reference = "Tm: Constantinou + Gani First Order Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:14 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Melting Point
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Critical Temperature
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Critical Temperature";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 694.622257983032;
         mksDtm.valueUnits = "K";
         mksDtm.reference = "Tc: Joback Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:14 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Critical Temperature
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Boiling Point
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Boiling Point";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 499.102763295;
         mksDtm.valueUnits = "K";
         mksDtm.reference = "Tb: Stein + Brown Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:14 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Boiling Point
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Autoignition Temperature
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Autoignition Temperature";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 679.788890395386;
         mksDtm.valueUnits = "K";
         mksDtm.reference = "AIT: Chen + Liaw + Kuo Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:14 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Autoignition Temperature
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Critical Pressure
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Critical Pressure";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 3975224.54599847;
         mksDtm.valueUnits = "Pa";
         mksDtm.reference = "Pc: Wilson + Jasperson Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:14 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Critical Pressure
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Critical Volume
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Critical Volume";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 0.00297549842828231;
         mksDtm.valueUnits = "m3/kg";
         mksDtm.reference = "Vc: Joback Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:14 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Critical Volume
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Enthalpy of Combustion at 298K
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Enthalpy of Combustion at 298K";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = -20920092.4179591;
         mksDtm.valueUnits = "J/kg";
         mksDtm.reference = "Hc,298: Enthalpy Difference Calculation [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:15 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Enthalpy of Combustion at 298K
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Enthalpy of Formation, Ideal at 298K
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Enthalpy of Formation, Ideal at 298K";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = -5248073.03104681;
         mksDtm.valueUnits = "J/kg";
         mksDtm.reference = "dHf,id,298: Joback Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:16 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Enthalpy of Formation, Ideal at 298K
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Enthalpy of Fusion at Tm
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Enthalpy of Fusion at Tm";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 176101.278904534;
         mksDtm.valueUnits = "J/kg";
         mksDtm.reference = "Hm,tm: Joback Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:16 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Enthalpy of Fusion at Tm
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Enthalpy of Vaporization at Tb
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Enthalpy of Vaporization at Tb";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 476323.919137337;
         mksDtm.valueUnits = "J/kg";
         mksDtm.reference = "Hv,tb: Vetere Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:16 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Enthalpy of Vaporization at Tb
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Flash Point, Closed Cup
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Flash Point, Closed Cup";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 396.182000713888;
         mksDtm.valueUnits = "K";
         mksDtm.reference = "Tf,cc: Affens Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:16 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Flash Point, Closed Cup
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Gibbs Energy of Formation, Ideal at 298K
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Gibbs Energy of Formation, Ideal at 298K";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = -4023597.29578435;
         mksDtm.valueUnits = "J/kg";
         mksDtm.reference = "dGf,id,298: Joback Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:18 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Gibbs Energy of Formation, Ideal at 298K
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Acentric Factor
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Acentric Factor";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 0.776720906112163;
         mksDtm.reference = "AcF: Lee + Kesler Relation [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:19 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Acentric Factor
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Critical Compressibility
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Critical Compressibility";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 0.237807937649115;
         mksDtm.reference = "Zc: Definition [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:19 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Critical Compressibility
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Flammability Limit, Lower
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Flammability Limit, Lower";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 2.21973618713628;
         mksDtm.reference = "LFL: Seaton Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:19 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Flammability Limit, Lower
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Flammability Limit, Upper
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Flammability Limit, Upper";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 10.6265969001309;
         mksDtm.reference = "UFL: High + Danner Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:19 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Flammability Limit, Upper
      mksEnt.props(end+1) = mksPrp;

      % Property Start: Refractive Index, Liquid at 293K
      mksPrp = MKSProperty;
      mksPrp.status = "Estimated";
      mksPrp.name = "Refractive Index, Liquid at 293K";
      mksPrp.component = "0";
      mksPrp.dataType = "CDblUnRefDatum";

         mksDtm = MKSDatum;
         mksDtm.value = 1.4262584506739;
         mksDtm.reference = "RI,l,293: Vogel nD Method [MKS]";
         mksDtm.comment = "Feb 27, 2024 at 20:18:19 Estimated by SYNAPSE 4.0 export ...";
         mksPrp.data(end+1) = mksDtm;

      % Property End: Refractive Index, Liquid at 293K
      mksEnt.props(end+1) = mksPrp;

   % Entity End: Levulinic acid
   mksReq.entities(end+1) = mksEnt;