Phenylethyl Alcohol (CAS 60-12-8)

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Physical Properties

Property	Value	Unit	Source
ω	0.6124		Relay (1.0) Calculated Property
Δ_fG°	-7.93	kJ/mol	Joback Calculated Property
Δ_fH°_gas	-127.26	kJ/mol	Relay (1.0) Calculated Property
Δ_fusH°	14.61	kJ/mol	Joback Calculated Property
Δ_vapH°	67.11	kJ/mol	Relay (1.0) Calculated Property
IE	8.83	eV	Relay (1.0) Calculated Property
log₁₀WS	-0.74		Aq. Solubility Prediction
logP_oct/wat	1.221		Crippen Calculated Property
McVol	105.690	ml/mol	McGowan Calculated Property
P_c	[3850.00; 3990.00]	kPa
P_c	3990.00	kPa	Critical Point and Vapor Pressure Measurements for Seven Compounds by a Low Residence Time Flow Method
P_c	3850.00	kPa	Vapor-Liquid Critical Properties of Phenol and (C8 to C10) Phenylalkanols
I_np	[195.30; 1159.00]
I_np	1085.50		NIST
I_np	1088.47		NIST
I_np	1091.65		NIST
I_np	1095.04		NIST
I_np	1100.00		NIST
I_np	1073.43		NIST
I_np	1074.60		NIST
I_np	1076.16		NIST
I_np	1078.09		NIST
I_np	1080.29		NIST
I_np	1082.78		NIST
I_np	1092.00		NIST
I_np	1092.00		NIST
I_np	1060.00		NIST
I_np	1127.00		NIST
I_np	1128.00		NIST
I_np	1099.00		NIST
I_np	1092.00		NIST
I_np	1099.00		NIST
I_np	1084.00		NIST
I_np	1086.00		NIST
I_np	1110.00		NIST
I_np	1089.00		NIST
I_np	1121.00		NIST
I_np	1124.00		NIST
I_np	1102.00		NIST
I_np	1102.00		NIST
I_np	1114.00		NIST
I_np	1092.00		NIST
I_np	1117.00		NIST
I_np	1120.00		NIST
I_np	1096.00		NIST
I_np	1105.00		NIST
I_np	1102.00		NIST
I_np	1102.00		NIST
I_np	1104.00		NIST
I_np	1105.00		NIST
I_np	1107.00		NIST
I_np	1105.00		NIST
I_np	1104.00		NIST
I_np	1116.00		NIST
I_np	1091.00		NIST
I_np	1097.00		NIST
I_np	1117.00		NIST
I_np	1060.00		NIST
I_np	1139.00		NIST
I_np	1120.00		NIST
I_np	1082.40		NIST
I_np	1083.70		NIST
I_np	1144.00		NIST
I_np	1149.00		NIST
I_np	1114.00		NIST
I_np	1112.00		NIST
I_np	1141.00		NIST
I_np	1110.00		NIST
I_np	1117.00		NIST
I_np	1118.40		NIST
I_np	1060.00		NIST
I_np	1129.00		NIST
I_np	1108.00		NIST
I_np	1139.00		NIST
I_np	1135.00		NIST
I_np	1116.30		NIST
I_np	1120.00		NIST
I_np	1110.00		NIST
I_np	1150.00		NIST
I_np	1130.00		NIST
I_np	1114.00		NIST
I_np	1150.00		NIST
I_np	1088.00		NIST
I_np	1115.10		NIST
I_np	1116.20		NIST
I_np	1116.80		NIST
I_np	1125.00		NIST
I_np	1113.00		NIST
I_np	1100.00		NIST
I_np	1110.00		NIST
I_np	1111.00		NIST
I_np	1084.00		NIST
I_np	1113.00		NIST
I_np	1086.00		NIST
I_np	1080.00		NIST
I_np	1111.00		NIST
I_np	1112.00		NIST
I_np	1116.00		NIST
I_np	1080.00		NIST
I_np	1076.20		NIST
I_np	1113.00		NIST
I_np	1113.00		NIST
I_np	1114.00		NIST
I_np	1110.00		NIST
I_np	1081.00		NIST
I_np	1116.00		NIST
I_np	1102.00		NIST
I_np	1114.00		NIST
I_np	1109.00		NIST
I_np	1109.00		NIST
I_np	1081.00		NIST
I_np	1081.00		NIST
I_np	1121.00		NIST
I_np	1069.11		NIST
I_np	1069.74		NIST
I_np	1127.00		NIST
I_np	1107.00		NIST
I_np	1105.00		NIST
I_np	1090.00		NIST
I_np	1090.00		NIST
I_np	1091.00		NIST
I_np	1109.00		NIST
I_np	1111.00		NIST
I_np	1089.00		NIST
I_np	1089.00		NIST
I_np	1079.00		NIST
I_np	1080.00		NIST
I_np	1086.00		NIST
I_np	1086.00		NIST
I_np	1081.00		NIST
I_np	1086.00		NIST
I_np	1075.00		NIST
I_np	1080.00		NIST
I_np	1080.00		NIST
I_np	1080.00		NIST
I_np	1080.00		NIST
I_np	1083.00		NIST
I_np	1083.00		NIST
I_np	1102.00		NIST
I_np	1083.00		NIST
I_np	1078.00		NIST
I_np	1090.00		NIST
I_np	1104.00		NIST
I_np	1079.80		NIST
I_np	1080.40		NIST
I_np	1078.00		NIST
I_np	1119.00		NIST
I_np	1092.00		NIST
I_np	1100.00		NIST
I_np	1095.00		NIST
I_np	1097.00		NIST
I_np	1096.00		NIST
I_np	1096.00		NIST
I_np	1113.00		NIST
I_np	1116.00		NIST
I_np	1113.00		NIST
I_np	1111.00		NIST
I_np	1112.00		NIST
I_np	1109.00		NIST
I_np	1116.00		NIST
I_np	1141.00		NIST
I_np	1116.00		NIST
I_np	1115.00		NIST
I_np	1136.00		NIST
I_np	1140.00		NIST
I_np	1121.00		NIST
I_np	1112.00		NIST
I_np	1116.00		NIST
I_np	1110.00		NIST
I_np	1113.00		NIST
I_np	1103.00		NIST
I_np	1103.00		NIST
I_np	1110.00		NIST
I_np	1114.00		NIST
I_np	1110.00		NIST
I_np	1103.00		NIST
I_np	1118.00		NIST
I_np	1117.00		NIST
I_np	1103.00		NIST
I_np	1118.00		NIST
I_np	1106.00		NIST
I_np	1118.00		NIST
I_np	1113.00		NIST
I_np	1110.00		NIST
I_np	1120.00		NIST
I_np	1122.00		NIST
I_np	1117.00		NIST
I_np	1116.00		NIST
I_np	1099.00		NIST
I_np	1120.00		NIST
I_np	1114.00		NIST
I_np	1112.00		NIST
I_np	1115.00		NIST
I_np	1111.00		NIST
I_np	1113.00		NIST
I_np	1114.00		NIST
I_np	1116.00		NIST
I_np	1120.00		NIST
I_np	1116.00		NIST
I_np	1116.00		NIST
I_np	1116.00		NIST
I_np	1117.00		NIST
I_np	1117.00		NIST
I_np	1108.00		NIST
I_np	1117.00		NIST
I_np	1118.00		NIST
I_np	1118.00		NIST
I_np	1082.00		NIST
I_np	1083.00		NIST
I_np	1092.00		NIST
I_np	1104.00		NIST
I_np	1084.00		NIST
I_np	1123.00		NIST
I_np	1117.00		NIST
I_np	1123.00		NIST
I_np	1075.00		NIST
I_np	1110.00		NIST
I_np	1109.00		NIST
I_np	1132.00		NIST
I_np	1112.00		NIST
I_np	1120.00		NIST
I_np	1117.00		NIST
I_np	1118.00		NIST
I_np	1159.00		NIST
I_np	1102.00		NIST
I_np	1112.00		NIST
I_np	1118.00		NIST
I_np	1111.00		NIST
I_np	1109.00		NIST
I_np	1120.00		NIST
I_np	1120.00		NIST
I_np	1105.00		NIST
I_np	1112.00		NIST
I_np	1111.00		NIST
I_np	1092.00		NIST
I_np	1125.00		NIST
I_np	1129.00		NIST
I_np	1129.00		NIST
I_np	1129.00		NIST
I_np	1122.00		NIST
I_np	1127.00		NIST
I_np	1137.00		NIST
I_np	1117.10		NIST
I_np	1105.00		NIST
I_np	1086.00		NIST
I_np	1110.00		NIST
I_np	1137.00		NIST
I_np	1109.00		NIST
I_np	1110.00		NIST
I_np	1086.00		NIST
I_np	1129.00		NIST
I_np	1076.00		NIST
I_np	1078.00		NIST
I_np	1078.00		NIST
I_np	1081.00		NIST
I_np	1120.00		NIST
I_np	1104.00		NIST
I_np	1104.00		NIST
I_np	1119.00		NIST
I_np	1088.00		NIST
I_np	1110.00		NIST
I_np	1110.00		NIST
I_np	1082.00		NIST
I_np	1120.00		NIST
I_np	1076.00		NIST
I_np	1108.00		NIST
I_np	1110.00		NIST
I_np	1111.00		NIST
I_np	1089.00		NIST
I_np	1083.00		NIST
I_np	1112.00		NIST
I_np	1127.00		NIST
I_np	1105.00		NIST
I_np	1140.00		NIST
I_np	1116.00		NIST
I_np	1116.00		NIST
I_np	1112.00		NIST
I_np	1084.90		NIST
I_np	1146.00		NIST
I_np	1120.00		NIST
I_np	1078.00		NIST
I_np	1095.00		NIST
I_np	1112.00		NIST
I_np	1118.00		NIST
I_np	1125.00		NIST
I_np	1118.00		NIST
I_np	1108.00		NIST
I_np	1078.00		NIST
I_np	1078.00		NIST
I_np	1105.00		NIST
I_np	1088.00		NIST
I_np	1080.00		NIST
I_np	1098.00		NIST
I_np	1130.00		NIST
I_np	1096.00		NIST
I_np	1104.00		NIST
I_np	1120.00		NIST
I_np	1120.00		NIST
I_np	1085.00		NIST
I_np	1104.00		NIST
I_np	1114.00		NIST
I_np	1081.00		NIST
I_np	1081.00		NIST
I_np	1081.00		NIST
I_np	1081.00		NIST
I_np	1104.00		NIST
I_np	1121.00		NIST
I_np	1082.00		NIST
I_np	1079.00		NIST
I_np	1080.00		NIST
I_np	1081.00		NIST
I_np	1130.00		NIST
I_np	1119.00		NIST
I_np	1083.00		NIST
I_np	1081.00		NIST
I_np	1080.00		NIST
I_np	1101.00		NIST
I_np	1101.00		NIST
I_np	1090.00		NIST
I_np	1107.00		NIST
I_np	1118.00		NIST
I_np	1115.00		NIST
I_np	1118.00		NIST
I_np	1090.00		NIST
I_np	1117.00		NIST
I_np	1118.00		NIST
I_np	1108.00		NIST
I_np	1136.00		NIST
I_np	1090.00		NIST
I_np	1108.00		NIST
I_np	1107.00		NIST
I_np	1119.00		NIST
I_np	1127.00		NIST
I_np	1120.00		NIST
I_np	1122.00		NIST
I_np	1064.00		NIST
I_np	1113.00		NIST
I_np	1096.00		NIST
I_np	1093.00		NIST
I_np	1112.00		NIST
I_np	1112.00		NIST
I_np	1064.00		NIST
I_np	1126.00		NIST
I_np	1114.00		NIST
I_np	1118.00		NIST
I_np	1111.00		NIST
I_np	1083.00		NIST
I_np	1109.00		NIST
I_np	1081.00		NIST
I_np	1113.00		NIST
I_np	1095.00		NIST
I_np	1074.00		NIST
I_np	1117.00		NIST
I_np	1123.00		NIST
I_np	1123.00		NIST
I_np	1118.00		NIST
I_np	1117.00		NIST
I_np	1115.00		NIST
I_np	1113.00		NIST
I_np	1107.00		NIST
I_np	1115.00		NIST
I_np	1090.00		NIST
I_np	1090.00		NIST
I_np	1125.00		NIST
I_np	1079.00		NIST
I_np	1080.00		NIST
I_np	1107.00		NIST
I_np	1116.00		NIST
I_np	1079.00		NIST
I_np	1079.00		NIST
I_np	1093.00		NIST
I_np	1120.00		NIST
I_np	1111.00		NIST
I_np	1118.00		NIST
I_np	1117.00		NIST
I_np	1084.00		NIST
I_np	1108.00		NIST
I_np	1124.00		NIST
I_np	1124.00		NIST
I_np	1096.00		NIST
I_np	1104.00		NIST
I_np	1113.00		NIST
I_np	1130.00		NIST
I_np	1110.00		NIST
I_np	1090.00		NIST
I_np	1113.00		NIST
I_np	1108.00		NIST
I_np	1092.00		NIST
I_np	1087.00		NIST
I_np	1116.00		NIST
I_np	1125.00		NIST
I_np	1132.00		NIST
I_np	1126.00		NIST
I_np	1106.00		NIST
I_np	1118.00		NIST
I_np	1113.00		NIST
I_np	1108.00		NIST
I_np	1108.00		NIST
I_np	1092.00		NIST
I_np	1091.00		NIST
I_np	1112.00		NIST
I_np	1087.00		NIST
I_np	1091.00		NIST
I_np	1091.00		NIST
I_np	1080.00		NIST
I_np	1115.00		NIST
I_np	1116.00		NIST
I_np	1116.00		NIST
I_np	1118.00		NIST
I_np	1118.00		NIST
I_np	1118.00		NIST
I_np	1098.00		NIST
I_np	1089.00		NIST
I_np	1120.00		NIST
I_np	1119.00		NIST
I_np	1081.00		NIST
I_np	1118.00		NIST
I_np	1118.00		NIST
I_np	1104.00		NIST
I_np	1148.00		NIST
I_np	1150.00		NIST
I_np	1143.00		NIST
I_np	1146.00		NIST
I_np	Outlier 195.30		NIST
I_np	1116.00		NIST
I_np	Outlier 195.30		NIST
I	[1856.00; 1955.90]
I	1931.00		NIST
I	1865.00		NIST
I	1874.00		NIST
I	1892.00		NIST
I	1904.00		NIST
I	1906.00		NIST
I	1914.00		NIST
I	1874.00		NIST
I	1912.00		NIST
I	1912.00		NIST
I	1904.00		NIST
I	1922.00		NIST
I	1923.00		NIST
I	1919.00		NIST
I	1923.00		NIST
I	Outlier 1858.00		NIST
I	1876.00		NIST
I	Outlier 1859.00		NIST
I	1890.00		NIST
I	1890.00		NIST
I	1861.00		NIST
I	1868.00		NIST
I	1888.00		NIST
I	1901.00		NIST
I	1915.00		NIST
I	1931.00		NIST
I	1920.00		NIST
I	1925.00		NIST
I	1924.00		NIST
I	Outlier 1858.00		NIST
I	1914.00		NIST
I	1872.00		NIST
I	1900.00		NIST
I	1935.00		NIST
I	1900.00		NIST
I	1915.00		NIST
I	1920.00		NIST
I	1920.00		NIST
I	1946.00		NIST
I	1921.00		NIST
I	1905.00		NIST
I	1895.00		NIST
I	1875.00		NIST
I	1944.00		NIST
I	1896.00		NIST
I	1862.00		NIST
I	1873.00		NIST
I	1872.00		NIST
I	1946.00		NIST
I	Outlier 1952.00		NIST
I	1902.00		NIST
I	1878.00		NIST
I	1883.00		NIST
I	1892.00		NIST
I	1890.00		NIST
I	1901.00		NIST
I	1911.00		NIST
I	1914.00		NIST
I	1902.00		NIST
I	1906.00		NIST
I	1862.00		NIST
I	1901.00		NIST
I	1915.00		NIST
I	1885.00		NIST
I	1939.00		NIST
I	1905.00		NIST
I	1929.00		NIST
I	1888.00		NIST
I	1919.00		NIST
I	1893.00		NIST
I	1897.00		NIST
I	1894.00		NIST
I	1879.00		NIST
I	1873.30		NIST
I	1888.00		NIST
I	1888.00		NIST
I	1878.00		NIST
I	1902.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	1925.00		NIST
I	1917.00		NIST
I	1933.00		NIST
I	1893.00		NIST
I	1924.00		NIST
I	1917.00		NIST
I	1912.00		NIST
I	1908.00		NIST
I	1866.00		NIST
I	1866.00		NIST
I	1946.00		NIST
I	Outlier 1856.00		NIST
I	1893.00		NIST
I	1893.00		NIST
I	1923.00		NIST
I	1924.00		NIST
I	1923.00		NIST
I	1886.00		NIST
I	1903.00		NIST
I	1932.00		NIST
I	1873.00		NIST
I	1903.00		NIST
I	1890.00		NIST
I	1899.00		NIST
I	1873.00		NIST
I	1888.00		NIST
I	1899.00		NIST
I	1899.00		NIST
I	1907.80		NIST
I	1910.50		NIST
I	1899.00		NIST
I	1902.00		NIST
I	1871.00		NIST
I	1923.00		NIST
I	1925.00		NIST
I	1901.00		NIST
I	1902.00		NIST
I	1906.00		NIST
I	1907.00		NIST
I	1909.00		NIST
I	1919.00		NIST
I	1896.00		NIST
I	1873.00		NIST
I	1875.00		NIST
I	1894.00		NIST
I	1939.00		NIST
I	1909.00		NIST
I	1902.00		NIST
I	1925.00		NIST
I	1910.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	1871.00		NIST
I	1871.00		NIST
I	1871.00		NIST
I	1871.00		NIST
I	1944.00		NIST
I	1911.00		NIST
I	1909.00		NIST
I	1936.00		NIST
I	1896.00		NIST
I	1948.00		NIST
I	1905.00		NIST
I	1918.00		NIST
I	1918.00		NIST
I	1918.00		NIST
I	1909.00		NIST
I	Outlier 1952.00		NIST
I	1908.00		NIST
I	1911.00		NIST
I	1902.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	1889.00		NIST
I	1894.00		NIST
I	1893.00		NIST
I	1911.00		NIST
I	1914.00		NIST
I	1891.00		NIST
I	1883.00		NIST
I	1888.00		NIST
I	1886.00		NIST
I	1932.00		NIST
I	1915.00		NIST
I	1920.00		NIST
I	1915.00		NIST
I	Outlier 1955.90		NIST
I	1898.00		NIST
I	Outlier 1953.00		NIST
I	1921.00		NIST
I	1926.00		NIST
I	1903.00		NIST
I	1944.00		NIST
I	1947.00		NIST
I	1947.00		NIST
I	1921.00		NIST
I	1888.00		NIST
I	1929.00		NIST
I	1911.00		NIST
I	1911.00		NIST
I	1905.00		NIST
I	1932.00		NIST
I	1929.00		NIST
I	1918.00		NIST
I	1899.00		NIST
I	1910.00		NIST
I	1941.00		NIST
I	1929.00		NIST
I	1928.00		NIST
I	1925.00		NIST
I	1906.00		NIST
I	1886.00		NIST
I	1937.00		NIST
I	1918.00		NIST
I	1906.00		NIST
I	1906.00		NIST
I	1906.00		NIST
I	1906.00		NIST
I	1936.00		NIST
I	1926.00		NIST
I	1886.00		NIST
I	1907.00		NIST
I	1938.00		NIST
I	1936.00		NIST
I	1917.00		NIST
I	Outlier 1857.00		NIST
I	1943.00		NIST
I	1929.00		NIST
I	1891.00		NIST
I	1905.00		NIST
I	1950.00		NIST
I	1891.00		NIST
I	1890.00		NIST
I	1892.00		NIST
I	1926.00		NIST
I	1870.00		NIST
I	1927.00		NIST
I	1940.00		NIST
I	1916.00		NIST
I	1932.00		NIST
I	1944.00		NIST
I	1910.00		NIST
I	1909.00		NIST
I	1938.00		NIST
I	1907.00		NIST
I	1929.00		NIST
I	1929.00		NIST
I	1916.00		NIST
I	1917.00		NIST
I	1919.00		NIST
I	1894.00		NIST
I	1947.00		NIST
I	1947.00		NIST
I	1944.00		NIST
I	1942.00		NIST
I	1878.00		NIST
I	1910.00		NIST
I	1865.00		NIST
I	1896.00		NIST
I	1899.00		NIST
I	1909.00		NIST
I	1899.00		NIST
I	1931.00		NIST
I	1931.00		NIST
I	1928.00		NIST
I	1912.00		NIST
I	1901.00		NIST
I	Outlier 1859.00		NIST
I	1890.00		NIST
I	1902.00		NIST
I	1902.00		NIST
I	1913.00		NIST
I	1899.00		NIST
I	1908.00		NIST
I	1893.00		NIST
I	1899.00		NIST
I	1908.00		NIST
I	1929.00		NIST
I	Outlier 1859.00		NIST
I	1931.00		NIST
I	1905.00		NIST
I	1909.00		NIST
I	1907.00		NIST
I	1926.00		NIST
I	1931.00		NIST
I	1931.00		NIST
I	1931.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	1892.00		NIST
I	1899.00		NIST
I	1875.00		NIST
I	1929.00		NIST
I	1943.00		NIST
I	1930.00		NIST
I	1861.00		NIST
I	1883.00		NIST
I	1929.00		NIST
I	1908.00		NIST
I	1863.00		NIST
I	1863.00		NIST
I	1863.00		NIST
I	Outlier 1859.00		NIST
I	1863.00		NIST
I	1863.00		NIST
I	1902.00		NIST
I	1902.00		NIST
I	1942.00		NIST
I	1901.00		NIST
I	1889.00		NIST
I	1890.00		NIST
I	1942.00		NIST
I	1865.00		NIST
I	1865.00		NIST
I	1920.00		NIST
I	1890.00		NIST
I	1865.00		NIST
I	1865.00		NIST
I	1890.00		NIST
I	1890.00		NIST
I	1890.00		NIST
I	1890.00		NIST
I	1890.00		NIST
I	1915.00		NIST
I	1921.00		NIST
I	1913.00		NIST
I	1929.00		NIST
I	1928.00		NIST
I	1919.00		NIST
I	1933.00		NIST
I	1898.00		NIST
I	1900.00		NIST
I	1939.00		NIST
I	1939.00		NIST
I	1925.00		NIST
I	1907.00		NIST
I	1935.00		NIST
I	1921.00		NIST
I	1927.00		NIST
I	1865.00		NIST
I	1916.00		NIST
I	1933.00		NIST
I	1922.00		NIST
I	1919.00		NIST
I	1921.00		NIST
I	1923.00		NIST
I	1939.00		NIST
I	1925.00		NIST
I	1916.00		NIST
I	1892.00		NIST
I	1903.00		NIST
I	1913.00		NIST
I	1888.00		NIST
I	1896.00		NIST
I	1884.00		NIST
I	1931.00		NIST
I	1891.00		NIST
I	1891.00		NIST
I	1902.00		NIST
I	1931.00		NIST
I	1873.00		NIST
I	1906.00		NIST
I	1902.00		NIST
I	1911.00		NIST
I	1931.00		NIST
I	1896.00		NIST
I	1897.00		NIST
I	1909.00		NIST
I	1906.00		NIST
I	1926.00		NIST
I	1931.00		NIST
I	1939.00		NIST
I	1873.00		NIST
I	1921.00		NIST
I	1921.00		NIST
I	1889.00		NIST
I	1888.00		NIST
I	1878.00		NIST
I	1907.00		NIST
I	Outlier 1860.00		NIST
I	1942.00		NIST
I	1912.00		NIST
I	1905.00		NIST
I	1937.00		NIST
I	1890.00		NIST
I	1915.00		NIST
I	1941.00		NIST
I	1922.00		NIST
I	1899.00		NIST
I	1937.00		NIST
I	1937.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	Outlier 1860.00		NIST
I	1878.00		NIST
I	1951.00		NIST
I	1906.00		NIST
I	1904.00		NIST
I	1888.00		NIST
I	1896.00		NIST
I	1887.00		NIST
I	1937.00		NIST
I	1862.00		NIST
I	1933.00		NIST
I	1908.00		NIST
I	1929.00		NIST
I	1895.00		NIST
I	1905.00		NIST
I	1905.00		NIST
I	1889.00		NIST
I	1910.00		NIST
I	1915.00		NIST
I	1915.00		NIST
I	1910.00		NIST
I	Outlier 1859.00		NIST
I	1902.00		NIST
I	1906.00		NIST
I	1880.00		NIST
I	1916.00		NIST
I	1925.00		NIST
I	1933.00		NIST
I	1908.00		NIST
I	1873.00		NIST
I	1868.00		NIST
I	Outlier 1859.00		NIST
I	1939.00		NIST
I	1905.00		NIST
I	1871.00		NIST
I	1896.00		NIST
I	1918.00		NIST
I	1902.00		NIST
I	1893.00		NIST
I	1888.00		NIST
I	1915.00		NIST
I	1926.00		NIST
I	1901.00		NIST
I	Outlier 1858.00		NIST
I	1900.00		NIST
I	1921.00		NIST
I	Outlier 1952.00		NIST
I	1890.00		NIST
I	1906.00		NIST
I	1924.00		NIST
I	1866.00		NIST
I	1923.00		NIST
I	1932.00		NIST
I	1873.00		NIST
I	1910.50		NIST
I	1925.00		NIST
I	1909.00		NIST
I	1894.00		NIST
T_boil	[491.40; 492.90]	K
T_boil	491.40	K	NIST
T_boil	492.55 ± 0.40	K	NIST
T_boil	492.90 ± 0.30	K	NIST
T_c	734.23	K	Relay (1.0) Calculated Property
T_fus	[246.00; 254.00]	K
T_fus	246.00	K	Phase equilibrium in binary systems of ionic liquids, or deep eutectic solvents with 2-phenylethanol (PEA), or water
T_fus	254.00 ± 2.00	K	NIST
V_c	0.369	m³/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[223.55; 279.10]	J/mol×K	[501.30; 698.78]

C_p,gas	223.55	J/mol×K	501.30	Joback Calculated Property
C_p,gas	234.25	J/mol×K	534.21	Joback Calculated Property
C_p,gas	244.34	J/mol×K	567.13	Joback Calculated Property
C_p,gas	253.84	J/mol×K	600.04	Joback Calculated Property
C_p,gas	262.79	J/mol×K	632.95	Joback Calculated Property
C_p,gas	271.20	J/mol×K	665.87	Joback Calculated Property
C_p,gas	279.10	J/mol×K	698.78	Joback Calculated Property
C_p,liquid	252.64	J/mol×K	298.15	NIST
η	[0.0001462; 0.0201132]	Pa×s	[267.16; 501.30]

η	0.0201132	Pa×s	267.16	Joback Calculated Property
η	0.0052469	Pa×s	306.18	Joback Calculated Property
η	0.0018546	Pa×s	345.21	Joback Calculated Property
η	0.0008098	Pa×s	384.23	Joback Calculated Property
η	0.0004119	Pa×s	423.25	Joback Calculated Property
η	0.0002349	Pa×s	462.28	Joback Calculated Property
η	0.0001462	Pa×s	501.30	Joback Calculated Property
Δ_vapH	55.10	kJ/mol	503.50	NIST
P_vap	[2.51e-03; 95.30]	kPa	[287.80; 489.79]

P_vap	2.51e-03	kPa	287.80	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	2.85e-03	kPa	289.70	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	3.99e-03	kPa	292.70	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	4.82e-03	kPa	295.10	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	6.26e-03	kPa	297.50	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	9.76e-03	kPa	302.50	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.02	kPa	308.20	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.02	kPa	312.50	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.03	kPa	316.60	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.03	kPa	317.60	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.05	kPa	322.70	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.05	kPa	322.70	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.05	kPa	322.80	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.07	kPa	327.80	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.10	kPa	332.80	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.14	kPa	337.90	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.21	kPa	342.90	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.28	kPa	348.10	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.38	kPa	353.20	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.52	kPa	358.30	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	0.69	kPa	363.30	Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
P_vap	95.30	kPa	489.79	Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
n₀	[1.52670; 1.53210]		[298.15; 308.15]
n₀	1.53210		298.15	Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
n₀	1.52690		308.15	Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
n₀	1.52670		308.15	Excess Enthalpies, Heat Capacities, Densities, Viscosities and Refractive Indices of Dimethyl Sulfoxide + Three Aryl Alcohols at 308.15 K and Atmospheric Pressure
n₀	1.52852		308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Ternary Mixtures of 2-Propanol + Benzyl Alcohol + 2-Phenylethanol at T = 308.15 K
ρ_l	[985.48; 1019.00]	kg/m³	[293.15; 338.15]

ρ_l	1019.00	kg/m³	293.15	Phase equilibrium investigation with ionic liquids and selectivity in separation of 2-phenylethanol from water
ρ_l	1016.14	kg/m³	298.15	Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρ_l	1016.20	kg/m³	298.15	Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
ρ_l	1016.16	kg/m³	298.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρ_l	1016.16	kg/m³	298.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	1012.34	kg/m³	303.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρ_l	1012.40	kg/m³	303.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	1012.39	kg/m³	303.15	Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρ_l	1008.63	kg/m³	308.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρ_l	1008.62	kg/m³	308.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	1008.61	kg/m³	308.15	Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρ_l	1008.68	kg/m³	308.15	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
ρ_l	1008.61	kg/m³	308.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρ_l	1008.72	kg/m³	308.15	Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
ρ_l	1004.84	kg/m³	313.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρ_l	1004.83	kg/m³	313.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	1004.75	kg/m³	313.15	Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρ_l	1000.94	kg/m³	318.15	Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
ρ_l	1001.00	kg/m³	318.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	1000.98	kg/m³	318.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρ_l	1000.93	kg/m³	318.15	Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρ_l	997.16	kg/m³	323.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	997.08	kg/m³	323.15	Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρ_l	993.29	kg/m³	328.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρ_l	985.48	kg/m³	338.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
γ	[0.04; 0.04]	N/m	[298.15; 318.15]
γ	0.04	N/m	298.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
γ	0.04	N/m	308.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
γ	0.04	N/m	318.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_boilr	493.20	K	100.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.63]	kPa	[373.34; 518.37]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.70642e+01
Coefficient B			-5.69212e+03
Coefficient C			-3.40500e+01
Temperature range, min.			373.34
Temperature range, max.			518.37

P_vap	1.33	kPa	373.34	Calculated Property
P_vap	2.85	kPa	389.45	Calculated Property
P_vap	5.71	kPa	405.57	Calculated Property
P_vap	10.80	kPa	421.68	Calculated Property
P_vap	19.41	kPa	437.80	Calculated Property
P_vap	33.35	kPa	453.91	Calculated Property
P_vap	55.05	kPa	470.03	Calculated Property
P_vap	87.67	kPa	486.14	Calculated Property
P_vap	135.22	kPa	502.26	Calculated Property
P_vap	202.63	kPa	518.37	Calculated Property
P_vap	[6.36e-05; 3766.05]	kPa	[247.00; 684.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			7.90388e+01
Coefficient B			-9.76816e+03
Coefficient C			-8.96993e+00
Coefficient D			4.34164e-06
Temperature range, min.			247.00
Temperature range, max.			684.00

P_vap	6.36e-05	kPa	247.00	Calculated Property
P_vap	9.46e-03	kPa	295.56	Calculated Property
P_vap	0.29	kPa	344.11	Calculated Property
P_vap	3.51	kPa	392.67	Calculated Property
P_vap	22.70	kPa	441.22	Calculated Property
P_vap	97.21	kPa	489.78	Calculated Property
P_vap	312.50	kPa	538.33	Calculated Property
P_vap	819.27	kPa	586.89	Calculated Property
P_vap	1853.59	kPa	635.44	Calculated Property
P_vap	3766.05	kPa	684.00	Calculated Property

Similar Compounds

Find more compounds similar to Phenylethyl Alcohol.

Mixtures

Find more mixtures with Phenylethyl Alcohol.

Sources

KDB Vapor Pressure Data
Cheméo Relay (1.0)
Crippen Method
Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
Phase equilibrium in binary systems of ionic liquids, or deep eutectic solvents with 2-phenylethanol (PEA), or water
Separation of 2-phenylethanol (PEA) from water using ionic liquids
Partial molar volumes of organic solutes in water. XI. Phenylmethanol and 2-phenylethanol at T=(298 to 573) K and at pressures up to 30 MPa
Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
Solubility of ionic liquids in water and octan-1-ol and octan-1-ol/water, or 2-phenylethanol/water partition coefficients
Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
Phase equilibrium investigation with ionic liquids and selectivity in separation of 2-phenylethanol from water
Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
High Pressure Phase Equilibrium of CO2 + 2-Phenylethanol and CO2 + 3-Methyl-1-butanol
Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
Excess Enthalpies, Heat Capacities, Densities, Viscosities and Refractive Indices of Dimethyl Sulfoxide + Three Aryl Alcohols at 308.15 K and Atmospheric Pressure
Critical Point and Vapor Pressure Measurements for Seven Compounds by a Low Residence Time Flow Method
Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
Vapor-Liquid Critical Properties of Phenol and (C8 to C10) Phenylalkanols
Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
Solubilities of Hexanal, Benzaldehyde, 2-Furfural, 2-Phenylethanol, Phenylethanal, and c-Nonalactone in Water at Temperatures between (50 and 100) deg C
Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
Densities, Viscosities, Refractive Indices, and Surface Tensions for the Ternary Mixtures of 2-Propanol + Benzyl Alcohol + 2-Phenylethanol at T = 308.15 K
Partitioning of Phenylalkanols between Micelles and Water Studied by Limiting Interdiffusion Coefficients in Water and Tetradecyltrimethylammonium Bromide Solutions
Joback Method
KDB
Aqueous Solubility Prediction Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure

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Chemical Properties of Phenylethyl Alcohol (CAS 60-12-8)