Combustion

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Boron Oxide (B₂O₃), Ideal Gas, mol. wt. = 69.6182
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−14.337	−834.847	−834.847	Infinite
100	40.042	226.986	334.961	−10.797	−835.713	−832.354	434.777
200	55.330	259.361	289.548	−6.037	−835.985	−828.844	216.472
250	61.832	272.432	284.842	−3.102	−835.979	−827.059	172.805
298.15	66.855	283.768	283.768	0.	−835.963	−825.343	144.597
300	67.028	284.182	283.789	0.124	−835.963	−825.277	143.694
350	71.228	294.841	284.601	3.584	−835.972	−823.496	122.900
400	74.727	304.587	286.499	7.235	−836.033	−821.710	107.304
450	77.728	313.566	289.014	11.048	−836.152	−819.913	95.173
500	80.362	321.894	291.891	15.002	−836.317	−818.100	85.466
600	84.817	336.954	298.173	23.269	−836.752	−814.418	70.901
700	88.439	350.310	304.685	31.938	−837.275	−810.655	60.492
800	91.403	362.320	311.151	40.935	−837.849	−806.814	52.680
900	93.830	373.230	317.452	50.200	−838.455	−802.898	46.599
1000	95.822	383.223	323.537	59.686	−839.087	−798.914	41.731
1100	97.462	392.435	329.387	69.353	−839.743	−794.864	37.745
1200	98.819	400.975	335.001	79.169	−840.428	−790.755	34.421
1300	99.950	408.931	340.386	89.109	−841.146	−786.586	31.605
1400	100.897	416.374	345.550	99.153	−841.902	−782.361	29.190
1500	101.696	423.363	350.507	109.284	−842.701	−778.081	27.095
1600	102.375	429.949	355.269	119.488	−843.550	−773.746	25.260
1700	102.955	436.173	359.846	129.755	−844.453	−769.355	23.639
1800	103.454	442.072	364.252	140.076	−845.415	−764.911	22.197
1900	103.886	447.677	368.496	150.444	−846.440	−760.411	20.905
2000	104.262	453.016	372.590	160.852	−847.531	−755.855	19.741
2100	104.591	458.111	376.542	171.295	−848.691	−751.243	18.686
2200	104.880	462.983	380.361	181.769	−849.924	−746.573	17.726
2300	105.136	467.651	384.056	192.270	−851.230	−741.847	16.848
2400	105.363	472.131	387.633	202.795	−953.131	−734.924	15.995
2500	105.565	476.436	391.099	213.342	−954.747	−725.799	15.165
2600	105.746	480.580	394.462	223.907	−956.376	−716.609	14.397
2700	105.908	484.574	397.726	234.490	−958.019	−707.356	13.685
2800	106.054	488.428	400.897	245.088	−959.677	−698.041	13.022
2900	106.186	492.152	403.980	255.700	−961.351	−688.669	12.404
3000	106.306	495.754	406.979	266.325	−963.042	−679.237	11.827
3100	106.415	499.242	409.899	276.961	−964.749	−669.748	11.285
Table Continued

Boron Oxide (B₂O₃), Ideal Gas, mol. wt. = 69.6182
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3200	106.515	502.622	412.744	287.608	−966.474	−660.205	10.777
3300	106.606	505.901	415.518	298.264	−968.214	−650.608	10.298
3400	106.689	509.085	418.223	308.929	−969.971	−640.956	9.847
3500	106.765	512.178	420.864	319.602	−971.744	−631.254	9.421
3600	106.836	515.187	423.442	330.282	−973.532	−621.500	9.018
3700	106.901	518.115	425.961	340.969	−975.337	−611.697	8.636
3800	106.961	520.967	428.424	351.662	−977.156	−601.843	8.273
3900	107.017	523.746	430.833	362.361	−978.991	−591.943	7.928
4000	107.069	526.456	433.190	373.065	−980.840	−581.996	7.600
4100	107.117	529.100	435.497	383.774	−982.703	−572.001	7.287
4200	107.161	531.682	437.756	394.488	−1944.280	−547.913	6.814
4300	107.203	534.204	439.970	405.206	−1943.998	−514.669	6.252
4400	107.242	536.669	442.140	415.929	−1943.734	−481.433	5.715
4500	107.279	539.080	444.267	426.655	−1943.488	−448.202	5.203
4600	107.313	541.438	446.354	437.384	−1943.261	−414.977	4.712
4700	107.345	543.746	448.402	448.117	−1943.055	−381.755	4.243
4800	107.375	546.006	450.412	458.853	−1942.871	−348.538	3.793
4900	107.403	548.221	452.386	469.592	−1942.709	−315.323	3.361
5000	107.430	550.391	454.324	480.334	−1942.570	−282.113	2.947
5100	107.455	552.518	456.229	491.078	−1942.457	−248.904	2.549
5200	107.479	554.605	458.101	501.825	−1942.370	−215.700	2.167
5300	107.502	556.653	459.941	512.574	−1942.312	−182.494	1.799
5400	107.523	558.662	461.750	523.325	−1942.285	−149.291	1.444
5500	107.543	560.636	463.530	534.078	−1942.289	−116.088	1.103
5600	107.562	562.574	465.282	544.834	−1942.328	−82.883	0.773
5700	107.580	564.477	467.005	555.591	−1942.403	−49.678	0.455
5800	107.597	566.349	468.702	566.350	−1942.517	−16.470	0.148
5900	107.613	568.188	470.373	577.110	−1942.672	16.736	−0.148
6000	107.629	569.997	472.018	587.872	−1942.870	49.949	−0.435

Beryllium (Be), Crystal−Liquid, mol. wt. = 9.01218
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−1.932	0.	0.	0.
100	1.819	0.503	19.434	−1.893	0.	0.	0.
200	9.984	4.174	10.751	−1.315	0.	0.	0.
250	13.574	6.801	9.695	−0.723	0.	0.	0.
298.15	16.380	9.440	9.440	0.	0.	0.	0.
300	16.472	9.542	9.440	0.030	0.	0.	0.
350	18.520	12.245	9.649	0.909	0.	0.	0.
400	19.965	14.817	10.136	1.872	0.	0.	0.
450	21.061	17.235	10.792	2.899	0.	0.	0.
500	21.943	19.501	11.551	3.975	0.	0.	0.
600	23.336	23.630	13.227	6.242	0.	0.	0.
700	24.463	27.314	14.981	8.634	0.	0.	0.
800	25.458	30.647	16.734	11.130	0.	0.	0.
900	26.384	33.699	18.452	13.723	0.	0.	0.
1000	27.274	36.525	20.119	16.406	0.	0.	0.
1100	28.147	39.166	21.732	19.177	0.	0.	0.
1200	29.016	41.652	23.290	22.035	0.	0.	0.
1300	29.886	44.009	24.793	24.980	0.	0.	0.
1400	30.763	46.256	26.247	28.013	0.	0.	0.
1500	31.650	48.409	27.653	31.133	0.	0.	0.
1527.000	31.892	48.975	28.025	31.991	Alpha–Beta transition
1527.000	30.000	53.461	28.025	38.840
1560.000	30.000	54.102	28.570	39.830	Beta–liquid transition
1560.000	28.788	59.163	28.570	47.725
1600	28.874	59.893	29.344	48.879	0.	0.	0.
1700	29.089	61.650	31.193	51.777	0.	0.	0.
1800	29.304	63.319	32.932	54.696	0.	0.	0.
1900	29.519	64.909	34.573	57.638	0.	0.	0.
2000	29.734	66.429	36.128	60.600	0.	0.	0.
2100	29.949	67.884	37.606	63.584	0.	0.	0.
2200	30.164	69.283	39.014	66.590	0.	0.	0.
2300	30.379	70.628	40.360	69.617	0.	0.	0.
2400	30.594	71.926	41.648	72.666	0.	0.	0.
2500	30.809	73.179	42.885	75.736	0.	0.	0.
2600	31.024	74.391	44.073	78.828	0.	0.	0.
2700	31.239	75.566	45.218	81.941	0.	0.	0.
Table Continued

Beryllium (Be), Crystal−Liquid, mol. wt. = 9.01218
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
2741.437	31.328	76.043	45.680	83.237	Fugacity = 1 bar
2800	31.454	76.706	46.322	85.075	−290.957	6.223	−0.116
2900	31.669	77.814	47.389	88.232	−289.894	16.817	−0.303
3000	31.884	78.891	48.421	91.409	−288.814	27.375	−0.477
3100	32.099	79.940	49.421	94.608	−287.718	37.897	−0.639
3200	32.314	80.963	50.391	97.829	−286.609	48.383	−0.790
3300	32.529	81.960	51.333	101.071	−285.488	58.834	−0.931
3400	32.744	82.934	52.248	104.335	−284.356	69.251	−1.064
3500	32.959	83.887	53.138	107.620	−283.215	79.635	−1.188

Beryllium (Be), Ideal Gas, mol. wt. = 9.01218
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−6.197	319.735	319.735	Infinite
100	20.786	113.567	154.755	−4.119	321.774	310.468	−162.172
200	20.786	127.975	138.176	−2.040	323.275	298.515	−77.964
250	20.786	132.613	136.617	−1.001	323.723	292.269	−61.066
298.15	20.786	136.274	136.274	0.	324.000	286.184	−50.138
300	20.786	136.403	136.275	0.038	324.008	285.950	−49.788
350	20.786	139.607	136.528	1.078	324.169	279.592	−41.727
400	20.786	142.383	137.090	2.117	324.245	273.218	−35.679
450	20.786	144.831	137.817	3.156	324.257	266.839	−30.974
500	20.786	147.021	138.630	4.196	324.221	260.460	−27.210
600	20.786	150.811	140.354	6.274	324.032	247.724	−21.566
700	20.786	154.015	142.082	8.353	323.719	235.029	−17.538
800	20.786	156.791	143.751	10.431	323.301	222.386	−14.520
900	20.786	159.239	145.339	12.510	322.787	209.802	−12.177
1000	20.786	161.429	146.840	14.589	322.183	197.279	−10.305
1100	20.786	163.410	148.258	16.667	321.490	184.822	−8.776
1200	20.786	165.219	149.597	18.746	320.711	172.431	−7.506
1300	20.786	166.882	150.863	20.824	319.844	160.109	−6.433
1400	20.786	168.423	152.063	22.903	318.890	147.857	−5.517
1500	20.786	169.857	153.202	24.982	317.848	135.676	−4.725
1600	20.786	171.198	154.286	27.060	302.182	124.093	−4.051
1700	20.786	172.458	155.318	29.139	301.362	112.988	−3.472
1800	20.787	173.647	156.303	31.218	300.521	101.931	−2.958
1900	20.787	174.770	157.246	33.296	299.659	90.922	−2.500
2000	20.789	175.837	158.149	35.375	298.775	79.958	−2.088
2100	20.791	176.851	159.016	37.454	297.870	69.040	−1.717
2200	20.795	177.818	159.849	39.533	296.943	58.165	−1.381
2300	20.801	178.743	160.650	41.613	295.996	47.332	−1.075
2400	20.811	179.628	161.423	43.694	295.028	36.541	−0.795
2500	20.824	180.478	162.168	45.775	294.039	25.791	−0.539
2600	20.844	181.295	162.888	47.859	293.031	15.081	−0.303
2700	20.870	182.082	163.584	49.944	292.003	4.410	−0.085
2741.437	20.883	182.400	163.867	50.809	Fugacity = 1 bar
2800	20.905	182.842	164.259	52.033	0.	0.	0.
2900	20.949	183.576	164.912	54.126	0.	0.	0.
3000	21.006	184.287	165.546	56.223	0.	0.	0.
Table Continued

Beryllium (Be), Ideal Gas, mol. wt. = 9.01218
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3100	21.075	184.977	166.162	58.327	0.	0.	0.
3200	21.159	185.648	166.761	60.439	0.	0.	0.
3300	21.259	186.300	167.343	62.559	0.	0.	0.
3400	21.376	186.937	167.910	64.691	0.	0.	0.
3500	21.512	187.558	168.462	66.835	0.	0.	0.
3600	21.668	188.166	169.001	68.994	0.	0.	0.
3700	21.844	188.762	169.527	71.170	0.	0.	0.
3800	22.041	189.347	170.041	73.364	0.	0.	0.
3900	22.259	189.923	170.544	75.578	0.	0.	0.
4000	22.500	190.489	171.035	77.816	0.	0.	0.
4100	22.761	191.048	171.516	80.079	0.	0.	0.
4200	23.045	191.600	171.988	82.369	0.	0.	0.
4300	23.349	192.146	172.451	84.689	0.	0.	0.
4400	23.674	192.686	172.904	87.040	0.	0.	0.
4500	24.019	193.222	173.350	89.424	0.	0.	0.
4600	24.383	193.754	173.788	91.844	0.	0.	0.
4700	24.764	194.282	174.218	94.301	0.	0.	0.
4800	25.162	194.808	174.642	96.798	0.	0.	0.
4900	25.576	195.331	175.058	99.334	0.	0.	0.
5000	26.003	195.852	175.469	101.913	0.	0.	0.
5100	26.443	196.371	175.874	104.535	0.	0.	0.
5200	26.894	196.889	176.273	107.202	0.	0.	0.
5300	27.354	197.405	176.667	109.914	0.	0.	0.
5400	27.822	197.921	177.056	112.673	0.	0.	0.
5500	28.296	198.436	177.440	115.479	0.	0.	0.
5600	28.776	198.950	177.819	118.333	0.	0.	0.
5700	29.258	199.464	178.195	121.234	0.	0.	0.
5800	29.743	199.977	178.566	124.184	0.	0.	0.
5900	30.227	200.489	178.933	127.183	0.	0.	0.
6000	30.711	201.001	179.296	130.230	0.	0.	0.

Beryllium Oxide (BeO), Crystal-Liquid, mol. wt. = 25.01158
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−2.835	−604.914	−604.914	Infinite
100	2.636	0.824	28.539	−2.771	−606.343	−597.709	312.211
200	14.159	5.887	15.759	−1.974	−607.579	−588.573	153.719
298.15	25.560	13.770	13.770	0.	−608.354	−579.062	101.449
300	25.744	13.928	13.770	0.047	−608.364	−578.880	100.792
400	33.757	22.513	14.886	3.051	−608.688	−568.992	74.303
500	38.920	30.641	17.235	6.703	−608.668	−559.065	58.405
600	42.376	38.061	20.098	10.778	−608.440	−549.163	47.809
700	44.823	44.786	23.152	15.144	−608.092	−539.310	40.244
800	46.656	50.897	26.244	19.722	−607.680	−529.511	34.574
900	48.091	56.478	29.298	24.462	−607.235	−519.767	30.166
1000	49.262	61.607	32.276	29.331	−606.780	−510.073	26.643
1100	50.254	66.350	35.161	34.308	−606.329	−500.424	23.763
1200	51.116	70.760	37.946	39.377	−605.892	−490.815	21.365
1300	51.882	74.882	40.630	44.527	−605.478	−481.243	19.337
1400	52.580	78.753	43.216	49.751	−605.094	−471.701	17.599
1500	53.225	82.403	45.708	55.042	−604.744	−462.185	16.095
1600	53.827	85.857	48.111	60.394	−618.971	−452.166	14.762
1700	54.396	89.138	50.428	65.806	−618.303	−441.761	13.574
1800	54.944	92.262	52.666	71.273	−617.614	−431.396	12.519
1900	55.467	95.247	54.829	76.794	−616.904	−421.069	11.576
2000	55.974	98.105	56.922	82.366	−616.176	−410.781	10.729
2100	56.467	100.848	58.949	87.988	−615.430	−400.530	9.963
2200	56.948	103.486	60.914	93.659	−614.669	−390.314	9.267
2300	57.421	106.028	62.820	99.378	−613.893	−380.133	8.633
2373.001	57.756	107.827	64.177	103.582	Alpha–Beta transition
2373.001	57.758	110.649	64.177	110.276
2400	57.881	111.303	64.704	111.837	−606.409	−370.063	8.054
2500	58.338	113.675	66.616	117.648	−605.605	−360.232	7.527
2600	58.789	115.972	68.470	123.504	−604.789	−350.433	7.040
2700	59.233	118.199	70.271	129.406	−603.959	−340.665	6.591
2800	59.676	120.361	72.021	135.351	−894.074	−324.707	6.057
2821.220	59.770	120.812	72.386	136.618	Beta–liquid transition
2821.220	79.496	148.834	72.386	215.676
2900	79.496	151.024	74.493	221.939	−811.558	−306.635	5.523
3000	79.496	153.719	77.089	229.888	−807.695	−289.290	5.037
3100	79.496	156.325	79.603	237.838	−803.847	−272.073	4.584
3200	79.496	158.849	82.041	245.787	−800.016	−254.980	4.162
3300	79.496	161.295	84.405	253.737	−796.202	−238.007	3.767
3400	79.496	163.669	86.702	261.687	−792.408	−221.149	3.398
Table Continued

Beryllium Oxide (BeO), Crystal-Liquid, mol. wt. = 25.01158
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3500	79.496	165.973	88.934	269.636	−788.635	−204.402	3.051
3600	79.496	168.213	91.105	277.586	−784.884	−187.763	2.724
3700	79.496	170.391	93.219	285.535	−781.157	−171.228	2.417
3800	79.496	172.511	95.278	293.485	−777.455	−154.792	2.128
3900	79.496	174.576	97.285	301.435	−773.782	−138.454	1.854
4000	79.496	176.588	99.242	309.384	−770.138	−122.211	1.596
4100	79.496	178.551	101.153	317.334	−766.525	−106.057	1.351
4200	79.496	180.467	103.018	325.283	−762.946	−89.992	1.119
4300	79.496	182.337	104.841	333.233	−759.403	−74.011	0.899
4400	79.496	184.165	106.624	341.183	−755.897	−58.112	0.690
4500	79.496	185.952	108.367	349.132	−752.431	−42.293	0.491
4600	79.496	187.699	110.072	357.082	−749.007	−26.550	0.301
4700	79.496	189.408	111.742	365.031	−745.626	−10.881	0.121
4800	79.496	191.082	113.378	372.981	−742.290	4.717	−0.051
4900	79.496	192.721	114.980	380.931	−739.001	20.246	−0.216
5000	79.496	194.327	116.551	388.880	−735.761	35.708	−0.373

Beryllium Oxide (BeO), Ideal Gas, mol. wt. = 25.01158
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−8.688	133.984	133.984	Infinite
100	29.108	165.763	223.605	−5.784	135.397	127.536	−66.618
200	29.139	185.943	200.307	−2.873	136.275	119.270	−31.150
298.15	29.481	197.625	197.625	0.	136.398	110.873	−19.425
300	29.493	197.807	197.626	0.055	136.395	110.715	−19.277
400	30.348	206.400	198.791	3.043	136.056	102.198	−13.346
500	31.421	213.286	201.023	6.131	135.513	93.793	−9.799
600	32.454	219.108	203.564	9.326	134.860	85.509	−7.444
700	33.345	224.179	206.155	12.617	134.133	77.340	−5.771
800	34.084	228.682	208.694	15.990	133.340	69.280	−4.524
900	34.704	232.733	211.144	19.430	132.485	61.324	−3.559
1000	35.252	236.418	213.490	22.928	131.569	53.465	−2.793
1100	35.784	239.803	215.730	26.480	130.595	45.702	−2.170
1200	36.357	242.941	217.869	30.086	129.569	38.029	−1.655
1300	37.023	245.876	219.911	33.755	128.501	30.444	−1.223
1400	37.825	248.648	221.866	37.496	127.403	22.942	−0.856
1500	38.788	251.290	223.740	41.325	126.291	15.519	−0.540
1600	39.927	253.829	225.542	45.259	110.646	8.696	−0.284
1700	41.236	256.288	227.278	49.316	109.959	2.346	−0.072
1800	42.698	258.685	228.957	53.511	109.377	−3.967	0.115
1900	44.285	261.036	230.584	57.860	108.914	−10.250	0.282
2000	45.956	263.350	232.164	62.371	108.582	−16.513	0.431
2100	47.670	265.633	233.704	67.052	108.386	−22.762	0.566
2200	49.379	267.890	235.206	71.905	108.329	−29.005	0.689
2300	51.042	270.122	236.676	76.927	108.408	−35.249	0.801
2400	52.616	272.328	238.116	82.110	108.617	−41.499	0.903
2500	54.070	274.506	239.528	87.446	108.944	−47.761	0.998
2600	55.375	276.653	240.915	92.919	109.378	−54.037	1.086
2700	56.514	278.765	242.277	98.515	109.902	−60.332	1.167
2800	57.474	280.838	243.618	104.216	−180.457	−60.425	1.127
2900	58.255	282.869	244.936	110.004	−178.741	−56.168	1.012
3000	58.856	284.854	246.234	115.861	−176.970	−51.972	0.905
3100	59.286	286.792	247.511	121.770	−175.163	−47.834	0.806
3200	59.556	288.679	248.768	127.713	−173.338	−43.757	0.714
3300	59.681	290.514	250.006	133.676	−171.511	−39.735	0.629
3400	59.676	292.295	251.223	139.645	−169.698	−35.769	0.550
3500	59.553	294.024	252.422	145.608	−167.911	−31.856	0.475
3600	59.345	295.699	253.601	151.554	−166.164	−27.994	0.406
3700	59.051	297.321	254.760	157.474	−164.466	−24.180	0.341
Table Continued

Beryllium Oxide (BeO), Ideal Gas, mol. wt. = 25.01158
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3800	58.691	298.891	255.901	163.362	−162.827	−20.410	0.281
3900	58.279	300.410	257.023	169.210	−161.254	−16.682	0.223
4000	57.827	301.880	258.126	175.016	−159.754	−12.995	0.170
4100	57.347	303.302	259.211	180.775	−158.332	−9.344	0.119
4200	56.848	304.678	260.277	186.485	−156.993	−5.726	0.071
4300	56.337	306.010	261.325	192.144	−155.740	−2.139	0.026
4400	55.822	307.299	262.356	197.752	−154.576	1.419	−0.017
4500	55.308	308.548	263.368	203.309	−153.503	4.952	−0.057
4600	54.801	309.758	264.364	208.814	−152.523	8.462	−0.096
4700	54.303	310.931	265.342	214.269	−151.636	11.952	−0.133
4800	53.818	312.069	266.304	219.675	−150.844	15.424	−0.168
4900	53.348	313.174	267.249	225.033	−150.146	18.881	−0.201
5000	52.895	314.247	268.178	230.345	−149.544	22.324	−0.233
5100	52.460	315.291	269.092	235.613	−149.035	25.756	−0.264
5200	52.044	316.305	269.990	240.838	−148.621	29.179	−0.293
5300	51.647	317.293	270.873	246.022	−148.301	32.595	−0.321
5400	51.271	318.255	271.742	251.168	−148.073	36.006	−0.348
5500	50.914	319.192	272.596	256.277	−147.937	39.413	−0.374
5600	50.577	320.106	273.436	261.351	−147.892	42.819	−0.399
5700	50.259	320.999	274.263	266.393	−147.936	46.225	−0.424
5800	49.961	321.870	275.076	271.404	−148.069	49.633	−0.447
5900	49.681	322.722	275.877	276.386	−148.289	53.042	−0.470
6000	49.418	323.555	276.665	281.340	−148.596	56.458	−0.492

Carbon (C), Reference State −graphite, mol. wt. = 12.011
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−1.051	0.	0.	0.
100	1.674	0.952	10.867	−0.991	0.	0.	0.
200	5.006	3.082	6.407	−0.665	0.	0.	0.
250	6.816	4.394	5.871	−0.369	0.	0.	0.
298.15	8.517	5.740	5.740	0.	0.	0.	0.
300	8.581	5.793	5.741	0.016	0.	0.	0.
350	10.241	7.242	5.851	0.487	0.	0.	0.
400	11.817	8.713	6.117	1.039	0.	0.	0.
450	13.289	10.191	6.487	1.667	0.	0.	0.
500	14.623	11.662	6.932	2.365	0.	0.	0.
600	16.844	14.533	7.961	3.943	0.	0.	0.
700	18.537	17.263	9.097	5.716	0.	0.	0.
800	19.827	19.826	10.279	7.637	0.	0.	0.
900	20.824	22.221	11.475	9.672	0.	0.	0.
1000	21.610	24.457	12.662	11.795	0.	0.	0.
1100	22.244	26.548	13.831	13.989	0.	0.	0.
1200	22.766	28.506	14.973	16.240	0.	0.	0.
1300	23.204	30.346	16.085	18.539	0.	0.	0.
1400	23.578	32.080	17.167	20.879	0.	0.	0.
1500	23.904	33.718	18.216	23.253	0.	0.	0.
1600	24.191	35.270	19.234	25.658	0.	0.	0.
1700	24.448	36.744	20.221	28.090	0.	0.	0.
1800	24.681	38.149	21.178	30.547	0.	0.	0.
1900	24.895	39.489	22.107	33.026	0.	0.	0.
2000	25.094	40.771	23.008	35.525	0.	0.	0.
2100	25.278	42.000	23.883	38.044	0.	0.	0.
2200	25.453	43.180	24.734	40.581	0.	0.	0.
2300	25.618	44.315	25.561	43.134	0.	0.	0.
2400	25.775	45.408	26.365	45.704	0.	0.	0.
2500	25.926	46.464	27.148	48.289	0.	0.	0.
2600	26.071	47.483	27.911	50.889	0.	0.	0.
2700	26.212	48.470	28.654	53.503	0.	0.	0.
2800	26.348	49.426	29.379	56.131	0.	0.	0.
2900	26.481	50.353	30.086	58.773	0.	0.	0.
3000	26.611	51.253	30.777	61.427	0.	0.	0.
3100	26.738	52.127	31.451	64.095	0.	0.	0.
Table Continued

Carbon (C), Reference State −graphite, mol. wt. = 12.011
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3200	26.863	52.978	32.111	66.775	0.	0.	0.
3300	26.986	53.807	32.756	69.467	0.	0.	0.
3400	27.106	54.614	33.387	72.172	0.	0.	0.
3500	27.225	55.401	34.005	74.889	0.	0.	0.
3600	27.342	56.170	34.610	77.617	0.	0.	0.
3700	27.459	56.921	35.203	80.357	0.	0.	0.
3800	27.574	57.655	35.784	83.109	0.	0.	0.
3900	27.688	58.372	36.354	85.872	0.	0.	0.
4000	27.801	59.075	38.913	88.646	0.	0.	0.
4100	27.913	59.763	37.462	91.432	0.	0.	0.
4200	28.024	60.437	38.001	94.229	0.	0.	0.
4300	28.134	61.097	38.531	97.037	0.	0.	0.
4400	28.245	61.745	39.051	99.856	0.	0.	0.
4500	28.354	62.381	39.562	102.685	0.	0.	0.
4600	28.462	63.006	40.065	105.526	0.	0.	0.
4700	28.570	63.619	40.560	108.378	0.	0.	0.
4800	28.678	64.222	41.047	111.240	0.	0.	0.
4900	28.785	64.814	41.526	114.114	0.	0.	0.
5000	28.893	65.397	41.997	116.997	0.	0.	0.
5100	28.999	65.970	42.462	119.892	0.	0.	0.
5200	29.106	66.534	42.919	122.797	0.	0.	0.
5300	29.211	67.089	43.370	125.713	0.	0.	0.
5400	29.317	67.636	43.814	128.640	0.	0.	0.
5500	29.422	68.175	44.252	131.577	0.	0.	0.
5600	29.528	68.706	44.684	134.524	0.	0.	0.
5700	29.632	69.230	45.110	137.482	0.	0.	0.
5800	29.737	69.746	45.531	140.451	0.	0.	0.
5900	29.842	70.255	45.945	143.429	0.	0.	0.
6000	29.946	70.758	46.355	146.419	0.	0.	0.

Carbon (C), Ideal Gas, mol. wt. = 12.011
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−6.536	711.185	711.185	Infinite
100	21.271	135.180	176.684	−4.150	713.511	700.088	−365.689
200	20.904	149.768	160.007	−2.048	715.287	685.950	−179.152
250	20.861	154.427	158.443	−1.004	716.035	678.527	−141.770
298.15	20.838	158.100	158.100	0.	716.670	671.244	−117.599
300	20.838	158.228	158.100	0.039	716.693	670.962	−116.825
350	20.824	161.439	158.354	1.080	717.263	663.294	−98.991
400	20.815	164.219	158.917	2.121	717.752	655.550	−85.606
450	20.809	166.671	159.645	3.162	718.165	647.749	−75.189
500	20.804	168.863	160.459	4.202	718.507	639.906	−66.851
600	20.799	172.655	162.185	6.282	719.009	624.135	−54.336
700	20.795	175.861	163.916	8.362	719.315	608.296	−45.392
800	20.793	178.638	165.587	10.441	719.474	592.424	−38.681
900	20.792	181.087	167.175	12.520	719.519	576.539	−33.461
1000	20.791	183.278	168.678	14.600	719.475	560.654	−29.286
1100	20.791	185.259	170.097	16.679	719.360	544.777	−25.869
1200	20.793	187.068	171.437	18.758	719.188	528.913	−23.023
1300	20.796	188.733	172.704	20.837	718.968	513.066	−20.615
1400	20.803	190.274	173.905	22.917	718.709	497.237	−18.552
1500	20.814	191.710	175.044	24.998	718.415	481.427	−16.765
1600	20.829	193.053	176.128	27.080	718.092	465.639	−15.202
1700	20.850	194.317	177.162	29.164	717.744	449.871	−13.823
1800	20.878	195.509	178.148	31.250	717.373	434.124	−12.598
1900	20.912	196.639	179.092	33.340	716.984	418.399	−11.503
2000	20.952	197.713	179.996	35.433	716.577	402.694	−10.517
2100	20.999	198.736	180.864	37.530	716.156	387.010	−9.626
2200	21.052	199.714	181.699	39.633	715.722	371.347	−8.817
2300	21.110	200.651	182.503	41.741	715.277	355.703	−8.078
2400	21.174	201.551	183.278	43.855	714.821	340.079	−7.402
2500	21.241	202.417	184.026	45.976	714.357	324.474	−6.780
2600	21.313	203.251	184.750	48.103	713.884	308.888	−6.206
2700	21.387	204.057	185.450	50.238	713.405	293.321	−5.675
2800	21.464	204.836	186.129	52.381	712.920	277.771	−5.182
2900	21.542	205.591	186.787	54.531	712.429	262.239	−4.723
3000	21.621	206.322	187.426	56.689	711.932	246.723	−4.296
3100	21.701	207.032	188.047	58.856	711.431	231.224	−3.896
Table Continued

Carbon (C), Ideal Gas, mol. wt. = 12.011
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3200	21.780	207.723	188.651	61.030	710.925	215.742	−3.522
3300	21.859	208.394	189.239	63.212	710.414	200.275	−3.170
3400	21.936	209.048	189.812	65.401	709.899	184.824	−2.839
3500	22.012	209.685	190.371	67.599	709.380	169.389	−2.528
3600	22.087	210.306	190.916	69.804	708.857	153.968	−2.234
3700	22.159	210.912	191.448	72.016	708.329	138.561	−1.956
3800	22.230	211.504	191.968	74.235	707.797	123.169	−1.693
3900	22.298	212.082	192.477	76.462	707.260	107.791	−1.444
4000	22.363	212.648	192.974	78.695	706.719	92.427	−1.207
4100	22.426	213.201	193.461	80.934	706.173	77.077	−0.982
4200	22.487	213.742	193.937	83.180	705.621	61.740	−0.768
4300	22.544	214.272	194.404	85.432	705.065	46.416	−0.564
4400	22.600	214.791	194.861	87.689	704.503	31.105	−0.369
4500	22.652	215.299	195.310	89.951	703.936	15.807	−0.183
4600	22.702	215.797	195.750	92.219	703.363	0.521	−0.006
4700	22.750	216.286	196.182	94.492	702.784	−14.752	0.164
4800	22.795	216.766	196.605	96.769	702.199	−30.012	0.327
4900	22.838	217.236	197.022	99.051	701.607	−45.261	0.482
5000	22.878	217.698	197.431	101.337	701.009	−60.497	0.632
5100	22.917	218.151	197.832	103.626	700.404	−75.721	0.776
5200	22.953	218.597	198.227	105.920	699.793	−90.933	0.913
5300	22.987	219.034	198.616	108.217	699.174	−106.133	1.046
5400	23.020	219.464	196.998	110.517	698.548	−121.322	1.174
5500	23.051	219.887	199.374	112.821	697.914	−136.499	1.296
5600	23.080	220.302	199.744	115.127	697.273	−151.664	1.415
5700	23.107	220.711	200.108	117.437	696.625	−166.818	1.529
5800	23.133	221.113	200.467	119.749	695.968	−181.961	1.639
5900	23.157	221.509	200.820	122.063	695.304	−197.092	1.745
6000	23.181	221.898	201.168	124.380	694.631	−212.211	1.847

Methane (CH₄), Ideal Gas, mol. wt. = 16.04276
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−10.024	−66.911	−66.911	Infinite
100	33.258	149.500	216.485	−6.698	−69.644	−64.353	33.615
200	33.473	172.577	189.418	−3.368	−72.027	−58.161	15.190
250	34.216	180.113	186.829	−1.679	−73.426	−54.536	11.395
298.15	35.639	186.251	186.251	0.	− 74.873	−50.768	8.894
300	35.708	186.472	186.252	0.066	−74.929	−50.618	8.813
350	37.874	192.131	186.694	1.903	−76.461	−46.445	6.932
400	40.500	197.356	187.704	3.861	−77.969	−42.054	5.492
450	43.374	202.291	189.053	5.957	−79.422	−37.476	4.350
500	46.342	207.014	190.614	8.200	−80.802	−32.741	3.420
600	52.227	215.987	194.103	13.130	−83.308	−22.887	1.993
700	57.794	224.461	197.840	18.635	−85.452	−12.643	0.943
800	62.932	232.518	201.675	24.675	−87.238	−2.115	0.138
900	67.601	240.205	205.532	31.205	−88.692	8.616	−0.500
1000	71.795	247.549	209.370	38.179	−89.849	19.492	−1.018
1100	75.529	254.570	213.162	45.549	−90.750	30.472	−1.447
1200	78.833	261.287	216.895	53.270	−91.437	41.524	−1.807
1300	81.744	267.714	220.558	61.302	−91.945	52.626	−2.115
1400	84.305	273.868	224.148	69.608	−92.308	63.761	−2.379
1500	86.556	279.763	227.660	78.153	−92.553	74.918	−2.609
1600	88.537	285.413	231.095	86.910	−92.703	86.088	−2.810
1700	90.283	290.834	234.450	95.853	−92.780	97.265	−2.989
1800	91.824	296.039	237.728	104.960	−92.797	108.445	−3.147
1900	93.188	301.041	240.930	114.212	−92.770	119.624	−3.289
2000	94.399	305.853	244.057	123.592	−92.709	130.802	−3.416
2100	95.477	310.485	247.110	133.087	−92.624	141.975	−3.531
2200	96.439	314.949	250.093	142.684	−92.521	153.144	−3.636
2300	97.301	319.255	253.007	152.371	−92.409	164.308	−3.732
2400	98.075	323.413	255.854	162.141	−92.291	175.467	−3.819
2500	98.772	327.431	258.638	171.984	−92.174	186.622	−3.899
2600	99.401	331.317	261.359	181.893	−92.060	197.771	−3.973
2700	99.971	335.080	264.020	191.862	−91.954	208.916	−4.042
2800	100.489	338.725	266.623	201.885	−91.857	220.058	−4.105
2900	100.960	342.260	269.171	211.958	−91.773	231.196	−4.164
3000	101.389	345.690	271.664	222.076	−91.705	242.332	−4.219
3100	101.782	349.021	274.106	232.235	−91.653	253.465	−4.271
Table Continued

Methane (CH₄), Ideal Gas, mol. wt. = 16.04276
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3200	102.143	352.258	276.498	242.431	−91.621	264.598	−4.319
3300	102.474	355.406	278.842	252.662	−91.609	275.730	−4.364
3400	102.778	358.470	281.139	262.925	−91.619	286.861	−4.407
3500	103.060	361.453	283.391	273.217	−91.654	297.993	−4.447
3600	103.319	364.360	285.600	283.536	−91.713	309.127	−4.485
3700	103.560	367.194	287.767	293.881	−91.798	320.262	−4.521
3800	103.783	369.959	289.894	304.248	−91.911	331.401	−4.555
3900	103.990	372.658	291.982	314.637	−92.051	342.542	−4.588
4000	104.183	375.293	294.032	325.045	−92.222	353.687	−4.619
4100	104.363	377.868	296.045	335.473	−92.422	364.838	−4.648
4200	104.531	380.385	298.023	345.918	−92.652	375.993	−4.676
4300	104.688	382.846	299.967	356.379	−92.914	387.155	−4.703
4400	104.834	385.255	301.879	366.855	−93.208	398.322	−4.729
4500	104.972	387.612	303.758	377.345	−93.533	409.497	−4.753
4600	105.101	389.921	305.606	387.849	−93.891	420.679	−4.777
4700	105.223	392.182	307.424	398.365	−94.281	431.869	−4.800
4800	105.337	394.399	309.213	408.893	−94.702	443.069	−4.822
4900	105.445	396.572	310.973	419.432	−95.156	454.277	−4.843
5000	105.546	398.703	312.707	429.982	−95.641	465.495	−4.863
5100	105.642	400.794	314.414	440.541	−96.157	476.722	−4.883
5200	105.733	402.847	316.095	451.110	−96.703	487.961	−4.902
5300	105.818	404.861	317.750	461.688	−97.278	499.210	−4.920
5400	105.899	406.840	319.382	472.274	−97.882	510.470	−4.938
5500	105.976	408.784	320.990	482.867	−98.513	521.741	−4.955
5600	106.049	410.694	322.575	493.469	−99.170	533.025	−4.972
5700	106.118	412.572	324.137	504.077	−99.852	544.320	−4.988
5800	106.184	414.418	325.678	514.692	−100.557	555.628	−5.004
5900	106.247	416.234	327.197	525.314	−101.284	566.946	−5.019
6000	106.306	418.020	328.696	535.942	−102.032	578.279	−5.034

Carbon Monoxide (CO), Ideal Gas, mol. wt. = 28.0104
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−8.671	−113.805	−113.805	Infinite
100	29.104	165.850	223.539	−5.769	−112.415	−120.239	62.807
200	29.108	186.025	200.317	−2.858	−111.286	−128.526	33.568
298.15	29.142	197.653	197.653	0.	−110.527	−137.163	24.030
300	29.142	197.833	197.653	0.054	−110.516	−137.328	23.911
400	29.342	206.238	198.798	2.976	−110.102	−146.338	19.110
500	29.794	212.831	200.968	5.931	−110.003	−155.414	16.236
600	30.443	218.319	203.415	8.942	−110.150	−164.486	14.320
700	31.171	223.066	205.890	12.023	−110.469	−173.518	12.948
800	31.899	227.277	208.305	15.177	−110.905	−182.497	11.916
900	32.577	231.074	210.628	18.401	−111.418	−191.416	11.109
1000	33.183	234.538	212.848	21.690	−111.983	−200.275	10.461
1100	33.710	237.726	214.967	25.035	−112.586	−209.075	9.928
1200	34.175	240.679	216.988	28.430	−113.217	−217.819	9.481
1300	34.572	243.431	218.917	31.868	−113.870	−226.509	9.101
1400	34.920	246.006	220.761	35.343	−114.541	−235.149	8.774
1500	35.217	248.426	222.526	38.850	−115.229	−243.740	8.488
1600	35.480	250.707	224.216	42.385	−115.933	−252.284	8.236
1700	35.710	252.865	225.839	45.945	−116.651	−260.784	8.013
1800	35.911	254.912	227.398	49.526	−117.384	−269.242	7.813
1900	36.091	256.859	228.897	53.126	−118.133	−277.658	7.633
2000	36.250	258.714	230.342	56.744	−118.896	−286.034	7.470
2100	36.392	260.486	231.736	60.376	−119.675	−294.372	7.322
2200	36.518	262.182	233.081	64.021	−120.470	−302.672	7.186
2300	36.635	263.809	234.382	67.683	−121.278	−310.936	7.062
2400	36.321	265.359	235.641	71.324	−122.133	−319.164	6.946
2500	36.836	266.854	236.860	74.985	−122.994	−327.356	6.840
2600	36.924	268.300	238.041	78.673	−123.854	−335.514	6.741
2700	37.003	269.695	239.188	82.369	−124.731	−343.638	6.648
2800	37.083	271.042	240.302	86.074	−125.623	−351.729	6.562
2900	37.150	272.345	241.384	89.786	−126.532	−359.789	6.480
3000	37.217	273.605	242.437	93.504	−127.457	−367.816	6.404
3100	37.279	274.827	243.463	97.229	−128.397	−375.812	6.332
3200	37.338	276.011	244.461	100.960	−129.353	−383.778	6.265
3300	37.392	277.161	245.435	104.696	−130.325	−391.714	6.200
3400	37.443	278.278	246.385	108.438	−131.312	−399.620	6.139
3500	37.493	279.364	247.311	112.185	−132.313	−407.497	6.082
3600	37.543	280.421	248.216	115.937	−133.329	−415.345	6.027
Table Continued

Carbon Monoxide (CO), Ideal Gas, mol. wt. = 28.0104
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3700	37.589	281.450	249.101	119.693	−134.360	−423.165	5.974
3800	37.631	282.453	249.965	123.454	−135.405	−430.956	5.924
3900	37.673	283.431	250.811	127.219	−136.464	−438.720	5.876
4000	37.715	284.386	251.638	130.989	−137.537	−446.457	5.830
4100	37.756	285.317	252.449	134.762	−138.623	−454.166	5.786
4200	37.794	286.228	253.242	138.540	−139.723	−461.849	5.744
4300	37.832	287.117	254.020	142.321	−140.836	−469.506	5.703
4400	37.869	287.988	254.782	146.106	−141.963	−477.136	5.664
4500	37.903	288.839	255.529	149.895	−143.103	−484.741	5.627
4600	37.941	289.673	256.262	153.687	−144.257	−492.321	5.590
4700	37.974	290.489	256.982	157.483	−145.424	−499.875	5.555
4800	38.007	291.289	257.688	161.282	−146.605	−507.404	5.522
4900	38.041	292.073	258.382	165.084	−147.800	−514.908	5.489
5000	38.074	292.842	259.064	168.890	−149.009	−522.387	5.457
5100	38.104	293.596	259.733	172.699	−150.231	−529.843	5.427
5200	38.137	294.336	260.392	176.511	−151.469	−537.275	5.397
5300	38.171	295.063	261.039	180.326	−152.721	−544.681	5.368
5400	38.200	295.777	261.676	184.146	−153.987	−552.065	5.340
5500	38.074	296.476	262.302	187.957	−155.279	−559.426	5.313
5600	38.263	297.164	262.919	191.775	−156.585	−566.762	5.287
5700	38.296	297.842	263.525	195.603	−157.899	−574.075	5.261
5800	38.325	298.508	264.123	199.434	−159.230	−581.364	5.236
5900	38.355	299.163	264.711	203.268	−160.579	−588.631	5.211
6000	38.388	299.808	265.291	207.106	−161.945	−595.875	5.188

Carbon Dioxide (CO₂), Ideal Gas, mol. wt. = 44.0098
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−9.364	−393.151	−393.151	Infinite
100	29.208	179.009	243.568	−6.456	−393.208	−393.683	205.639
200	32.359	199.975	217.046	−3.414	−393.404	−394.085	102.924
298.15	37.129	213.795	213.795	0.	−393.522	−394.389	69.095
300	37.221	214.025	213.795	0.069	−393.523	−394.394	68.670
400	41.325	225.314	215.307	4.003	−393.583	−394.675	51.539
500	44.627	234.901	218.290	8.305	−393.666	−394.939	41.259
600	47.321	243.283	221.772	12.907	−393.803	−395.182	34.404
700	49.564	250.750	225.388	17.754	−393.983	−395.398	29.505
800	51.434	257.494	228.986	22.806	−394.168	−395.586	25.829
900	52.999	263.645	232.500	28.030	−394.405	−395.748	22.969
1000	54.308	269.299	235.901	33.397	−394.623	−395.886	20.679
1100	55.409	274.528	239.178	38.884	−394.838	−396.001	18.805
1200	56.342	279.390	242.329	44.473	−395.050	−396.098	17.242
1300	57.137	283.932	245.356	50.148	−395.257	−396.177	15.919
1400	57.802	288.191	248.265	55.896	−395.462	−396.240	14.784
1500	58.379	292.199	251.062	61.705	−395.668	−396.288	13.800
1600	58.886	295.983	253.753	67.569	−395.876	−396.323	12.939
1700	59.317	299.566	256.343	73.480	−396.090	−396.344	12.178
1800	59.701	302.968	258.840	79.431	−396.311	−396.353	11.502
1900	60.049	306.205	261.248	85.419	−396.542	−396.349	10.896
2000	60.350	309.293	263.574	91.439	−396.784	−396.333	10.351
2100	60.622	312.244	265.822	97.488	−397.039	−396.304	9.858
2200	60.865	315.070	267.996	103.562	−397.309	−396.262	9.408
2300	61.086	317.781	270.102	109.660	−397.596	−396.209	8.998
2400	61.287	320.385	272.144	115.779	−397.900	−396.142	8.622
2500	61.471	322.890	274.124	121.917	−398.222	−396.062	8.275
2600	61.647	325.305	276.046	128.073	−398.562	−395.969	7.955
2700	61.802	327.634	277.914	134.246	−398.921	−395.862	7.658
2800	61.952	329.885	279.730	140.433	−399.299	−395.742	7.383
2900	62.095	332.061	281.497	146.636	−399.695	−395.609	7.126
3000	62.229	334.169	283.218	152.852	−400.111	−395.461	6.886
3100	62.347	336.211	284.895	159.081	−400.545	−395.298	6.661
3200	62.462	338.192	286.529	165.321	−400.998	−395.122	6.450
3300	62.573	340.116	288.124	171.573	−401.470	−394.932	6.251
3400	62.681	341.986	289.681	177.836	−401.960	−394.726	6.064
3500	62.785	343.804	291.202	184.109	−402.467	−394.506	5.888
3600	62.884	345.574	292.687	190.393	−402.991	−394.271	5.721
Table Continued

Carbon Dioxide (CO₂), Ideal Gas, mol. wt. = 44.0098
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3700	62.980	347.299	294.140	196.686	−403.532	−394.022	5.563
3800	63.074	348.979	295.561	202.989	−404.089	−393.756	5.413
3900	63.166	350.619	296.952	209.301	−404.662	−393.477	5.270
4000	63.254	352.219	298.314	215.622	−405.251	−393.183	5.134
4100	63.341	353.782	299.648	221.951	−405.856	−392.874	5.005
4200	63.426	355.310	300.955	228.290	−406.475	−392.550	4.882
4300	63.509	356.803	302.236	234.637	−407.110	−392.210	4.764
4400	63.588	358.264	303.493	240.991	−407.760	−391.857	4.652
4500	63.667	359.694	304.726	247.354	−408.426	−391.488	4.544
4600	63.745	361.094	305.937	253.725	−409.106	−391.105	4.441
4700	63.823	362.466	307.125	260.103	−409.802	−390.706	4.342
4800	63.893	363.810	308.292	266.489	−410.514	−390.292	4.247
4900	63.968	365.126	309.438	272.882	−411.242	−389.892	4.156
5000	64.046	366.422	310.565	279.283	−411.986	−389.419	4.068
5100	64.128	367.691	311.673	285.691	−412.746	−388.959	3.984
5200	64.220	368.937	312.762	292.109	−413.522	−388.486	3.902
5300	64.312	370.161	313.833	298.535	−414.314	−387.996	3.824
5400	64.404	371.364	314.888	304.971	−415.123	−387.493	3.748
5500	64.496	372.547	315.925	311.416	−415.949	−386.974	3.675
5600	64.588	373.709	316.947	317.870	−416.794	−386.439	3.605
5700	64.680	374.853	317.953	324.334	−417.658	−385.890	3.536
5800	64.772	375.979	318.944	330.806	−418.541	−385.324	3.470
5900	64.865	377.087	319.920	337.288	−419.445	−384.745	3.406
6000	64.957	378.178	320.882	343.779	−420.372	−384.148	3.344

Acetylene (C₂H₂), Ideal Gas, mol. wt. = 26.03,788
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−10.012	235.755	235.755	Infinite
100	29.347	163.294	234.338	−7.104	232.546	236.552	−123.562
200	35.585	185.097	204.720	−3.925	229.685	241.663	−63.116
298.15	44.095	200.958	200.958	0.	226.731	248.163	−43.477
300	44.229	201.231	200.959	0.082	226.674	248.296	−43.232
400	50.480	214.856	202.774	4.833	223.568	255.969	−33.426
500	54.869	226.610	206.393	10.108	220.345	264.439	−27.626
600	58.287	236.924	210.640	15.771	216.993	273.571	−23.816
700	61.149	246.127	215.064	21.745	213.545	283.272	−21.138
800	63.760	254.466	219.476	27.992	210.046	293.471	−19.162
900	66.111	262.113	223.794	34.487	206.522	304.111	−17.650
1000	68.275	269.192	227.984	41.208	202.989	315.144	−16.461
1100	70.245	275.793	232.034	48.136	199.451	326.530	−15.506
1200	72.053	281.984	235.941	55.252	195.908	338.239	−14.723
1300	73.693	287.817	239.709	62.540	192.357	350.244	−14.073
1400	75.178	293.334	243.344	69.985	188.795	362.523	−13.526
1500	76.530	298.567	246.853	77.572	185.216	375.057	−13.061
1600	77.747	303.546	250.242	85.286	181.619	387.830	−12.661
1700	78.847	308.293	253.518	93.117	177.998	400.829	−12.316
1800	79.852	312.829	256.688	101.053	174.353	414.041	−12.015
1900	80.760	317.171	259.758	109.084	170.680	427.457	−11.752
2000	81.605	321.335	262.733	117.203	166.980	441.068	−11.520
2100	82.362	325.335	265.620	125.401	163.250	454.864	−11.314
2200	83.065	329.183	268.422	133.673	159.491	468.838	−11.132
2300	83.712	332.890	271.145	142.012	155.701	482.984	−10.969
2400	84.312	336.465	273.793	150.414	151.881	497.295	−10.823
2500	84.858	339.918	276.369	158.873	148.029	511.767	−10.693
2600	85.370	343.256	278.878	167.384	144.146	526.393	−10.575
2700	85.846	346.487	281.322	175.945	140.230	541.169	−10.470
2800	86.295	349.618	283 706	184.553	136.282	556.090	−10.374
2900	86.713	352.653	286 031	193.203	132.302	571.154	−10.288
3000	87.111	355.600	288.301	201.895	128.290	586.355	−10.209
3100	87.474	358.462	290.519	210.624	124.245	601.690	−10.138
3200	87.825	361.245	292.686	219.389	120.166	617.157	−10.074
3300	88.164	363.952	294.804	228.189	116.053	632.751	−10.016
3400	88.491	366.589	296.877	237.022	111.908	648.471	−9.963
3500	88.805	369.159	298.906	245.886	107.731	664.313	−9.914
Table Continued

Acetylene (C₂H₂), Ideal Gas, mol. wt. = 26.03,788
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3600	89.101	371.665	300.892	254.782	103.519	680.275	−9.871
3700	89.388	374.110	302.838	263.706	99.274	696.354	−9.831
3800	89.666	376.498	304.745	272.659	94.996	712.549	−9.795
3900	89.935	378.830	306.615	281.639	90.683	728.856	−9.762
4000	90.194	381.110	308.449	290.646	86.336	745.275	−9.732
4100	90.439	383.341	310.248	299.678	81.955	761.803	−9.705
4200	90.678	385.523	312.015	308.733	77.538	778.438	−9.681
4300	90.910	387.659	313.749	317.813	73.087	795.178	−9.660
4400	91.137	389.752	315.453	326.915	68.601	812.023	−9.640
4500	91.358	391.802	317.127	336.040	64.080	828.969	−9.622
4600	91.563	393.813	318.772	345.186	59.524	846.017	−9.607
4700	91.768	395.784	320.390	354.353	54.933	863.164	−9.593
4800	91.970	397.718	321.981	363.540	50.307	880.410	−9.581
4900	92.171	399.617	323.546	372.747	45.648	897.751	−9.570
5000	92.370	401.481	325.086	381.974	40.957	915.189	−9.561
5100	92.571	403.312	326.602	391.221	36.234	932.720	−9.553
5200	92.768	405.111	328.094	400.488	31.481	950.345	−9.546
5300	92.963	406.880	329.564	409.774	26.699	968.061	−9.541
5400	93.153	408.620	331.012	419.080	21.889	985.868	−9.536
5500	93.341	410.331	332.439	428.405	17.052	1003.763	−9.533
5600	93.525	412.014	333.845	437.748	12.189	1021.748	−9.530
5700	93.706	413.671	335.231	447.110	7.303	1039.819	−9.529
5800	93.883	415.302	336.597	456.489	2.393	1057.976	−9.528
5900	94.057	416.909	337.945	465.886	−2.537	1076.217	−9.528
6000	94.228	418.491	339.274	475.301	−7.488	1094.543	−9.529

Ethene (C₂H₄), Ideal Gas, mol. wt. = 28.05376
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−10.518	60.986	60.986	Infinite
100	33.270	180.542	252.466	−7.192	58.194	60.476	−31.589
200	35.359	203.955	222.975	−3.804	55.542	63.749	−16.649
250	38.645	212.172	220.011	−1.960	54.002	65.976	−13.785
298.15	42.886	219.330	219.330	0.	52.467	68.421	−11.987
300	43.063	219.596	219.331	0.079	52.408	68.521	−11.930
350	48.013	226.602	219.873	2.355	50.844	71.330	−10.645
400	53.048	233.343	221.138	4.882	49.354	74.360	−9.710
450	57.907	239.874	222.858	7.657	47.951	77.571	−9.004
500	62.477	246.215	224.879	10.668	46.641	80.933	−8.455
600	70.663	258.348	229.456	17.335	44.294	88.017	−7.663
700	77.714	269.783	234.408	24.763	42.300	95.467	−7.124
800	83.840	280.570	239.511	32.847	40.637	103.180	−6.737
900	89.200	290.761	244.644	41.505	39.277	111.082	−6.447
1000	93.899	300.408	249.742	50.665	38.183	119.122	−6.222
1100	98.018	309.555	254.768	60.266	37.318	127.259	−6.043
1200	101.626	318.242	259.698	70.252	36.645	135.467	−5.897
1300	104.784	326.504	264.522	80.576	36.129	143.724	−5.775
1400	107.550	334.372	269.233	91.196	35.742	152.016	−5.672
1500	109.974	341.877	273.827	102.074	35.456	160.331	−5.583
1600	112.103	349.044	278.306	113.181	35.249	168.663	−5.506
1700	113.976	355.898	282.670	124.486	35.104	177.007	−5.439
1800	115.628	362.460	286.922	135.968	35.005	185.357	−5.379
1900	117.089	368.752	291.064	147.606	34.938	193.712	−5.326
2000	118.386	374.791	295.101	159.381	34.894	202.070	−5.278
2100	119.540	380.596	299.035	171.278	34.864	210.429	−5.234
2200	120.569	386.181	302.870	183.284	34.839	218.790	−5.195
2300	121.491	391.561	306.610	195.388	34.814	227.152	−5.159
2400	122.319	396.750	310.258	207.580	34.783	235.515	−5.126
2500	123.064	401.758	313.818	219.849	34.743	243.880	−5.096
2600	123.738	406.596	317.294	232.190	34.688	252.246	−5.068
2700	124.347	411.280	320.689	244.595	34.616	260.615	−5.042
2800	124.901	415.812	324.006	257.058	34.524	268.987	−5.018
2900	125.404	420.204	327.248	269.573	34.409	277.363	−4.996
3000	125.864	424.463	330.418	282.137	34.269	285.743	−4.975
3100	126.284	428.597	333.518	294.745	34.102	294.128	−4.956
Table Continued

Ethene (C₂H₄), Ideal Gas, mol. wt. = 28.05376
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
3200	126.670	432.613	336.553	307.393	33.906	302.518	−4.938
3300	127.024	436.516	339.523	320.078	33.679	310.916	−4.921
3400	127.350	440.313	342.432	332.797	33.420	319.321	−4.906
3500	127.650	444.009	345.281	345.547	33.127	327.734	−4.891
3600	127.928	447.609	348.074	358.326	32.800	336.156	−4.877
3700	128.186	451.118	350.812	371.132	32.436	344.588	−4.865
3800	128.424	454.539	353.497	383.962	32.035	353.030	−4.853
3900	128.646	457.878	356.130	396.816	31.596	361.482	−4.842
4000	128.852	461.138	358.715	409.691	31.118	369.947	−4.831
4100	129.045	464.322	361.252	422.586	30.600	378.424	−4.821
4200	129.224	467.434	363.743	435.500	30.041	388.915	−4.812
4300	129.392	470.476	366.190	448.430	29.441	395.418	−4.803
4400	129.549	473.453	368.594	461.378	28.799	403.937	−4.795
4500	129.696	476.366	370.957	474.340	28.116	412.470	−4.788
4600	129.835	479.218	373.280	487.317	27.390	421.019	−4.781
4700	129.965	482.012	375.563	500.307	26.623	429.584	−4.774
4800	130.087	484.749	377.810	513.309	25.813	438.167	−4.768
4900	130.202	487.433	380.020	526.324	24.962	446.766	−4.763
5000	130.311	490.064	382.194	539.349	24.069	455.384	−4.757
5100	130.413	492.646	384.335	552.386	23.136	464.019	−4.753
5200	130.510	495.179	386.442	565.432	22.162	472.673	−4.748
5300	130.602	497.666	388.517	578.488	21.149	481.346	−4.744
5400	130.689	500.108	390.561	591.552	20.097	490.040	−4.740
5500	130.771	502.507	392.575	604.625	19.008	498.751	−4.737
5600	130.849	504.864	394.559	617.706	17.884	507.485	−4.734
5700	130.923	507.180	396.515	630.795	16.724	516.238	−4.731
5800	130.993	509.458	398.442	643.891	15.531	525.012	−4.728
5900	131.060	511.698	400.343	656.993	14.306	533.806	−4.726
6000	131.124	513.901	402.217	670.103	13.051	542.621	−4.724

Hydrogen, Monatomic (H), Ideal Gas, mol. wt. = 1.00794
Enthalpy Reference Temperature = T_r = 298.15 K				Standard State Pressure= p^o = 0.1 MPa
T (K)	C_p^o(J/K/mol)	S^o(J/K/mol)	−[G^o−H^o(T_r)]/T(J/mol/K)	H^o−H^o(T_r)(kJ/mol)	Δ_fH^o(kJ/mol)	Δ_fG^o(kJ/mol)	log K_f
0	0.	0.	Infinite	−6.197	216.035	216.035	Infinite
100	20.786	92.009	133.197	−4.119	216.614	212.450	−110.972
200	20.786	106.417	116.618	−2.040	217.346	208.004	−54.325
250	20.786	111.055	115.059	−1.001	217.687	205.629	−42.964
298.15	20.786	114.716	114.716	0.	217.999	203.278	−35.613
300	20.786	114.845	114.717	0.038	218.011	203.186	−35.378
350	20.786	118.049	114.970	1.078	218.326	200.690	−29.951
400	20.786	120.825	115.532	2.117	218.637	198.150	−25.876
450	20.786	123.273	116.259	3.156	218.946	195.570	−22.701
500	20.786	125.463	117.072	4.196	219.254	192.957	−20.158
600	20.786	129.253	118.796	6.274	219.868	187.640	−16.335
700	20.786	132.457	120.524	8.353	220.478	182.220	−13.597
800	20.788	135.232	122.193	10.431	221.080	176.713	−11.538
900	20.786	137.681	123.781	12.510	221.671	171.132	−9.932
1000	20.786	139.871	125.282	14.589	222.248	165.485	−8.644
1100	20.786	141.852	126.700	16.667	222.807	159.782	−7.587
1200	20.786	143.660	128.039	18.746	223.346	154.028	−6.705
1300	20.786	145.324	129.305	20.824	223.865	148.230	−5.956
1400	20.786	146.865	130.505	22.903	224.361	142.394	−5.313
1500	20.786	148.299	131.644	24.982	224.836	136.522	−4.754
1600	20.786	149.640	132.728	27.060	225.289	130.620	−4.264
1700	20.786	150.900	133.760	29.139	225.721	124.689	−3.831
1800	20.786	152.088	134.745	31.217	226.132	118.734	−3.446
1900	20.786	153.212	135.688	33.296	226.525	112.757	−3.100
2000	20.786	154.278	136.591	35.375	226.898	106.760	−2.788
2100	20.786	155.293	137.458	37.453	227.254	100.744	−2.506
2200	20.786	156.260	138.291	39.532	227.593	94.712	−2.249
2300	20.786	157.184	139.092	41.610	227.916	88.664	−2.014
2400	20.786	158.068	139.864	43.689	228.224	82.603	−1.798
2500	20.786	158.917	140.610	45.768	228.518	76.530	−1.599
2600	20.786	159.732	141.330	47.846	228.798	70.444	−1.415
2700	20.786	160.516	142.026	49.925	229.064	64.349	−1.245
2800	20.786	161.272	142.700	52.004	229.318	58.243	−1.087
2900	20.786	162.002	143.353	54.082	229.560	52.129	−0.939
3000	20.786	162.706	143.986	56.161	229.790	46.007	−0.801
3100	20.786	163.388	144.601	58.239	230.008	39.877	−0.672
3200	20.786	164.048	145.199	60.318	230.216	33.741	−0.551
Table Continued

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Combustion