R-101生产装置运行情况（2010.国产第三批催化剂.一期运行）日期1.291.301.312.12.22.32.4反应器负荷（kg/h）640640///6406401013温度147.7147.8138.4140.6140.6149.8149.51014温度146.1146.1140.3142.6143.2148.7148.41015温度143.2143.2139.7141.9142.2145.6145.21018温度139.5139.5138.4140.8140.8141.6141.5AAL产量（吨）FI-2520/19.2426.5631.1353.0758.5645.19气相O22.874.230.390.440.455.725.37CO215.1329.861.701.381.3832.7427.85C3H635.9740.198.892.320.6726.5337.96液相油相ACR0.020.050.14//0.270.10AAC5.2463.4369.20//19.5560.47AAL5.770.260.32//10.110.73HOAC35.7021.7320.78//31.5623.02HACR///////H2O53.1612.6011.55//37.9615.01水相AAC/AAL/HOAC/HACR/H2O/备注11:55投氧，负荷640kg/hLV-9610表有问题，造成T-211蒸汽波动,停车（23:00）20:16投氧开车R-101生产装置运行情况（国产催化剂）日期2.52.62.72.82.92.102.11反应器负荷（kg/h）6406406406407507507501013温度149.6149.8149.6149.9149.6151.4150.91014温度148.5148.8148.6148.9150.4150.9150.91015温度145.1145.5145.1145.4146.4146.9146.81018温度141.5141.9141.5141.5143.1143.1143.0AAL产量（吨）FI-252044.6148.4346.9457.7257.9862.8061.83气相O25.525.575.155.756.476.856.87CO222.1928.0529.9030.4429.4328.5027.76C3H636.7538.4236.8036.4541.1340.0838.60液相油相ACR0.240.160.110.130.190.170.18AAC48.6246.6344.3748.3753.6455.4655.16AAL1.690.991.231.620.482.162.39HOAC26.9327.1429.5728.4224.2124.7025.07HACR///////H2O21.6024.8324.3821.0519.9016.5916.47水相AAC11.4811.42AAL0.160.17HOAC30.4727.59HACR//H2O57.5860.57备注8:05提负荷至750.14:09降负荷至700，14:40恢复至750R-101生产装置运行情况（国产催化剂）日期2.122.132.142.152.162.172.18反应器负荷（kg/h）7507507507508608608601013温度151.5151.4151.5154.7153.9153.5153.41014温度150.9150.8150.9153.7155.5155.5155.41015温度146.9146.8146.7149.9151.4151.6151.41018温度143.0142.6142.8146.0148.0148.0148.1AAL产量（吨）FI-252067.0964.6366.5169.3877.9272.9973.54气相O26.696.736.836.916.446.446.47CO231.6829.7427.9828.9631.5428.3930.67C3H638.2138.3341.2638.2438.2939.4738.76液相油相ACR0.120.140.130.120.110.120.13AAC56.3658.9260.6557.9262.3862.5064.56AAL2.320.102.402.302.280.151.83HOAC21.7024.3922.0123.0721.7921.4019.98HACR///////H2O18.9514.4814.1616.0612.5314.1612.80水相AAC10.759.01AAL0.200.10HOAC26.8128.09HACR//H2O62.0562.63备注2:30左右T-211蒸汽波动，O2浓度急度上升，临时降负荷，1h后正常8:15开始提负荷，9:30至860kg/hR-101生产装置运行情况（国产催化剂）日期2.192.202.212.222.232.242.25反应器负荷（kg/h）8608608608609509509501013温度153.3153.6153.5157.5157.4157.6157.51014温度155.5155.4155.4159.6159.7159.7159.91015温度151.5151.3151.3155.9155.9155.9156.01018温度148.1148.2148.1151.7151.7151.7151.8AAL产量（吨）FI-252076.2377.7676.3176.7883.983.7381.01气相O26.566.876.736.086.046.076.04CO229.2128.4430.5929.1028.3228.7428.46C3H638.9938.4938.7439.0038.5338.1338.12液相油相ACR0.120.090.120.120.090.030.11AAC62.7655.8659.4364.8564.2764.1862.99AAL2.011.700.261.331.491.381.39HOAC21.5724.8223.4519.1721.4621.6421.67HACR///////H2O12.6017.0615.1714.0212.0912.0213.16水相AAC8.7911.25AAL0.120.16HOAC21.0127.94HACR//H2O69.8560.42备注8:23开始提负荷，8:53至970kg/hR-101生产装置运行情况（国产催化剂）日期2.262.272.283.13.23.33.4反应器负荷（kg/h）9509509509501050105010501013温度157.5157.6158.0160.8161.5161.5161.41014温度159.8159.9160.1162.7163.4163.3163.31015温度155.8156156.2159.1160.4160.4160.31018温度151.6151.8151.9154.1154.8155.0154.9AAL产量（吨）FI-252083.9982.3582.2183.4491.9292.2590.62气相O26.185...
