劣质原油脱钙技术在常减压装置的工业应用

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中国石油天然气股份有限公司乌鲁木齐石化分公司6 Mt/a常减压装置加工北疆原油时掺炼20%~30%高钙风城稠油,采用TS-888脱钙剂对该劣质原油进行脱钙工业试验。结果表明:(1)当剂钙比为(3.0~3.5)∶1时,原油脱钙率达到65%~68%;(2)当剂钙比提高到4∶1时,原油脱钙率超过70%,加注期间脱后原油含盐合格率为97.78%,脱后原油水分最大值0.030%,含盐污水化学需氧量最大值为1 927 mg/L,氨氮最大值为64.3 mg/L,加注脱钙剂后原油含盐含水和外排含盐污水指标合格,加注脱钙剂对电脱盐装置运行没有影响;(3)当剂钙比为(3.0~3.5)∶1时,减四线脱钙率达到59.00%,渣油脱钙率达到64.60%,加热炉温升由0.51℃/d下降到0.18℃/d,焦炭灰分由0.91%降至0.72%,减压渣油钙含量降低,焦化装置加热炉运行工况明显改善。 PetroChina Urumqi Petrochemical Company Urumqi Petrochemical Company 6 Mt / a Atmospheric and Vacuum Decompression Unit Processing North Xinjiang crude oil blending 20% ​​~ 30% high calcium Fengcheng heavy oil, the use of TS-888 decalcification of the inferior crude oil off Calcium industry test. The results showed that: (1) When the ratio of calcium to calcium was (3.0-3.5): 1, the decalcification rate of crude oil reached 65% -68%; (2) When the ratio of calcium to calcium was increased to 4:1, 70% of crude oil, 97.78% of crude oil after debonding and 0.030% of crude oil after debonding, the maximum value of chemical oxygen demand of salt water is 1 927 mg / L and the maximum value of ammonia nitrogen is 64.3 mg / L (3) When the ratio of calcium to calcium is (3.0-3.5): 1, the decalcifying agent can not affect the operation of the electric desalination unit. (3) The rate of four-line decalcification reached 59.00%, the decalcification rate of residue reached 64.60%, the temperature of furnace decreased from 0.51 ℃ / d to 0.18 ℃ / d, the coke ash content decreased from 0.91% to 0.72% Reduce the content, coking plant heating furnace operating conditions improved significantly.
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