Regarding the oil issue in the reformation unit header
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My company has just installed a set of reconditioning equipment. I would like to ask how the extraction oil from such equipment is handled? If stored separately, what type of storage tank would be used? What model of pump is used for the delivery loading pump, and what are its flow rate and head? What form is the loading crane position in?
The degreasing oil is stored in spherical tanks, and a regular centrifugal pump can be used for loading it.
The dry point of the Enneberg distillation of the oil taken out from the reprocessing unit should be controlled at 84 degrees Celsius, with a vapor pressure exceeding 100 KPa. In accordance with regulatory requirements, it should be stored separately in spherical pressure tanks; loading is carried out underwater, using loading facilities equipped with oil and gas recovery systems. The oil loading pump must be calculated based on the location of the platform and the distance involved in the transfer process.
The tapping oil from the reformation unit is also stored in low-pressure dome tanks (with nitrogen blanketing).
Reply to 1# fujq07: I use spherical tanks for storage, and naphtha is added to those with low pressure in order to increase the yield. The loading system is in gas phase connection with the spherical tank; otherwise, loading is difficult. The flexible hose is installed fixedly at the bottom and connected using pressure-resistant hoses. Problems still often arise during the loading process.