Hydroskimming

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Hydroskimming is one of the simplest types of refinery used in the petroleum industry [1] and still represents a large proportion of refining facilities, particularly in developing countries. [2] A hydroskimming refinery is defined as a refinery equipped with atmospheric distillation, naphtha reforming and necessary treating processes. [3] A hydroskimming refinery is therefore more complex than a topping refinery (which just separates the crude into its constituent petroleum products by distillation, known as atmospheric distillation, and produces naphtha but no gasoline) and it produces gasoline. The addition of catalytic reformer enables a hydroskimming refinery to generate higher octane reformate; benzene, toluene, and xylene; and hydrogen for hydrotreating units. [4] However, a hydroskimming refinery produces a surplus of fuel oil with a relatively unattractive price and demand. [3]

Most refineries, therefore, add vacuum distillation and catalytic cracking, which adds one more level of complexity by reducing fuel oil by conversion to light distillates and middle distillates. A coking refinery adds further complexity to the cracking refinery by high conversion of fuel oil into distillates and petroleum coke.

Catalytic cracking, coking and other such conversion units are referred to as secondary processing units. The Nelson Complexity Index, captures the proportion of the secondary conversion unit capacities relative to the primary distillation or topping capacity. The Nelson Complexity Index typically varies from about 2 for hydroskimming refineries, to about 5 for the Cracking refineries and over 9 for the Coking refineries. [5]

En español: El hidroskimming es uno de los tipos de refinería más simples utilizados en la industria petrolera y todavía representa una gran proporción de las instalaciones de refinación, particularmente en los países en desarrollo. Una refinería de hidrodesnatado se define como una refinería equipada con los procesos de destilación atmosférica, reformado de nafta y tratamiento necesarios. Por lo tanto, una refinería con hidrodesnatado es más compleja que una refinería de cobertura (que simplemente separa el crudo en sus productos petrolíferos constituyentes mediante destilación, conocida como destilación atmosférica, y produce nafta pero no gasolina) y produce gasolina. La adición de un reformador catalítico permite que una refinería con hidrodesnatado genere reformado de mayor octanaje; benceno, tolueno y xileno; e hidrógeno para unidades de hidrotratamiento. Sin embargo, una refinería de hidrodesnatado produce un excedente de fueloil con un precio y una demanda relativamente poco atractivos.

Por lo tanto, la mayoría de las refinerías añaden destilación al vacío y craqueo catalítico, lo que añade un nivel más de complejidad al reducir el fueloil mediante su conversión a destilados ligeros y destilados medios. Una refinería de coquización añade mayor complejidad a la refinería de craqueo debido a la alta conversión de fueloil en destilados y coque de petróleo.

El craqueo catalítico, la coquización y otras unidades de conversión similares se denominan unidades de procesamiento secundario. El Índice de Complejidad de Nelson captura la proporción de las capacidades de las unidades de conversión secundaria en relación con la destilación primaria o la capacidad de cobertura. El índice de complejidad de Nelson generalmente varía desde aproximadamente 2 para las refinerías de hidrodesnatado, hasta aproximadamente 5 para las refinerías de craqueo y más de 9 para las refinerías de coquización

Notes and references

  1. Info from HPI Consultants
  2. Masseron, Jean (1990). Petroleum Economics, 4th edition. Paris: Editions OPHRYS. p. 255. ISBN   2710805979.
  3. 1 2 Speight, James G. (2019). Heavy Oil Recovery and Upgrading. Cambridge, MA: Gulf Professional Publishing. p. 286. ISBN   9780128130254.
  4. Oyekan, Soni O. (2019). Catalytic Naphtha Reforming Process. Boca Raton, FL: CRC Press. pp. 2–21. ISBN   9781138034303.
  5. Info from Reliance Industries

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