HDD Regenerator 2018 Incl Crack Serial Key Keygen
in our ecc, the c.sub.2.sup.+ alkanes are converted to a mixture of isobutane (ib) and isoamylenes (ia) in the presence of hydrogen at the relatively low temperature and low pressure typical of a fcc regenerator. in our preferred embodiment, the feedstream to the ecc contains a mixture of propane (c.3) and butane (c.4) which is typically in the range from about 50% propane to about 50% butane. the c.5.+ hydrocarbons which are also present in the feedstream are generally removed, and they are the principal fuel products of the ecc.
in the oligomerization reactor, now referred to as a fourth bed, heat is supplied from the first regenerator through the catalyst transfer line to fluid bed 62 of catalyst in the oligomerization reactor which is then heated to the desired temperature. the olefins and paraffins are oligomerized, or cracked, and the product separated by means of quench ring 30 to produce a gasoline stream in line 56. an alternate quench tank 58 may be provided. the gasoline stream is transferred to the fifth regenerator, which is maintained at a lower temperature than the first regenerator. the gasoline may be transferred from the fifth regenerator directly to the fcc in line 66, or may be transferred to a second quench tank 60 through line 62. the cracked products, including hydrogen, carbon monoxide, methane, and other gases, are separated in a second quench tank 62. the cracked products are combined with steam from the hydrogen plant (not shown) and passed through a shift conversion unit (not shown) in which the cracked products are reacted with steam to form more methane gas, and hydrogen, and to form carbon monoxide and water. the cracked products are then transferred to the carbon monoxide shift conversion unit and water shift conversion unit (not shown) where additional carbon monoxide is formed by reacting the cracked products with water to form carbon dioxide and hydrogen. the cracked products from the carbon monoxide and water shift conversion units are transferred to the hydrogen plant (not shown) to form more hydrogen. the cracked products from the hydrogen plant are transferred to the steam methane reformer (not shown) where the cracked products are reacted with steam to form additional hydrogen and methane. the cracked products are transferred to a quench tank to cool and separate them from other products of the steam methane reformer. the cracked products are transferred to a carbon dioxide removal unit (not shown) where carbon dioxide is removed from the cracked products. the cracked products are transferred to a carbon dioxide absorber (not shown) where carbon dioxide is absorbed from the cracked products. the cracked products are then transferred to a hydrogen product separation and purification unit (not shown) in which steam is used to form additional hydrogen from the cracked products. the cracked products are transferred to a hydrogen purification unit (not shown) in which additional hydrogen is purged from the cracked products. the cracked products are transferred to a paraffin product separation and purification unit (not shown) in which additional paraffins are purged from the cracked products. the cracked products are transferred to a propane product separation and purification unit (not shown) in which additional propane is purged from the cracked products. the cracked products are transferred to a butane product separation and purification unit (not shown) in which additional butanes are purged from the cracked products.
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