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The unit is designed to simulate and study the processes of delayed coking occurring at elevated temperature and pressure in a stainless steel reactor made in the form of a flask with a spherical bottom and a removable lid. The installation allows you to obtain experimental data, select and optimize the parameters of the technological process, test various variants of raw mixtures, determine the material balance of the process, the characteristics of the process products. Ambient temperature from +10 to +35C; The relative humidity of the air is not more than 80% at a temperature of 25C;. The power supply is a single-phase AC network with a voltage of 230-240V 50-60 Hz. The average service life of the autoclave is 6 years. TECHNICAL CHARACTERISTICS Operating pressure range, MPa 0÷0.6 Reactor operating temperature range, 0C 50÷550 The discreteness of the temperature setting is 0C 1 Relative error of temperature maintenance, 0C ± 0.2 Reactor material steel 12x18N10T Power consumption, kW not more than 3 Overall dimensions (HxWxD) 1600x1100x495 Weight, kg 240 Continuous operation mode

Catalytic reforming is used to produce high-octane components of automobile gasoline, flavored concentrate for the production of individual aromatic hydrocarbons, as well as technical water. Isomerization of paraffin hydrocarbons is used to increase the octane number of C5 - C6 oil fractions by converting paraffins of normal structure into their isomers having a higher octane number.oroda. Hydrotreating of distillates is used to improve the quality and stability of light distillates, raw materials of catalytic cracking, as a result of the use of reactions of destructive hydrogenation of organosulfur compounds and hydrogenation of unsaturated hydrocarbons. Catalytic cracking is used to obtain additional amounts of light petroleum products, namely high-octane gasoline and diesel fuel, by decomposition of heavy oil fractions in the presence of a catalyst. Alkylation of isobutane with olefins is used to produce gasoline fractions with high stability and detonation resistance using the reaction of interaction of isobutane with olefins in the presence of a catalyst. Polymerization (oligomerization) of olefins is used to produce low molecular weight polymers (oligomers) of propylene and butylene used as motor fuel or raw materials for petrochemical synthesis. Hydrocracking is used to obtain an additional amount of light petroleum products by catalytic decomposition of heavy raw materials in the presence of hydrogen. Thermal cracking and Visbreaking is used to obtain in the mode of thermal cracking – additional amounts of light petroleum products by thermal decomposition of residues from oil distillation, in the mode of visbreaking – improving the quality of boiler fuel Coking is used to produce petroleum coke and an additional amount of light petroleum products from heavy residues. The raw materials are tar, thermal cracking residue, heavy gas oil. The products are, for example, petroleum coke.

The PCU-1 laboratory catalytic unit is designed to perform the following tasks: 1. Educational and scientific research of chemical processes; 2. Improvement of current industrial processes and development of new ones; 3. Studies of homogeneous and heterogeneous catalysts. The PCU-1 laboratory catalytic unit is manufactured in accordance with the technical requirements of customers so as to correspond to a wide range of technological parameters. Additionally, embedded equipment is designed to control the flow of raw materials and products, as well as data collection and processing. The unit can be subsequently modernized for new purposes. Main advantages: 1. A reliable and high-precision system of control and regulation of technological parameters; 2. Easy replacement of catalyst samples; 3. The possibility of conducting long-term tests in continuous mode; 4. The possibility of upgrading the unit for new purposes; 5. The possibility of conducting tests in flow and flow-circulation modes; 6. Control and accurate reproduction.