Classifications

• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
  • C10M175/00—Working-up used lubricants to recover useful products ; Cleaning

Definitions

• the objective of the present invention is to provide a means and equipment for the processing of inadequate waste of goods, which increase the profit of the carbohydrates. 4
• a vacuum distillate is selected from the middle of the vacuum distillation cube column.
• the obtained cubical method is the boiler fuel with a quick heating of 40560 UJ / kg;
• ⁇ eshaemaya task us ⁇ an ⁇ v ⁇ e for ⁇ susches ⁇ vleniya s ⁇ s ⁇ ba ⁇ e ⁇ e ⁇ ab ⁇ i smeshanny ⁇ ne ⁇ yany ⁇ ⁇ d ⁇ v, v ⁇ lyuchayuschey node ⁇ bezv ⁇ zhivaniya is ⁇ dn ⁇ g ⁇ sy ⁇ ya Node dis ⁇ illyatsii, us ⁇ ys ⁇ v ⁇ for nag ⁇ eva sy ⁇ ya, ⁇ e ⁇ l ⁇ bmenni ⁇ , ⁇ ndensa ⁇ , se ⁇ a ⁇ a ⁇ y and ⁇ il ⁇ y, d ⁇ s ⁇ igae ⁇ sya ⁇ em, ch ⁇ ⁇ bezv ⁇ zhivaniya node s ⁇ vmescheniem ⁇ un ⁇ tsy ⁇ bess ⁇ livaniya and ⁇ chis ⁇ i is ⁇ dn ⁇ g ⁇ sy ⁇ ya vy ⁇ lnen in in the form
• the distillation unit provides vacuum distillation.
• Received on the installation of the target product in the form of a slurry is a bulk fuel and has a load of 40560 UJ / kg.
• the resulting liver oil has an ignition temperature of 40 ° C, and a light hydrocarbon fraction has a temperature of ⁇ 180 ° C.
• Two-stage preparation of raw materials, two-stage heating, circulation and recirculation of the heated mass of hydrocarbon have the advantage of reducing the consumption of heat. 7 niz ⁇ m ⁇ le ⁇ ulya ⁇ ny ⁇ ⁇ m ⁇ nen ⁇ v sy ⁇ ya, ch ⁇ in sv ⁇ yu ⁇ che ⁇ ed snizhae ⁇ ⁇ ud ⁇ em ⁇ s ⁇ and s ⁇ ve ⁇ s ⁇ venn ⁇ ene ⁇ g ⁇ za ⁇ a ⁇ y and ⁇ a ⁇ zhe znachi ⁇ eln ⁇ umenshae ⁇ ⁇ dy ⁇ e ⁇ e ⁇ ab ⁇ i and vyb ⁇ sy a ⁇ m ⁇ s ⁇ e ⁇ u in making this ⁇ e ⁇ n ⁇ l ⁇ giyu e ⁇ l ⁇ giches ⁇ i s ⁇ ve ⁇ shenn ⁇ bezv ⁇ edn ⁇ y.
• FIG. 1 shows the general scheme of the installation for the processing of mixed non-food products; on ⁇ ig. 2 - vertical dental furnace in the case of; on ⁇ ig. 3 - town, view of the sky; on ⁇ ig. 4 - town, view ⁇ ⁇ - ⁇ .
• Spaces 1 and 2 have spacious, rotating vibrating devices 15, which are stored in the upper part of the tanks.
• the plant is connected in the general technological scheme with lines 16 - 32.
• ⁇ ubcha ⁇ aya ⁇ ech ( ⁇ ig. 2) ⁇ as ⁇ l ⁇ zhennaya ve ⁇ i ⁇ aln ⁇ , s ⁇ de ⁇ zhi ⁇ zmeevi ⁇ i 33, 34, 35, and ⁇ b ⁇ azuyuschie ⁇ adian ⁇ nuyu ⁇ nventsi ⁇ nnuyu ⁇ ame ⁇ y and g ⁇ el ⁇ u 36 as ⁇ e ⁇ i ⁇ vann ⁇ y ⁇ las ⁇ iny ( ⁇ ig. 3) in ⁇ nus ⁇ b ⁇ aznymi ⁇ ve ⁇ s ⁇ iyami ⁇ e ⁇ echn ⁇ m section ( ⁇ ig. 4).
• Heating in the furnace 4 carries out the supply of 36 hot agents to the city, for example, a mixture of air and natural gas. By doing this, the cooking of the city and the inconvenience of the process will speed up the achievement of the required mode of operation.
• the raw material in the liquid is empty of line 22;
• the distillate is removed from the middle of the column with a vacuum distillation pipe at a temperature of 180 ° C to 360 ° C and a constant pressure of 50 mm rt.
• the physical and mechanical indicators of the cubic discharge are provided in the table.
• the total vacuum in the system is created by known components, for example, by type ⁇ -12. With this, capacities 12, 13, 14 turn off the vacuum system for unloading the target products through line 28, 29, 30 to the receiver, and not to the receiver.
• the mass of hydrocarbons is circulating throughout the system and through line 32 through tank 2 and line 20 under pressure, generated, for example, by the pump returning to the system.
• the dispensing control for lines 27 and 32 is carried out by any known means, such as valves.
• P ⁇ i is ⁇ lz ⁇ vanii iz ⁇ b ⁇ e ⁇ eniya d ⁇ s ⁇ igae ⁇ sya s ⁇ aschenie v ⁇ emeni ⁇ s ⁇ ya and demulsification siln ⁇ ⁇ bv ⁇ dnenny ⁇ smeshanny ⁇ ne ⁇ yany ⁇ ⁇ d ⁇ v, reduction ene ⁇ g ⁇ za ⁇ a ⁇ d ⁇ 1, 5 -.

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• 2002
  • 2002-08-26 WO PCT/AZ2002/000001 patent/WO2003029385A2/ru active Application Filing
  • 2002-08-26 AU AU2002325463A patent/AU2002325463A1/en not_active Abandoned
  • 2002-08-26 AT AT02757985T patent/ATE432333T1/de not_active IP Right Cessation
  • 2002-08-26 EP EP02757985A patent/EP1452576B1/de not_active Expired - Lifetime

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