METHOD OF HYDROCARBONS vapor recovery steam mixture from the storage and handling of oil products AND INSTALLATION FOR CARRYING OUT

摘要

1.method u0443u043bu0430u0432u043bu0438u0432u0430u043du0438u00a0 volatile hydrocarbons from mixtures u043eu0431u0440u0430u0437u0443u044eu0449u0438u0445u0441u00a0 u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du044bu0445 storage and transshipment of oil, comprising an u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture with following the absorption of hydrocarbon vapors are cooled with liquid u0430u0431u0441u043eu0440u0431u0435u043du0442u043eu043c and withdrawal of air from the process, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 orderwhat u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du0443u044e mixture and the liquid absorbent are in opposite u043du0430u043fu0440u0430u0432u043bu0435u043du0438u00a0u0445 - towards each other in a horizontal rotary u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du044bu0439 apparatusat the same time, the process in which u043fu0440u043eu0432u043eu0434u00a0u0442 hydrocarbon vapour absorption of u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture and its cooling in the consistent u043fu0440u043eu0442u0435u043au0430u043du0438u00a0 on u0449u0435u043bu0435u0432u044bu043c for u0437u043eu0440u0430u043c between the contact disk in contact with the surface of the film u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture liquid cooled absorbent continuously on the surface of the u043eu0431u0440u0430u0437u0443u044eu0449u0435u0439u0441u00a0 u0432u0440u0430u0449u0430u044eu0449u0438u0445u0441u00a0 contact disks u0430u0431u0441u043eu0440u0431u0435u0440u0430 andat the same time, the process of absorption, the purified air u0432u044bu0432u043eu0434u00a0u0442 directly into the atmosphere, and the saturated hydrocarbons in the process of absorption of absorbent u043du0430u043fu0440u0430u0432u043bu00a0u044eu0442 as a product in the tank and on to the consumer, with the absorbent using diesel fuel.;2. method for p.1, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 because diesel fuel that u043fu043eu0434u0430u0435u0442u0441u00a0 in u0430u0431u0441u043eu0440u0431u0435u0440 - horizontal rotary u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du044bu0439 apparatus at a temperature of from 3 to - 5c in proportion for the wsp range ratios: one m3 pvc comes from 7 to 25 litres of absorbent and process for the removal u043fu0440u043eu0432u043eu0434u00a0u0442 in u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture (v, m3 / h) the surface of the contact discs (s, m), the v / s = 0.3.the speed u0442u0435u0447u0435u043du0438u00a0 u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture and absorbent on the surface of contact are not more than 4 m / s, the time u043fu0440u0435u0431u044bu0432u0430u043du0438u00a0 u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixtures in contact the zone is not less than 1.8 - 2 and the speed u0432u0440u0430u0449u0435u043du0438u00a0 contact discs of 10 rpm to 100 rpm.;3. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the storage tank after u0446u0438u0440u043au0443u043bu00a0u0446u0438u043eu043du043du043eu0433u043e selection and return him absorbent - dt, a light u0444u0440u0430u043au0446u0438u00a0u043cu0438 petrol vapor lengua inglesa u00a0u00a0 u0434u043eu043fu0443u0441u0442u0438u043cu0430u00a0 u043au043eu043du0446u0435u043du0442u0440u0430u0446u0438u00a0 not u0434u043eu0432u043eu0434u0438u0442u0441u00a0 above 1%.;4. method for p.1, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, saturated hydrocarbon in the process of absorption of u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture absorbent comes in u0434u0435u0441u043eu0440u0431u0435u0440 - horizontal rotary u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431 u043cu0435u043du043du044bu0439 apparatus containing u043au0438u043fu00a0u0442u0438u043bu044cu043du0438u043a, u0434u0435u0444u043bu0435u0433u043cu0430u0442u043eu0440 and capacitor, where u043fu0440u043eu0432u043eu0434u00a0u0442 absorbent desorption process, simultaneously with u043fu0440u043eu0432u043eu0434u00a0u0442 process unnecessary m pressuredirectly in the horizontal disc u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du043eu043c apparatus in the treatment of u043fu0440u043eu0442u0438u0432u043eu0442u043eu043au0430 absorbent and vapour phase by heating the absorbent and u0438u0441u043fu0430u0440u0435u043du0438u00a0 from on u0440u0430u0437u043eu0432u0430u0432u0448u0435u0439u0441u00a0 on u0432u0440u0430u0449u0430u044eu0449u0438u0445u0441u00a0 contact disk film light fractions from the absorbent from the horizontal disk u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du043eu0433u043e apparatus, with u0435u043au0446u0438u00a0u0445 forming u043au0438u043fu00a0u0442u0438u043bu044cu043du0438u043a,and u043eu0445u043bu0430u0436u0434u0435u043du0438u00a0 u0444u043bu0435u0433u043cu044b simultaneously on the opposite side u0433u0434u0442u0430, with u043fu0430u0440u043eu043eu0431u0440u0430u0437u043du044bu0435 hydrocarbons u043au043eu043du0434u0435u043du0441u0438u0440u0443u044eu0442 on disks (which consistently u0434u0435u0444u043bu0435u0433 u043cu0430u0442u043eu0440 and capacitor), and the u0441u043au043eu043du0434u0435u043du0441u0438u0440u043eu0432u0430u043du043du044bu0435 liquid fractions of light hydrocarbons (gasoline) is partly returned to a horizontal rotary u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431u043cu0435u043d its apparatus u0438u0441u043fu043eu043bu044cu0437u0443u00a0 as u0444u043bu0435u0433u043cu044b u0434u043bu00a0 stabilization processpartially u0432u044bu0432u043eu0434u00a0u0442 of u0434u0435u0441u043eu0440u0431u0435u0440u0430 and returned to the line (a) of gasoline, and the purified absorbent of u0434u0435u0441u043eu0440u0431u0435u0440u0430 (section forming the u043au0438u043fu00a0u0442u0438u043bu044cu043du0438u043a) u043du0430u043fu0440u0430u0432u043bu00a0u044eu0442 ilb. u0430u0442u043du043e through accumulation capacity in the process of u0430u0431u0441u043eu0440u0431u0435u0440 u0434u043bu00a0 removals.;5.installation of u0443u043bu0430u0432u043bu0438u0432u0430u043du0438u00a0 volatile hydrocarbons from u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture u043eu0431u0440u0430u0437u0443u044eu0449u0435u0439u0441u00a0 storage and transshipment of oil, u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 u0430u0431u0441u043eu0440u0431u0435u0440, refrigeration machine , heat exchangers, pumps, piping and u043eu0442u0432u043eu0434u00a0u0449u0438u0435 u043fu043eu0434u0432u043eu0434u00a0u0449u0438u0435 absorbent u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixtures and pure air, vehicle automation, including the valve, venti lee, sensors, and the automatic u0443u043fu0440u0430u0432u043bu0435u043du0438u00a0 her work, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 orderwhat u0430u0431u0441u043eu0440u0431u0435u0440 designed as a horizontal disk u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du043eu0433u043e u0430u043fu043fu043fu0430u0440u0430u0442u0430, which is installed with inclination, and the possibility of its u0440u0435u0433u0443u043bu0438u0440u043eu0432u0430u043du0438u00a0 u043eu0442u043du043eu0441u0438u0442u0435u043b u044cu043du043e axis in the direction of withdrawal from the absorbent, in which capacity u0438u0441u043fu043eu043bu044cu0437u0443u0435u0442u0441u00a0 diesel fuel and the implemented module principle, namely u0430u0431u0441u043eu0440 ber pipeline supply and drainage u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixtureair and absorbent, located on them means of automation, water pump and heat exchangers form a loop u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture and absorption, which u0441u0432u00a0u0437u0430u043d s between an inner space u0430u0431u0441u043eu0440u0431u0435u0440u0430 and placed in a separate block box so that the u0430u0431u0441u043eu0440u0431u0435u0440 is situated in the upper part of the box on the pump and u0442u0435u043fu043bu043eu043eu0431u043c u0435u043du043du0438u043au0430u043cu0438 coolant removaland u0445u043eu043bu043eu0434u0438u043bu044cu043du0430u00a0 machine and the automatic installation u0443u043fu0440u0430u0432u043bu0435u043du0438u00a0 work outside the block box and connected, respectively, with the heat exchanger located on the pipeline of the absorbent, and the means of automation.;6. installation for p.5 u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, additionally equipped with circuit desorption, which is located in a separate block box and consists of u0434u0435u0441u043eu0440u0431u0435u0440u0430 carried out in the form of mountains u0438u0437u043eu043du0442u0430u043bu044cu043du043eu0433u043e disk u0442u0435u043fu043bu043eu043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du043eu0433u043e apparatus installed with inclination, and u0432u0437u043cu043eu0436u043du043eu0441u0442u044cu044e his u0440u0435u0433u0443u043bu0438u0440u043eu0432u0430u043du0438u00a0 from 1 to 10 on the side of not the pure absorbentand the connected pipeline of a drainage and pure absorbent, located on the pump and the heat exchangers, with u0435u043cu043au043eu0441u0442u00a0u043cu0438 u043du0430u043au043eu043fu043bu0435u043du0438u00a0 u043du0430u0441u044bu0449u0435u043du043d wow and pure absorbent, the relevant pipeline pipeline of pure and diversion of an absorbent absorption circuit the block box removalwith the u0434u0435u0441u043eu0440u0431u0435u0440 is installed in the upper part of the box above the u0435u043cu043au043eu0441u0442u00a0u043cu0438, of which the pure absorbent is located inside the tank an absorbent u043eu0431u0440u0430u0437u0443u00a0 single reservoir, and located on the connecting pipeline, and the elements of desorption, means connected to the u0443u043fu0440u0430u0432u043bu0435u043du0438u00a0 work automation the installation.;7. install the p.5 u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 being further provided with u043eu0433u043du0435u043fu0440u0435u0433u0440u0430u0434u0438u0442u0435u043bu00a0u043cu0438 set in the circuit u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture of absorption in the u0442u0440u0443u0431u043eu043f u0440u043eu0432u043eu0434u0430u0445 filing in u0430u0431u0441u043eu0440u0431u0435u0440 u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture and remove from the purified air.;8. the on clause 5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, u0430u0431u0441u043eu0440u0431u0435u0440u0430 u0440u0435u0433u0443u043bu0438u0440u0443u0435u0442u0441u00a0 slope in the range of 1 to 10.;9. the on clause 5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, u0430u0431u0441u043eu0440u0431u0435u0440 installed in the block box install it with the possibility of u043au0430u0447u0430u043du0438u00a0, with one flange u0430u0431u0441u043eu0440u0431u0435u0440u0430 u0437u0430u043au0440u0435u043fu043bu00a0u0435u0442u0441u00a0 with the possibility of turning about the axis u043au0440u0435u043fu043bu0435u043du0438u00a0 and another flange affixed to the drive, which is installed in the box and is connected with the u0443u043fu0440u0430u0432u043bu0435u043du0438u00a0 installation. the connecting piping u0430u0431u0441u043eu0440u0431u0435u0440u0430 are flexible.;10. installation for p.5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 being further provided with filter cyclone installed in circuit u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture block absorption so that the output u043eu0447u0438u0449u0435 x is connected to the entrance of the air from the u0430u0431u0441u043eu0440u0431u0435u0440u0430 filter cyclone and two exits, upper and lower, are connected, respectively, with the withdrawal of pure u0432u043eu0437u0434u0443 pipeline ha in the atmosphere and with the conduit line of the absorbent in the u0430u0431u0441u043eu0440u0431u0435u0440.;11. the on clause 5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 being further provided with series to the flowmeter, which is installed in the circuit u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture of absorption on the pipeline a u043fu0430u0440u043eu0432u043eu0437u0434u0443u0448u043du043eu0439 mixture in u0430u0431u0441u043eu0440u0431u0435u0440 and is connected with a u0443u043fu0440u0430u0432u043bu0435u043du0438u00a0 work settings, and through it with the transmission u0430u0431u0441u043eu0440u0431u0435u0440u0430 and pump on the pipeline of the u0430u0431u0441u043eu0440 bent in the u0430u0431u0441u043eu0440u0431u0435u0440 coolant absorption.;12. installation for u043fu043f.5 - 11, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 as block boxes are in the form of a spatially extensive construction, u0441u043eu0441u0442u043eu00a0u0449u0435u0439 of u043eu0441u043du043eu0432u0430u043du0438u00a0 contained therein u0432u0435u0440u0442u0438u043au0430u043b u044cu043du044bu043cu0438 uprights and horizontal u043fu043eu043fu0435u0440u0435u0447u0438u043du0430u043cu0438 provided with detachable u043fu0430u043du0435u043bu00a0u043cu0438 embodied in them.