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METHOD AND SYSTEM FOR REMOVAL OF ORGANIC MATTER OF produced water oil fields

机译:去除采出水油田有机物的方法和系统

摘要

1. method u0443u0434u0430u043bu0435u043du0438u00a0 dissolved organic substances from the water catch a field, including;the introduction of catch a water received by the crude oil from the mixture of crude oil and salt water, in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c,;u0430u0434u0441u043eu0440u0431u0446u0438u044e and removal of dissolved organic matter from the water and catch a;u0434u0435u0441u043eu0440u0431u0446u0438u044e u0430u0434u0441u043eu0440u0431u0438u0440u043eu0432u0430u043du043du043eu0433u043e substances from u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 and regeneration u0430u0434u0441u043eu0440u0431u0435u043du0442u0430.;2. method for 1, in which the oil from the water to catch a u043eu0442u0434u0435u043bu00a0u044eu0442 u0432u0432u0435u0434u0435u043du0438u00a0 catch a water in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c.;3. method for 1, in which a magnetic u0441u0435u043fu0430u0440u0430u0446u0438u0435u0439 from catch a water u043eu0442u0434u0435u043bu00a0u044eu0442 u0441u043eu0434u0435u0440u0436u0430u0449u0438u0435u0441u00a0 it drops of oil.;4. method for 1, in which u0430u0434u0441u043eu0440u0431u0435u043du0442 used as particles, pellets, rods, fibers, plates, u0444u043eu0440u043cu043eu0432u0430u043du043du044bu0445 bodies or their combination.;5. method for 1, in which u0430u0434u0441u043eu0440u0431u0435u043du0442 u043du0430u0445u043eu0434u0438u0442u0441u00a0 in part of the water to catch a u0441u043eu0441u0442u043eu00a0u043du0438u0438, where it can be easily separated from the catch a water.;6. method for u0430u0434u0441u043eu0440u0431u0435u043du0442 p.5, which used in the form of powder, pellets, rods, or their combination, with an average diameter of 1 to 10 mm.;7. method for p.6, which as a u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 use inorganic u0430u0434u0441u043eu0440u0431u0435u043du0442, the main component of which u00a0u0432u043bu00a0u044eu0442u0441u00a0 SiO2 - Al2O3 or SiO2 - Al2O3 - Na2O.;8. way on p.7, in which inorganic u0430u0434u0441u043eu0440u0431u0435u043du0442 serves as the host of another metallic element.;9. method for 1, in which a u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 using activated charcoal.;10. method for 1, in which the use of at least two kinds of u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu0432 with different sizes.;11. way on p.10, which use two types of u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu0432: one with the size of the pores of about 7 angstroms or less, the other with the size about 7 angstroms or more.;12. method for 1, in which u0434u043bu00a0 desorption of organic matter and the regeneration of u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 last heated in oxidizing atmosphere.;13. method for 1, in which the organic matter, u0441u043eu0434u0435u0440u0436u0430u0449u0435u0435u0441u00a0 in u0434u0435u0441u043eu0440u0431u0438u0440u043eu0432u0430u043du043du043eu043c substance, decompose or burn through u043du0430u0433u0440u0435u0432u0430u043du0438u00a0 u0434u0435u0441u043eu0440u0431u0438u0440u043eu0432u0430u043du043du043eu0433u043e of u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 ve the business.;14. method for 1, in which u0434u043bu00a0 desorption in the layer u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 serves air.;15. method for 1, in which to catch a contact processing water u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c in u043fu043eu043fu0443u0442u043du0443u044e water u0434u043eu0431u0430u0432u043bu00a0u044eu0442 u043au043eu0430u0433u0443u043bu00a0u043du0442 u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 suspended substances.;16. method for 1, in which u043fu043eu043fu0443u0442u043du0443u044e water prior to its contact processing u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c is passed between the electrodes, which accompanied by the electric field, and decompose it u0435u043au0443u043bu044b dissolved organic compounds.;17. method for p.1, in which the need u043fu0440u043eu0432u0435u0434u0435u043du0438u00a0 processing drainage water u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 u0441u043eu0434u0435u0440u0436u0430u0449u0438u0445u0441u00a0 in organic compounds by u0432u0432u0435u0434u0435u043du0438u00a0 drainage water, u0441u043eu0434u0435u0440u0436u0430u0449u0435 in the organic compound and sodium, in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c system based on inorganic compoundsas well as the need to u043fu0440u043eu0434u043eu043bu0436u0435u043du0438u00a0 such processing u0441u0443u0434u00a0u0442 u043du0430u0442u0440u0438u00a0 concentration in drainage water before and after contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c system based on u043du0435u043eu0440u0433u0430u043du0438 as compounds.;18. way on p.7, which as a u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 use u0446u0435u043eu043bu0438u0442 proton type.;19. method for p.17, in which drain water processing, re u043fu0440u043eu0432u043eu0434u00a0 process of adsorption of organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c system based on inorganic compounds and the process of desorption u0430u0434u0441u043eu0440u0431u0438u0440u043eu0432u0430u043du043du043eu0433u043e organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 of u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 system based on inorganic compoundswith the u0438u0437u043cu0435u0440u00a0u044eu0442 u043du0430u0442u0440u0438u00a0 concentration in drainage water before and after the processing u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c system based on inorganic compounds, and both the measured display u0430u0442u0435u043bu00a0u043c u0441u0443u0434u00a0u0442 need u0432u0432u0435u0434u0435u043du0438u00a0 drainage of water in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c.;20. method u0443u0434u0430u043bu0435u043du0438u00a0 dissolved organic substances from the water catch a field, including;the u0440u0430u0437u0434u0435u043bu0435u043du0438u00a0 water and oil disposal of oil and u043du0435u0440u0430u0441u0442u0432u043eu0440u0435u043du043du044bu0445 particles floating in the water and catch a suspended therein.;the process of electrolysis of organic substances dissolved in the treated water of the process u0440u0430u0437u0434u0435u043bu0435u043du0438u00a0 oil and water;the u0443u0434u0430u043bu0435u043du0438u00a0 organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 u0441u0435u043fu0430u0440u0430u0446u0438u0435u0439 from water, held the second processing in the process of electrolysis,;the u0443u0434u0430u043bu0435u043du0438u00a0 organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 adsorption from water, held the third processing in the process of separation.;the u0441u0436u0438u0433u0430u043du0438u00a0 organic compounds from water in the processes of separation and adsorption, and release of products u0433u043eu0440u0435u043du0438u00a0 in atmosphere.;21. way on p.20, which in the process of adsorption using u0430u0434u0441u043eu0440u0431u0435u043du0442 system based on inorganic compounds, which after the adsorption is used again for mid units no desorption and regeneration in the atmosphere at a temperature of 380 to 600u0441.;22. installation of u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 dissolved organic substances from the water catch a field, u0441u043eu0434u0435u0440u0436u0430u0449u0430;a u043fu043eu043bu0443u0447u0435u043du0438u00a0 catch a water by u043eu0442u0434u0435u043bu0435u043du0438u00a0 crude oil from the mixture of oil and salt water.;a u0440u0430u0437u043cu0435u0449u0435u043du0438u00a0 u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 with adsorption ability to organic substance being dissolved in catch a water;a u0432u0432u0435u0434u0435u043du0438u00a0 catch a water in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c,;a regeneration u0430u0434u0441u043eu0440u0431u0435u043du0442u0430, which u0430u0434u0441u043eu0440u0431u0438u0440u0443u0435u0442u0441u00a0 u0440u0430u0441u0442u0432u043eu0440u0435u043du043du043eu0435 organic matter.;23. installing p.22, which means u0432u0432u0435u0434u0435u043du0438u00a0 catch a water in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c u043fu0440u0435u0434u0441u0442u0430u0432u043bu00a0u0435u0442 a few u0430u0434u0441u043eu0440u0431u0446u0438u043eu043du043du044bu0445 columns filled with u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c.;24. install the p.23, which u0430u0434u0441u043eu0440u0431u0446u0438u043eu043du043du044bu0435 columns are located in parallel on the cultivated catch a water flow.;25. installation for u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 p.22, different types of u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu0432 located sequentially or in parallel to the flow of the treated water catch a.;26. installing p.22, u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 microwave heating device heating u0434u043bu00a0 u0430u0434u0441u043eu0440u0431u0435u043du0442u0430.;27. installation for u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 p.22, a magnetic separation u0434u043bu00a0 u043eu0442u0434u0435u043bu0435u043du0438u00a0 crude oil from catch a salt water.;28. system, p.22, u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 means u043eu043fu0440u0435u0434u0435u043bu0435u043du0438u00a0 concentration of salt in the salt water and the means of installing the u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 dissolved organic matter through the signal from the means of u043eu043fu0440u0435u0434u0435u043bu0435u043du0438u00a0 concentrations of salt.;29.the system u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 dissolved organic substances from the water catch a field, u0432u043au043bu044eu0447u0430u044eu0449u0430u00a0 in u0441u0435u0431u00a0 u0434u043bu00a0 processing installation of drainage water, u043fu0440u0435u0434u043du0430u0437u043du0430u0447u0435 u043du043du0443u044e u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 dissolved in the drainage water of organic substances by u0432u0432u0435u0434u0435u043du0438u00a0 drainage water containing organic compound and sodium, in contact with and u0434u0441u043eu0440u0431u0435u043du0442u043eu043c system based on inorganic compoundscontaining device u0443u043fu0440u0430u0432u043bu0435u043du0438u00a0 for interruption of the drainage water to the u0430u0434u0441u043eu0440u0431u0435u043du0442u0443 system based on inorganic compounds on the basis of okay u0435u043du0438u0439 u043du0430u0442u0440u0438u00a0 concentrations in drainage water entered in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c system based on inorganic compounds, and in the drainage water, as from the specified the u0430u0434u0441u043eu0440u0431u0435u043du0442u0430.;30. system, p.29, u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 analyzer u0434u043bu00a0 u043eu043fu0440u0435u0434u0435u043bu0435u043du0438u00a0 u043du0430u0442u0440u0438u00a0 concentrations in drainage water by selecting part of the drainage water entered in contact with the u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c at the basis of inorganic compounds, and the u0434u043bu00a0 u043eu043fu0440u0435u0434u0435u043bu0435u043du0438u00a0 u043du0430u0442u0440u0438u00a0 concentrations in drainage water, as from the u0430u0434u0441u043eu0440u0431u0435u043du0442u0430.;31. installing p.30, which device contains a device u0434u043bu00a0 u0443u043fu0440u0430u0432u043bu0435u043du0438u00a0 data collection data collection analysis, u0438u0437u043cu0435u0440u00a0u0435u043cu044bu0445 u0434u0432u0443u043cu00a0 analyzers, and u0432u044bu0447u0438u0441u043bu0438u0442u0435u043bu044cu043du043eu0435 mouth u0440u043eu0439u0441u0442u0432u043e, which issues a signal for termination of drainage water to the u0430u0434u0441u043eu0440u0431u0435u043du0442u0443, based on the data accumulated in the data collection device.;32. the system u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 dissolved organic substances from the water catch a field, u0432u043au043bu044eu0447u0430u044eu0449u0430u00a0 in seb;u0434u043bu00a0 u0440u0430u0437u0434u0435u043bu0435u043du0438u00a0 reservoir oil and water, which is removed from the oil and drain water u043du0435u0440u0430u0441u0442u0432u043eu0440u0435u043du043du044bu0445 particles floating in the drainage water or suspended in her;means of electrolysis, which is the decomposition of organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0, u0441u043eu0434u0435u0440u0436u0430u0449u0435u0433u043eu0441u00a0 in drainage water held in the tank u0434u043bu00a0 u0440u0430u0437u0434u0435u043bu0435u043du0438u00a0 oil and water;the tank u0434u043bu00a0 separation u0443u0434u0430u043bu0435u043du0438u00a0 organic substance, which is the removal of water and organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 held the second turn in the formulation of an electrolysis.;the tank u0434u043bu00a0 u0430u0434u0441u043eu0440u0431u0446u0438u043eu043du043du043eu0433u043e u0443u0434u0430u043bu0435u043du0438u00a0 organic substance, which is u0430u0434u0441u043eu0440u0431u0446u0438u00a0 organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 u0430u0434u0441u043eu0440u0431u0435u043du0442u043eu043c system based on u043du0435u043eu0440u0433u0430u043du0438u0447u0435 removal of organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0) compounds from water, held the third treatment tank u0434u043bu00a0 separation u0443u0434u0430u043bu0435u043du0438u00a0 organic substances;the camera u0441u0433u043eu0440u0430u043du0438u00a0, in which there is a mixture of organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 emitted from the water in the tank u0434u043bu00a0 separation u0443u0434u0430u043bu0435u043du0438u00a0 organic substances, and organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 emitted from the water in the tank u0434u043bu00a0 u0430u0434u0441u043eu0440u0431u0446u0438u043eu043du043du043eu0433u043e u0443u0434u0430u043bu0435u043du0438u00a0 organic substance, the obtained mixture and the release of products of combustion u0435u043du0438u00a0 in atmosphere.;33. system for the p.32, in which, after the adsorption and u0443u0434u0430u043bu0435u043du0438u00a0 organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 u0430u0434u0441u043eu0440u0431u0435u043du0442 system based on inorganic compounds are heated at a temperature of 380 to 600u0441 in the atmosphere for its regeneration and repeated use.;34. system in which u0434u043bu00a0 u0440u0430u0437u0434u0435u043bu0435u043du0438u00a0 p.32, reservoir water and oil also functions as the magnetic separator and u044du043bu0435u043au0442u0440u043eu043bu0438u0437u0435u0440u0430.;35. system for the p.32, which u0430u0434u0441u043eu0440u0431u0435u043du0442 system based on inorganic compounds contains u043au0440u0435u043cu043du0438u00a0 dioxide and oxide in the u043cu043eu043bu00a0u0440u043du043eu043c u0430u043bu044eu043cu0438u043du0438u00a0 against SiO2 to Al2O3, u0441u043eu0441u0442u0430u0432u043bu00a0 u044eu0449u0435u043c 5 or more, and the microporous material u0430u0434u0441u043eu0440u0431u0435u043du0442u0430 have a nervous tunic of eyeball structure.;36. system for the p.32, in which the reservoir u0434u043bu00a0 separation u0443u0434u0430u043bu0435u043du0438u00a0 organic matter has the possibility of wide water, held the second processing, u0434u043bu00a0 uda u043bu0435u043du0438u00a0 volatile organic u0441u043eu0435u0434u0438u043du0435u043du0438u00a0.
机译:1.从水中捕捞田中溶解的有机物的方法包括:从原油和盐的混合物中捕集由原油接收的水与 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c接触;; u0430 u0434 u0441 u043e u0440 u0431 u0431 u0446 u0438 u044e从水中溶解的有机物并捕获; u0434 u0435 u0441 u043e u0440 u0431 u0446 u0438 u044e u0430 u0434 u0441 u043e u0440 u0431 u0438 u04438 u0440 u043e u0432 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430中的u0430 u043d u043d u043e u0433 u043e物质和再生 u0430 u0434 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430。; 2。 1的方​​法,其中从水中捕获 u043e u0442 u0434 u0435 u043b u00a0 u044e u0442 u0432 u0432 u0435 u0434 u0434 u0435 u043d u0438 u00a0与 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c .; 3。 1的方​​法,其中磁性 u0441 u0435 u043f u0430 u0440 u0430 u0446 u0438 u0435 u0439从水中取水 u043e u0442 u0434 u0435 u043b u00a0 u044e u0442 u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0438 u0435 u0441 u00a0滴油; 4。 1的方​​法,其中 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442用作粒子,粒料,棒,纤维,板, u0444 u043e u0440 u043c u043e u0432 u0430 u043d u043d u044b u0445实体或它们的组合; 5。 1的方​​法,其中 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u043d u0442 u043d u0430 u0445 u043e u0434 u0438 u0442 u0441 u0040 u0441 u043e u0441 u0442 u043e u00a0 u043d u0438 u0438,可以很容易地将其与下水道分离。6。第5页的方法,以粉末,小丸,棒或它们的组合形式使用,平均直径为1到10毫米。 ; 7。第6页的方法,作为 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u044d u0442 u0430使用无机 u0430 u0434 u0441 u043e u0440 u0431 u0431 u0435 u043d u0442其中的主要成分是SiO2-Al2O3或SiO2-Al2O3-Na2O。; 8。第7页的方法,其中无机 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442充当另一种金属元素的主体。; 9。 1的方​​法,其中使用活性炭 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430; 10。 1的方​​法,其中至少使用两种大小不同的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u0432。第10页的方法,它使用两种类型的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u0432:一种孔的大小约为7埃或更小具有约7埃或更大的尺寸;; 12。 1的方​​法,其中最后一次在氧化气氛中加热 u0434 u043b u00a0有机物的解吸和 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430的再生; 13。 1的方​​法,其中 u0434 u0435 u0441 u0431 u043e u0440 u0431 u0438 u0440 u043e u0432 u0430 u043d u043d u043e u043c物质,分解或燃烧通过 u043d u0430 u0433 u0440 u0435 u0432 u0430 u043d u0438 u00a0 u0434 u0435 u0441 u043e ; u1440 u0431 u0438 u0440 u043e u0432 u0430 u043d u043d u0434 u0431 u0431 u043e u04340 u0431 u0431 u0435 u043d u043d u0442 u0430 ve ve business。; 14 。 1的方​​法,其中 u0430 u0434 u0441 u043e u04e u0440 u0431 u0435 u043d u0442 u0430层中的解吸为空气服务; 15。 1的方​​法,其中在 u043f u043e u043f u0443 u0442 u0442 u043d u043e u043c u0434 u0441 u043d u0442 u043e u043c u044e水 u0434 u043e u0431 u0430 u0432 u043b u00a0 u044e u0442 u043a u043e u0430 u0433 u0443 u043b u00a0 u043d u0442 u0434 u043b u00a0 u0443 u043b u0435 u043d u0438 u00a0悬浮物; 16。 1的方​​法,其中 u043f u043e u043f u0443 u0442 u043d u0443 u044e接触处理之前的水 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0432 u043e u043c在电极之间通过电场作用,并使其分解,使溶解的有机化合物分解。17。第1页的方法,其中需要 u043f u0440 u043e u0432 u0435 u0434 u0435 u043d u0438 u00a0处理排水 u0434 u043b u00a0 u0443 u0434 u0434 u0430 u043b u0435 u043d u0438 u00a0 u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0438 u0445 u0441 u00a0通过有机溶剂 u0432 u0432 u0435 u0435 u0434 u0435 u043d u0438 u00水,有机化合物和钠中的 u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0435,与基于无机化合物的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0432 u043e u043c系统以及需要 u043f u0440 u043e u043e u0434 u043e u043b u0436 u0435 u043d u0438 u00a0这样的处理 u0441 u0443 u0434 u00a0 u0442 u043d u0430 u0442 u0440 u0438 u00a0与 u0430 u0434 u0441接触前后的废水中浓度基于化合物的u043e u0440 u0431 u0435 u043d u0442 u043e u043c系统; 18。第7页上的方式,作为 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u043d u0442 u0430使用 u0446 u0435 u043e u043e u043b u0438 u0442质子类型。; 19。 p.17的方法,其中处理废水,重新吸附有机物的过程 u0431 u043e u043e u0435 u0434 u0434 u0438 u043d u0435 u043d u043d u00a0 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c基于无机化合物的系统和解吸过程 u0430 u0434 u0441 u0431 u043e u0440 u0431 u0438 u0440 u043e u0432 u0430 u043d u043d u043e u0433 u043e有机 u0441 u043e u0435 u0434 u0438 u043d u043d u0435 u043d u0438 u00a0 u0430 u0434 u0434 u0431 u043e u0440 u0435 u043d u0442 u0430系统基于无机化合物,且排水前后的浓度分别为 u0438 u0437 u043c u0435 u0440 u00a0 u044e u044e u0442 u043d u0430 u0442 u0440 u0438 u00a0处理基于无机化合物的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c系统,并且实测显示 u0430 u0442 u0435 u043b u00a0 u043c u0441 u0443 u0434 u00a0 u0442需要 u0432 u0432 u0435 u0434 u0435 u043d u0438 u00 a0与 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c接触的排水。方法 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0溶解了水中的有机物质,其中包括 u0440 u0430 u0437 u0434 u0435 u043b u0435 u043d u043d u0438 u00a0水和油的处置,以及水中漂浮的颗粒并捕获其中的悬浮物。该过程的过程如下:。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。。电解溶解在处理过的水中的有机物质 u0440 u0430 u0437 u0434 u0435 u043b u0435 u043d u0438 u00a0油和水; u0443 u0434 u0430 u043b u043b u0435 u043d u0438 u00a0有机 u0441 u043e u0435 u0434 u0438 u043d u0435 u043d u043d u04d u0438 u00a0 u0441 u0435 u043f u04f u0430 u0440 u0430 u0446 u0438 u0435 u0439从水中保持第二在电解过程中进行处理; u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0有机物 u0441 u043e u0435 u0434 u0434 u0438 u043d u0435 u0435 u043d u043d u0438 u00a0在分离过程中进行了第三次处理。在大气中从水中分离和吸附并释放产物 u0433 u043e u0440 u0435 u043d u0438 u00a0的过程中, u0441 u0436 u0438 u0433 u0430 u043d u0438 u00a0 ; 21。第20页的方法,在吸附过程中使用基于无机化合物的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442系统,该吸附后再次用于中型单元,无解吸和在温度为380至600的大气中再生; 22。从水中捕获 u0434 u043b u00a0 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0溶解的有机物质的安装区域 u0441 u043e u0434 u0435 u0435 u0440 u0436 u0430 u0449 u0430; a u043f u043e u043b u0443 u0447 u0435 u043d u0438 u00a0从 u043e u0442 u0434 u0435 u043b u0435 u043d u043d u0438 u00a0的原油中取水油和盐水。;具有吸附能力的 u0440 u0430 u0437 u043c u0435 u0449 u0435 u043d u043d u0431 u04e u0440 u0431 u0431 u0435 u0431 u043e u04e溶解于水中的有机物质; u0432 u0432 u0435 u0434 u0435 u043d u0438 u00a0与 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d接触 u0442 u043e u043c ;;再生 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430,其中 u0430 u0434 u0441 u043e u043e u0440 u0431 u0438 u0440 u0443 u0435 u0442 u0441 u00a0 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0435 u043d u043d u043e u0435有机物。; 23。安装第22页,这意味着 u0432 u0432 u0435 u0434 u0435 u043d u0438 u00a0与 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u043d u0442 u043e u043c u043f u0440 u0435 u0434 u0441 u0442 u0430 u0432 u043b u00a0 u0435 u0442一些 u0430 u0434 u0441 u043e u0440 u0431 u0446 u0438 u043e u043d u044b u0445列填充为 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c。; 24。安装第23页,其中 u0430 u0434 u0441 u043e u0440 u0431 u0446 u0438 u043e u043d u043d u044b u0435列平行放置在耕作的水流上; 25。安装 u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0430 u00a0第22页,不同类型的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u0432顺序或平行于处理后的水流a.26放置。安装第22页, u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0430 u00a0微波加热设备加热 u0434 u043b u00a0 u0430 u0434 u0441 u043e u04e u0440 u0431 u0435 u043d u0442 u0430。; 27。 u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0430 u00a0 p.22的安装,磁隔离 u0434 u043b u00a0 u043e u0442 u0434 u0434 u0435 u043b u0435 u043d 28.从盐水中捕获原油。系统,第22页, u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0430 u00a0表示 u043e u043f u0440 u0435 u0434 u0435 u043b u043b u0435 u043d u0438 u00a0浓度盐水中的盐分以及通过 u043e u043f u0440发出的信号安装 u0434 u043b u00a0 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0溶解有机物的方法 u0435 u0434 u0435 u043b u0435 u043d u0438 u00a0浓度的盐; 29。系统 u0434 u043b u00a0 u0443 u0434 u0430 u043b u043b u0435 u043d u043d u0438 u00a0从水域取水, u0431 u0435 u0431 u0030 u0430 u0435 u0435 u0431 u00a0中的 u0432 u043a u043b u04e u0430 u00a0 u0440 u0435 u0434 u043d u0430 u0437 u043d u0430 u0447 u0435 u043d u043d u0443 u044e u0434 u043b u00a0 u0443 u0434 u0430 u043b u0435 u043d u0d通过 u0432 u0432 u0435 u0434 u0435 u043d u0438 u00a0 d将有机物溶解在排水中包含有机化合物和钠的雨水,与基于设备的无机化合物的 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c系统接触,并与该系统接触。 u0443 u043f u0440 u0440 u0430 u0432 u043b u0435 u043d u0438 u00a0,以便在基于okay u0435 u043d的基础上中断基于无机化合物的 u0430 u0434 u0441 u043e u04e u0440 u0431 u0435 u043d u044d u0442 u0443 u0438 u0439 u043d u0430 u0442 u0440 u0438 u00a0输入的污水浓度与基于系统的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0432 u043e u043c无机化合物,以及在排水中,按照指定的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430。; 30。系统,第29页, u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0430 u00a0分析仪 u0434 u043b u00a0 u043e u043f u0440 u0435 u0435 u0434 u0435 u043b u0435 u043d u0438 u00a0 u043d u0430 u0442 u0440 u0438 u00a0的浓度,方法是选择与 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u043e u043c(基于无机化合物)和 u0434 u043b u00a0 u043e u043f u0440 u0435 u0434 u0435 u043b u0435 u043d u0438 u00a0 u043d u0430 u0442 u04a 31。从 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430开始计算。31。安装第30页,该设备包含一个设备 u0434 u043b u00a0 u0443 u043f u0440 u0430 u0432 u043b u0435 u043d u043d u0438 u00a0数据收集数据收集分析, u0438 u0437 u043c u0435 u0440 u00a0 u0435 u043c u044b u0445 u0434 u0432 u0443 u043c u00a0分析仪和 u0432 u044b u0447 u0438 u0441 u043b u0438 u0442 u0435 u043b u044c u043e u0435口 u0440 u043e u0439 u0441 u0442 u0432 u043e,发出终止排水信号到 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u043d u0442 u0443 ;根据数据收集设备中累积的数据; 32。系统 u0434 u043b u00a0 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0从水中溶解的有机物质会捕获一个字段, u0432 u043a u043b u044e u044e u0447 u0430 u044e u0449 u0430 u00a0 in seb; u0434 u043b u00a0 u0440 u0430 u0437 u0434 u0435 u043b u0435 u043d u0438 u00a0从油和排水中取出的油和水 u043d u0435 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0435 u043d u043d u043d u044b u0445 u04b u0445漂浮在排水中或悬浮在排水中的粒子;电解的方法,是有机物的分解。 u0435 u0434 u0438 u043d u0435 u043d u0438 u00a0, u0441 u043e u0434 u0435 u0440 u0436 u0430 u0449 u0435 u0433 u0433 u043e u0441 u00a0 u0434 u043b u00a0 u0440 u0430 u0437 u0434 u0435 u043b u0435 u043d u0438 u00a0油和水;水箱 u0434 u043b u00a0分离 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0有机物,即去除水和有机物 u0441 u043e u043 5 u0434 u0438 u043d u0435 u043d u0438 u00a0进行了第二轮电解;油箱 u0434 u043b u00a0 u0430 u0434 u0441 u0431 u043e u0440 u0431 u0446 u0438 u043e u043d u043d u043e u0433 u043e u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0有机物,即 u0430 u0434 u0441 u043e u0440 u0431 u0446 u0438 u00a0天然 u0441 u043e u0435 u0434 u0438 u043d u0435 u043d u0438 u00a0 u0430 u0434 u0434 u0441 u0441 u0440 u0431 u0435 u043d u0442 u043e u043c系统基于 u043d u0435 u043e u0440 u0433 u0430 u043d u0438 u0447 u0435移除有机物 u0441 u043e u0435 u0434 u0438 u043d u0435 u043d u0438 u00a0)中的化合物,将第三个处理槽 u0434 u043b u00b0分离出来 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0有机物;相机 u0441 u0433 u043e u0440 u0430 u043d u0438 u00a0,其中混合了从水箱中的水排放的有机物 u0441 u043e u0435 u0434 u0438 u043d u0435 u043d u0438 u00a0 u0434 u043b u00a0分离 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0有机物和有机物 u0441 u043e u0435 u0434 u0438 u043d u043d u0435 u043d u0438 u00438水箱中的水 u0434 u043b u00a0 u0430 u0434 u0441 u043e u0440 u0431 u0446 u0438 u043e u043e u043d u043d u 043e u0433 u043e u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0有机物质,所得混合物和在大气中释放燃烧产物 u0435 u043d u0438 u00a0; 33。 p.32的系统,其中,吸附后, u0443 u0434 u0430 u043b u0435 u043d u043d u0438 u00a0有机 u0441 u043e u0435 u0434 u0434 u0438 u043d u0435 u043d u043d u0438 34.将基于无机化合物的系统在大气中于380至600 u0441的温度下加热至380至600 u0441,以使其再生和重复使用。34。其中 u0434 u043b u00a0 u0440 u0430 u0437 u0434 u0435 u043b u0435 u043d u0438 u00a0 p.32的系统,储油罐中的水和油也起磁性分离器的作用,而 u044d u043b u0435 u043a u0442 u0440 u043e u043b u0438 u0437 u0435 u0440 u0430。; 35。 p.32的系统,其中基于无机化合物的 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442包含 u043a u0440 u0435 u043c u043d u0438 u00a0中的二氧化物和氧化物 u043c u043e u043b u00a0 u0440 u043d u043e u043c u0430 u043b u044e u043c u0438 u043d u0438 u00a0针对SiO2至Al2O3, u0441 u043e u0441 u0442 u042 u043b u00a0 u044e u0449 u0435 u043c 5以上,并且微孔材料 u0430 u0434 u0441 u043e u0440 u0431 u0435 u043d u0442 u0430的眼球结构很紧张。 。 p.32的系统,其中水库 u0434 u043b u00a0分离 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0有机物可能有宽水,第二步处理是 u043b u00a0 uda u043b u0435 u043d u0438 u00a0挥发性有机物 u0441 u043e u0435 u0434 u0438 u043d u0435 u043d u0438 u00a0。

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