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INSTALLATION FOR phase-selective sorption (adsorption, ion exchange) of the component with the fluid dispersion medium and method for phase-selective sorption components from the dispersion medium FLUID
INSTALLATION FOR phase-selective sorption (adsorption, ion exchange) of the component with the fluid dispersion medium and method for phase-selective sorption components from the dispersion medium FLUID
1.installation of u0434u043bu00a0 u0444u0430u0437u043eu0441u0435u043bu0435u043au0442u0438u0432u043du043eu0439 means of sorption (adsorption, u0438u043eu043du043eu043eu0431u043cu0435u043du0430) component of the fluid internal environment mainly slurry or liquid u0441u043eu0434u0435u0440u0436u0430u0449u0430u00a0 u0441u043eu0435u0434u0438u043du0435u043du043du044b e pipes in the reactor u0446u0438u0440u043au0443u043bu00a0u0446u0438u043eu043du043du044bu0439 u0441u043cu0435u0448u0435u043du0438u00a0, pump, u043au043eu0436u0443u0445u043eu0442u0440u0443u0431u043du044bu0439 u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043a with porous pipes and u043fu0443u043bu044cu0441u0430u0442u043eu0440u043eu043c and pump line pitches and the cultivated environment in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043a,the line of withdrawal from both environment and the circuit source of fresh sorbent and the diversion of spent sorbent, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 what he and is equipped with devices u0432u044bu0442u0435u0441u043du0435u043du0438u00a0 established circuit sequentially at the entrance and exit u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0430, a transport fluid, united with lin it of the cultivated environment and the compendium of transport fluidthe drainage line processed environment, u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043a is designed in the form of two connected in parallel to the environment and a sorbent suspension patterns of mass transfer sections and the installation also has u043au043bu0430u043fu0430u043du043du043e - u043fu0443u043bu044cu0441u0430u0446u0438u043eu043du043du043eu0439 system containing a computer and u0443u043fu0440u0430u0432u043bu00a0u0435u043cu044bu0435 them valves mounted at the outlet of a supply and exhaust flow metre u0430u0441u0441u043eu043eu0431u043cu0435u043du043du044bu0445 sections, sources and collections.;2. unit 1, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 what source of fresh sorbent is connected with a circuit on the input devices u0432u044bu0442u0435u0441u043du0435u043du0438u00a0 and pipeline diversion of spent sorbent a compendium of spent sorbent and connected to the circuit between the devices u0432u044bu0442u0435u0441u043du0435u043du0438u00a0.;3. unit 1, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 because the reactor is in the form of u043au043eu043bu043eu043du043du043eu0433u043e apparatus with human made neck fixed, or u0434u0432u0438u0436u0443u0449u0438u043cu0441u00a0 or sensitive layer of a sorbent, or u0441u0435u043au0446u0438u043e u043du0438u0440u043eu0432u0430u043du043du044bu043c with u043fu0435u0440u0435u043cu0435u0448u0438u0432u0430u044eu0449u0438u043cu0438 devices in u0441u0435u043au0446u0438u00a0u0445.;4. unit 1, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0 because it has additional reactors connected in circuit in parallel and / or consistently with the core.;5. unit 1, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0430u00a0 u0441u0435u043au0446u0438u00a0 implemented in the form of u043au043eu043du0442u0430u043au0442u043du043e - u043fu043bu0430u0441u0442u0438u043du043du043eu0433u043e type comprising u0441u0436u0438u043cu0430u0435u043cu044bu0435 into a single unit u043fu0440u043eu0444u0438u043bu0438u0440u043eu0432u0430 u043du043du044bu0435 plates with them and united with the u043bu0438u043du0438u00a0u043cu0438 of cultivated environment and a sorbent suspension u043fu0440u043eu0442u00a0u0436u0435u043du043du044bu043cu0438 adjacent channels, between which the lips established u0441u043cu0435u043du043du0430u00a0 u043fu0440u043eu043du0438u0446u0430u0435u043cu0430u00a0 septum.;6. installation on any of the u043fu043f.1 and 5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, u043fu0440u043eu043du0438u0446u0430u0435u043cu0430u00a0 septum is accomplished in the form of cylindrical sleeves of a flexible elastic u043fu0440u043eu043du0438u0446u0430 u043fu0440u043eu0442u00a0u0436u0435u043du043du043eu0433u043e u0435u043cu043eu0433u043e material, preferably of fabric, or mesh, or u043fu0435u0440u0444u043eu0440u0438u0440u043eu0432u0430u043du043du043eu0439 film.;7. installation on any of the u043fu043f.1 and 5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, u043fu0440u043eu0444u0438u043bu0438u0440u043eu0432u0430u043du043du044bu0435 plates fitted with elements in the form of u043du0430u0442u00a0u0436u0435u043du0438u00a0 u043fu0440u0438u0436u0438u043cu043du044bu0445 u0443u043fu043bu043eu0442u043du0435u043du0438u00a0u043cu0438 type projection - paz, rigid or elastic bands or cords, hoses.;8. installation on any of the u043fu043f.1 and 5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, u043fu0440u043eu043du0438u0446u0430u0435u043cu0430u00a0 partition has two outdoor u0441u043bu043eu00a0 of u043au0440u0443u043fu043du043eu00a0u0447u0435u0438u0441u0442u043eu0439 u0430u0440u043cu0438u0440u0443u044eu0449u0435u0439 fabric, or mesh, or u043fu0435u0440u0444u043eu0440u0438u0440u043eu0432 anna film, between which a partition of u043cu0435u043bu043au043eu00a0u0447u0435u0438u0441u0442u043eu0439 fabric, or mesh, or u043fu0435u0440u0444u043eu0440u0438u0440u043eu0432u0430u043du043du043eu0433u043e or porous material.;9. installation on any of the u043fu043f.1 and 5, u043eu0442u043bu0438u0447u0430u044eu0449u0430u00a0u0441u00a0, u043fu0440u043eu043du0438u0446u0430u0435u043cu0430u00a0 septum wholly or partly made of u043fu0435u0440u0444u043eu0440u0438u0440u043eu0432u0430u043du043du043eu0439 shrink film or mesh.;10.method u0444u0430u0437u043eu0441u0435u043bu0435u043au0442u0438u0432u043du043eu0439 means of sorption (adsorption, u0438u043eu043du043eu043eu0431u043cu0435u043du0430) component of the fluid internal environment mainly slurry or liquid, comprising mixing u043cu0435u043bu043au043eu0434u0438u0441 u043fu0435u0440u0441u043du043eu0433u043e sorbent (u0430u0434u0441u043eu0440u0431u0435u043du0442u0430, u0438u043eu043du0438u0442u0430) with the liquid phase environment in the reactor, the extract obtained in u0446u0438u0440u043au0443u043bu00a0u0446u0438u0438 sorbent suspension in the circuit.u043fu0440u043eu0442u0438u0432u043eu0442u043eu0447u043du044bu0439 u043au043eu043du0432u0435u043au0442u0438u0432u043du044bu0439 u043cu0430u0441u0441u043eu043eu0431u043cu0435u043d on part of the coolant flow between the suspension and the cultivated environment in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 with permeable bulkhead in u0441u043eu0437u0434u0430u043du0438 and it u0437u043du0430u043au043eu043fu0435u0440u0435u043cu0435u043du043du044bu0445 swings u0434u0430u0432u043bu0435u043du0438u00a0, lodge in the fresh, clump and withdrawal of spent sorbent, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 orderwhat fresh u0441u043eu0440u0431u0435u043du0442 source and exhaust u0441u043eu0440u0431u0435u043du0442 the contain in their concentrated u0442u0435u043au0443u0447u0438u0445 suspensions in a transport u043au043eu043du0441u0435u0440u0432u0438u0440u0443u044eu0449u0435u0439 fluid the u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 in the endless cycle of installing a reactor u0441u043cu0435u0448u0435u043du0438u00a0 in circuit.in the first cycle of the source in the reactor are estimated in the form of a sorbent suspension with a share in the transport of fluids in the liquid phase in the cultivated environment, in the second cycle slurry in the circuit u0440u0430u0437u0431u0430u0432u043bu00a0u044eu0442 to optimum working u043fu043eu0440u043eu0437u043du043eu0441u0442u0438,the third is the u0441u043eu0440u0431u0446u0438u043eu043du043du043eu043c cycle from the volume of the cultivated environment have u0441u043eu0434u0435u0440u0436u0430u0449u0435u0439u0441u00a0 component in circuit u0441u0443u0441u043fu0435u043du0437u0438u0435u0439 sorbent in the fourth cec le slurry in the circuit u0441u0433u0443u0449u0430u044eu0442 before starting u043fu043eu0440u043eu0437u043du043eu0441u0442u0438, u043fu00a0u0442u043eu043c cycle slurry of spent sorbent from the reactor is in a preliminary exchange in in the liquid phase for both environment to transport fluid.;11.method u0444u0430u0437u043eu0441u0435u043bu0435u043au0442u0438u0432u043du043eu0439 means of sorption (adsorption, u0438u043eu043du043eu043eu0431u043cu0435u043du0430) component of the fluid internal environment mainly slurry or liquid, comprising mixing u043cu0435u043bu043au043eu0434u0438u0441 u043fu0435u0440u0441u043du043eu0433u043e sorbent (u0430u0434u0441u043eu0440u0431u0435u043du0442u0430, u0438u043eu043du0438u0442u0430) with the liquid phase environment in the reactor, the extract obtained in u0446u0438u0440u043au0443u043bu00a0u0446u0438u0438 sorbent suspension in the circuit.u043fu0440u043eu0442u0438u0432u043eu0442u043eu0447u043du044bu0439 u043au043eu043du0432u0435u043au0442u0438u0432u043du044bu0439 u043cu0430u0441u0441u043eu043eu0431u043cu0435u043d on part of the coolant flow between the suspension and the cultivated environment in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 with permeable bulkhead in u0441u043eu0437u0434u0430u043du0438 and it u0437u043du0430u043au043eu043fu0435u0440u0435u043cu0435u043du043du044bu0445 swings u0434u0430u0432u043bu0435u043du0438u00a0, lodge in the fresh and withdrawal of spent sorbent, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 orderwhat fresh u0441u043eu0440u0431u0435u043du0442 source and exhaust u0441u043eu0440u0431u0435u043du0442 the contain in their u0442u0435u043au0443u0447u0438u0445 suspensions in a transport u043au043eu043du0441u0435u0440u0432u0438u0440u0443u044eu0449u0435u0439 fluid process u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0 s in a continuous, endless cycle in installation with several parallel circuit installed in the reactors.in which pre then cook fresh sorbent slurry in the liquid phase the cultivated environment by application of source in reactors or with the exchange her transport fluid to the liquid phase of cultivated environment and further from the cultivated environment have u0446u0438u0440u043au0443u043bu0438u0440u0443u0435u043cu043eu0439 component in circuit u0441u0443u0441u043fu0435u043du0437u0438u0435u0439 sorbent with the continuous application of cultivated environmentu0446u0438u043au043bu0438u0447u0435u0441u043au043eu043c connecting in the reactor with fresh u0441u043eu0440u0431u0435u043du0442u043eu043c and disconnecting from the contour of the reactor spent u0441u043eu0440u0431u0435u043du0442u043eu043c.;12.method u0444u0430u0437u043eu0441u0435u043bu0435u043au0442u0438u0432u043du043eu0439 means of sorption (adsorption, u0438u043eu043du043eu043eu0431u043cu0435u043du0430) component of the fluid internal environment mainly slurry or liquid, comprising mixing u043cu0435u043bu043au043eu0434u0438u0441 u043fu0435u0440u0441u043du043eu0433u043e sorbent (u0430u0434u0441u043eu0440u0431u0435u043du0442u0430, u0438u043eu043du0438u0442u0430) with the liquid phase environment in the reactor, the extract obtained in u0446u0438u0440u043au0443u043bu00a0u0446u0438u0438 sorbent suspension in the circuit.u043fu0440u043eu0442u0438u0432u043eu0442u043eu0447u043du044bu0439 u043au043eu043du0432u0435u043au0442u0438u0432u043du044bu0439 u043cu0430u0441u0441u043eu043eu0431u043cu0435u043d on part of the coolant flow between the suspension and the cultivated environment in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 with permeable bulkhead in u0441u043eu0437u0434u0430u043du0438 and it u0437u043du0430u043au043eu043fu0435u0440u0435u043cu0435u043du043du044bu0445 swings u0434u0430u0432u043bu0435u043du0438u00a0, lodge in the fresh and withdrawal of spent sorbent, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, fresh u0441u043eu0440u0431u0435u043du0442 source contained in the take him in the flowing suspension transport u043au043eu043du0441u0435u0440u0432u0438u0440u0443u044eu0449u0435u0439 fluidexhaust u0441u043eu0440u0431u0435u043du0442 the contain of the fluid suspension in the liquid phase for both environments, the u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 continuously extended to the cultivated de and sorbent suspension installation mode with one or more consistently established in circuit reactorsfrom the cultivated environment have u0446u0438u0440u043au0443u043bu0438u0440u0443u0435u043cu043eu0439 component in circuit u0441u0443u0441u043fu0435u043du0437u0438u0435u0439 sorbent with continuous application in it from the source region in the fresh sorbent the transport fluid and the continuous challenge of the contour in the region of spent sorbent in the liquid phase for both environments.;13. way on any of the u043fu043f.10 and 11, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 because exchange transport fluid in the liquid phase u0441u0443u0441u043fu0435u0437u0438u0438 fresh sorbent in the cultivated environment, laundering of tr u0430u043du0441u043fu043eu0440u0442u043du043eu0439 fluid and u043fu0440u043eu043fu0438u0442u044bu0432u0430u043du0438u0435 cultivated environment u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 by u043au043eu043du0432u0435u043au0442u0438u0432u043du043eu0433u043e u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du0430 suspension in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 in u043fu0440u043eu0442u0438u0432u043eu0442u043eu043au0435 with handle oh environment.;14. way on any of the u043fu043f.10 u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 12, so that the cultivated environment have u0446u0438u0440u043au0443u043bu0438u0440u0443u0435u043cu043eu0439 component in circuit u0441u0443u0441u043fu0435u043du0437u0438u0435u0439 sorbent by u043au043eu043du0432u0435u043au0442u0438u0432u043du043eu0433u043e mas u0441u043eu043eu0431u043cu0435u043du0430 cultivated environment in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 in u043fu0440u043eu0442u0438u0432u043eu0442u043eu043au0435 with u0441u0443u0441u043fu0435u043du0437u0438u0435u0439 sorbent.;15. way on any of the u043fu043f.10 and 11, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, exchange of liquid phase suspension treated environment spent sorbent to transport liquid, washing it from both environment and u043fu0440u043eu043fu0438u0442u044bu0432u0430u043du0438u0435 transport fluid u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 by u043au043eu043du0432u0435u043au0442u0438u0432u043du043eu0433u043e u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du0430 suspension in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 in u043fu0440u043eu0442u0438u0432u043eu0442u043eu043au0435 with transport noah fluid.;16. way on any of the u043fu043f.10 - 12, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, u043au043eu043du0432u0435u043au0442u0438u0432u043du044bu0439 u043cu0430u0441u0441u043eu043eu0431u043cu0435u043d between flows in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 u043fu0440u043eu0432u043eu0434u00a0u0442 u043fu043eu043fu0435u0440u0435u043cu0435u043du043du044bu043c reverse u0444u0438u043bu044cu0442u0440u043eu0432u0430u043du0438u0435u043c them in the u043fu0440u043eu043du0438u0446u0430u0435u043cu0443u044e septum under pressure make the flows of pumps with equal bars u0437u043du0430u043au043eu043fu0435u0440u0435u043cu0435u043du043du043eu0439 filtration.;17. method for p.10, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, dilution of the suspension of the sorbent in the external circuit, the liquid phase of cultivated environment to optimum working u043fu043eu0440u043eu0437u043du043eu0441u0442u0438 u043fu0440u043eu0432u043eu0434u00a0u0442 u0440u0435u0432u0435u0440u0441u0438u0432u043d u0444u0438u043bu044cu0442u0440u043eu0432u0430u043du0438u0435u043c. in u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 at which time increased u0434u0430u0432u043bu0435u043du0438u00a0 environment more sensitivity increased u0434u0430u0432u043bu0435u043du0438u00a0 in suspension.a clump of spent sorbent suspension in the circuit to the reference u043fu043eu0440u043eu0437u043du043eu0441u0442u0438 u043fu0440u043eu0432u043eu0434u00a0u0442 reverse u0444u0438u043bu044cu0442u0440u043eu0432u0430u043du0438u0435u043c, at which time the increased u0434u0430u0432u043bu0435u043du0438u00a0 in u0441u0443u0441u043fu0435u043d zia's sensitivity increased u0434u0430u0432u043bu0435u043du0438u00a0 in environment.;18. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 p.12, so that the circuit is u043fu0440u043eu043cu044bu0432u0430u0435u043cu044bu0439 u0441u043eu0440u0431u0435u043du0442, who supplied him with his u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0435 u043fu0440u043eu043cu044bu0432u0430u044eu0449u0435u0439 fluid from the contour of the u0442u0432u043eu0434u00a0u0442 washed u0441u043eu0440u0431u0435u043du0442 and u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0430 solution rinsing fluid.;19. way on any of the u043fu043f.10 - 12, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, use u0430u0434u0441u043eu0440u0431u0435u043du0442u044b, u0438u043eu043du0438u0442u044b and processed by the environment with the size of the particle u0434u0438u0441u043fu0435u0440u0441u043du044bu0445 large size long u00a0u0447u0435u0435u043a or p u0435u0440u0444u043eu0440u0430u0446u0438u0439 in u043fu0440u0438u043cu0435u043du00a0u0435u043cu043eu0439 permeable partition u043cu0430u0441u0441u043eu043eu0431u043cu0435u043du043du0438u043au0430 within 0.03 - 0.7 mm.;20. way on any of the u043fu043f.10 u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 12, so that u0446u0438u0440u043au0443u043bu00a0u0446u0438u043eu043du043du043eu043c circuit supports the working u043fu043eu0440u043eu0437u043du043eu0441u0442u044c sorbent suspension of 0.81 is 0.96.;21. way on any of the u043fu043f.10 u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 12, so that u0446u0438u0440u043au0443u043bu00a0u0446u0438u043eu043du043du043eu043c circuit supports the working concentration of sorbent suspension within 25.2 - 380 kg / m3 in the u043eu0442u043du043eu0441u0438u0442u0435u043b the dose of steel used sorbent to cultivated environment within 0.65 - 164 kg / m3.;22. way on any of the u043fu043f.10, 12 - 18, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, as transport u043au043eu043du0441u0435u0440u0432u0438u0440u0443u044eu0449u0435u0439 and u043fu0440u043eu043cu044bu0432u0430u044eu0449u0435u0439 fluids using water or liquid phase treatment environment, including the addition of antiseptic, mainly sulphur dioxide.
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