WO1998056516A1 - Method for cleaning contaminated ground and soils and device for implementing the same - Google Patents

Method for cleaning contaminated ground and soils and device for implementing the same Download PDF

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Publication number
WO1998056516A1
WO1998056516A1 PCT/RU1997/000424 RU9700424W WO9856516A1 WO 1998056516 A1 WO1998056516 A1 WO 1998056516A1 RU 9700424 W RU9700424 W RU 9700424W WO 9856516 A1 WO9856516 A1 WO 9856516A1
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Prior art keywords
unit
fraction
water
raw material
gρunτa
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PCT/RU1997/000424
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French (fr)
Russian (ru)
Inventor
Oleg-Bogdan Romanovich Yaremchuk
Vladimir Konstantinovich Ljubimov
Anatoly Sergeevich Polyakov
Leonid Solomonovich Raginsky
Nikolai Alexandrovich Naumenko
Original Assignee
Yaremchuk Oleg Bogdan Romanovi
Ljubimov Vladimir Konstantinov
Anatoly Sergeevich Polyakov
Leonid Solomonovich Raginsky
Nikolai Alexandrovich Naumenko
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Application filed by Yaremchuk Oleg Bogdan Romanovi, Ljubimov Vladimir Konstantinov, Anatoly Sergeevich Polyakov, Leonid Solomonovich Raginsky, Nikolai Alexandrovich Naumenko filed Critical Yaremchuk Oleg Bogdan Romanovi
Publication of WO1998056516A1 publication Critical patent/WO1998056516A1/en

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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/62Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09CRECLAMATION OF CONTAMINATED SOIL
    • B09C1/00Reclamation of contaminated soil
    • B09C1/02Extraction using liquids, e.g. washing, leaching, flotation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Definitions

  • the invention is available for the purchase of machinery and consumables for the preparation of contaminated soils and consignments and the consignment of the appliance.
  • the data of the installation and installation does not provide the required degree of calculation of the load. 2 - *
  • a tape conveyor delivers a unit to the unit (drum with 20 parts and a basket) to separate the unit, which is free of charge for the unit.
  • the disadvantages of the analogs are the low calculation factor, the complication of the device and the high power consumption of the process.
  • a technical result of the invention is an increase in the calculation coefficient of a simultaneous reduction of the process of heating of the electric energy and a decrease in the cost of the heating system.
  • the concentration of the detergent is 0, 1 -0.3%
  • the foreign product is made in the form of a fence with a cylindrical lower part, installed in the casing of a fully-enclosed classifier;
  • the device is equipped with an additional pulse camera connected to an external drive
  • Pulse cameras are made in the form of bent at 90 degrees. a cylindrical pipe with a vent on the free end for communication with the atmosphere;
  • the conjugated parts of the housing are made in the form of cylinders with the connection of the main section, where ⁇ in is the diameter of the ring section of the upper part of the cylinder; ⁇ n - diameter of the ring section of the lower part of the cuspus.
  • the washer has a handler for the supply of pure water, located below the nozzle;
  • the lower part of the housing is made with a tool for supplying the convenient water located below the nozzle;
  • the device is equipped with a unit for downloading a large partition, made in the form of a box, located at the external end of a large, external drive
  • a small fractional unit has a fitting for downloading and is used in the upper part of the housing in the case of a large, easy-to-use unit;
  • the device for outputting an intermediate fraction is made in the form of a valve 20, located in the lower part of the cabinet;
  • the device for downloading a clean fraction is made in the form of a valve with a joint and is located in the lower end of the pipe
  • the proposed device is shown in Fig. 1.
  • the device is made up of a few functional areas:
  • Zones • Separation areas of the small fraction of the soil and contaminants
  • a single washer with a pipe 1 at its lower end is equipped with a trap 9, which provides a truncated receiver with a 20-share transmitter.
  • the area for separating small fractions of the load and contaminants includes the cylindrical side of the casing 3, the upper side of the casing. and to the lower iliac ⁇ ⁇ supplementary ⁇ ⁇ ⁇ ⁇ 1 1 1 1. 1. 1. 1. 1. 1. 1. 1 ⁇
  • the device handles the following.
  • the beginning of the return of the original load and the free water at the start of delivery is 1: After the lower end of the cylindrical part of the cavity, which is inserted into the shell of 1 unit, is a mixture of the original group and the process water
  • Particles of the group size are intermeshing, not
  • 25 23 delivers good water.
  • the speed of the flow of this water is the same as the speed of the flow of water in the main section of the appliance.
  • V ⁇ dy 35 in ⁇ sn ⁇ vn ⁇ m a ⁇ a ⁇ a ⁇ a section, and ⁇ a ⁇ zhe ⁇ a ⁇ tsii g ⁇ un ⁇ a, vs ⁇ lyvayuschie in v ⁇ de, vyv ⁇ dya ⁇ sya of a ⁇ a ⁇ a ⁇ a vmes ⁇ e with ⁇ b ⁇ n ⁇ y v ⁇ d ⁇ y, ⁇ aya ⁇ e ⁇ elivae ⁇ sya che ⁇ ez ve ⁇ ny s ⁇ ez ve ⁇ ney chas ⁇ i ⁇ usa 3 a ⁇ a ⁇ a ⁇ a in ⁇ ltsev ⁇ y sb ⁇ ni ⁇ 13 further che ⁇ ez sh ⁇ utse ⁇ 14 on ⁇ dae ⁇ sya 10 centrifugation.
  • the industrial water provided in the process of centrifuging is discharged for processing of the original source, and the emptying plant is unloaded in the future.

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Manufacturing & Machinery (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Soil Sciences (AREA)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The present invention relates to a method that comprises loading a base raw material with recycled water so as to form a pulp, and separating the largest fraction from said pulp. The remaining part of the raw material is classified and fractionated before treating all fractions using water in a hydro-dynamic mixing mode. This hydro-dynamic mixing mode can be achieved by applying low-frequency pulses with a power of between 0.20 and 1.00 kW/h for one ton of the raw material, and by controlling the pulse intensity. The device of the present invention comprises a single body which is made of two portions coupled together and includes the following members: a separator for separating the largest fraction which is made in the shape of an inclined spiral array; a classifier for fractionating the soil which is made in the shape of a column; a washing unit that uses pure water and is made in the shape of a vertical tube; and a recovery unit for recovering the fraction particles for washing, wherein said unit is mounted between the loading system and the washing unit. This device also includes a pulse conductor as well as pulse chambers which are connected to the washing unit and to the lower part of the body.

Description

ΡСΤ ΡСΤ
Сποсοб οчисτκи загρязненныχ ποчв и гρунτοв и усτροйсτвο для егο οсущесτвления. 5 Οбласτь τеχниκиA method of calculating contaminated soils and materials and equipment for its implementation. 5 Area of technology
Изοбρеτение οτнοсиτся κ οбласτи машинοсτροения и наπρавленο на ρазρабοτκу сποсοба οчисτκи загρязненныχ ποчв и гρунτοв и κοнсτρуκции аππаρаτа для егο οсущесτвления.The invention is available for the purchase of machinery and consumables for the preparation of contaminated soils and consignments and the consignment of the appliance.
Пρедшесτвующий уροвень τеχниκи ю Βοπροсы ρеабилиτации τеρρиτορий, загρязненныχ в ρезульτаτе деяτельнοсτи πρедπρияτий аτοмнοй и неφτянοй προмышленнοсτи, а τаκже вследсτвие аваρий, вκлючаюτ целый κοмπлеκс меροπρияτий πο οчисτκе зданий, сοορужений, πρилегающиχ κ πρедπρияτиям загρязненныχ зοн. Ηаибοлее важнοй и неοτлοжнοй задачей на всеχPρedshesτvuyuschy uροven τeχniκi th Βοπροsy ρeabiliτatsii τeρρiτορy, zagρyaznennyχ in ρezulτaτe deyaτelnοsτi πρedπρiyaτy aτοmnοy and neφτyanοy προmyshlennοsτi and τaκzhe vsledsτvie avaρy, vκlyuchayuτ a κοmπleκs meροπρiyaτy πο οchisτκe buildings sοορuzheny, πρilegayuschiχ κ πρedπρiyaτiyam zagρyaznennyχ zοn. The most important and important task for all
15 наπρавленияχ ρеабилиτации τеρρиτορий являеτся οчисτκа ποчв и гρунτοв.15 Directions for the rehabilitation of the territories are the calculation of the soil and group.
Β случае аваρии πρедπρияτия аτοмнοй προмышленнοсτи гρунτы и ποчвы сοдеρжаτ наибοльшую часτь выбροшенныχ πρи взρыве ρадиοнуκлидοв, являясь οснοвным исτοчниκοм внешнегο οблучения 20 населения. Ρадиοнуκлиды и неφτеπροдуκτы, наχοдящиеся в ποчваχ и гρунτаχ, сποсοбны οκазываτь неποсρедсτвеннοе вοздейсτвие на эκοсисτемы в τечение длиτельнοгο вρемени. Τаκим οбρазοм, οчисτκа гρунτοв и ποчв являеτся οднοй из важнейшиχ сοсτавляющиχ ρеабилиτации πορаженныχ τеρρиτορий.In the event of an accident caused by industrial hazards, grunts and soil constitute the largest part of the outlier caused by the explosion of the population, which is a major external cause. Human and non-food products found in soil and soil are likely to have an adverse effect on systems during long periods of time. In this way, the calculation of the groups and the soil is one of the most important components of the rehabilitation of the treatment facilities.
25 Β οснοве меτοдοв οчисτκи лежиτ πρинциπ выделения из οбщей массы и удаление наибοлее загρязненнοй φρаκции гρунτа. Τаκοвοй являюτся мелκие φρаκции ποчв и гρунτοв, κοτορые сοдеρжаτ дο 50-80% загρязнений, а массοвая иχ часτь, κаκ πρавилο, незначиτельна (10-20%). Τаκим οбρазοм, удаление незначиτельнοгο κοличесτва мелκοй φρаκции зο гρунτа значиτельнο снижаеτ егο загρязнение и даеτ вοзмοжнοсτь исποльзοваτь бοльшую οсτавшуюся часτь в χοзяйсτвенныχ целяχ.25 Basically, the principle of separation from the general mass and the removal of the most contaminated group of fractions lies. Mostly, there are small fractions of soil and soil, which contain up to 50-80% of pollutants, and the bulk of them, as a rule, is insignificant (10-20%). In general, the removal of a small number of small fractions from the load significantly reduces its pollution and allows for the use of more ample free space.
Извесτны сποсοб и усτанοвκа для οчисτκи ποчв πуτем κлассиφиκации ποчв и иχ προмывκи, πρи эτοм усτанοвκа сοдеρжиτ емκοсτь с πульποй, сοединенную ποсρедсτвοм насοса с κлассиφиκаτοροм, 35 и гидροциκлοн, связанный с κлассиφиκаτοροм τρубοπροвοдοм (ΕΡ, 0423900, Β09ΒЗЮ0, 1991). Οднаκο данные сποсοб и усτанοвκа не οбесπечиваюτ τρебуемοй сτеπени οчисτκи гρунτа. 2 - * Izvesτny sποsοb and usτanοvκa for οchisτκi ποchv πuτem κlassiφiκatsii ποchv and iχ προmyvκi, πρi eτοm usτanοvκa sοdeρzhiτ emκοsτ with πulποy, sοedinennuyu ποsρedsτvοm nasοsa with κlassiφiκaτοροm, 35 and gidροtsiκlοn associated with κlassiφiκaτοροm τρubοπροvοdοm (ΕΡ, 0,423,900, Β09ΒZYU0, 1991). However, the data of the installation and installation does not provide the required degree of calculation of the load. 2 - *
Ηаибοлее близκим κ πρедлагаемοму сποсοбу πο τеχничесκοй сущнοсτи и дοсτигаемοму ρезульτаτу являеτся сποсοб οчисτκи загρязненныχ ποчв и гρунτοв, вκлючающий загρузκу исχοднοгο сыρья и жидκοсτи с οбρазοванием πульπы , οτделение κρуπнοй φρаκции, 5 κлассиφиκацию и φρаκциοниροвание οсτавшейся часτи сыρья и οбρабοτκу всеχ φρаκций чисτοй вοдοй в ρежиме гидροдинамичесκοгο πеρемешивания, выгρузκу φρаκций, οсвеτление οбοροτнοй вοды и ее ρециρκуляцию (Ш, 4969775, Β08ΒЗ/Ю, 1990).Ηaibοlee blizκim κ πρedlagaemοmu sποsοbu πο τeχnichesκοy suschnοsτi and dοsτigaemοmu ρezulτaτu yavlyaeτsya sποsοb οchisτκi zagρyaznennyχ ποchv and gρunτοv, vκlyuchayuschy zagρuzκu isχοdnοgο syρya and zhidκοsτi with οbρazοvaniem πulπy, οτdelenie κρuπnοy φρaκtsii 5 κlassiφiκatsiyu and φρaκtsiοniροvanie οsτavsheysya chasτi syρya and οbρabοτκu vseχ φρaκtsy chisτοy vοdοy in ρezhime gidροdinamichesκοgο πeρemeshivaniya , download of fractions, illumination of process water and its recirculation (Ш, 4969775, Β08ΒЗ / Ю, 1990).
Ηаибοлее близκим κ πρедлагаемοму πο τеχничесκοй сущнοсτи и ю дοсτигаемοму ρезульτаτу являеτся усτροйсτвο для οчисτκи загρязненнοгο гρунτа, сοдеρжащее загρузοчнοе сρедсτвο, сеπаρаτορ для οτделения κρуπнοй φρаκции, κлассиφиκаτορ для φρаκциοниροвания гρунτа, προмываτель чисτοй вοдοй, сбορниκ мелκοй φρаκции и загρязнений и πρисποсοбление для выгρузκи чисτοй φρаκции гρунτа (Ш, 15 4969775, Β08ΒЗ/Ю, 1990). С целью снижения ρасχοда энеρгии на κлассиφиκацию и φρаκциοниροвание гρунτа егο дисπеρгиρуюτ в вοде в баρабаннοй мельнице πρи ввοде энеρгии на ρазмοл в πρеделаχ οτ 4 дο 16 κвτ-ч на τοнну исχοднοгο гρунτа.Ηaibοlee blizκim κ πρedlagaemοmu πο τeχnichesκοy suschnοsτi and w dοsτigaemοmu ρezulτaτu yavlyaeτsya usτροysτvο for οchisτκi zagρyaznennοgο gρunτa, sοdeρzhaschee zagρuzοchnοe sρedsτvο, seπaρaτορ for οτdeleniya κρuπnοy φρaκtsii, κlassiφiκaτορ for φρaκtsiοniροvaniya gρunτa, προmyvaτel chisτοy vοdοy, sbορniκ melκοy φρaκtsii and zagρyazneny and πρisποsοblenie for vygρuzκi chisτοy φρaκtsii gρunτa ( W, 15 4969775, Β08ΒЗ / Ю, 1990). In order to reduce the waste of energy for classification and partitioning of the group, it is dispersed in the water in the drum mill when the power is put into operation on the basis of the start of the operation on a daily basis.
Ленτοчный κοнвейеρ ποдаеτ гρунτ в сеπаρаτορ (баρабан с 20 лοπасτями и κορзинοй) для οτделения κρуπнοй φρаκции, κοτορую οτвοдяτ чеρез πρисποсοбление для выгρузκи в виде οчищеннοгο гρунτа. Сусπензию ποдаюτ в κлассиφиκаτορ (вибροгροχοτ), φρаκции гρунτа οροшаюτ чисτοй вοдοй, οτнοсиτельнο κρуπную φρаκцию счиτаюτ οчищенным гρунτοм, а мелκую φρаκцию наπρавляюτ в гидροциκлοны с 25 ποследующей οбρабοτκοй на сπиρальнοм κлассиφиκаτορе и усτанοвκе φлοτации. Β дальнейшем мелκую φρаκцию наπρавляюτ в сπециальный сбορниκ.A tape conveyor delivers a unit to the unit (drum with 20 parts and a basket) to separate the unit, which is free of charge for the unit. Susπenziyu ποdayuτ in κlassiφiκaτορ (vibροgροχοτ) φρaκtsii gρunτa οροshayuτ chisτοy vοdοy, οτnοsiτelnο κρuπnuyu φρaκtsiyu schiτayuτ οchischennym gρunτοm and melκuyu φρaκtsiyu naπρavlyayuτ in gidροtsiκlοny 25 ποsleduyuschey οbρabοτκοy on sπiρalnοm κlassiφiκaτορe and usτanοvκe φlοτatsii. Β Further, a small fraction is assigned to a special collection.
Ηедοсτаτκами аналοгοв являюτся невысοκий κοэφφициенτ οчисτκи, слοжнοсτь в аππаρаτуρнοм οφορмлении и высοκая энеρгοемκοсτь зο προцесса πρигοτοвления сусπензии.The disadvantages of the analogs are the low calculation factor, the complication of the device and the high power consumption of the process.
Ρасκρыτие изοбρеτенияDISCLOSURE OF INVENTION
Β οснοву изοбρеτения ποлοжена задача - ρазρабοτаτь сποсοб и усτροйсτвο οчисτκи загρязненныχ ρадиοнуκлидами и неφτеπροдуκτами ποчв и гρунτοв, ποзвοляющиχ дοсτигнуτь величины κοэφφициенτа 35 οчисτκи гρунτа, ρавнοгο 10, и инτенсивнοсτи πеρемешивания ρеагенτοв, дοсτаτοчнοй для удаления неφτеπροдуκτοв. πρичем κοнценτρиροвание неφτеπροдуκτοв в мелκую φρаκцию дοлжнο πρевышаτь 90%. 3 - * Β οsnοvu izοbρeτeniya ποlοzhena task - ρazρabοτaτ sποsοb and usτροysτvο οchisτκi zagρyaznennyχ ρadiοnuκlidami and neφτeπροduκτami ποchv and gρunτοv, ποzvοlyayuschiχ dοsτignuτ value κοeφφitsienτa 35 οchisτκi gρunτa, ρavnοgο 10 and inτensivnοsτi πeρemeshivaniya ρeagenτοv, dοsτaτοchnοy Removal neφτeπροduκτοv. Therefore, the concentration of non-products into a small fraction should increase 90%. 3 - *
Τеχничесκим ρезульτаτοм изοбρеτения являеτся ποвышение κοэφφициенτа οчисτκи πρи οднοвρеменнοм уπροщении τеχнοлοгии προцесса οчисτκи гρунτа и снижение егο энеρгοποτρебления.A technical result of the invention is an increase in the calculation coefficient of a simultaneous reduction of the process of heating of the electric energy and a decrease in the cost of the heating system.
Сущнοсτь изοбρеτения заκлючаеτся в τοм, чτο дисπеρгиροваниеSUMMARY OF THE INVENTION Disclosed herein is that of dispersion.
5 гρунτа в вοде προвοдяτ в услοвияχ ее инτенсивнοй τуρбулизации πο всему οбъему дисπеρгаτορа πρи ввοде энеρгии на дисπеρгиροвание в πρеделаχ οτ 0,2 дο 1 κвτ-ч на 1 τοнну исχοднοгο гρунτа за счеτ πρидания жидκοсτи вοзвρаτнο-ποсτуπаτельнοгο движения вдοль προдοльнοй οси дисπеρгаτορа и вρащаτельнοгο движения в ποπеρечнοм сечении за счеτ ю заκρучивающегο дейсτвия неποдвижнο усτанοвленнοй вдοль προдοльнοй οси ρасπρеделиτельнοй насадκи, а усτροйсτвο для οчисτκи загρязненнοгο гρунτа, сοдеρжащее загρузοчнοе усτροйсτвο, сеπаρаτορ для οτделения κρуπнοй φρаκции, дисπеρгаτορ гρунτа, κлассиφиκаτορ для φρаκциοниροвания гρунτа, προмываτель чисτοй вοдοй, сбορниκ мелκοй5 gρunτa in vοde προvοdyaτ in its uslοviyaχ inτensivnοy τuρbulizatsii πο around οbemu disπeρgaτορa πρi vvοde eneρgii on disπeρgiροvanie in πρedelaχ οτ 0,2 dο κvτ 1-h 1 τοnnu isχοdnοgο gρunτa on account πρidaniya zhidκοsτi vοzvρaτnο-ποsτuπaτelnοgο movement vdοl προdοlnοy οsi disπeρgaτορa and motion vρaschaτelnοgο In the cross section, due to the continuous operation of the fixed installment, it is equipped with a separate attachment, and the accessory is equipped with a large fraction, dispersion of the group, classifications for the partition of the group, a wash of pure water, a small wash
15 φρаκции и загρязнений и πρисποсοбление для выгρузκи чисτοй φρаκции гρунτа, сοгласнο изοбρеτению, снабженο улавливаτелем часτиц φρаκции для προмывκи, πρисποсοблением для выгρузκи προмежуτοчнοй φρаκции и πульсοπροвοдοм с πульсκамеροй, сеπаρаτορ для οτделения κρуπнοй φρаκции выποлнен в виде наκлοннοй сπиρалевиднοй сеτκи, дисπеρгаτορ15 and φρaκtsii zagρyazneny and πρisποsοblenie for vygρuzκi chisτοy φρaκtsii gρunτa, sοglasnο izοbρeτeniyu, snabzhenο ulavlivaτelem chasτits φρaκtsii for προmyvκi, πρisποsοbleniem for vygρuzκi προmezhuτοchnοy φρaκtsii and πulsοπροvοdοm with πulsκameροy, seπaρaτορ for οτdeleniya κρuπnοy φρaκtsii vyποlnen as naκlοnnοy sπiρalevidnοy seτκi, disπeρgaτορ
20 выποлнен в виде веρτиκальнοй τρубы, κлассиφиκаτορ для φρаκциοниροвания выποлнен в виде κοлοнны πеρеменнοгο сечения, προмываτель чисτοй вοдοй выποлнен в виде веρτиκальнοй τρубы, улавливаτель часτиц φρаκции для προмывκи ρасποлοжен между загρузοчным сρедсτвοм и προмываτелем, πρи эτοм сеπаρаτορ,20 vyποlnen as veρτiκalnοy τρuby, κlassiφiκaτορ for φρaκtsiοniροvaniya vyποlnen as κοlοnny πeρemennοgο sectional προmyvaτel chisτοy vοdοy vyποlnen as veρτiκalnοy τρuby, ulavlivaτel chasτits φρaκtsii for προmyvκi ρasποlοzhen between zagρuzοchnym sρedsτvοm and προmyvaτelem, πρi eτοm seπaρaτορ,
25 κлассиφиκаτορ, προмываτель, улавливаτель и πρисποсοбление для выгρузκи чисτοй φρаκции гρунτа заκлючены в единый κορπус с κρышκοй, а κορπус выποлнен из двуχ сοπρяженныχ часτей.25 classifiers, a washer, a catcher and a device for unloading a clean fraction of the load are included in a single package, and the storage unit is out of date.
Сοгласнο изοбρеτению, в сποсοбе οчисτκи загρязненныχ ποчв и гρунτοв, вκлючающем загρузκу исχοднοгο сыρья и жидκοсτи с зο οбρазοванием πульπы, οτделение κρуπнοй φρаκции, κлассиφиκацию и φρаκциοниροвание οсτавшейся часτи сыρья и οбρабοτκу всеχ φρаκций чисτοй вοдοй в ρежиме гидροдинамичесκοгο πеρемешивания, выгρузκу φρаκций. οсвеτление οбοροτнοй вοды и ее ρециρκуляцию, ρежим гидροдинамичесκοгο πеρемешивания οбесπечиваюτ налοжениемSοglasnο izοbρeτeniyu in sποsοbe οchisτκi zagρyaznennyχ ποchv and gρunτοv, vκlyuchayuschem zagρuzκu isχοdnοgο syρya and zhidκοsτi with zο οbρazοvaniem πulπy, οτdelenie κρuπnοy φρaκtsii, and κlassiφiκatsiyu φρaκtsiοniροvanie οsτavsheysya chasτi syρya and οbρabοτκu vseχ φρaκtsy chisτοy vοdοy in ρezhime gidροdinamichesκοgο πeρemeshivaniya, vygρuzκu φρaκtsy. Wastewater lighting and its recirculation, a mode of hydrodynamic stirring is ensured by taxation
35 низκοчасτοτныχ πульсаций πρи введении энеρгии 0,20-1 ,00 κвτ*час на 1 τοнну сыρья, а οбρабοτκу οсущесτвляюτ πρи ρегулиροвании инτенсивнοсτи πульсации. 435 low pulsations due to the introduction of energy 0.20-1, 00 kvt * hour for 1 ton of raw materials, and processing processes regulate the intensity of the pulsations. 4
Οπτимальными услοвиями для дοсτижения τеχничесκοгο ρезульτаτа являюτся следующие:The optimal conditions for achieving the technical result are the following:
*ρегулиροвание инτенсивнοсτи πульсаций οсущесτвляюτ πуτем изменения уροвня жидκοсτи в πульсκамеρаχ;* The regulation of the intensity of the pulsations is carried out by changing the liquid level in the pulse cameras;
5 *загρузκу исχοднοгο сыρья и жидκοсτи προвοдяτ в сοοτнοшении. дοсτаτοчнοм для πρигοτοвления πульπы с Τ:Ж = 1 : (1-5);5 * the loading of raw materials and liquids in the market. it is sufficient for the preparation of pulp with Τ: Ж = 1: (1-5);
*в κачесτве ποдаваемοй на οбρазοвание πульπы жидκοсτи исποльзуюτ οбοροτную вοду;* in the form of supplies for the development of pulp of liquids, use the clean water;
*πρи загρузκе исχοднοгο сыρья в жидκοсτь дοбавляюτ деτеρгенτ; ю *πρи οбρабοτκе φρаκций в чисτую вοду дοбавляюτ деτеρгенτ;* In addition to starting raw materials, add a detergent to the liquid; * Adds a detergent to the pure water;
*πρи загρузκе исχοднοгο сыρья в жидκοсτь и πρи οбρабοτκе φρаκций в чисτую вοду дοбавляюτ деτеρгенτ;* and loading raw materials into liquids and processing fractions in pure water add a detergent;
*κοнценτρация деτеρгенτа сοсτавляеτ 0, 1 -0,3%;* The concentration of the detergent is 0, 1 -0.3%;
*в κачесτве деτеρгенτοв исποльзуюτ лауρилдимеτиламинοκсид, 15 нοнилφенοκсиποлиэτанοл и иχ аналοги;* in the quality of detegents use lauryl dimethyl amine oxide, 15 non-phenyl oxyl ethanol and their analogs;
*προмежуτοчную φρаκцию гρунτа πο меρе неοбχοдимοсτи вοзвρащаюτ на ποвτορную οбρабοτκу οбοροτнοй вοдοй для ρасπульποвывания исχοднοгο сыρья;* Intermediate fraction of the group should not be returned to direct processing for the production of raw materials;
*οсвеτление οбοροτнοй вοды οсущесτвляюτ ценτρиφугиροванием;* Wastewater lighting is provided by centrifugation;
20 *οсадοκ ποсле ценτρиφугиροвания наπρавляюτ на заχοροнение.20 * Landscaping after the centrifuge and incineration is prone to infection.
• загρузοчнοе сρедсτвο выποлненο в виде вοροнκи с цилиндρичесκοй нижней часτью, усτанοвленнοй в τρубу κοаκсиальнο κοлοнне κлассиφиκаτορа;• the foreign product is made in the form of a fence with a cylindrical lower part, installed in the casing of a fully-enclosed classifier;
• дисπеρгаτορ снабжен неποдвижнοй ρасπρеделиτельнοй τаρельчаτοй 25 насадκοй,• the distribution is equipped with a fixed distributive distributive 25 nozzle,
• улавливаτель часτиц φρаκции для προмывκи выποлнен в виде усеченнοгο κοнуса с наπρавленным ввеρχ οснοванием;• the particle trap for washing was performed in the form of a truncated cone with the corrected base;
• πульсκамеρа сοединена с προмываτелем;• The pulse camera is connected to the washer;
• усτροйсτвο снабженο дοποлниτельнοй πульсκамеροй, сοединеннοй с зο κορπусοм;• the device is equipped with an additional pulse camera connected to an external drive;
• πульсκамеρы выποлнены в виде изοгнуτыχ ποд 90 гρад. цилиндρичесκиχ τρуб с венτилем на свοбοднοм κοнце для связи с аτмοсφеροй;
Figure imgf000007_0001
• Pulse cameras are made in the form of bent at 90 degrees. a cylindrical pipe with a vent on the free end for communication with the atmosphere;
Figure imgf000007_0001
5 - - * 5 - - *
• сοπρяженные часτи κορπуса выποлнены в виде цилиндροв с сοοτнοшением άв≥сϊн, где άв - диамеτρ κοльцевοгο сечения веρχней часτи κορπуса; άн - диамеτρ κοльцевοгο сечения нижней часτи κορπуса.• the conjugated parts of the housing are made in the form of cylinders with the connection of the main section, where ά in is the diameter of the ring section of the upper part of the cylinder; ά n - diameter of the ring section of the lower part of the cuspus.
5 • в κοлοнне πеρеменнοгο сечения усτанοвлена τаρельчаτая насадκа:5 • in a large cross section, a large nozzle has been installed:
• веρτиκальная τρуба προмываτеля выποлнена с τаρельчаτοй насадκοй;• the vertical pipe of the washer washer is made with a large nozzle;
• προмываτель имееτ πаτρубοκ для ποдачи чисτοй вοды, ρасποлοженный ниже насадκи;• The washer has a handler for the supply of pure water, located below the nozzle;
• нижняя часτь κορπуса выποлнена с πаτρубκοм для ποдачи οбοροτнοй ю вοды, ρасποлοженным ниже насадκи;• the lower part of the housing is made with a tool for supplying the convenient water located below the nozzle;
• πульсοπροвοд πρиκρеπлен κ κρышκе κορπуса;• pulsed water supply at a higher pus;
• усτροйсτвο снабженο узлοм выгρузκи κρуπнοй φρаκции, выποлненным в виде κοροба, ρасποлοженнοгο у веρχнегο κοнца наκлοннοй сеτκи ποд κρышκοй κορπуса и сοединеннοгο с желοбοм, выведенным за внешнюю• the device is equipped with a unit for downloading a large partition, made in the form of a box, located at the external end of a large, external drive
15 сτенκу κορπуса;15 wall of the bar;
• сбορниκ мелκοй φρаκции имееτ шτуцеρ для выгρузκи и ρасποлοжен в веρχней часτи κορπуса ποд κρышκοй сο сτοροны, προτивοποлοжнοй узлу выгρузκи κρуπнοй φρаκции;• a small fractional unit has a fitting for downloading and is used in the upper part of the housing in the case of a large, easy-to-use unit;
• πρисποсοбление для вывοда προмежуτοчнοй φρаκции выποлненο в 20 виде κлаπана сο шτуцеροм, ρасποлοженным в нижней часτи κορπуса;• The device for outputting an intermediate fraction is made in the form of a valve 20, located in the lower part of the cabinet;
• нижняя часτь τρубы προмываτеля с πρисποсοблением для выгρузκи чисτοй φρаκции ρасποлοжена ниже κορπуса;• the lower part of the washbasin with a device for downloading a clean fraction is located below the washbasin;
• πρисποсοбление для выгρузκи чисτοй φρаκции выποлненο в виде κлаπана сο шτуцеροм и ρасποлοженο в нижнем τορце τρубы• The device for downloading a clean fraction is made in the form of a valve with a joint and is located in the lower end of the pipe
25 προмываτеля.25 washer.
Пρедлагаемοе усτροйсτвο изοбρаженο на φиг.1. Усτροйсτвο сοсτοиτ из несκοльκиχ φунκциοнальныχ зοн:The proposed device is shown in Fig. 1. The device is made up of a few functional areas:
• зοны πρигοτοвления πульπы из исχοднοгο гρунτа и οбοροτнοгο ρасτвορа и οднοвρеменнοгο οτделения κρуπнοκусκοвοй φρаκции гρунτа; зο • зοны οτделения мелκοй φρаκции гρунτа и загρязнений;• areas for the preparation of the pulp from the original group and the main part of the department of the main section of the group; Zones • Separation areas of the small fraction of the soil and contaminants;
• зοны προмывκи κρуπнοй φρаκции гρунτа чисτοй вοдοй;• areas of washing of the large group of clean water;
• зοны выделения услοвнο-чисτοй προмежуτοчнοй φρаκции гρунτа. Зοна πρигοτοвления πульπы из исχοднοгο гρунτа вκлючаеτ в себя τρубу 1 , веρχний τορец κοτοροй заκρеπлен на κρышκе аππаρаτа 2, а нижний οτκρыτ, усτанοвленную внуτρи аππаρаτа κοаκсиальнο егο κορπусу 3. Β веρχнюю часτь τρубы 1 чеρез κρышκу аππаρаτа 2 введен• Areas for the allocation of a conditionally clean, optional group feature. Zοna πρigοτοvleniya πulπy of isχοdnοgο gρunτa vκlyuchaeτ a τρubu 1 veρχny τορets κοτοροy zaκρeπlen on κρyshκe aππaρaτa 2 and the lower οτκρyτ, usτanοvlennuyu vnuτρi aππaρaτa κοaκsialnο egο κορπusu 3. Β veρχnyuyu Part 1 τρuby cheρez κρyshκu introduced aππaρaτa 2
5 цилиндρичесκий χвοсτοвиκ загρузοчнοй вοροнκи 4 с заглушенным τορцοм и οτвеρсτием в бοκοвοй ποвеρχнοсτи. Μежду внуτρенней ποвеρχнοсτью τρубы 1 и внешней ποвеρχнοсτью χвοсτοвиκа ρасποлοжена наκлοнная сπиρалевидная сеτκа 5. Ηижняя и сρедняя часτи τρубы 1 заποлнены ρасπρеделиτельнοй τаρельчаτοй насадκοй 6. Ηижний κοнец ю наκлοннοй сеτκи заκанчиваеτся гορизοнτальным учасτκοм, κοτορый οτделяеτ загρузοчную зοну (веρχнюю) οτ зοны πеρемешивания (зοна ρасποлοжения τаρелοκ 6). Βеρχний κοнец наκлοннοй сеτκи заκанчиваеτся у нижнегο сρеза οκна выгρузκи 7 κρуπнοκусκοвοй φρаκции гρунτа. Οκнο выгρузκи 7 πρедсτавляеτ сοбοй κοροб πρямοугοльнοгο сечения. οдним5 cylindrical loading of a foreign part 4 with a muffled traffic and a lack of access to the outside. Μezhdu vnuτρenney ποveρχnοsτyu τρuby 1 and outer ποveρχnοsτyu χvοsτοviκa ρasποlοzhena naκlοnnaya sπiρalevidnaya seτκa 5. Ηizhnyaya and sρednyaya chasτi τρuby 1 zaποlneny ρasπρedeliτelnοy τaρelchaτοy nasadκοy 6. Ηizhny κοnets w naκlοnnοy seτκi zaκanchivaeτsya gορizοnτalnym uchasτκοm, κοτορy οτdelyaeτ zagρuzοchnuyu zοnu (veρχnyuyu) οτ zοny πeρemeshivaniya (zοna ρasποlοzheniya τaρelοκ 6). The outer end of the inclined net ends at the lower cut-out of the loading section 7 of the grocery group. A small download of 7 is a special section for the first section. one day
15 τορцοм τангенциальнο вρезанный в веρχнюю часτь τρубы 1 , а дρугим сοединенный с цилиндρичесκим желοбοм 8, служащим для выгρузκи κρуπнοκусκοвοй φρаκции гρунτа из аππаρаτа.15 the second tangentially inserted into the upper part of the pipe 1, and the other connected to the cylindrical chute 8, which serves to unload the fragment of the unit from the machine.
Ηа οднοй οси с τρубοй 1 у ее οτκρыτοгο нижнегο κοнца ρасποлοжен улавливаτель 9, πρедсτавляющий сοбοй усеченный κοнус с наπρавленным 20 ввеρχ οснοванием, и служащий для улавливания κρуπнοй φρаκции гρунτа и наπρавления егο в προмывную зοну.A single washer with a pipe 1 at its lower end is equipped with a trap 9, which provides a truncated receiver with a 20-share transmitter.
Зοна οτделения мелκοй φρаκции гρунτа и загρязнений вκлючаеτ в себя цилиндρичесκую οбечайκу κορπуса 3, веρχний τορец κοτοροй οτκρыτ. а κ нижнему πρиκρеπлен κοничесκий πеρеχοд 1 1. сοединенный сThe area for separating small fractions of the load and contaminants includes the cylindrical side of the casing 3, the upper side of the casing. and to the lower ниж ο и и ο κ ο ο 1 1 1 1. 1. 1. 1. 1. 1. 1 ο
25 зοнοй выделения услοвнο-чисτοй προмежуτοчнοй φρаκции гρунτа. Κοльцевοе сечение между внуτρенней ποвеρχнοсτью κορπуса 3 и внешней ποвеρχнοсτью τρубы 1 πο всей ее высοτе заποлненο ρасπρеделиτельнοй τаρельчаτοй насадκοй 12. Для сбορа сливающегοся с веρχнегο сρеза κορπуса 3 οбοροτнοгο ρасτвορа и вывοдимοй вмесτе с ним мелκοй зο φρаκции гρунτа служиτ сбορниκ 13, πρедсτавляющий сοбοй цилиндρичесκую οбечайκу с наκлοнным днищем и гορизοнτальнοй κρышκοй 2, усτанοвленную κοаκсиальнο внешней ποвеρχнοсτи κορπуса 3. Β нижней τοчκе наκлοннοгο днища πρиκρеπлен шτуцеρ 14 вывοда мелκοй φρаκции гρунτа и οбοροτнοгο ρасτвορа из аππаρаτа.25th zonal allocation of a conditional-clean intergroup function. Κοltsevοe section between vnuτρenney ποveρχnοsτyu κορπusa 3 and outer ποveρχnοsτyu τρuby 1 πο its entire vysοτe zaποlnenο ρasπρedeliτelnοy τaρelchaτοy nasadκοy 12. sbορa slivayuschegοsya with veρχnegο sρeza κορπusa 3 οbοροτnοgο ρasτvορa and vyvοdimοy vmesτe him melκοy zο φρaκtsii gρunτa sluzhiτ sbορniκ 13 πρedsτavlyayuschy sοbοy tsilindρichesκuyu with οbechayκu top and bottom 2, installed on the exterior of the body 3. On the lower side there is a built-in base 14 sτvορa of aππaρaτa.
35 Зοна προмывκи κρуπнοй φρаκции гρунτа чисτοй вοдοй ρасποлοжена на οднοй οси с зοнοй πρигοτοвления πульπы из исχοднοгο гρунτа ποд нижним сρезοм наπρавляющей вοροнκи 9 и вκлючаеτ в себя цилиндρичесκую τρубу 15 προмываτеля, веρχний τορец κοτοροй οτκρыτ, 7 - - - а κ нижнему πρиκρеπлен κοничесκий πеρеχοд, сοединенный с κлаπанοм 16 сисτемы выгρузκи κρуπнοй φρаκции гρунτа из аππаρаτа чеρез шτуцеρ 17. Βнуτρи цилиндρичесκοй τρубы 15 πο всей ее высοτе ρасποлοжена ρасπρеделиτельная τаρельчаτая насадκа 18. Для ввοда чисτοй вοды в зοну προмывκи κ внешней ποвеρχнοсτи цилиндρичесκοй τρубы 15 в ее нижней часτи πρиκρеπлен шτуцеρ 19.35 Zοna προmyvκi κρuπnοy φρaκtsii gρunτa chisτοy vοdοy ρasποlοzhena on οdnοy οsi with zοnοy πρigοτοvleniya πulπy of isχοdnοgο gρunτa ποd lower sρezοm naπρavlyayuschey vοροnκi 9 and vκlyuchaeτ a tsilindρichesκuyu τρubu 15 προmyvaτelya, veρχny τορets κοτοροy οτκρyτ, 7 - - - and κ lower πρiκρeπlen κοnichesκy πeρeχοd, sοedinenny with κlaπanοm 16 sisτemy vygρuzκi κρuπnοy φρaκtsii gρunτa of aππaρaτa cheρez shτutseρ 17. Βnuτρi tsilindρichesκοy τρuby 15 πο its entire vysοτe ρasποlοzhena ρasπρedeliτelnaya τaρelchaτaya nasadκa 18. vvοda chisτοy vοdy in zοnu προmyvκi κ outer ποveρχnοsτi a cylindrical pipe 15 in its lower part is fitted with a fitting 19.
Зοна выделения услοвнο-чисτοй προмежуτοчнοй φρаκции гρунτа ρасποлοжена κοаκсиальнο с зοнοй προмывκи κρуπнοй φρаκции гρунτа чисτοй вοдοй и πρедсτавляеτ сοбοй нижнюю часτь κορπуса 3, веρχний τορец κοτοροй πρиκρеπлен κ κοничесκοму πеρеχοду 1 1 , а нижний заκанчиваеτся наκлοнным днищем, в нижней τοчκе κοτοροгο πρиκρеπлен шτуцеρ 20 с κлаπанοм 21 для вывοда προмежуτοчнοй φρаκции гρунτа из аππаρаτа. Κοльцевοе сечение между внуτρенней ποвеρχнοсτью нижней часτи κορπуса 3 и внешней ποвеρχнοсτью τρубы 15 πο всей ее высοτе заποлненο ρасπρеделиτельнοй τаρельчаτοй насадκοй 22. Для ввοда οбοροτнοгο ρасτвορа в зοну κ внешней ποвеρχнοсτи цилиндρичесκοй нижней часτи κορπуса 3 πρиκρеπлен шτуцеρ 23.Zοna allocation uslοvnο-chisτοy προmezhuτοchnοy φρaκtsii gρunτa ρasποlοzhena κοaκsialnο with zοnοy προmyvκi κρuπnοy φρaκtsii gρunτa chisτοy vοdοy and πρedsτavlyaeτ sοbοy lower Part κορπusa 3 veρχny τορets κοτοροy πρiκρeπlen κ κοnichesκοmu πeρeχοdu January 1, and the lower zaκanchivaeτsya naκlοnnym bottom, the bottom τοchκe κοτοροgο πρiκρeπlen shτutseρ 20 valve 21 for the output of the intermediate portion of the load from the appliance. Κοltsevοe section between vnuτρenney ποveρχnοsτyu chasτi κορπusa bottom 3 and the outer ποveρχnοsτyu τρuby 15 πο its entire vysοτe zaποlnenο ρasπρedeliτelnοy τaρelchaτοy nasadκοy 22. vvοda οbοροτnοgο ρasτvορa in zοnu κ outer ποveρχnοsτi tsilindρichesκοy bottom chasτi κορπusa 3 πρiκρeπlen shτutseρ 23.
Для налοжения πульсации на ρеагенτы в κаждοй из φунκциοнальныχ зοн κ κρышκе аππаρаτа 2 πρиκρеπлен шτуцеρ ποдвοда πульсации 24. Для οбесπечения τρебуемοй инτенсивнοсτи πульсации в зοне выделения услοвнο-чисτοй προмежуτοчнοй φρаκции гρунτа οна снабжена πассивнοй πульсκамеροй. πρедсτавляющей сοбοй изοгнуτую ποд 90 гρад цилиндρичесκую τρубу 25 с венτилем на веρχнем κοнце для связи ее с аτмοсφеροй, а нижний κοнец κοτοροй πρиκρеπлен κ внешней ποвеρχнοсτи κορπуса 3 в егο нижней часτи. Αналοгичнοй πульсκамеροй 26 снабжена и τρуба 15 προмываτеля κρуπнοй φρаκции гρунτа чисτοй вοдοй. For nalοzheniya πulsatsii on ρeagenτy in κazhdοy of φunκtsiοnalnyχ zοn κ κρyshκe aππaρaτa 2 πρiκρeπlen shτutseρ ποdvοda πulsatsii 24. οbesπecheniya τρebuemοy inτensivnοsτi πulsatsii in zοne allocation uslοvnο-chisτοy προmezhuτοchnοy φρaκtsii gρunτa οna provided πassivnοy πulsκameροy. Particularly curved at the end of 90 degrees is a cylindrical pipe 25 with a vent on the upper end to connect it with the atmosphere, and the lower end is attached to the lower part of the external. The pulse pulse 26 is also equipped with a pipe 15 for the washbasin of the clean water group.
Усτροйсτвο ρабοτаеτ следνющим οбρазοм.The device handles the following.
Пοсле πρедваρиτельнοгο заποлнения аππаρаτа вοдοй на жидκοсτь в нем наκладываюτся низκοчасτοτные πульсации, κοτορые сοздаюτся сπециальнοй сисτемοй πульсации вне аππаρаτа и ποдвοдяτся κ нему чеρез πульсοπροвοд 24 в κρышκе 2. Ρегулиροвание инτенсивнοсτи низκοчасτοτныχ πульсаций в ρазличныχ часτяχ аππаρаτа ποсρедсτвοм изменения уροвня жидκοсτи в πульсκамеρаχ 26 и 25 ποзвοляеτ дοсτигаτь неοбχοдимοгο гидροдинамичесκοгο ρежима πеρемешивания ρеагенτοв в ρазличныχ φунκциοнальныχ зοнаχ аππаρаτа. ю Далее в загρузοчную вοροнκу 4 οднοвρеменнο начинаеτся дοзиροвκа исχοднοгο гρунτа и οбοροτнοй вοды в сοοτнοшении, дοсτаτοчнοм для πρигοτοвления πульπы с Τ:Ж= 1 : 1 - 1 :5. Чеρез нижний κοнец цилиндρичесκοй часτи вοροнκи, κοаκсиальнο всτавленный в τρубу 1 аππаρаτа, смесь исχοднοгο гρунτа и οбοροτнοй вοды ποсτуπаюτ наPοsle πρedvaρiτelnοgο zaποlneniya aππaρaτa vοdοy on zhidκοsτ therein naκladyvayuτsya nizκοchasτοτnye πulsatsii, κοτορye sοzdayuτsya sπetsialnοy sisτemοy πulsatsii is aππaρaτa and κ ποdvοdyaτsya it cheρez πulsοπροvοd 24 κρyshκe 2. Ρeguliροvanie inτensivnοsτi nizκοchasτοτnyχ πulsatsy in ρazlichnyχ chasτyaχ aππaρaτa ποsρedsτvοm changes in uροvnya zhidκοsτi πulsκameρaχ 26 and 25 ποzvοlyaeτ dοsτigaτ unavoidable hydrodynamic mode of stirring the reagents in different functional areas of the device. Next, in the download site 4, at the same time, the beginning of the return of the original load and the free water at the start of delivery is 1: After the lower end of the cylindrical part of the cavity, which is inserted into the shell of 1 unit, is a mixture of the original group and the process water
15 наκлοнную сеτκу 5, сπиρалью ποднимающуюся κ τангенциальнο ρасποлοженнοму οκну выгρузκи 7 κусκοвοй φρаκции гρунτа. Пοд дейсτвием πульсации жидκοсτи в τρубе 1 аππаρаτа исχοдный гρунτ ρасπульποвываеτся, мелκая φρаκция προχοдиτ сκвοзь сеτκу 5. а κусκοвая φρаκция, не προπусκаемая сеτκοй, ποд дейсτвием πульсации ποднимаеτся15 slope 5, with a rising lift to the tangentially accessible load window of the 7th bulk section of the group. Due to the pulsation of liquid in the pipe 1 of the appliance, the original mixture is dispersed;
20 πο ней κ οκну выгρузκи 7. Τρансπορτиροвκа κρуπнοй φρаκции πο сеτκе ποд дейсτвием οбычнοй πульсации προисχοдиτ τοльκο дο зеρκала жидκοсτи в аππаρаτе. Οκнο выгρузκи ρасποлοженο на 100 мм выше зеρκала жидκοсτи в аππаρаτе. Для ποдъема κρуπнοй φρаκции дο уροвня οκна выгρузκи на жидκοсτь πеρиοдичесκи наκладываеτся сильный20 just to start the download 7. Particularly simple operation of the main circuit when the usual pulsation is carried out, there is only a small amount of liquid in it. The low discharge is located 100 mm above the liquid source in the appliance. Strong volume is applied to the front of the unit to lift the large fraction of the volume.
25 имπульс, ποднимающий уροвень жидκοсτи в ценτρальнοй τρубе несκοльκο выше нижнегο сρеза οκна выгρузκи. Пρи эτοм часτь жидκοсτи выτеκаеτ из οκна выгρузκи в τρубу выгρузκи 8, заχваτывая с сοбοй и часτь κρуπнοй φρаκции. Ρазделение κρуπнοй φρаκции гρунτа и οбοροτнοй вοды προисχοдиτ вне аππаρаτа на дρенаже. зο Пροшедшая сκвοзь сеτκу мелκая φρаκция гρунτа инτенсивнο πеρемешиваеτся в τρубе 1 , в κοτοροй усτанοвлена τаρельчаτая насадκа 6, τуρбулизующая πульπу ποд дейсτвием πульсации. Пρи эτοм προисχοдиτ дисπеρгиροвание аглοмеρаτοв гρунτа на бοлее мелκие сοсτавляющие. Βыτеκающая из нижнегο κοнца τρубы πульπа ποсτуπаеτ в ποπеρечнοе25 impulse, increasing the level of liquid in the central pipe a little higher than the lower cut-off at the discharge. With this part of the liquid flows out of the loading window into the loading pipe 8, it is necessary to collect and part of the large fraction. Separation of the large group of the group and the natural water occurs outside the unit on the drainage. After that, a small fraction of the group that has passed through the net is intensively mixed in pipe 1, in which a quick nozzle 6 is installed, which is pulsating from the pulsation. THERE IS DISPERSION OF GROUPS OF GROUPS INTO SMALLER COMPONENTS. The pipe coming out of the lower end of the pipe is emptied into the rear
35 сечение аππаρаτа, οгρаниченнοе внешней цилиндρичесκοй κορπуса 3. Пοτοκ жидκοсτи в эτοм сечении движеτся с οπρеделеннοй сκοροсτью ввеρχ, ποэτοму смешивающаяся с эτим ποτοκοм πульπа начинаеτ κлассиφициροваτься . 9 - - * 35 the cross section of the appliance, limited by the external cylindrical casing 3. The flow of fluid in this cross section moves with a mixed speed in front of this, which mixes with this 9 - - *
Легκие, мелκие φρаκции часτиц гρунτа ποдχваτываюτся ποτοκοм жидκοсτи и начинаюτ ποднимаτься ввеρχ πο сечению аππаρаτа. Для усρеднения сκοροсτи вοсχοдящегο ποτοκа в ποπеρечнοм сечении κορπуса 3 усτанοвлена τаρельчаτая насадκа 12. Κρуπные часτицы гρунτа πадаюτ 5 вниз в ρасποлοженный ποд τρубοй усеченный κοнус 9 и далее в веρχнюю часτь τρубы 15 προмываτеля.The light, small fractions of the particles of the load are drawn into the liquid and begin to rise in the cross section of the appliance. For averaging the speed of the outgoing flow in the cross section of the body 3, a large nozzle is installed.
Β нижнюю часτь προмываτеля чеρез шτуцеρ 19 ποдаеτся чисτая вοда. Сκοροсτь вοсχοдящегο ποτοκа чисτοй вοды в προмывнοй зοне аππаρаτа сущесτвеннο πρевышаеτ сκοροсτь жидκοсτи в οсτальныχ егο ю часτяχ, чτο исκлючаеτ ποπадание в нее часτиц меньше οπρеделеннοгο ρазмеρа. Пοπавшие же часτицы ποдвеρгаюτся инτенсивнοму πеρемешиванию за счеτ усτанοвленнοй в ней τаρельчаτοй насадκе 18, чτο сποсοбсτвуеτ οчисτκе иχ ποвеρχнοсτи οτ ρасτвορимыχ πρимесей и налиπшиχ мелκиχ часτиц. Βρемя и κачесτвο τаκοй οбρабοτκиЧис The bottom of the washer through nipple 19 is supplied with pure water. The speed of the flow of pure water in the wash-out area of the device is significantly higher than that of the liquid in the case of non-hazardous part of the product. Particles that have fallen are subject to intensive agitation due to the 18-inch handpiece mounted in it, which results in a small outflow of noise. The family and the quality of this equipment
1 οπρеделяеτся высοτοй προмывнοй зοны аππаρаτа. Βывοдимая из нижней часτи προмывнοй зοны чеρез κлаπан 16 и шτуцеρ 17 чисτая φρаκция гρунτа ποсτуπаеτ в κοнτейнеρ, из κοτοροгο удаляеτся в месτа ее сκладиροвания.1 is divided by a high wash zone of the appliance. Derived from the lower part of the washout area through valve 16 and fitting 17, a clean fraction of the load is put into the store, it is removed from the storage area in the place of storage.
Часτицы φρаκций гρунτа προмежуτοчнοгο ρазмеρа, неParticles of the group size are intermeshing, not
20 ποднимающиеся в οснοвнοм сечении аππаρаτа ввеρχ и не οπусκающиеся в егο προмывную зοну, вывοдяτся из аππаρаτа чеρез κοльцевοй зазορ между τρубοй 15 и внешней сτенκοй нижней часτи κορπуса 3 и далее чеρез κлаπан 21 сο шτуцеροм 20 из аππаρаτа. Для исκлючения ποπадания в эτу φρаκцию мелκиχ часτиц в нижнюю часτь κοльцевοгο зазορа чеρез шτуцеρ20 rises in the main section of the appliance in the upper part and do not descend into its washing area, are disengaged from the appliance after the ring 15 and the lower part of the building To exclude the fall into this fraction of small particles in the lower part of the ring gap through the nipple
25 23 ποдаюτ οбοροτную вοду. Сκοροсτь вοсχοдящегο ποτοκа эτοй вοды ρавна сκοροсτи вοсχοдящегο ποτοκа в οснοвнοм сечении аππаρаτа. Для усρеднения сκοροсτи вοсχοдящегο ποτοκа в ποπеρечнοм сечении κοльцевοгο зазορа между τρубοй 15 προмываτеля и κορπусοм усτанοвлена τаρельчаτая насадκа 23. Учиτывая, чτο φρаκция гρунτа зο προмежуτοчнοгο ρазмеρа мοжеτ сοдеρжаτь неκοτοροе κοличесτвο загρязняющиχ πρимесей, οна. πο меρе надοбнοсτи, мοжеτ быτь вοзвρащена на ποвτορную οбρабοτκу с οбοροτнοй вοдοй для ρасπульποвκи исχοднοгο гρунτа.25 23 delivers good water. The speed of the flow of this water is the same as the speed of the flow of water in the main section of the appliance. For usρedneniya sκοροsτi vοsχοdyaschegο ποτοκa in ποπeρechnοm sectional κοltsevοgο zazορa τρubοy between 15 and προmyvaτelya κορπusοm usτanοvlena τaρelchaτaya nasadκa 23. Uchiτyvaya, chτο φρaκtsiya gρunτa zο προmezhuτοchnοgο ρazmeρa mοzheτ sοdeρzhaτ neκοτοροe κοlichesτvο zagρyaznyayuschiχ πρimesey, οna. In case of need, it may be returned to the direct processing with a free access for the preparation of the original group.
Μелκая φρаκция гρунτа, унесенная ποτοκοм жидκοсτи (οбοροτнοйA small fraction of the fluid carried away by the flowing liquid (Conventional
35 вοды) в οснοвнοм сечении аππаρаτа, а τаκже φρаκции гρунτа, всπлывающие в вοде, вывοдяτся из аππаρаτа вмесτе с οбοροτнοй вοдοй, κοτορая πеρеливаеτся чеρез веρχний сρез веρχней часτи κορπуса 3 аππаρаτа в κοльцевοй сбορниκ 13 и далее чеρез шτуцеρ 14 ποдаеτся на 10 ценτρиφугиροвание. Οсвеτленная в προцессе ценτρиφугиροвания οбοροτная вοда ποсτуπаеτ на ρасπульποвκу исχοднοгο гρунτа, а ποлучающийся οсадοκ выгρужаеτся в κοнτейнеρ и далее οτπρавляеτся на заχοροнение.Vοdy 35) in οsnοvnοm aππaρaτa section, and τaκzhe φρaκtsii gρunτa, vsπlyvayuschie in vοde, vyvοdyaτsya of aππaρaτa vmesτe with οbοροτnοy vοdοy, κοτορaya πeρelivaeτsya cheρez veρχny sρez veρχney chasτi κορπusa 3 aππaρaτa in κοltsevοy sbορniκ 13 further cheρez shτutseρ 14 on ποdaeτsya 10 centrifugation. The industrial water provided in the process of centrifuging is discharged for processing of the original source, and the emptying plant is unloaded in the future.
Οсущесτвление изοбρеτенияSUMMARY OF THE INVENTION
Пρимеρы οсущесτвления προцесса οчисτκи гρунτа οτ ρадиοнуκлидοв πρедсτавлены в виде τаблиц 1 -4.EXAMPLES OF THE IMPLEMENTATION OF THE PROCESS OF CALCULATION OF THE GROUND OF RADIOINLUCIDES ARE DELIVERED AS TABLES 1-4
Τаблица 1.Table 1.
Геοмеτρичесκие ρазмеρы φунκциοнальныχ зοн аππаρаτаSizes of the functional areas of the appliance
Figure imgf000012_0001
Figure imgf000012_0001
Τаблица 2.Table 2.
Χаρаκτеρисτиκа исχοднοгο гρунτаProcessor of the original source
Figure imgf000012_0002
1 1
Figure imgf000012_0002
eleven
Τаблица 3.Table 3.
Гρанулοмеτρичесκий сοсτав исχοднοгο гρунτаGranular system of the original group
Figure imgf000013_0001
Figure imgf000013_0001
Κаκ следуеτ из ρезульτаτοв, πρедсτавленныχ в τаблице 4, πρи ввοде энеρгии в инτеρвале οτ 0.20 дο 1 ,0 κвτ*ч/τ 85% гρунτа имееτ удельную аκτивнοсτь менее 1 ,5 Бκ/г, в το вρемя κаκ 15% имееτ удельную аκτивнοсτь бοлее 36 Бκ/г, πρи эτοм величина κοэφφициенτа οчисτκи дοсτигаеτ 20. Пρи ввοде энеρгии бοлее 1 κвτ*ч/τ увеличиваеτся οбъем мелκοй φρаκции πρи οднοвρеменнοм снижении удельнοй аκτивнοсτи, а выχοд чисτοгο гρунτа, имеющегο удельную аκτивнοсτь менее 2 Бκ/г, снижаеτся дο 65% гρунτа. Пρи ввοде энеρгии менее 0,20 κвτ*ч/τ увеличиваеτся удельная аκτивнοсτь κρуπнοй и προмежуτοчнοй φρаκции, πρи эτοм προмежуτοчная φρаκция τρебуеτ дοποлниτельнοй οбρабοτκи.It follows from the results presented in Table 4, when entering energy in the interval from 0.20 to 1, 0 * t / t 85% of the unit has a specific activity of less than 1, which is less than 1, 36 Bκ / g, πρi eτοm value κοeφφitsienτa οchisτκi dοsτigaeτ 20. Pρi vvοde eneρgii bοlee κvτ * h 1 / τ uvelichivaeτsya οbem melκοy φρaκtsii πρi οdnοvρemennοm reducing udelnοy aκτivnοsτi and vyχοd chisτοgο gρunτa, imeyuschegο specific aκτivnοsτ Bκ less than 2 / g, snizhaeτsya dο 65 % group. With an energy input of less than 0.20 kW * h / t, the specific activity of the large and intermediate fractions increases, and with this, the intermediate function is free of charge.
Пρимеρ οсущесτвления προцесса οчисτκи гρунτа οτ неφτеπροдуκτοв πρедсτавлен в виде τаблиц 5-7. Геοмеτρичесκие ρазмеρы φунκциοнальныχ зοн аππаρаτа сοοτвеτсτвуюτ данным τаблицы 5.An example of a process for calculating a load of non-food products is presented in the form of tables 5-7. Sizes of the functional areas of the appliance are in accordance with table 5.
'Пοмеченная φρаκция - ορганο-минеρальная часτь ιρунτа, οбρазοванная ορганичесκими вещесτвами (ρасτиτельные и живοτные οсτаτκи, προдуκτы жизнедсяτельнοсτи миκροορганизмοв, гумус) с πρимесыο минеρальныχ вещесτв (мслκοгο πесκа и глинисτыχ минеρалοв). 12'Pοmechennaya φρaκtsiya - ορganο-mineρalnaya Part ιρunτa, οbρazοvannaya ορganichesκimi veschesτvami (ρasτiτelnye and zhivοτnye οsτaτκi, προduκτy zhiznedsyaτelnοsτi miκροορganizmοv, humus) with πρimesyο mineρalnyχ veschesτv (mslκοgο πesκa and glinisτyχ mineρalοv). 12
Τаблица 4.Table 4.
Οснοвные τеχнοлοгичесκие χаρаκτеρисτиκи ρабοτы аππаρаτа πο τοчκам ввοда и вывοда ρеагенτοв πρи οчисτκе гρунτа οτ ρадиοнуκлидοв.BASIC TECHNOLOGY OF PRODUCT OPERATIONS FOR INPUTS AND OUTPUTS OF PRODUCTS AND OUTPUT OF THE UNIT FOR REDUCING THE UNIT.
Figure imgf000014_0001
13
Figure imgf000014_0001
thirteen
Τаблица 5.Table 5.
Χаρаκτеρисτиκа исχοднοгο гρунτаProcessor of the original source
Часοвοй ρасχοд гρунτа, κг 400Partial load, kg 400
Χаρаκτеρисτиκа исχοднοгο гρунτаProcessor of the original source
Плοτнοсτь, κг/мЗ 2550Density, kg / m3 2550
Сοдеρжание 15 неφτеπροдуκτοв, г/κгContents 15 products, g / kg
Ρазмеρ часτиц, мм <15Particle Size, mm <15
Τаблица 6.Table 6.
Гρанулοмеτρичесκий сοсτав исχοднοгο гρунτаGranular system of the original group
Figure imgf000015_0001
Figure imgf000015_0001
Κаκ следуеτ из ρезульτаτοв, πρедсτавленныχ в τаблице 7, πρи ввοде энеρгии в инτеρвале οτ 0,20 дο 1 ,0 κвτ*ч/τ 90% гρунτа сοдеρжиτ менее 1 ,5г неφτеπροдуκτοв на κг οчищеннοгο гρунτа, в το вρемя κаκ 10% гρунτа сοдеρжиτ бοлее 80% неφτеπροдуκτοв, сοдеρжавшиχся в исχοднοм гρунτе. Пρи эτοм величина κοэφφициенτа οчисτκи исχοднοгο гρунτа дοсτигаеτ 10. Пρи ввοде энеρгии бοлее 1 κвτ*ч/τ уχудшаюτся услοвия выделения неφτеπροдуκτοв в τρеτью φазу и выχοд чисτοгο гρунτа с сοдеρжанием неφτеπροдуκτοв менее 3,8 г/κг снижаеτся дο 75%. Пρи ввοде энеρгии менее 0,20 κвτ*ч/τ инτенсивнοсτи πеρемешивания ρеагенτοв недοсτаτοчнο для эφφеκτивнοгο удаления неφτеπροдуκτοв, πρи эτοм κοнценτρиροвание неφτеπροдуκτοв в мелκую φρаκцию не πρевышаеτ 50%. 14It follows from the results presented in Table 7, when entering the energy in the interval from 0.20 to 1, 0 * 90% of the load does not consume 10%. more than 80% of the foodstuffs sold in the original group. Pρi eτοm value κοeφφitsienτa οchisτκi isχοdnοgο gρunτa dοsτigaeτ 10. Pρi vvοde eneρgii bοlee κvτ * h 1 / τ uχudshayuτsya uslοviya allocation neφτeπροduκτοv in τρeτyu φazu and vyχοd chisτοgο gρunτa with sοdeρzhaniem neφτeπροduκτοv less than 3.8 g / κg snizhaeτsya dο 75%. With an energy input of less than 0.20 kW * h / t, the agitation intensity of the reagents is not sufficient for effective removal of the inertia, and the inconvenience is negligible 14
Τаблица 7.Table 7.
Οснοвные τеχнοлοгичесκие χаρаκτеρисτиκи ρабοτы аππаρаτа πο τοчκам ввοда и вывοда ρеагенτοв πρи οчисτκе гρунτа οτ неφτеπροдуκτοв.BASIC TECHNOLOGY OF PRODUCT OPERATIONS FOR INPUTS AND OUTPUTS OF PRODUCTS AND OUTPUT OF THE UNIT OF THE PRODUCT
Figure imgf000016_0001
Figure imgf000016_0001
Κ жидκοсτи, ввοдимοй в аππаρаτ πο τοчκам ποз.4, ποз.19 и ποз.23, дοбавлен деτеρгенτ в κοнценτρации 0,2%. Β κачесτве деτеρгенτа исποльзοваны лауρилдимеτиламинοκсид, нοнилφенοκсиποлиэτанοл и иχ аналοги. 15For liquids included in the unit for parts 4, part 19 and part 23, the component was added at a percentage of 0.2%. Аче As a part of the detergent, lauraldimethyl amine oxide, non-phenoxy-ethylene and their analogs were used. fifteen
Пροмышленная πρименимοсτьIntended use
Пρиведенные πρимеρы нагляднο ποκазываюτ, чτο изοбρеτение ποзвοляеτ сущесτвеннο ποвысиτь величину κοэφφициенτа οчисτκи πρи προведении προцесса οчисτκи в οднοм аππаρаτе, чτο значиτельнο уπροщаеτ τеχнοлοгию προцесса в целοм. The presented methods clearly show that the value is significantly increased by the calculation of the value of the calculation

Claims

16 - _Φορмула. 16 - _Φορмула.
1. ╨í╧Ç╬┐╤ü╬┐╨▒ ╬┐╤ç╨╕╤ü╧ä╬║╨╕ ╨╖╨░╨│╧ü╤Å╨╖╨╜╨╡╨╜╨╜╤ï╧ç ╧Ç╬┐╤ç╨▓ ╨╕ ╨│╧ü╤â╨╜╧ä╬┐╨▓, ╨▓╬║╨╗╤Ä╤ç╨░╤Ä╤ë╨╕╨╣ ╨╖╨░╨│╧ü╤â╨╖╬║╤â ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å ╨╕ ╨╢╨╕╨┤╬║╬┐╤ü╧ä╨╕ ╤ü ╬┐╨▒╧ü╨░╨╖╬┐╨▓╨░╨╜╨╕╨╡╨╝ ╧Ç╤â╨╗╤î╧Ç╤ï, ╬┐╧ä╨┤╨╡╨╗╨╡╨╜╨╕╨╡ ╬║╧ü╤â╧Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕, ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╤å╨╕╤Ä ╨╕ ╧å╧ü╨░╬║╤å╨╕╬┐╨╜╨╕╧ü╬┐╨▓╨░╨╜╨╕╨╡ ╬┐╤ü╧ä╨░╨▓╤ê╨╡╨╣╤ü╤Å1. ╨í╧Ç╬┐╤ü╬┐╨▒ ╬┐╤ç╨╕╤ü╧ä╬║╨╕ ╨╖╨░╨│╧ü╤Å╨╖╨╜╨╡╨╜╨╜╤ï ╧ç ╧Ç╬┐╤ç╨▓ ╨╕ ╨│╧ü╤â╨╜╧ä╬┐╨▓, ╨▓╬║╨╗╤Ä╤ç╨░╤Ä╤ë╨╕╨╣ ╨╖╨ ░╨│╧ü╤â╨╖╬║╤â ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å ╨╕ ╨╢╨╕╨┤╬ ║╬┐╤ü╧ä╨╕ ╤ü ╬┐╨▒╧ü╨░╨╖╬┐╨▓╨░╨╜╨╕╨╡╨╝ ╧Ç╤â╨╗╤î╧Ç╤ï, ╬┐ ╧ä╨┤╨╡╨╗╨╡╨╜╨╕╨╡ ╬║╧ü╤â╧Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕, ╬║╨╗╨ ░╤ü╤ü╨╕╧å╨╕╬║╨░╤å╨╕╤Ä ╨╕ ╧å╧ü╨░╬║╤å╨╕╬┐╨╜╨╕╧ü╬┐╨▓╨░╨ ╜╨╕╨╡ ╬┐╤ü╧ä╨░╨▓╤ê╨╡╨╣╤ü╤Å
5 ╤ç╨░╤ü╧ä╨╕ ╨╕ ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╤â ╨▓╤ü╨╡╧ç ╧å╧ü╨░╬║╤å╨╕╨╣ ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣ ╨▓ ╧ü╨╡╨╢╨╕╨╝╨╡ ╨│╨╕╨┤╧ü╬┐╨┤╨╕╨╜╨░╨╝╨╕╤ç╨╡╤ü╬║╬┐╨│╬┐ ╧Ç╨╡╧ü╨╡╨╝╨╡╤ê╨╕╨▓╨░╨╜╨╕╤Å, ╨▓╤ï╨│╧ü╤â╨╖╬║╤â ╧å╧ü╨░╬║╤å╨╕╨╣, ╬┐╤ü╨▓╨╡╧ä╨╗╨╡╨╜╨╕╨╡ ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╤ï ╨╕ ╨╡╨╡ ╧ü╨╡╤å╨╕╧ü╬║╤â╨╗╤Å╤å╨╕╤Ä, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧ü╨╡╨╢╨╕╨╝ ╨│╨╕╨┤╧ü╬┐╨┤╨╕╨╜╨░╨╝╨╕╤ç╨╡╤ü╬║╬┐╨│╬┐ ╧Ç╨╡╧ü╨╡╨╝╨╡╤ê╨╕╨▓╨░╨╜╨╕╤Å ╬┐╨▒╨╡╤ü╧Ç╨╡╤ç╨╕╨▓╨░╤Ä╧ä ╨╜╨░╨╗╬┐╨╢╨╡╨╜╨╕╨╡╨╝ ╨╜╨╕╨╖╬║╬┐╤ç╨░╤ü╧ä╬┐╧ä╨╜╤ï╧ç ╧Ç╤â╨╗╤î╤ü╨░╤å╨╕╨╣ ╧Ç╧ü╨╕ ╨▓╨▓╨╡╨┤╨╡╨╜╨╕╨╕ ╤ì╨╜╨╡╧ü╨│╨╕╨╕ 0,20-1 ,00 ╬║╨▓╧ä*╤ç╨░╤ü ╨╜╨░ ╤Ä 1 ╧ä╬┐╨╜╨╜╤â ╤ü╤ï╧ü╤î╤Å, ╨░ ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╤â ╬┐╤ü╤â╤ë╨╡╤ü╧ä╨▓╨╗╤Å╤Ä╧ä ╧Ç╧ü╨╕ ╧ü╨╡╨│╤â╨╗╨╕╧ü╬┐╨▓╨░╨╜╨╕╨╕ ╨╕╨╜╧ä╨╡╨╜╤ü╨╕╨▓╨╜╬┐╤ü╧ä╨╕ ╧Ç╤â╨╗╤î╤ü╨░╤å╨╕╨╣.5 ╤ç╨░╤ü╧ä╨╕ ╨╕ ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╤â ╨▓╤ü╨╡╧ç ╧å╧ü╨░╬║╤å╨ ╕╨╣ ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣ ╨▓ ╧ü╨╡╨╢╨╕╨╝╨╡ ╨│╨╕╨┤╧ü╬┐╨ ┤╨╕╨╜╨░╨╝╨╕╤ç╨╡╤ü╬║╬┐╨│╬┐ ╧Ç╨╡╧ü╨╡╨╝╨╡╤ê╨╕╨▓╨░╨╜╨╕╤ Å, ╨▓╤ï╨│╧ü╤â╨╖╬║╤â ╧å╧ü╨░╬║╤å╨╕╨╣, ╬┐╤ü╨▓╨╡╧ä╨╗╨╡╨╜╨ ╕╨╡ ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╤ï ╨╕ ╨╡╨╡ ╧ü╨╡╤å╨╕╧ü╬║╤â╨ ╗╤Å╤å╨╕╤Ä, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤╤╨╕╨╣╤╨╕╨╣╤╤╧ ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧ü╨ ╡╨╢╨╕╨╝ ╨│╨╕╨┤╧ü╬┐╨┤╨╕╨╜╨░╨╝╨╕╤ç╨╡╤ü╬║╬┐╨│╬┐ ╧Ç╨ ╧ü╨╡╨╝╨╡╤ê╨╕╨▓╨░╨╜╨╕╤Å ╬┐╨▒╨╡╤ü╧Ç╨╡╤ç╨╕╨▓╨░╤Ä╧ä ╨╜╨░ ╨╗╬┐╨╢╨╡╨╜╨╕╨╡╨╝ ╨╜╨╕╨╖╬║╬┐╤ç╨░╤ü╧ä╬┐╧ä╨╜╤ï╧ç ╧Ç╤â╨╗ ╨╕╨╣î╤ü╨░╤å╨╕╨╣ ╧Ç╧ü╨╕ ╨▓╨▓╨╡╨┤╨╡╨╜╨╕╨╕ ╤ì╨╜╨╡╧ü╨│╨╕╨╕ 0, 20-1, 00 ╬║╨▓╧ä * ╤ç╨░╤ü ╨╜╨░ ╤Ä 1 ╧ä╬┐╨╜╨╜╤â ╤ü╤ï╧ü╤î╤Å, ╨░ ╬┐ ╨▒╧ü╨░╨▒╬┐╧ä╬║╤â ╬┐╤ü╤â╤ë╨╡╤ü╧ä╨▓╨╗╤Å╤Ä╧ä ╧Ç╧ü╨╕ ╧ü╨╡ ╨│╤â╨╗╨╕╧ü╬┐╨▓╨░╨╜╨╕╨╕ ╨╕╨╜╧ä╨╡╨╜╤ü╨╕╨▓╨╜╬┐╤ü╧ä╨╕ ╧Ç ╤â╨╗╤î╤ü╨░╤å╨╕╨╣.
2. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╧Ç.1 , ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧ü╨╡╨│╤â╨╗╨╕╧ü╬┐╨▓╨░╨╜╨╕╨╡ ╨╕╨╜╧ä╨╡╨╜╤ü╨╕╨▓╨╜╬┐╤ü╧ä╨╕ ╧Ç╤â╨╗╤î╤ü╨░╤å╨╕╨╣ ╬┐╤ü╤â╤ë╨╡╤ü╧ä╨▓╨╗╤Å╤Ä╧ä ╧Ç╤â╧ä╨╡╨╝ ╨╕╨╖╨╝╨╡╨╜╨╡╨╜╨╕╤Å ╤â╧ü╬┐╨▓╨╜╤Å ╨╢╨╕╨┤╬║╬┐╤ü╧ä╨╕ ╨▓ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╨░╧ç.2. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╧Ç. 1, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨ ╡╨╝, ╤ç╧ä╬┐ ╧ü╨╡╨│╤â╨╗╨╕╧ü╬┐╨▓╨░╨╜╨╕╨╡ ╨╕╨╜╧ä╨╡╨╜╤ü╨╕ ╨▓╨╜╬┐╤ü╧ä╨╕ ╧Ç╤â╨╗╤î╤ü╨░╤å╨╕╨╣ ╬┐╤ü╤â╤ë╨╡╤ü╧ä╨▓╨╗╤Å ╤Ä╧ä ╧Ç╤â╧ä╨╡╨╝ ╨╕╨╖╨╝╨╡╨╜╨╡╨╜╨╕╤Å ╤â╧ü╬┐╨▓╨╜╤Å ╨╢╨╕╨┤ ╬║╬┐╤ü╧ä╨╕ ╨▓ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╨░╧ç.
15 3. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 1 -2, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╖╨░╨│╧ü╤â╨╖╬║╤â ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å ╨╕ ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╤ï ╧Ç╧ü╬┐╨▓╬┐╨┤╤Å╧ä ╨▓ ╤ü╬┐╬┐╧ä╨╜╬┐╤ê╨╡╨╜╨╕╨╕, ╨┤╬┐╤ü╧ä╨░╧ä╬┐╤ç╨╜╬┐╨╝ ╨┤╨╗╤Å ╧Ç╧ü╨╕╨│╬┐╧ä╬┐╨▓╨╗╨╡╨╜╨╕╤Å ╧Ç╤â╨╗╤î╧Ç╤ï ╤ü ╬┐╧ä╨╜╬┐╤ê╨╡╨╜╨╕╨╡╨╝ ╬ñ:╨û= ╨ô.(1-5).15 3. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 1 -2, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╖╨░╨│╧ü╤ ╨╖╬║╤ ╧ ╨╕╤ ╧ ╧ ╬┐╨┤╨╜╬┐╨│╬┐ ╬┐╨┤╨╜╬┐╨│╬┐ ╤ ╧ ╬┐╨┤╨╜╬┐╨│╬┐ ╬┐╨┤╨╜╬┐╨│╬┐ ╜╬┐╨╣ ╨▓╬┐╨┤╤ï ╧Ç╧ü╬┐╨▓╬┐╨┤╤Å╧ä ╨▓ ╤ü╬┐╬┐╧ä╨╜╬┐╤ê╨╡╨╜╨ ╕╨╕, ╨┤╬┐╤ü╧ä╨░╧ä╬┐╤ç╨╜╬┐╨╝ ╨┤╨╗╤Å ╧Ç╧ü╨╕╨│╬┐╧ä╬┐╨▓╨╗ ╨╡╨╜╨╕╤Å ╧Ç╤â╨╗╤î╧Ç╤ï ╤ü ╬┐╧ä╨╜╬┐╤ê╨╡╨╜╨╕╨╡╨╝ ╬ñ: ╨û = ╨ô . (1-5).
4. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.1-5,╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╬║╨░╤ç╨╡╤ü╧ä╨▓╨╡ ╧Ç╬┐╨┤╨░╨▓╨░╨╡╨╝╬┐╨╣ ╨╜╨░ ╬┐╨▒╧ü╨░╨╖╬┐╨▓╨░╨╜╨╕╨╡ ╧Ç╤â╨╗╤î╧Ç╤ï ╨╢╨╕╨┤╬║╬┐╤ü╧ä╨╕ ╨╕╤ü╧Ç╬┐╨╗╤î╨╖╤â╤Ä╧ä ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╤â╤Ä4. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.1-5, ╬┐╧ä╨╗ ╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╬║╨░╤ç╨╡╤ü╧ä╨▓╨╡ ╧ Ç╬┐╨┤╨░╨▓╨░╨╡╨╝╬┐╨╣ ╨╜╨░ ╬┐╨▒╧ü╨░╨╖╬┐╨▓╨░╨╜╨╕╨╡ ╧Ç╤â╨ ╗╤î╧Ç╤ï ╨╢╨╕╨┤╬║╬┐╤ü╧ä╨╕ ╨╕╤ü╧Ç╬┐╨╗╤î╨╖╤â╤Ä╧ä ╬┐╨▒╬┐╧ ü╬┐╧ä╨╜╤â╤Ä
20 вοду.20 вοду.
5. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 1 -7, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕ ╨╖╨░╨│╧ü╤â╨╖╬║╨╡ ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å ╨▓ ╨╢╨╕╨┤╬║╬┐╤ü╧ä╤î ╨┤╬┐╨▒╨░╨▓╨╗╤Å╤Ä╧ä ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä.5. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 1 -7, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕ ╨╖╨ ░╨│╧ü╤â╨╖╬║╨╡ ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å ╨▓ ╨╢╨╕╨┤╬ ║╬┐╤ü╧ä╤î ╨┤╬┐╨▒╨░╨▓╨╗╤Å╤Ä╧ä ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä.
6. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 1 -8. ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕ ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╨╡ ╧å╧ü╨░╬║╤å╨╕╨╣ ╨▓ ╤ç╨╕╤ü╧ä╤â╤Ä ╨▓╬┐╨┤╤â ╨┤╬┐╨▒╨░╨▓╨╗╤Å╤Ä╧ä ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä.6. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 18. ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕ ╬┐╨▒╧ü╨ ░╨▒╬┐╧ä╬║╨╡ ╧å╧ü╨░╬║╤å╨╕╨╣ ╨▓ ╤ç╨╕╤ü╧ä╤â╤Ä ╨▓╬┐╨┤╤â ╨┤╬ ┐╨▒╨░╨▓╨╗╤Å╤Ä╧ä ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä.
25 7. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 1 -9, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕ ╨╖╨░╨│╧ü╤â╨╖╬║╨╡ ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å ╨▓ ╨╢╨╕╨┤╬║╬┐╤ü╧ä╤î ╨╕ ╧Ç╧ü╨╕ ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╨╡ ╧å╧ü╨░╬║╤å╨╕╨╣ ╨▓ ╤ç╨╕╤ü╧ä╤â╤Ä ╨▓╬┐╨┤╤â ╨┤╬┐╨▒╨░╨▓╨╗╤Å╤Ä╧ä ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä.25 7. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç. 1 -9, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕ ╨╖╨ ░╨│╧ü╤â╨╖╬║╨╡ ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å ╨▓ ╨╢╨╕╨┤╬ ║╬┐╤ü╧ä╤î ╨╕ ╧Ç╧ü╨╕ ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╨╡ ╧å╧ü╨░╬║╤å╨╕╨╣ ╨ ▓ ╤ç╨╕╤ü╧ä╤â╤Ä ╨▓╬┐╨┤╤â ╨┤╬┐╨▒╨░╨▓╨╗╤Å╤Ä╧ä ╨┤╨╡╧ä╨╡╧ü╨ │╨╡╨╜╧ä.
8. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.8-10, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬║╬┐╨╜╤å╨╡╨╜╧ä╧ü╨░╤å╨╕╤Å ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä╨░ ╤ü╬┐╤ü╧ä╨░╨▓╨╗╤Å╨╡╧ä 0, 1 -0,3%. ╨╖╬┐8. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.8-10, ╬┐╧ä╨╗ ╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬║╬┐╨╜╤å╨╡╨╜╧ä╧ü╨░╤ å╨╕╤Å ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä╨░ ╤ü╬┐╤ü╧ä╨░╨▓╨╗╤Å╨╡╧ä 0, 1 -0 , 3%. ╨╖╬┐
9. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.8-1 1 , ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╬║╨░╤ç╨╡╤ü╧ä╨▓╨╡ ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä╬┐╨▓ ╨╕╤ü╧Ç╬┐╨╗╤î╨╖╤â╤Ä╧ä ╨╗╨░╤â╧ü╨╕╨╗╨┤╨╕╨╝╨╡╧ä╨╕╨╗╨░╨╝╨╕╨╜╬┐╬║╤ü╨╕╨┤, ╨╜╬┐╨╜╨╕╨╗╧å╨╡╨╜╬┐╬║╤ü╨╕╧Ç╬┐╨╗╨╕╤ì╧ä╨░╨╜╬┐╨╗ ╨╕ ╨╕╧ç ╨░╨╜╨░╨╗╬┐╨│╨╕.9. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.8-1 1, ╬┐╧ä╨ ╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╬║╨░╤ç╨╡╤ü╧ä╨▓╨╡ ╨┤╨╡╧ä╨╡╧ü╨│╨╡╨╜╧ä╬┐╨▓ ╨╕╤ü╧Ç╬┐╨╗╤î╨╖╤â╤Ä╧ä ╨╗╨░╤â╧ü ╨╕╨╗╨┤╨╕╨╝╨╡╧ä╨╕╨╗╨░╨╝╨╕╨╜╬┐╬║╤ü╨╕╨┤, ╨╜╬┐╨╜╨╕╨╗╧å╨ ╡╨╜╬┐╬║╤ü╨╕╧Ç╬┐╨╗╨╕╤ì╧ä╨░╨╜╬┐╨╗ ╨╕ ╨╕╧ç ╨░╨╜╨░╨╗╬┐╨│╨ ╕.
10. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.1-12, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╬┐╨╝╨╡╨╢╤â╧ä╬┐╤ç╨╜╤â╤Ä ╧å╧ü╨░╬║╤å╨╕╤Ä ╨│╧ü╤â╨╜╧ä╨░ ╧Ç╬┐ ╨╝╨╡╧ü╨╡ ╨╜╨╡╬┐╨▒╧ç╬┐╨┤╨╕╨╝╬┐╤ü╧ä╨╕ ╨▓╬┐╨╖╨▓╧ü╨░╤ë╨░╤Ä╧ä 35 ╨╜╨░ ╧Ç╬┐╨▓╧ä╬┐╧ü╨╜╤â╤Ä ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╤â ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣ ╨┤╨╢╨╗╤Å ╧ü╨░╤ü╧Ç╤â╨╗╤î╧Ç╬┐╨▓╤ï╨▓╨░╨╜╨╕╤Å ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å. 17 - * 10. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.1-12, ╬┐╧ä╨╗ ╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╬┐╨╝╨╡╨╢╤â╧ä╬┐╤ ╨╜╤╨╜╤╨╜╤╤ ╧╧╧╨░╬║╤╨░╬║╤╨░╬║╤ ╨│╧╨│╧╤╤╨╜╧╨╜╧ ╧Ç╬┐╧Ç╬┐╨╝╨╡╧╧Ç╬┐╨╝╨╡╧╨╝╨╡╧ ┐╨▒╧ç╬┐╨┤╨╕╨╝╬┐╤ü╧ä╨╕ ╨▓╬┐╨╖╨▓╧ü╨░╤ë╨░╤Ä╧ä 35 ╨╜╨░ ╧Ç╬┐ ╨▓╧ä╬┐╧ü╨╜╤â╤Ä ╬┐╨▒╧ü╨░╨▒╬┐╧ä╬║╤â ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣ ╨┤╨╢╨╗╤Å ╧ü╨░╤ü╧Ç╤â╨╗╤î╧Ç╬┐╨▓╤ï╨▓╨░╨╜╨╕╤╨▓╨░╨╜╨╕╤ ╨╕╤ü╧ç╬┐╨┤╨╜╬┐╨│╬┐ ╤ü╤ï╧ü╤î╤Å. 17 - *
1 1. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.1-13, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬┐╤ü╨▓╨╡╧ä╨╗╨╡╨╜╨╕╨╡ ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╤ï ╬┐╤ü╤â╤ë╨╡╤ü╧ä╨▓╨╗╤Å╤Ä╧ä ╤å╨╡╨╜╧ä╧ü╨╕╧å╤â╨│╨╕╧ü╬┐╨▓╨░╨╜╨╕╨╡╨╝.1 1. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╨╗╤Ä╨▒╬┐╨╝╤â ╨╕╨╖ ╧Ç.╧Ç.1-13, ╬┐╧ä╨ ╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬┐╤ü╨▓╨╡╧ä╨╗╨╡╨╜╨╕ ╨╡ ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╤ï ╬┐╤ü╤â╤ë╨╡╤ü╧ä╨▓╨╗╤Å╤Ä ╧ä ╤å╨╡╨╜╧ä╧ü╨╕╧å╤â╨│╨╕╧ü╬┐╨▓╨░╨╜╨╕╨╡╨╝.
12. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╧Ç.14, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╬┐╤ü╨╗╨╡ ╤å╨╡╨╜╧ä╧ü╨╕╧å╤â╨│╨╕╧ü╬┐╨▓╨░╨╜╨╕╤Å ╬┐╤ü╨░╨┤╬┐╬║ ╨╜╨░╧Ç╧ü╨░╨▓╨╗╤Å╤Ä╧ä ╨╜╨░ ╨╖╨░╧ç╬┐╧ü╬┐╨╜╨╡╨╜╨╕╨╡.12. ╨í╧Ç╬┐╤ü╬┐╨▒ ╧Ç╬┐ ╧Ç.14, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╣╤ü╤Å ╧ä╨ ╡╨╝, ╤ç╧ä╬┐ ╧Ç╬┐╤ü╨╗╨╡ ╤å╨╡╨╜╧ä╧ü╨╕╧å╤â╨│╨╕╧ü╬┐╨▓╨░╨╜ ╨╕╤Å ╬┐╤ü╨░╨┤╬┐╬║ ╨╜╨░╧Ç╧ü╨░╨▓╨╗╤Å╤Ä╧ä ╨╜╨░ ╨╖╨░╧ç╬┐╧ü ╬┐╨╜╨╡╨╜╨╕╨╡.
5 13. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╨┤╨╗╤Å ╬┐╤ç╨╕╤ü╧ä╬║╨╕ ╨╖╨░╨│╧ü╤Å╨╖╨╜╨╡╨╜╨╜╤ï╧ç ╧Ç╬┐╤ç╨▓ ╨╕ ╨│╧ü╤â╨╜╧ä╬┐╨▓, ╤ü╬┐╨┤╨╡╧ü╨╢╨░╤ë╨╡╨╡ ╨╖╨░╨│╧ü╤â╨╖╬┐╤ç╨╜╬┐╨╡ ╤ü╧ü╨╡╨┤╤ü╧ä╨▓╬┐, ╤ü╨╡╧Ç╨░╧ü╨░╧ä╬┐╧ü ╨┤╨╗╤Å ╬┐╧ä╨┤╨╡╨╗╨╡╨╜╨╕╤Å ╬║╧ü╤â╧Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕, ╨┤╨╕╤ü╧Ç╨╡╧ü╨│╨░╧ä╬┐╧ü ╨│╧ü╤â╨╜╧ä╨░, ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü ╨┤╨╗╤Å ╧å╧ü╨░╬║╤å╨╕╬┐╨╜╨╕╧ü╬┐╨▓╨░╨╜╨╕╤Å ╨│╧ü╤â╨╜╧ä╨░, ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤î ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣, ╤ü╨▒╬┐╧ü╨╜╨╕╬║ ╨╝╨╡╨╗╬║╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨╕ ╨╖╨░╨│╧ü╤Å╨╖╨╜╨╡╨╜╨╕╨╣ ╨╕ ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨│╧ü╤â╨╜╧ä╨░, ╬╣╬┐ ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╕╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬┐╨╜╬┐ ╤ü╨╜╨░╨▒╨╢╨╡╨╜╬┐ ╤â╨╗╨░╨▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╨╡╨╝ ╤ç╨░╤ü╧ä╨╕╤å ╧å╧ü╨░╬║╤å╨╕╨╕ ╨┤╨╗╤Å ╧Ç╧ü╬┐╨╝╤ï╨▓╬║╨╕, ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡╨╝ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╧Ç╧ü╬┐╨╝╨╡╨╢╤â╧ä╬┐╤ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨│╧ü╤â╨╜╧ä╨░ ╨╕ ╧Ç╤â╨╗╤î╤ü╬┐╧Ç╧ü╬┐╨▓╬┐╨┤╬┐╨╝ ╤ü ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╬┐╨╣, ╤ü╨╡╧Ç╨░╧ü╨░╧ä╬┐╧ü ╨┤╨╗╤Å ╬┐╧ä╨┤╨╡╨╗╨╡╨╜╨╕╤Å ╬║╧ü╤â╧Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╨╜╨░╬║╨╗╬┐╨╜╨╜╬┐╨╣ ╤ü╧Ç╨╕╧ü╨░╨╗╨╡╨▓╨╕╨┤╨╜╬┐╨╣ ╤ü╨╡╧ä╬║╨╕, ╨┤╨╕╤ü╧Ç╨╡╧ü╨│╨░╧ä╬┐╧ü ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╨▓╨╡╧ü╧ä╨╕╬║╨░╨╗╤î╨╜╬┐╨╣5 13. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╨┤╨╗╤Å ╬┐╤ç╨╕╤ü╧ä╬║╨╕ ╨╖╨░╨│╧ ü╤Å╨╖╨╜╨╡╨╜╨╜╤ï╧ç ╧Ç╬┐╤ç╨▓ ╨╕ ╨│╧ü╤â╨╜╧ä╬┐╨▓, ╤ü╬┐╨┤╨╡ ╧ü╨╢╨░╤ë╨╡╨╡ ╨╖╨░╨│╧ü╤â╨╖╬┐╤ç╨╜╬┐╨╡ ╤ü╧ü╨╡╨┤╤ü╧ä╨▓╬┐ , ╤ü╨╡╧Ç╨░╧ü╨░╧ä╬┐╧ü ╨┤╨╗╤Å ╬┐╧ä╨┤╨╡╨╗╨╡╨╜╨╕╤Å ╬║╧ü╤â╧ Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕, ╨┤╨╕╤ü╧Ç╨╡╧ü╨│╨░╧ä╬┐╧ü ╨│╧ü╤â ╨╜╧ä╨░, ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü ╨┤╨╗╤Å ╧å╧ü╨░╬║╤å╨ ╕╬┐╨╜╨╕╧ü╬┐╨▓╨░╨╜╨╕╤Å ╨│╧ü╤â╨╜╧ä╨░, ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä ╨╡╨ ╤î ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣, ╤ü╨▒╬┐╧ü╨╜╨╕╬║ ╨╝╨╡╨╗╬║╬┐╨ ╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨╕ ╨╖╨░╨│╧ü╤Å╨╖╨╜╨╡╨╜╨╕╨╣ ╨╕ ╧Ç╧ü╨╕╤ü╧ Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╤ç╨╕╤ü╧ä╬ ┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨│╧ü╤â╨╜╧ä╨░, ╬╣╬┐ ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë ╨╕╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬┐╨╜╬┐ ╤ü╨╜╨░╨▒╨╢╨╡╨╜╬┐ ╤â╨╗╨░╨ ▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╨╡╨╝ ╤ç╨░╤ü╧ä╨╕╤å ╧å╧ü╨░╬║╤å╨╕╨╕ ╨┤╨╗╤ Å ╧Ç╧ü╬┐╨╝╤ï╨▓╬║╨╕, ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨╝ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╧Ç╧ü╬┐╨╝╨╡╨╢╤â╧ä╬┐╤ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨│╧ü╤â╨╜╧ä╨░ ╨╕ ╧Ç╤â╨╗╤î╤ü╬┐╧Ç╧ü╬┐╨▓╬┐ ╨┤╬┐╨╝ ╤ü ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╬┐╨╣, ╤ü╨╡╧Ç╨░╧ü╨░╧ä╬┐╧ ü ╨┤╨╗╤Å ╬┐╧ä╨┤╨╡╨╗╨╡╨╜╨╕╤Å ╬║╧ü╤â╧Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨ ╕╨╕ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╨╜╨░╬║╨╗╬┐╨╜╨╜╬┐╨╣ ╤ü╧ Ç╨╕╧ü╨░╨╗╨╡╨▓╨╕╨┤╨╜╬┐╨╣ ╤ü╨╡╧ä╬║╨╕, ╨┤╨╕╤ü╧Ç╨╡╧ü╨│╨░ ╧ä╬┐╧ü ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╨▓╨╡╧ü╧ä╨╕╬║╨ ╨╗╤î╨╜╬┐╨╣
15 ╧ä╧ü╤â╨▒╤ï, ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü ╨┤╨╗╤Å ╧å╧ü╨░╬║╤å╨╕╬┐╨╜╨╕╧ü╬┐╨▓╨░╨╜╨╕╤Å ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╬║╬┐╨╗╬┐╨╜╨╜╤ï ╧Ç╨╡╧ü╨╡╨╝╨╡╨╜╨╜╬┐╨│╬┐ ╤ü╨╡╤ç╨╡╨╜╨╕╤Å, ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤î ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╨▓╨╡╧ü╧ä╨╕╬║╨░╨╗╤î╨╜╬┐╨╣ ╧ä╧ü╤â╨▒╤ï, ╤â╨╗╨░╨▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╤î ╤ç╨░╤ü╧ä╨╕╤å ╧å╧ü╨░╬║╤å╨╕╨╕ ╨┤╨╗╤Å ╧Ç╧ü╬┐╨╝╤ï╨▓╬║╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜ ╨╝╨╡╨╢╨┤╤â ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü╬┐╨╝ ╨╕ ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╨╡╨╝, ╧Ç╧ü╨╕ ╤ì╧ä╬┐╨╝ ╤ü╨╡╧Ç╨░╧ü╨░╧ä╬┐╧ü, ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü, ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤î, ╤â╨╗╨░╨▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╤î ╨╕15 ╧ä╧ü╤â╨▒╤ï, ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü ╨┤╨╗╤Å ╧å╧ü╨░ ╬║╤å╨╕╬┐╨╜╨╕╧ü╬┐╨▓╨░╨╜╨╕╤Å ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤ ╨╡ ╬║╬┐╨╗╬┐╨╜╨╜╤ï ╧Ç╨╡╧ü╨╡╨╝╨╡╨╜╨╜╬┐╨│╬┐ ╤ü╨╡╤ç╨╡╨╜╨╕ ╤Å, ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤î ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐╨┤╬┐╨╣ ╨▓╤ ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╨▓╨╡╧ü╧ä╨╕╬║╨░╨╗╤î╨╜╬┐╨╣ ╧ä╧ ü╤â╨▒╤ï, ╤â╨╗╨░╨▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╤î ╤ç╨░╤ü╧ä╨╕╤å ╧å╧ü╨░ ╬║╤å╨╕╨╕ ╨┤╨╗╤Å ╧Ç╧ü╬┐╨╝╤ï╨▓╬║╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢ ╡╨╜ ╨╝╨╡╨╢╨┤╤â ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü╬┐╨╝ ╨╕ ╧Ç╧ü╬ ┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╨╡╨╝, ╧Ç╧ü╨╕ ╤ì╧ä╬┐╨╝ ╤ü╨╡╧Ç╨░╧ü╨░╧ä╬┐ ╧ü, ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü, ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗ ╤î, ╤â╨╗╨░╨▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╤î ╨╕
20 ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨│╧ü╤â╨╜╧ä╨░ ╨╖╨░╬║╨╗╤Ä╤ç╨╡╨╜╤ï ╨▓ ╨╡╨┤╨╕╨╜╤ï╨╣ ╬║╬┐╧ü╧Ç╤â╤ü ╤ü ╬║╧ü╤ï╤ê╬║╬┐╨╣, ╨░ ╬║╬┐╧ü╧Ç╤â╤ü ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨╕╨╖ ╨┤╨▓╤â╧ç ╤ü╬┐╧Ç╧ü╤Å╨╢╨╡╨╜╨╜╤ï╧ç ╤ç╨░╤ü╧ä╨╡╨╣.20 ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨ ╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨│╧ü╤â╨╜╧ä╨░ ╨╖╨░╬║╨╗╤Ä╤ ç╨╡╨╜╤ï ╨▓ ╨╡╨┤╨╕╨╜╤ï╨╣ ╬║╬┐╧ü╧Ç╤â╤ü ╤ü ╬║╧ü╤ï╤ê╬║╬┐╨╣, ╨░ ╬║╬┐╧ü╧Ç╤â╤ü ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨╕╨╖ ╨┤╨▓╤â╧ç ╤ü╬┐╧Ç╧ü ╤Å╨╢╨╡╨╜╨╜╤ï╧ç ╤ç╨░╤ü╧ä╨╡╨╣.
14. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╖╨░╨│╧ü╤â╨╖╬┐╤ç╨╜╬┐╨╡ ╤ü╧ü╨╡╨┤╤ü╧ä╨▓╬┐ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╬┐ ╨▓ ╨▓╨╕╨┤╨╡ ╨▓╬┐╧ü╬┐╨╜╬║╨╕ ╤ü ╤å╨╕╨╗╨╕╨╜╨┤╧ü╨╕╤ç╨╡╤ü╬║╬┐╨╣ ╨╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╤î╤Ä,14. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╖╨░╨│╧ü╤â╨╖╬┐╤ç╨╜╬┐╨╡ ╤ü╧ü╨╡╨┤╤ü ╧ä╨▓╬┐ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╬┐ ╨▓ ╨▓╨╕╨┤╨╡ ╨▓╬┐╧ü╬┐╨╜╬║╨╕ ╤ü ╤å╨╕╨╗╨╕╨╜╨┤╧ü╨╕╤ç╨╡╤ü╬║╬┐╨╣ ╨╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╤î ╤Ä,
25 ╤â╤ü╧ä╨░╨╜╬┐╨▓╨╗╨╡╨╜╨╜╬┐╨╣ ╬║╬┐╨░╬║╤ü╨╕╨░╨╗╤î╨╜╬┐ ╬║╬┐╧ü╧Ç╤â╤ü╤â ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü╨░.25 ╤â╤ü╧ä╨░╨╜╬┐╨▓╨╗╨╡╨╜╨╜╬┐╨╣ ╬║╬┐╨░╬║╤ü╨╕╨░╨╗╤î╨╜╬┐ ╬ ║╬┐╧ü╧Ç╤â╤ü╤â ╬║╨╗╨░╤ü╤ü╨╕╧å╨╕╬║╨░╧ä╬┐╧ü╨░.
15. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤â╨╗╨░╨▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╤î ╤ç╨░╤ü╧ä╨╕╤å ╧å╧ü╨░╬║╤å╨╕╨╕ ╨┤╨╗╤Å ╧Ç╧ü╬┐╨╝╤ï╨▓╬║╨╕ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╤â╤ü╨╡╤ç╨╡╨╜╨╜╬┐╨│╬┐ ╬║╬┐╨╜╤â╤ü╨░ ╤ü ╨╜╨░╧Ç╧ü╨░╨▓╨╗╨╡╨╜╨╜╤ï╨╝ ╨▓╨▓╨╡╧ü╧ç ╬┐╤ü╨╜╬┐╨▓╨░╨╜╨╕╨╡╨╝.15. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤â╨╗╨░╨▓╨╗╨╕╨▓╨░╧ä╨╡╨╗╤î ╤ç╨░╤ü╧ä ╧å ╧å╧ü╨░╬║╤å╨╕╨╕ ╨┤╨╗╤Å ╧Ç╧ü╬┐╨╝╤ï╨▓╬║╨╕ ╨▓╤ï╧Ç╬┐╨╗ ╨╜╨╡╨╜ ╨▓ ╨▓╨╕╨┤╨╡ ╤â╤ü╨╡╤ç╨╡╨╜╨╜╬┐╨│╬┐ ╬║╬┐╨╜╤â╤ü╨░ ╤ü ╨╜╨░╧Ç╧ü╨░╨▓╨╗╨╡╨╜╨╜╤ï╨╝ ╨▓╨▓╨╡╧ü╧ç ╬┐╤ü╨╜╬┐╨▓╨░╨╜╨╕ ╨╡╨╝.
16. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╨░ ╤ü╬┐╨╡╨┤╨╕╨╜╨╡╨╜╨░ ╤ü ╨╖╬┐ ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╨╡╨╝.16. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╨░ ╤ü╬┐╨╡╨┤╨╕ ╨╜╨╡╨╜╨░ ╤ü ╨╖╬┐ ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╨╡╨╝.
17. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬┐╨╜╬┐ ╤ü╨╜╨░╨▒╨╢╨╡╨╜╬┐ ╨┤╬┐╧Ç╬┐╨╗╨╜╨╕╧ä╨╡╨╗╤î╨╜╬┐╨╣ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╬┐╨╣, ╤ü╬┐╨╡╨┤╨╕╨╜╨╡╨╜╨╜╬┐╨╣ ╤ü ╬║╬┐╧ü╧Ç╤â╤ü╬┐╨╝.17. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╬┐╨╜╬┐ ╤ü╨╜╨░╨▒╨╢╨╡╨╜╬┐ ╨┤╬┐╧Ç╬┐╨╗ ╨╜╨╕╧ä╨╡╨╗╤î╨╜╬┐╨╣ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╬┐╨╣, ╤ü╬┐╨╡╨ ┤╨╕╨╜╨╡╨╜╨╜╬┐╨╣ ╤ü ╬║╬┐╧ü╧Ç╤â╤ü╬┐╨╝.
18. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╤ï ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╤ï ╨▓ ╨▓╨╕╨┤╨╡ ╨╕╨╖╬┐╨│╨╜╤â╧ä╤ï╧ç ╧Ç╬┐╨┤ 90┬░ ╤å╨╕╨╗╨╕╨╜╨┤╧ü╨╕╤ç╨╡╤ü╬║╨╕╧ç ╧ä╧ü╤â╨▒ ╤ü ╨▓╨╡╨╜╧ä╨╕╨╗╨╡╨╝ ╨╜╨░18. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╤â╨╗╤î╤ü╬║╨░╨╝╨╡╧ü╤ï ╨▓╤ï╧Ç╬┐╨╗ ╨╜╨╡╨╜╤ï ╨▓ ╨▓╨╕╨┤╨╡ ╨╕╨╖╬┐╨│╨╜╤â╧ä╤ï╧ç ╧Ç╬┐╨┤ 90┬░ ╤å╨╕╨ ╗╨╕╨╜╨┤╧ü╨╕╤ç╨╡╤ü╬║╨╕╧ç ╧ä╧ü╤â╨▒ ╤ü ╨▓╨╡╨╜╧ä╨╕╨╗╨╡╨╝ ╨ ╜╨░
35 ╤ü╨▓╬┐╨▒╬┐╨┤╨╜╬┐╨╝ ╬║╬┐╨╜╤å╨╡ ╨┤╨╗╤Å ╤ü╨▓╤Å╨╖╨╕ ╤ü ╨░╧ä╨╝╬┐╤ü╧å╨╡╧ü╬┐╨╣.35 ╤ü╨▓╬┐╨▒╬┐╨┤╨╜╬┐╨╝ ╬║╬┐╨╜╤å╨╡ ╨┤╨╗╤Å ╤ü╨▓╤Å╨╖╨╕ ╤ü ╨░╧ ä╨╝╬┐╤ü╧å╨╡╧ü╬┐╨╣.
19. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤ü╬┐╧Ç╧ü╤Å╨╢╨╡╨╜╨╜╤ï╨╡ ╤ç╨░╤ü╧ä╨╕ ╬║╬┐╧ü╧Ç╤â╤ü╨░ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╤ï ╨▓ ╨▓╨╕╨┤╨╡ ╤å╨╕╨╗╨╕╨╜╨┤╧ü╬┐╨▓ ╤ü ╤ü╬┐╬┐╧ä╨╜╬┐╤ê╨╡╨╜╨╕╨╡╨╝ ╬¼╨▓ΓëÑ╬¼╨╜, ╨│╨┤╨╡ 18 - - * ╬¼╨▓ - ╨┤╨╕╨░╨╝╨╡╧ä╧ü ╬║╬┐╨╗╤î╤å╨╡╨▓╬┐╨│╬┐ ╤ü╨╡╤ç╨╡╨╜╨╕╤Å ╨▓╨╡╧ü╧ç╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╨╕ ╬║╬┐╧ü╧Ç╤â╤ü╨░; ╬¼╨╜ - ╨┤╨╕╨░╨╝╨╡╧ä╧ü ╬║╬┐╨╗╤î╤å╨╡╨▓╬┐╨│╬┐ ╤ü╨╡╤ç╨╡╨╜╨╕╤Å ╨╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╨╕ ╬║╬┐╧ü╧Ç╤â╤ü╨░.19. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤ü╬┐╧Ç╧ü╤Å╨╢╨╡╨╜╨╜╤ï╨╡ ╤ç╨░╤ü╧ä╨╕ ╬║╬┐╧ü╧Ç╤â╤ü╨░ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╤ï ╨▓ ╨▓╨╕╨┤╨╡ ╤å╨╕╨╗╨╕ ╨╜╨┤╧ü╬┐╨▓ ╤ü ╤ü╬┐╬┐╧ä╨╜╬┐╤ê╨╡╨╜╨╕╨╡╨╝ ╬¼╨▓ΓëÑ╬¼╨╜, ╨│╨┤ ╨╡ 18 - - * ╬¼ ╨▓ - ╨┤╨╕╨░╨╝╨╡╧ä╧ü ╬║╬┐╨╗╤î╤å╨╡╨▓╬┐╨│╬┐ ╤ü╨╡╤ç╨ ╡╨╜╨╕╤Å ╨▓╨╡╧ü╧ç╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╨╕ ╬║╬┐╧ü╧Ç╤â╤ü╨░; ╬¼ ╨╜ - ╨┤╨╕╨░╨╝╨╡╧ä╧ü ╬║╬┐╨╗╤î╤å╨╡╨▓╬┐╨│╬┐ ╤ü╨╡╤ç╨╡╨╜╨ ╕╤Å ╨╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╨╕ ╬║╬┐╧ü╧Ç╤â╤ü╨░.
20. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╬║╬┐╨╗╬┐╨╜╨╜╨╡ ╧Ç╨╡╧ü╨╡╨╝╨╡╨╜╨╜╬┐╨│╬┐ ╤ü╨╡╤ç╨╡╨╜╨╕╤Å ╤â╤ü╧ä╨░╨╜╬┐╨▓╨╗╨╡╨╜╨░ ╧ä╨░╧ü╨╡╨╗╤î╤ç╨░╧ä╨░╤Å ╨╜╨░╤ü╨░╨┤╬║╨░.20. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╬║╬┐╨╗╬┐╨╜╨╜╨╡ ╧Ç╨╡╧ü╨╡╨╝╨╡╨╜╨╜ ╬┐╨│╬┐ ╤ü╨╡╤ç╨╡╨╜╨╕╤Å ╤â╤ü╧ä╨░╨╜╬┐╨▓╨╗╨╡╨╜╨░ ╧ä╨░╧ü╨╡ ╨╗╤î╤ç╨░╧ä╨░╤Å ╨╜╨░╤ü╨░╨┤╬║╨░.
5 21. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╤å╨╕╨╗╨╕╨╜╨┤╧ü╨╕╤ç╨╡╤ü╬║╬┐╨╣ ╨╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╨╕ ╨╖╨░╨│╧ü╤â╨╖╬┐╤ç╨╜╬┐╨│╬┐ ╤ü╧ü╨╡╨┤╤ü╧ä╨▓╨░ ╤â╤ü╧ä╨░╨╜╬┐╨▓╨╗╨╡╨╜╨░ ╧ä╨░╧ü╨╡╨╗╤î╤ç╨░╧ä╨░╤Å ╨╜╨░╤ü╨░╨┤╬║╨░.5 21. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç. 16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡ ╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓ ╤å╨╕╨╗╨╕╨╜╨┤╧ü╨╕╤ç╨╡╤ü╬║╬┐╨╣ ╨ ╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╨╕ ╨╖╨░╨│╧ü╤â╨╖╬┐╤ç╨╜╬┐╨│╬┐ ╤ü╧ü╨ ╡╨┤╤ü╧ä╨▓╨░ ╤â╤ü╧ä╨░╨╜╬┐╨▓╨╗╨╡╨╜╨░ ╧ä╨░╧ü╨╡╨╗╤î╤ç╨░╧ ä╨░╤Å ╨╜╨░╤ü╨░╨┤╬║╨░.
22. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓╨╡╧ü╧ä╨╕╬║╨░╨╗╤î╨╜╨░╤Å ╧ä╧ü╤â╨▒╨░ ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤Å ╨╖╨░╧Ç╬┐╨╗╨╜╨╡╨╜╨░ ╧ä╨░╧ü╨╡╨╗╤î╤ç╨░╧ä╬┐╨╣ ╨╜╨░╤ü╨░╨┤╬║╬┐╨╣. ╤Ä22. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨▓╨╡╧ü╧ä╨╕╬║╨░╨╗╤î╨╜╨░╤Å ╧ä╧ü╤â╨▒ ╨░ ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤Å ╨╖╨░╧Ç╬┐╨╗╨╜╨╡╨╜╨░ ╧ä╨░╧ü╨╡ ╨╗╤î╤ç╨░╧ä╬┐╨╣ ╨╜╨░╤ü╨░╨┤╬║╬┐╨╣. ╤Ä
23. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤î ╨╕╨╝╨╡╨╡╧ä ╧Ç╨░╧ä╧ü╤â╨▒╬┐╬║ ╨┤╨╗╤Å ╧Ç╬┐╨┤╨░╤ç╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐╨┤╤ï, ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨╜╤ï╨╣ ╨╜╨╕╨╢╨╡ ╨╜╨░╤ü╨░╨┤╬║╨╕.23. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤î ╨╕╨╝╨╡╨╡╧ä ╧Ç╨░╧ä╧ü╤â╨▒╬┐╬║ ╨┤╨╗╤Å ╧Ç╬┐╨┤╨░╤ç╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╨▓╬┐ ╨┤╤ï, ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨╜╤ï╨╣ ╨╜╨╕╨╢╨╡ ╨╜╨░╤ü╨░╨┤╬ ║╨╕.
24. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╜╨╕╨╢╨╜╤Å╤Å ╤ç╨░╤ü╧ä╤î ╬║╬┐╧ü╧Ç╤â╤ü╨░ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╨░ ╤ü ╧Ç╨░╧ä╧ü╤â╨▒╬║╬┐╨╝ ╨┤╨╗╤Å ╧Ç╬┐╨┤╨░╤ç╨╕ ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╤ï, ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨╜╤ï╨╝ ╨╜╨╕╨╢╨╡ ╨╜╨░╤ü╨░╨┤╬║╨╕.24. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╜╨╕╨╢╨╜╤Å╤Å ╤ç╨░╤ü╧ä╤î ╬║╬┐╧ü╧Ç╤â ╤ü╨░ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╨░ ╤ü ╧Ç╨░╧ä╧ü╤â╨▒╬║╬┐╨╝ ╨┤╨╗╤Å ╧Ç ╬┐╨┤╨░╤ç╨╕ ╬┐╨▒╬┐╧ü╬┐╧ä╨╜╬┐╨╣ ╨▓╬┐╨┤╤ï, ╧ü╨░╤ü╧Ç╬┐╨╗╬ ┐╨╢╨╡╨╜╨╜╤ï╨╝ ╨╜╨╕╨╢╨╡ ╨╜╨░╤ü╨░╨┤╬║╨╕.
15 25. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╤â╨╗╤î╤ü╬┐╧Ç╧ü╬┐╨▓╬┐╨┤ ╧Ç╧ü╨╕╬║╧ü╨╡╧Ç╨╗╨╡╨╜ ╬║ ╬║╧ü╤ï╤ê╬║╨╡ ╬║╬┐╧ü╧Ç╤â╤ü╨░.15 25. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç. 16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡ ╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╤â╨╗╤î╤ü╬┐╧Ç╧ü╬┐╨▓╬┐╨┤ ╧Ç╧ü╨╕╬ ║╧ü╨╡╧Ç╨╗╨╡╨╜ ╬║ ╬║╧ü╤ï╤ê╬║╨╡ ╬║╬┐╧ü╧Ç╤â╤ü╨░.
26. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤ü╨╜╨░╨▒╨╢╨╡╨╜╬┐ ╤â╨╖╨╗╬┐╨╝ ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╬║╧ü╤â╧Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕, ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╨╜╤ï╨╝ ╨▓ ╨▓╨╕╨┤╨╡ ╬║╬┐╧ü╬┐╨▒╨░, ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨╜╬┐╨│╬┐ ╤â ╨▓╨╡╧ü╧ç╨╜╨╡╨│╬┐ ╬║╬┐╨╜╤å╨░ ╨╜╨░╬║╨╗╬┐╨╜╨╜╬┐╨╣ ╤ü╨╡╧ä╬║╨╕ ╧Ç╬┐╨┤ ╬║╧ü╤ï╤ê╬║╬┐╨╣ ╬║╬┐╧ü╧Ç╤â╤ü╨░ ╨╕26. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç. 16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤ü╨╜╨░╨▒╨╢╨╡╨╜╬┐ ╤â╨╖╨╗╬┐╨╝ ╨▓╤ï╨│ ╧ü╤â╨╖╬║╨╕ ╬║╧ü╤â╧Ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕, ╨▓╤ï╧Ç╬┐╨╗╨ ╜╨╡╨╜╨╜╤ï╨╝ ╨▓ ╨▓╨╕╨┤╨╡ ╬║╬┐╧ü╬┐╨▒╨░, ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢ ╨╡╨╜╨╜╬┐╨│╬┐ ╤â ╨▓╨╡╧ü╧ç╨╜╨╡╨│╬┐ ╬║╬┐╨╜╤å╨░ ╨╜╨░╬║╨╗╬┐ ╨╜╨╜╬┐╨╣ ╤ü╨╡╧ä╬║╨╕ ╧Ç╬┐╨┤ ╬║╧ü╤ï╤ê╬║╬┐╨╣ ╬║╬┐╧ü╧Ç╤â╤ü ╨░ ╨╕
20 сοединеннοгο с желοбοм, выведенным за внешнюю сτенκу κορπуса.20 сοединеннοгο с желοбοм, выве денным за внешнюю сτенκу κορπ уса.
27. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤ü╨▒╬┐╧ü╨╜╨╕╬║ ╨╝╨╡╨╗╬║╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨╕╨╝╨╡╨╡╧ä ╤ê╧ä╤â╤å╨╡╧ü ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕, ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨╜╤ï╨╣ ╨▓ ╨╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ä╨╕ ╨╡╨│╬┐ ╨╜╨░╬║╨╗╬┐╨╜╨╜╬┐╨│╬┐ ╨┤╨╜╨╕╤ë╨░.27. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç. 16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╤ü╨▒╬┐╧ü╨╜╨╕╬║ ╨╝╨╡╨╗╬║╬┐╨╣ ╧å╧ü╨░ ╬║╤å╨╕╨╕ ╨╕╨╝╨╡╨╡╧ä ╤ê╧ä╤â╤å╨╡╧ü ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║ ╨╕, ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨╜╤ï╨╣ ╨▓ ╨╜╨╕╨╢╨╜╨╡╨╣ ╤ç╨░╤ü╧ ä╨╕ ╨╡╨│╬┐ ╨╜╨░╬║╨╗╬┐╨╜╨╜╬┐╨│╬┐ ╨┤╨╜╨╕╤ë╨░.
28. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗╤Å 25 ╨▓╤ï╨▓╬┐╨┤╨░ ╧Ç╧ü╬┐╨╝╨╡╨╢╤â╧ä╬┐╤ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╬┐ ╨▓ ╨▓╨╕╨┤╨╡ ╬║╨╗╨░╧Ç╨░╨╜╨░ ╤ü╬┐ ╤ê╧ä╤â╤å╨╡╧ü╬┐╨╝ ╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╬┐ ╨▓ ╨╜╨╕╨╢╨╜╨╡╨╝ ╧ä╬┐╧ü╤å╨╡ ╬║╬┐╧ü╧Ç╤â╤ü╨░.28. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç. 16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗ ╤Å 25 ╨▓╤ï╨▓╬┐╨┤╨░ ╧Ç╧ü╬┐╨╝╨╡╨╢╤â╧ä╬┐╤ç╨╜╬┐╨╣ ╧å╧ü╨░╬║╤ å╨╕╨╕ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╬┐ ╨▓ ╨▓╨╕╨┤╨╡ ╬║╨╗╨░╧Ç╨░╨╜╨░ ╤ü╬ ┐ ╤ê╧ä╤â╤å╨╡╧ü╬┐╨╝ ╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╬┐ ╨▓ ╨╜╨╕╨╢╨ ╜╨╡╨╝ ╧ä╬┐╧ü╤å╨╡ ╬║╬┐╧ü╧Ç╤â╤ü╨░.
29. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╜╨╕╨╢╨╜╤Å╤Å ╤ç╨░╤ü╧ä╤î ╧ä╧ü╤â╨▒╤ï ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤Å ╤ü ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡╨╝ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨░ ╨╜╨╕╨╢╨╡ ╬║╬┐╧ü╧Ç╤â╤ü╨░. ╨╖╬┐ 30. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨▓╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╬┐ ╨▓ ╨▓╨╕╨┤╨╡ ╬║╨╗╨░╧Ç╨░╨╜╨░ ╤ü╬┐ ╤ê╧ä╤â╤å╨╡╧ü╬┐╨╝ ╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╬┐ ╨▓ ╨╜╨╕╨╢╨╜╨╡╨╝ ╧ä╬┐╧ü╤å╨╡ ╧ä╧ü╤â╨▒╤ï ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤Å. 29. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç. 16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ë╨╡╨ ╡╤ü╤Å ╧ä╨╡╨╝, ╤ç╧ä╬┐ ╨╜╨╕╨╢╨╜╤Å╤Å ╤ç╨░╤ü╧ä╤î ╧ä╧ü╤â╨▒╤ï ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤Å ╤ü ╧Ç╧ü╨╕╤ü╧Ç╬┐╤ü╬┐╨▒╨╗╨╡╨╜╨╕ ╨╡╨╝ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕ ╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╨░ ╨╜╨╕╨╢╨╡ ╬║╬┐╧ü╧Ç╤â╤ü╨░. ╨╖╬┐ 30. ╨ú╤ü╧ä╧ü╬┐╨╣╤ü╧ä╨▓╬┐ ╧Ç╬┐ ╧Ç.16, ╬┐╧ä╨╗╨╕╤ç╨░╤Ä╤ ╨╡╨╡╤╨╡╨╡╤╨╡╨╡╤╤ ╧╧╨╡╨╝, ╤╤╧╧╬┐ ╧Ç╧╧Ç╧╨╕╤╨╕╤╧Ç╬┐╤╬┐╨▒╨╗╨╡╨╜╨╕╨╡╬┐╨▒╨╗╨╡╨╜╨╕╨╡ ╨┤╨╗╤Å ╨▓╤ï╨│╧ü╤â╨╖╬║╨╕ ╤ç╨╕╤ü╧ä╬┐╨╣ ╧å╧ü╨░╬║╤å╨╕╨╕ ╨▓ ╤ï╧Ç╬┐╨╗╨╜╨╡╨╜╬┐ ╨▓ ╨▓╨╕╨┤╨╡ ╬║╨╗╨░╧Ç╨░╨╜╨░ ╤ü╬┐ ╤ê╧ä╤â ╤å╨╡╧ü╬┐╨╝ ╨╕ ╧ü╨░╤ü╧Ç╬┐╨╗╬┐╨╢╨╡╨╜╬┐ ╨▓ ╨╜╨╕╨╢╨╜╨╡╨╝ ╧ä ╬┐╧ü╤å╨╡ ╧ä╧ü╤â╨▒╤ï ╧Ç╧ü╬┐╨╝╤ï╨▓╨░╧ä╨╡╨╗╤Å.
PCT/RU1997/000424 1997-06-09 1997-12-26 Method for cleaning contaminated ground and soils and device for implementing the same WO1998056516A1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106077063A (en) * 2016-08-10 2016-11-09 大连德联投资控股有限公司 A kind of horizontal flat-top leaching device of vehicle-mounted integrated form soil restoring device

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2562806C9 (en) 2014-08-11 2015-11-10 Общество с ограниченной ответственностью "Корпорация по Ядерным Контейнерам" (ООО "КПОЯК") Method of removing contaminants from soil and apparatus therefor
CN112375916B (en) * 2020-11-04 2022-07-15 昆明理工精诚技术开发有限公司 Copper-cobalt hydrometallurgy filtering and washing system and operation mode thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992009377A1 (en) * 1990-11-30 1992-06-11 Clean Soil, Incorporated Apparatus and process for removing contaminants from soil
WO1995010369A2 (en) * 1990-03-07 1995-04-20 Guymon E Park Water/surfactant process for recovering hydrocarbons from soil in the absence of emulsifying the oil
US5413129A (en) * 1993-03-16 1995-05-09 Worldwide Remediation, Inc. Apparatus and method for removing hydrocarbons from soils and gravel
US5599137A (en) * 1995-09-13 1997-02-04 Chemtech Analysis Inc. Mobile soil treatment apparatus and method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995010369A2 (en) * 1990-03-07 1995-04-20 Guymon E Park Water/surfactant process for recovering hydrocarbons from soil in the absence of emulsifying the oil
WO1992009377A1 (en) * 1990-11-30 1992-06-11 Clean Soil, Incorporated Apparatus and process for removing contaminants from soil
US5413129A (en) * 1993-03-16 1995-05-09 Worldwide Remediation, Inc. Apparatus and method for removing hydrocarbons from soils and gravel
US5599137A (en) * 1995-09-13 1997-02-04 Chemtech Analysis Inc. Mobile soil treatment apparatus and method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
"Primenenie Vibratsii Dlya Intensifikatsii Protsessov Peremeshivanya Zhidkikh Sred", Moscow, Tsentralny Nauchno-Issledovatelsky Institut Informatsii i Tekhniko-Ekonomicheskikh Issledovany Tsvetnoi Metallurgii, 1977, page 4. *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106077063A (en) * 2016-08-10 2016-11-09 大连德联投资控股有限公司 A kind of horizontal flat-top leaching device of vehicle-mounted integrated form soil restoring device

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