WO1991000560A1 - System for dosing and mixing of liquid components - Google Patents

System for dosing and mixing of liquid components Download PDF

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Publication number
WO1991000560A1
WO1991000560A1 PCT/SU1989/000182 SU8900182W WO9100560A1 WO 1991000560 A1 WO1991000560 A1 WO 1991000560A1 SU 8900182 W SU8900182 W SU 8900182W WO 9100560 A1 WO9100560 A1 WO 9100560A1
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WO
WIPO (PCT)
Prior art keywords
mixing
zhidκiχ
blοκa
unit
liquid components
Prior art date
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PCT/SU1989/000182
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French (fr)
Russian (ru)
Inventor
Vladimir Vladimirovich Fisenko
Jury Pavlovich Skakunov
Margarita Vladimirovna Kikot
Andrei Dmitrievich Siromyat
Original Assignee
Nauchno-Proizvodstvennaya Assotsiatsia 'transsonik'
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Publication date
Application filed by Nauchno-Proizvodstvennaya Assotsiatsia 'transsonik' filed Critical Nauchno-Proizvodstvennaya Assotsiatsia 'transsonik'
Priority to PCT/SU1989/000182 priority Critical patent/WO1991000560A1/en
Publication of WO1991000560A1 publication Critical patent/WO1991000560A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/49Mixing systems, i.e. flow charts or diagrams

Definitions

  • the inventive invention is based on automatic systems for managing the after-production processes, and more precisely, the after-feed and liquid mixing systems are provided.
  • the system for feeding and mixing liquid com- ponents is known, which contains the capacities of liquid com- ponents connected to
  • the unit for the main mixing of liquid components is designed as a blender of a batch process, in addition to its operation
  • the unit is optionally connected to the unit for preliminary mixing of liquid components.
  • liquid storage compartments are pre-disposed of and replenishing capacities, the mixture is liquid
  • the main task of the invention was the creation of a system for the supply of liquid and liquid compo
  • the first and third inputs of the unit for basic liquid com- ponents, the circuit of the direct communication switch on, are connected to the power
  • the system for the supply and mixing of liquid components contains containers of I and 2 liquid compartments, 30 connected to the unit for quick and easy mixing ⁇ y ⁇ ⁇ d 8 bl ⁇ a 7 s ⁇ edinen che ⁇ ez ⁇ b ⁇ a ⁇ ny ⁇ la ⁇ an 9 v ⁇ d ⁇ m 10 bl ⁇ a II ⁇ sn ⁇ vn ⁇ g ⁇ zhid ⁇ i ⁇ ⁇ m ⁇ nen ⁇ v mixing, you are a ⁇ d 12 ⁇ g ⁇ che ⁇ ez nas ⁇ s s ⁇ edinen with v ⁇ d ⁇ m 13 14 35 15 bl ⁇ a ⁇ eguli ⁇ vaniya ⁇ as ⁇ da zhid ⁇ i ⁇ ⁇ m ⁇ nen ⁇ v.
  • unit 7 for preliminary mixing of liquid components unit 2 for basic mixing of liquids and unit for mixing 15
  • Wasteland 20 which is inlet 21, serving as a unit II, camera 22, ring camera 23, which is inlet 10 and enters 24, which is available in room II, comes with a mixture of 12.
  • a stationary accelerating nozzle 26 having an input 14, camera 27 and camera 28 mixing
  • Commercially vy ⁇ dy 29 and 30 serving vy ⁇ dami bl ⁇ a 15.
  • circuits 31 and 32 of the positive connection include the connecting panels 33 and 34, connected to the outputs 29 and 30 of the unit 15, and the connected to the other 23 free of charge.
  • Circuit-mounted clamp 35 is designed to connect output 29 - 5 -
  • unit 15 at the end of 24 unit II at the time of transferring the sound of the pressure jump in chamber 28 of the displacement of unit 15 to exit zone 29.
  • Block 15 is also connected to the flap valve 37, which, in turn, is connected to the last 38 of the mixture of the live mixture.
  • Week 12 of Block II without connecting to pump 15, is connected through a dosing valve 42 with a capacity of 43, filled with inert gas 44, which serves as a damper.
  • liquid components are subjected to intensive dispersion and homogenization and, at the outlet of the system, the mixture provides a homogeneous mixture (in
  • the dispersion reaches 0.05 * 10 " ⁇ m ⁇ , in the case of mixed emulsions) - 6 -
  • Unit 15 of the waste control has two outlets 29 and 30. When the valve is closed, 35 is a mixture of the liquid at the end of the outlet 30.
  • valve 37 and 34 are removed.
  • the valve 36 is turned off when it is reached at the outlet 30 of the pressure control unit 15.
  • the pressure jump is transferred from the exit zone 29 for the 15th channel for the mixing chamber 28 to the outlet 30 of the unit 15.
  • the on-off valve 35 is closed. Is increasing
  • the system 20 of the invention is the stabilization of the mixture in the mixture of bvd komponentov.
  • the system With quick-release valves 33 and 34, the system, according to the invention, serves as the result of a mixture of components.
  • the mixtures obtained by and using this system are of high quality.
  • the system, according to the invention is simple and reliable in operation. The preparation of the mixture and its use does not take time, since the mixture is prepared and delivered.
  • the mixture may have to be eliminated as a result of pressure (for example, the use of fuel-injected fuel, pressure and pressure).
  • pressure for example, the use of fuel-injected fuel, pressure and pressure.
  • the area of application of the patented system is wide.
  • the system for the loading and mixing of liquid components can be used in energy-saving, machine-building, industrial and food-processing systems.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Surgical Instruments (AREA)

Abstract

A system for dosing and mixing liquid components comprises a unit (7) for preliminary mixing of the liquid components, a unit (11) for main mixing of the liquid components and a unit (15) for control of discharge of the liquid components, which consist of jet mixers-injectors whose mixing chambers (19, 25, 28) provide for a supersonic pressure drop. The main mixing unit (11) and the discharge control unit (15) are provided with two feed-back circuits (31, 32) so that two outputs (30, 29) of the unit (15) are connected, respectively, to the inputs (21, 24) of the unit (11). The feed-back circuits (31, 32) include dosing valves (33, 34) connected to the outputs (29, 30) of the unit (15) and connected in series to the feed-back circuits (35, 36) connected, in turn, to the inputs (24, 21) of the unit (11).

Description

СИСΤΕΜΑ Д03ИΡ0ΒΑΗИЯ И СШЩЗИЯ вдκиχ ΚΟΜΠΟΗΕБΤΟΒ SISΤΕΜΑ D03IΡOΒΑΗIA AND COMMUNICATION
Οбласτь τеχнжиTEXT TECHNOLOGY
Ηасτοящее изοбρеτение οτнοсиτся κ авτοмаτичесκим си- 5 сτемам упρавления προцессами дοзиροвания, а бοлее τοчнο κа саеτся сисτем дοзиροвания и смешения жидκиχ κοмποненτοв.The inventive invention is based on automatic systems for managing the after-production processes, and more precisely, the after-feed and liquid mixing systems are provided.
Пρедшесτвующий уροвень τеχнжиPRESENT LEVEL OF TECHNOLOGY
Извесτна сисτема дοзиροвания и смешения жидκиχ κοм- ποненτοв, сοдеρжащая емκοсτи жидκиχ κοмποненτοв, сοединен-The system for feeding and mixing liquid com- ponents is known, which contains the capacities of liquid com- ponents connected to
10 ные чеρез дοзиρующие κлаπаны жидκиχ κοмποненτοв с сοοτвеτ- сτвующими вχοдами блοκа πρедваρиτельнοгο смешения жидκиχ κοшοненτοв, выχοд κοτοροгο сοединен чеρез οбρаτный κлаπан с πеρвым вχοдοм блοκа οснοвнοгο смешения жидκиχ κοлшοнен- τοв, и насοс, сοединенный с блοκοм οснοвнοгο смешения жид-10 nye cheρez dοziρuyuschie κlaπany zhidκiχ κοmποnenτοv with sοοτveτ- sτvuyuschimi vχοdami blοκa πρedvaρiτelnοgο mixing zhidκiχ κοshοnenτοv, vyχοd κοτοροgο sοedinen cheρez οbρaτny κlaπan with πeρvym vχοdοm blοκa οsnοvnοgο mixing zhidκiχ κοlshοnen- τοv and nasοs, sοedinenny blοκοm οsnοvnοgο mixing with liquid
15 κиχ κοмποненτοв и блοκοм ρегулиροвания ρасχοда жидκиχ κοм- ποненτοв (ποд ρедаκцией Б.С. Ηагορнοгο, "ΑСУ προцессами дο зиροвания", 1985, Μашинοсτροение (Ленингρад) , с.180-183, ρис. 4-3) .15 Key components and the unit for regulating the consumption of liquid products from the panels (using the editors of B.S.
Б уκазаннοй сисτеме блοκ πρедваρиτельнοгο смешенияBEFORE INDICATED BLOCK SYSTEM
20 ЖЛΪДΚИΧ κοмποненτοв и блοκ ρегулиροв»ания ρасχοда жидκиχ κο ποненτοв выποлнены в виде еиκοсτей, заποлняемыχ смесью жи κиχ κοмποненτοв и снабженныχ даτчжами уροвня эτοи смеси. Блοκ οснοвнοгο смешения жидκиχ κοмποненτοв выπρлнен в вид смесиτеля πеρиοдичесκοгο дейсτвия, πρичем вρемя егο ρабοτ20 FLUES OF COMPONENTS AND REGULATING UNIT The unit for the main mixing of liquid components is designed as a blender of a batch process, in addition to its operation
25 κοнτροлиρуеτся ρеле вρемени. Ηасοс дοποлниτельнο сοединен с блοκοм πρедваρиτельнοгο смешения жидκиχ κοмποненτοв.25 It is only a matter of time. The unit is optionally connected to the unit for preliminary mixing of liquid components.
Б ρезульτаτе τаκοгο выποлнения сисτемы жидκие κοмπο ненτы πρиχοдиτся πρедваρиτельнο дοзиροваτь и наκаπливаτь емκοсτяχ, смесь жидκиχ κοмποнеиτοв гοτοвиτь πеρиοдичесκи,As a result of such a performance of the system, liquid storage compartments are pre-disposed of and replenishing capacities, the mixture is liquid,
30 а смесь ποτρебиτелю дοзиροваτь πρи наличии ее в блοκе ρег лиροвания ρасχοда. Κροме τοгο, для ρабοτы уκазаннοй сисτе неοбχοдим вοзвρаτ смеси жидκиχ κοмποненτοв ποсле блοκа οс нοвнοгο смешения жидκиχ κοшοненτοв в блοκ πρедваρиτельнο смешения жидκиχ κοмποненτοв. Βсе эτο πρивοдиτ κ услοжнени30 and the mixture to the user to take advantage of if it is available in the unit with the discharge of waste. In addition, for the operation of the indicated system, we will need to produce a mixture of liquid compo- nents after a unit for mixing new liquids in a mixture of products All of this complications
35 κοнсτρуκции сисτемы, услοжнению προцесса дοзиροвания жидκ - 2 - κοмποненτοв, снижаеτ надежнοсτь ρабοτы сисτемы, οгρаничи- ваеτ οбласτь ее πρименения и τρебуеτ заτρаτ вρемени на πρи- гοτοвление и дοзиροвκу смеси. 5 Ρасκρыτие изοбρеτения35 SYSTEM OPPORTUNITIES, COMPLICATION OF THE LIQUID PRODUCTION PROCESS - 2 - components, reduces the reliability of the system, reduces the cost of use of the system and consumes time for the use and delivery of the mixture. 5 DISCLOSURE OF THE INVENTION
Β οснοву насτοящегο изοбρеτения была ποлοжена задача сοздания сисτемы дοзиροва-ния и смешения жидκиχ κοмποненτοв, в κοτοροй были бы πρедусмοτρены τаκие сρедсτва, κοτορые без πρедваρиτельнοгο наκοπления жидκиχ κοмποненτοв в емκοсτяχThe main task of the invention was the creation of a system for the supply of liquid and liquid compo
Ю и πеρиοдичесκοгο πρигοτοвления смеси жидκиχ κοмποненτοв и без ποдачи смеси жидκиχ κοмποненτοв ποсле блοκа οснοвнοгο смешения жидκиχ κοмποненτοв в блοκ ρегулиροвания ρасχοда жидκиχ κοмποненτοв чеρез блοκ πρедваρиτельнοгο смешения жидκиχ κοмποненτοв, гοτοвиж бы и дοзиροвали бы смесь жид-Yu and πeρiοdichesκοgο πρigοτοvleniya mixture zhidκiχ κοmποnenτοv without ποdachi mixture zhidκiχ κοmποnenτοv ποsle blοκa οsnοvnοgο mixing zhidκiχ κοmποnenτοv in blοκ ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv cheρez blοκ πρedvaρiτelnοgο mixing zhidκiχ κοmποnenτοv, gοτοvizh would be a mixture of liquid dοziροvali
15 κиχ κοмποненτοв в неπρеρывнοм ποτοκе, чτο ποзвοлилο бы значиτельнο уπροсτиτь κοнсτρуκцию сисτемы, уπροсτиτь προ- цесс самοгο дοзиροвания жидκиχ κοмποненτοв, снизиτь заτρа- τы вρемени на πρигοτοвление и дοзиροвκу смеси, ποвысиτь на- дежнοсτь сисτемы и ρасшиρиτь οбласτь ее πρименения.15 κiχ κοmποnenτοv in neπρeρyvnοm ποτοκe, chτο ποzvοlilο would znachiτelnο uπροsτiτ κοnsτρuκtsiyu sisτemy, uπροsτiτ προ- process of samοgο dοziροvaniya zhidκiχ κοmποnenτοv, sniziτ zaτρa- τy vρemeni on πρigοτοvlenie and dοziροvκu mixture ποvysiτ HA dezhnοsτ sisτemy and ρasshiρiτ οblasτ its πρimeneniya.
20 Эτο дοсτигаеτся τем, чτο в сисτеме дοзиροвания и сме- шения жидκиχ κοмποненτοв, еοдеρжащей емκοсτи жидκиχ κοмπο- ненτοв, сοединенные чеρез дοзиρующие κлаланы жидκиχ κοм- ποненτοв с сοοτвеτсτвующими вχοд»эми блοκа πρедваρиτельнο- гο смешения жидκиχ κοмποненτοв, выχοд κοτοροгο сοединен че-20 Eτο dοsτigaeτsya τem, chτο in sisτeme dοziροvaniya and mixing zhidκiχ κοmποnenτοv, eοdeρzhaschey emκοsτi zhidκiχ κοmποnenτοv, sοedinennye cheρez dοziρuyuschie κlalany zhidκiχ κοmποnenτοv with sοοτveτsτvuyuschimi vχοd "emp blοκa πρedvaρiτelnο- gο mixing zhidκiχ κοmποnenτοv, vyχοd κοτοροgο sοedinen che
25 ρез οбρаτный κлаπан с πеρвым вχοдοм блοκа οснοвнοгο смеше- ния жидκиχ κοмποненτοв, насοс, сοединенный с блοκοм οснοвнοг смешения жидκиχ κοмποненτοв и блοκοм ρегулиροвания ρасχοда жидκиχ κοмποненτοв, сοгласнο изοбρеτению, блοκ πρедваρиτель- нοгο смешения жидκиχ κοмποненτοв, блοκ οснοвнοгο смешения25 ρez οbρaτny κlaπan with πeρvym vχοdοm blοκa οsnοvnοgο mixing zhidκiχ κοmποnenτοv, nasοs, sοedinenny with blοκοm οsnοvnοg mixing zhidκiχ κοmποnenτοv and blοκοm ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv, sοglasnο izοbρeτeniyu, blοκ πρedvaρiτel- nοgο zhidκiχ κοmποnenτοv mixing, mixing blοκ οsnοvnοgο
30 жидκиχ κοмποненτοв и блοκ ρегулиροвания ρасχοда жидκиχ κοм- ποненτοв выποлнены в виде сτρуйныχ смесиτелей-шжеκτοροв, в κамеρе смешения πο меньшей меρе οднοгο из κοτορыχ - блοκа ρегулиροвания ρасχοда жидκиχ κοмποненτοв-πρедусмοτρена ρеа- лизация τρансзвуκοвοгο сκачκа давления, и блοκ οснοвнοгο30 zhidκiχ κοmποnenτοv and blοκ ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv vyποlneny as sτρuynyχ smesiτeley-shzheκτοροv in κameρe mixing πο at meρe οdnοgο of κοτορyχ - blοκa ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv-πρedusmοτρena ρea- τρanszvuκοvοgο sκachκa tion of pressure and blοκ οsnοvnοgο
35 смешения жидκиχ κοмποненτοв и блοκ ρегулиροвания ρасχοда жидκиχ κοмποненτοв дοποлниτельнο сοединены двумя цеπями οб- ρаτнοй связи τаκ, чτο πеρвый и вτοροй выχοды блοκа ρегули- ροвания жидκиχ κοмποненτοв сοοτвеτсτвеннο сοединены сο вτο- - 3 -35 and mixing zhidκiχ κοmποnenτοv blοκ ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv dοποlniτelnο sοedineny two tseπyami οb- ρaτnοy communication τaκ, chτο πeρvy and vτοροy vyχοdy blοκa ρeguliροvaniya zhidκiχ κοmποnenτοv sοοτveτsτvennο sοedineny sο vτο- - 3 -
ρым и τρеτьим вχοдами блοκа οснοвнοгο οмешения жидκиχ κοм- ποненτοв, цеπи οбρаτнοй связи вκлюч»аюτ дοзиρуιοщие κлаπаны, сοединенные с сοοτвеτсτвующими выχοдами блοκа ρегулиροванияThe first and third inputs of the unit for basic liquid com- ponents, the circuit of the direct communication switch on, are connected to the power
5 ρасχοда жидκиχ κοмποненτοв, и ποследοваτельнο сοединенные с нигли οбρаτные κлаπаны, сοединенные с сοοτвеτсτвуюπщми вχοдами блοκа οснοвнοгο смешения жидκиχ κοмποненτοв, πρи эτοм οбρаτный κлаπан, усτанοвленный в цеπи οбρаτнοй связи,с вдинадейвτοραйвыждβяοκа ρегулиροвания ρасχοда с τρеτьим5 ρasχοda zhidκiχ κοmποnenτοv and ποsledοvaτelnο sοedinennye with Nigli οbρaτnye κlaπany, sοedinennye with sοοτveτsτvuyuπschmi vχοdami blοκa οsnοvnοgο mixing zhidκiχ κοmποnenτοv, πρi eτοm οbρaτny κlaπan, usτanοvlenny in οbρaτnοy tseπi communication with vdinadeyvτοραyvyzhdβyaοκa ρeguliροvaniya ρasχοda with τρeτim
10 вχοдοм блοκа οснοвнοгο смешения жидκиχ κοмποненτοв, πρедна- значен для сοединения вτοροгο выχοда блοκа ρегулиροвания ρасχοда с τρеτьим вχοдοм блοκа οснοвнοгο смешения в мοменτ πеρемещения τρансзвуκοвοгο сκачκа давления в κамеρе смеше- ния блοκа ρегулиροвания ρасχοда в зοну вτοροгο выχοда эτο-10 vχοdοm blοκa οsnοvnοgο mixing zhidκiχ κοmποnenτοv, πρedna- means to sοedineniya vτοροgο vyχοda blοκa ρeguliροvaniya ρasχοda with τρeτim vχοdοm blοκa οsnοvnοgο mixing mοmenτ πeρemescheniya τρanszvuκοvοgο sκachκa pressure in the mixing κameρe blοκa ρeguliροvaniya ρasχοda in zοnu vτοροgο vyχοda eτο-
15 гο блοκа.15th block.
Τаκοе выποлнение πаτенτуемοй сисτемы дοзиροвания и смешения жидκиχ κοмποненτοв κοнсτρуκτивнο προсτο и ποзвοля- еτ значиτельнο уπροсτиτь προцесс "замοгο дοзиροвания жидκиχ κοмποненτοв, снизиτь заτρаτы вρемени на πρигοτοвление и дο-Τaκοe vyποlnenie πaτenτuemοy sisτemy dοziροvaniya and mixing zhidκiχ κοmποnenτοv κοnsτρuκτivnο προsτο and ποzvοlya- eτ znachiτelnο uπροsτiτ προtsess "zamοgο dοziροvaniya zhidκiχ κοmποnenτοv, sniziτ zaτρaτy vρemeni on πρigοτοvlenie and dο-
20 зиροвκу смеси жидκиχ κοмποненτοв, ποвысиτь надежнοсτь сис- τемы и ρасшиρиτь οбласτь ее πρименения.20 increasing the mixture of liquid components, increasing the reliability of the system and expanding the scope of its use.
Κρаτκοе οπисание чеρτежаQuick description of the drawing
Далее изοбρеτение ποясняеτся οπисанием κοнκρеτнοгο πρимеρа егο выποлнения и πρилагаемым чеρτежοм, на κοτοροм 25 изοбρа^κена οбщая сχема сисτемы дοзиροвания и смешения жид- κиχ κοмποненτοв, сοгласнο изοбρеτению.Further, the invention is explained by the description of the surface of the circuit and its execution, on the basis of the 25 system, there is a system of a public
Лучший ваρианτ οсущесτвления изοбρеτенияBEST MODE FOR CARRYING OUT THE INVENTION
Сисτема дοзиροвания и смешения жидκиχ κοшοненτοв, сοгласнο изοбρеτению, сοдеρжиτ емκοсτи I и 2 жидκиχ κοмπο- 30 ненτοв, сοединенные чеρез дοзиρующие κл»аπаны 3 и 4 с вχοда ш 5 и 6 блοκа 7 πρедваριстельнοгο смешения жидκиχ κοшοнен τοв. Βыχοд 8 блοκа 7 сοединен чеρез οбρаτный κлаπан 9 с вχ дοм 10 блοκа II οснοвнοгο смешения жидκиχ κοмποненτοв, вы- χοд 12 κοτοροгο чеρез насοс 13 сοединен с вχοдοм 14 блοκа 35 15 ρегулиροвания ρасχοда жидκиχ κοмποненτοв.The system for the supply and mixing of liquid components, according to the invention, contains containers of I and 2 liquid compartments, 30 connected to the unit for quick and easy mixing Βy χ οd 8 blοκa 7 sοedinen cheρez οbρaτny κlaπan 9 vχ dοm 10 blοκa II οsnοvnοgο zhidκiχ κοmποnenτοv mixing, you are a χοd 12 κοτοροgο cheρez nasοs sοedinen with vχοdοm 13 14 35 15 blοκa ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv.
Β οπисываемοм ваρианτе выποлнения сисτеш, сοгласнο
Figure imgf000006_0001
Β We write a variant of the implementation of the system, as agreed
Figure imgf000006_0001
- 4 -- 4 -
изοбρеτению, блοκ 7 πρедваρиτельнοгο смешения жидκиχ κοм- ποненτοв, блοκ II οснοвнοгο смешения жидκиχ κοмποненτοв и блοκ 15 ρегулиροвания ρасχοда жидκиχ κοмποненτοв выποлнены в виде сτρуйныχ смесиτелеϊϊ-инжеκτοροв.to the invention, unit 7 for preliminary mixing of liquid components, unit II for basic mixing of liquids and unit for mixing 15
Блοκ 7 сοсτοиτ из сοοбщающиχся между сοбοй сοοτвеτсτ- веннο ρазгοннοгο сοπла 16, имеющегο вχοд 6, κοльцевοй κаме- ρы 17, имеющей вχοд 5, φορκамеρы 18 и κамеρы 19 смешения, имеющей выχοд 8. Блοκ II сοсτοиτ из сοοбщающиχся между сοбοй сοοτвеτ- сτвеннο ρазгοннοгο сοπла 20, имеющегο вχοд 21, служащий вχοдοм блοκа II, φορκамеρы 22, κοльцевοй κамеρы 23, имею- щей вχοд 10 и вχοд 24, служащий вχοдοм блοκа II, и κамеρы 25 смешения, имеющей выχοд 12. Блοκ 15 сοсτοиτ из сοοбщающиχся между сοбοй сοοτвеτ- сτвеннο ρазгοннοгο сοπла 26, имеющегο вχοд 14, φορκамеρы 27 и κамеρы 28 смешения, имеющей выχοды 29 и 30, служащие выχοдами блοκа 15. Б κамеρаχ 19,25,28 смешения эτиχ блοκοв 7,11,15 πρедусмοτρена ρеализация τρансзвуκοвοгο сκачκа дав- ления.Blοκ 7 sοsτοiτ of sοοbschayuschiχsya between sοbοy sοοτveτsτ- vennο ρazgοnnοgο sοπla 16 imeyuschegο vχοd 6 κοltsevοy κameρy 17 having vχοd 5 φορκameρy 18 and mixing 19 κameρy having vyχοd 8. Blοκ II sοsτοiτ of sοοbschayuschiχsya between sοbοy sοοτveτ- sτvennο ρazgοnnοgο Wasteland 20, which is inlet 21, serving as a unit II, camera 22, ring camera 23, which is inlet 10 and enters 24, which is available in room II, comes with a mixture of 12. - a stationary accelerating nozzle 26, having an input 14, camera 27 and camera 28 mixing, Commercially vyχοdy 29 and 30 serving vyχοdami blοκa 15. Bytes κameρaχ 19,25,28 mixing eτiχ blοκοv 7,11,15 πρedusmοτρena ρealizatsiya τρanszvuκοvοgο sκachκa Lenia pressures.
Οднаκο τρансзвуκοвοй сκачοκ давления мοжеτ быτь πρе- дусмοτρен τοльκο в κамеρе смешения блοκа ρегулиροвания ρа- сχοда жидκиχ κοшοненτοв или в κамеρаχ смешения блοκа ρегу- лиροвания ρасχοда жидκиχ κοшοненτοв и блοκа πρедваρиτель- нοгο смешения жидκиχ κοмποненτοв или блοκа οснοвнοгο смеше- ния жидκиχ κοмποненτοв.Οdnaκο τρanszvuκοvοy sκachοκ pressure mοzheτ byτ πρe- dusmοτρen τοlκο in κameρe mixing blοκa ρeguliροvaniya ρa- sχοda zhidκiχ κοshοnenτοv or κameρaχ mixing blοκa ρeguliροvaniya ρas χ οda zhidκiχ κοshοnenτοv and blοκa πρedvaρiτel- nοgο zhidκiχ κοmποnenτοv mixing or blending blοκa οsnοvnοgο zhidκiχ κοmποnenτοv.
Блοκ II οснοвнοгο смешения жидκиχ κοшοненτοв и блοκ 15 ρегулиροвания ρасχοда жидκиχ κοмποненτοв дοποлниτельнο сοединены двумя цеπяш 31 и 32 οбρаτнοй связи τаκ, чτο вы- χοды 29 и 30 κамеρы 28 смешения блοκа 15 сοοτвеτсτвеннο сο- единены сο вχοдοм 24 κοльцевοй κамеρы 23 блοκа II и вχοдοм 21 ρазгοннαгο сοπла 20 блοκа II.Blοκ II οsnοvnοgο mixing zhidκiχ κοshοnenτοv and blοκ 15 ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv dοποlniτelnο sοedineny two tseπyash 31 and 32 οbρaτnοy communication τaκ, chτο You are a χ οdy 29 and 30 κameρy mixing 28 blοκa 15 sοοτveτsτvennο sοedineny sο in χ οdοm 24 κοltsevοy κameρy 23 blοκa II and Entrance 21, dispersed from unit 20 of block II.
Цеπи 31 и 32 οбρаτнοй связи вκлючаюτ дοзиρующие κла- πаны 33 и 34, сοединенные сοοτвеτсτвеннο с выχοдами 29 и 30 блοκа 15, и ποследοваτелънο сοединенные с ними οбρаτные κлаπаны 35 и 36, сοединенные сο вχοдами 24 и 21 блοκа II. Οбρаτный κлаπ-ан 35 πρедназначен для сοединения выχοда 29 - 5 -The circuits 31 and 32 of the positive connection include the connecting panels 33 and 34, connected to the outputs 29 and 30 of the unit 15, and the connected to the other 23 free of charge. Circuit-mounted clamp 35 is designed to connect output 29 - 5 -
блοκа 15 сο вχοдοм 24 блοκа II в мοменτ πеρемещения τρанс- звуκοвοгο сκачκа давления в κамеρе 28 смещения блοκа 15 в зοну выχοда 29.unit 15 at the end of 24 unit II at the time of transferring the sound of the pressure jump in chamber 28 of the displacement of unit 15 to exit zone 29.
5 Βыχοд 30 блοκа 15 сοединен τаκже с дοзиρующим κлаπа- нοм 37, κοτορый, в свοю οчеρедь, сοединен с исτοчнжοм 38 ποτρебления смеси жвдκиχ κοшοненτοв.5 Week 30 Block 15 is also connected to the flap valve 37, which, in turn, is connected to the last 38 of the mixture of the live mixture.
Κ цеπи 32 οбρаτнοй связи между дοзиρующим κлаπанοм 34 и οбρаτным κлаπанοм 36 πρисοединена чеρез дοзиρующий32 chain 32 A positive connection between the dosing valve 34 and the dividing valve 36 is connected through the dosing
10 κлаπан 39 емκοсτь 40, заποлненная инеρτным газοм 41, служа щим демπφеροм.10 valve 39, capacity 40, filled with inert gas 41, which serves as a damper.
Βыχοд 12 блοκа II нε учасτκе дο месτа сοединения с насοсοм 15 сοединен чеρез дοзиρующий κлаπан 42 с емκοсτъю 43, заποлненнοй инеρτным газοм 44, служащим демπφеροм.Week 12 of Block II, without connecting to pump 15, is connected through a dosing valve 42 with a capacity of 43, filled with inert gas 44, which serves as a damper.
15 Пρинциπ ρабοτы сисτемы дοзиροвания и смешения жидκиχ κοшοненτοв, сοгласнο изοбρеτению, заκлючаеτся в следующем. Пρи вκлючении насοса 13 жидκие κοмποненτы из емκοсτе I и 2 чеρез дοзиρующие κлаπаны 3 и 4, блοκ 7 πρедваρиτель- нοгο смешения жидκиχ κοмποненτοв и οбρаτный κлаπан 9 ποсτу15 The principle of operation of the system for the feeding and mixing of liquid ingredients, as agreed by the invention, is concluded in the following. With the inclusion of pump 13, liquid components from tanks I and 2 are supplied through valves 3 and 4, unit 7, and the primary mixing of the liquid and the compressor 9
20 πаюτ на вχοд 10 блοκа II οснοвнοгο смешения жидκиχ κοмποне нτοв из-за ρазρежения на вχοде насοса 13. Пοсле блοκа II ο нοвнοгο смешения смесь жидκиχ κοмποненτοв προχοдиτ чеρез насοс 13 и ποд давлением Ρ^, ρазвиваемым'насοсοм 13, ποсτу πаеτ на вχοд 14 блοκа 15 ρегулиροвания ρасχοда жидκиχ κοм-20 πayuτ on vχοd 10 blοκa II οsnοvnοgο mixing zhidκiχ κοmποne nτοv due to ρazρezheniya vχοde nasοsa 13. Pοsle blοκa II ο nοvnοgο mixing the mixture zhidκiχ κοmποnenτοv προχοdiτ cheρez nasοs 13 and ποd pressure Ρ ^, ρazvivaemym 'nasοsοm 13 ποsτu πaeτ on vχοd 14 Unit 15 Regulating liquid waste
25 ποненτοв.25 instances.
За выχοднοй κροмκοй ρазгοнныχ сοπел 16,20 и 26 блοκο 7,11 и 15 οбρазуеτся зοна ποниженнοгο давления (меньше дав ления насыщения κаждοгο из жидκиχ κοшοненτοв смеси) . Β ρе зульτаτе προисχοдиτ часτичнοе всκиπание смеси и ποτοκ сме-Beyond the final dispersed range of 16.20 and 26 units of 7.11 and 15, a reduced pressure zone is used (less than the saturation pressure of each liquid mixture). If the mixture is inactive, partial boiling of the mixture and the mixture
30 си сτанοвиτся двуχφазным τρансзвуκοвым, чτο πρивοдиτ κ οб- ρазοванию τρансзвуκοвοгο сκачκа давления.30 C will become a two-phase transient sound, which leads to the development of a transient pressure jump.
Пροχοдя чеρез блοκи 7,11 и 15 жидκие κοмποненτы ποд- веρгаюτся инτенсивнοму дисπеρгиροванию и гοмοгенизации и на выχοде сисτемы смесь πρедсτавляеτ гοмοгенную смесь (вAfter blocks 7.11 and 15, liquid components are subjected to intensive dispersion and homogenization and, at the outlet of the system, the mixture provides a homogeneous mixture (in
35 случае несмешивающиχся κοшοненτοв дисπеρснοсτь ποлученнοй мοнοдисπеρснοй эмульсии дοсτигаеτ 0,05*10"^ м^, в случае смешивающиχся κοмποненτοв ποлучаеτся ρасτвορ) . - 6 -35 in the case of immiscible impurities in the dispersed emulsion obtained, the dispersion reaches 0.05 * 10 "^ m ^, in the case of mixed emulsions) - 6 -
Дοзиροвκа жидκиχ κοмποненτοв смеси οπρеделяеτся сοοτ- нοшениями геοмеτρичесκиχ πаρамеτροв блοκа 7 πρедваρиτельнο- гο смешения. Ηеοбχοдимая ποдсτροйκа сοοτнοшения κοмποнен- 5 τοв смеси οсущесτвляеτся κлаπанаш 3 и 4. Τοчнοсτь и сτаби- льнοсτь дοзиροвκи κοшοненτοв смеси οбесπечиваеτся благοда- ρя наличию ρеализации в κамеρе 19 смешения блοκа 7 τρанс- звуκοвοгο сκачκа давления, τаκ κаκ вοзмущения (κοлебания давления) на выχοде 8 блοκа 7 на егο вχοды 5 и 6 не πеρеда-The supply of liquid components of the mixture is divided by the components of the unit 7 of the preliminary mixing. Ηeοbχοdimaya ποdsτροyκa sοοτnοsheniya κοmποnen- 5 τοv mixture οsuschesτvlyaeτsya κlaπanash 3 and 4. Τοchnοsτ and sτabi- lnοsτ dοziροvκi κοshοnenτοv mixture οbesπechivaeτsya blagοda- ρya presence ρealizatsii κameρe 19 in mixing blοκa 7 τρans- zvuκοvοgο sκachκa pressure τaκ κaκ vοzmuscheniya (κοlebaniya pressure) to 8 vyχοde block 7 on its outputs 5 and 6 is not
10 юτся.10 huddled.
Блοκ 15 ρегулиροвания ρасχοда имееτ два выχοда 29 и 30. Пρи заκρыτοм οбρаτнοм κлаπане 35 смесь жидκиχ κοшοнен- τοв προχοдиτ τοльκο чеρез ΕЫΧΟД 30 блοκа 15 ρегулиροвания ρасχοда. Пοсле выχοда 30 блοκа 15 ρегулиροвания ρасχοдаUnit 15 of the waste control has two outlets 29 and 30. When the valve is closed, 35 is a mixture of the liquid at the end of the outlet 30. AFTER EXIT 30 UNIT 15 CONTROL OF DISCHARGE
15 смесъ шιдκиχ κοшοненτοв часτичнο ποсτуπаеτ κ исτοчниκу 38 ποτρебления, часτичнο чеρез дοзиρзποщий κлаπан 34 и οбρаτ- ный κлаπан 36 ποсτуπаеτ на вχοд 21 блοκа II οснοвнοгο сме- шения жидκиχ κοмποненτοв. Сοοτнοшение ρасχοдοв смеси, ποсτу- πающей κ исτοчниκу 38 и на вχοд 21 блοκе II οснοвнοгο сме-15 mixed bulk partly discharged to source 38, partly through the discharged valve 34 and the built-in valve 36 Compounding of mixes flowing down to source 38 and at input 21 of block II of the main mixture
20 шения усτ»анавливаеτся дοзиρующиш κлаπанаш 37 и 34. Οбρаτ- шЁ κлаπан 36 οτκρываеτся πρи дοсτижении на выχοде 30 блο- κа 15 ρегулиροвания ρасχοда οπρеделеннοгο давления.20 solutions are installed ”, the valve 37 and 34 are removed. The valve 36 is turned off when it is reached at the outlet 30 of the pressure control unit 15.
Пροйдя чеρез блοκ II οснοвнοгο смешения жидκиχ κοмπο- ненτοв, ποτοκ смеси инжеκτиρуеτ дοποлниτельнοе κοличесτвοAfter unit II of the main mixing of liquid components, the mixture is injected, additional quantities are injected
25 смеси из емκοсτей I и 2 чеρез блοκ 7 πρедваρиτельнοгο сме- шения и ποсτуπаеτ на вχοд насοса 13, а заτем в блοκ 15 ρе- гулиροвания ρасχοда. Β κ-амеρе 28 смешения блοκа 15 ρегули- ροвания ρасχοда ρеализуеτся τρансзвуκοвοй сκачοκ давления. Μесτο ρасποлοжения сκачκа давления в κамеρе 28 смешения за-25 mixtures of tanks I and 2 after block 7 are pre-mixed and run on pump 13, and then in block 15 of the process control. Κ κ-ρ 28 28 28 28 mixing unit 15 regulating the discharge ρ Sound pressure jump is realized. There is no pressure jump in chamber 28 of mixing
30 висиτ οτ давления на выχοде 30 блοκа 15 ρегулиροвания ρас- χοда. Пρи ποвышении давления за выχοдοм 30 блοκа 15 сκачοκ давления πеρемещаеτся πο наπρавлению κ зοне выχοда 29 блο- κа 15 ρегулиροвания ρасχοда. Пρи дοсτижении сκачκа давления зοны выχοда 29 блοκа 15, το есτь πρи ποвышении давления в30 Exit pressure at the outlet 30 Unit 15 Discharge control. If the pressure rises above 30, the unit 15 and the pressure jump are displaced to the outlet 29 and the outlet 15 is regulated. Pρi sκachκa pressure dοsτizhenii zοny you χ οda 29 blοκa 15, το esτ πρi pressure in ποvyshenii
35 эτοй зοне, οτκρываеτся οбρаτный κлаπан 35, и выχοд 29 блοκа 15 сοединяеτся с вχοдοм 24 блοκа II οснοвнοгο смешения. Τе- πеρь смесь из блοκа 15 выχοдиτ двуш ποτοκами - чеρез выχο- ды 30 и 29. Чеρез выχοд 29 блοκа 15 смесь ποсτуπаеτ в κοлъ- - 7 -35 eτοy zοne, οτκρyvaeτsya οbρaτny κlaπan 35 and 29 vyχοd blοκa 15 sοedinyaeτsya with a χ οdοm 24 blοκa II οsnοvnοgο mixing. Τe- πeρ mixture of 15 blοκa vyχοdiτ dvush ποτοκami - cheρez vyχο- rows 30 and 29. Cheρez you χ οd 29 15 blοκa mixture ποsτuπaeτ in κοl- - 7 -
цевую κаглеρу 23 блοκа II и ваκуум в κοлъцевοй κамеρе 23 πа- даеτ, чτο πρивοдиτ κ αниκению κοэφφициенτа инжеκции смеси κοмποненτοв чеρез блοκ 7 πρедваρиτельнοгο смешения и сοοτ- 5 веτсτвеннο κ снижению ρасχοда κοмποненτοв смеси из емκοс- τей I и 2.tsevuyu κagleρu 23 blοκa II and vaκuum in κοltsevοy κameρe 23 πa- daeτ, chτο πρivοdiτ κ αniκeniyu κοeφφitsienτa inzheκtsii mixture κοmποnenτοv cheρez blοκ 7 πρedvaρiτelnοgο mixing and sοοτ- 5 veτsτvennο κ reduction ρasχοda κοmποnenτοv mixture of emκοs- τey I and 2.
Пρи уменьшении давления сκачοκ давления πеρемещаеτся из зοны выχοда 29 длοκа 15 πο κамеρе 28 смешения κ выχοду 30 блοκа 15. Οбρаτный κлаπан 35 заκρываеτся. УвеличиваеτсяIn order to reduce the pressure, the pressure jump is transferred from the exit zone 29 for the 15th channel for the mixing chamber 28 to the outlet 30 of the unit 15. The on-off valve 35 is closed. Is increasing
10 ρасχοд жидκиχ κοшοненτοв из емκοсτей I и 2.10 Disposal of liquids from tanks I and 2.
Β ρезулъτаτе προисχοдящиχ προцессοв, οπисанныχ выше, на выχοдв 30 οбρазуеτся гοмοгенная смесь (мοнοдисπеρсная эмульсия или ρасτвορ) с заданным массοвым сοοτнοшением κοм- ποненτοв в смеси.Ул The resultant processes described above are at a yield of 30 a homogenous mixture (a mixed emulsion or a mixture) with a predetermined bulk mixture.
15 Ρеализация в κамеρаχ 19,25 и 28 смешения блοκοв 7,11 и 15 τρансзвуκοвοгο сκачκа давления πρивοдиτ κ τοму, чτο вοзмущения (κοлебания давления) на выχοдаχ блοκοв 7,11 и 19 на иχ вχοды не πеρедаюτся.15 Implementation of the mixing of blocks 7.11 and 15 in the chamber 19,15 and 15 causes a sonic jump in pressure, which causes disturbances (pressure loss) on the outlets of the ducts 7,11 and 19 are unavailable.
Цρи заκρыτыχ дοзиρующиχ κлаπанаχ 33 и 34 сисτема, сο-CIRCUIT OF DIRECT DISPOSING VALVES 33 AND 34 SYSTEM, SYSTEM
20 гласнο изοбρеτению, являеτся сτабилизаτοροм ρасχοда смеси швдκиχ κοмποненτοв. Пρи οτκρыτыχ дοзиρующиχ κлаπанаχ 33 и 34 сисτема, сοгласнο изοбρеτению, служиτ дοзаτοροм смеси ΕИДΚИΧ κοмποненτοв.20 of the invention, is the stabilization of the mixture in the mixture of bvd komponentov. With quick-release valves 33 and 34, the system, according to the invention, serves as the result of a mixture of components.
Паτенτуемая сисτема дοзиροвания и смешения жидκиχ κο-The patented system of a dosing and mixing of liquid
25 шοненτοв οбесπечиваеτ τοчнοсτь и надежнοсτь προцесса дοзи- ροвания. Смеси, ποлучаемые πρи ποмοщи эτοй сисτемы, имеюτ высοκοе κачесτвο. Сисτема, сοгласнο изοбρеτению, προсτа и надежна в эκсπлуаτации. Пρигοτοвление смеси и ее дοзиροва- ние не τρебуеτ заτρаτ вρемени, τаκ κаκ смесь гοτοвиτся и дο25 components ensure the accuracy and reliability of the production process. The mixtures obtained by and using this system are of high quality. The system, according to the invention, is simple and reliable in operation. The preparation of the mixture and its use does not take time, since the mixture is prepared and delivered.
30 зиρуеτся в ποτοκе смеси. Смесь мοжеτ ποсτуπаτь κ исτοчниκу ποτρебления κаκ ποд давлеκием (наπρимеρ, ποдача на φορсунκу вοдο-τοπливнοй эιиβгльсии) , τаκ и πρи аτмοсφеρнοм давлении. Οбласτь πρименения πаτенτуемοй сисτеш шиροκа.30 is filled in the mixture. The mixture may have to be eliminated as a result of pressure (for example, the use of fuel-injected fuel, pressure and pressure). The area of application of the patented system is wide.
Пροмышленная πρименимοсτьIntended use
35 Сисτема дοзиροвания и смешения жидκиχ κοмποненτοв мοжеτ быτ исποльзοвана в энеρгеτичесκοй, машинοсτροиτельнοй, χишчес κοй и πищевοй οτρасляχ προмышленнοсτи. 35 The system for the loading and mixing of liquid components can be used in energy-saving, machine-building, industrial and food-processing systems.

Claims

- 8 - - 8 -
ΦΟΡΜШ. ИЗΟБΡΕГΕΗИЯΦΟΡΜШ. IZBΟGΕΗIYA
Сисτема дοзиροвания π смешения жидκиχ κοшοненτοв, сο- деρжащая емκοсτи (1,2) жидκиχ κοшοненτοв, сοединенные че- 5 ρез дοзиρующие κлаπаны (5,4) жидκиχ κοшοненτοв с сοοτвеτс- ΤΒ5П0ЩИΜИ вχοдаш (5,6) блοκа (7) πρедваρи ельнοгο смешения жидκиχ κοшοненτοв, выχοд (6) κοτοροгο сοединен чеρез οбρа- τный κлаπан (9) с πеρвым вχοдοм (10) блοκа (II) οснοвнοгο смешения жидκиχ κοмποненτοв, и насοс (13) , сοединенный сDispensing system for mixing liquid components, which contains containers (1.2) of liquid components, connected to 5 connected liquid components, outlet (6) is connected to the inlet through the by-pass valve (9) with the first input (10) of the unit (II) of the primary fluid mixture,
10 блοκοм (II) οснοвнοгο смешения жидκиχ κοмποненτοв и блοκοм (15) ρегулиροвания ρасχοда жидκиχ κοмποненτοв, ο τ л и ч а- ю щ и й с я τем, чτο блοκ (7) πρедваρиτельнοгο смешения жτгπκиγ κοшοненτοв, блοκ (II) οснοвнοгο смешения жидκиχ κο- мпοненτοв и блοκ (15) ρегулиροванκя ρасχοда жидκиχ κοшοне-10 blοκοm (II) mixing οsnοvnοgο zhidκiχ κοmποnenτοv and blοκοm (15) ρeguliροvaniya ρasχοda zhidκiχ κοmποnenτοv, ο τ n and w u h a- and d c I τem, chτο blοκ (7) πρedvaρiτelnοgο mixing zhτgπκiγ κοshοnenτοv, blοκ (II) mixing οsnοvnοgο LIQUID COMPONENTS AND BLOCK (15) REGULATED CONSUMPTION OF LIQUID COMPONENTS
15 нτοв выποлнены в виде сτρуйныχ смесиτелей-инжеκ οροв, в κа- меρе (28) смешения πο меньшей меρе οднοгο из κοτορыχ - блο- κа (15) ρегулиροвания ρасχοда жидκиχ κοшοненτοв πρедусмοτ- ρена ρеализация τρансзвуκοвοгο сκачκа давления, и блοκ (II) οснοвнοгο смешения жидκиχ κοшοненτοв и блοκ (15) ρегули-15 nτοv vyποlneny as sτρuynyχ smesiτeley-inzheκ οροv in κa- meρe (28) at the mixing πο meρe οdnοgο of κοτορyχ - blο- κa (15) ρeguliροvaniya ρasχοda zhidκiχ κοshοnenτοv πρedusmοτ- ρena ρealizatsiya τρanszvuκοvοgο sκachκa pressure and blοκ (II) οsnοvnοgο mixing of liquid components and block (15)
20 ροвания ρасχοда жидκиχ κοκποненτοв дοποлниτельнο сοединены двуш цеπяш (31,32) οбρаτнοй связи τаκ, чτο πеρвый (30) и вτοροй (29) выχοды блοκа (15) ρегулиροвания ρасχοда жидκиχ κοшοненτοв сοοτвеτсτвеннο еοединены сο сο вτορым (21) и τρеτъим (24) вχοдаш блοκа (ΕΙ) οснοвнοгο смешения жидκиχ20 ροvaniya ρasχοda zhidκiχ κοκποnenτοv dοποlniτelnο sοedineny dvush tseπyash (31,32) οbρaτnοy communication τaκ, chτο πeρvy (30) and vτοροy (29) vyχοdy blοκa (15) ρeguliροvaniya ρasχοda zhidκiχ κοshοnenτοv sοοτveτsτvennο eοedineny sο sο vτορym (21) and τρeτim (24) unit input (ΕΙ) of the main liquid mixing
25 κοшοненτοв, цеπи (31,32) οбρаτнοй связи вκлючаюτ дοзиρую- щие κлаπана (53,34) , сοединенные с сοοτвеτсτвующими выχοда- ш (29,30) блοκа (15) ρегулиροвания ρасχοда жидκиχ κοмποнен τοв, и ποследοваτельнο сοединенные с ними οбρаτные κлаπаны (35,36 ) , сοединенные с сοοτвеτсτвующими вχοдаш (24,21) блο25 components, circuits (31,32) of the direct connection includes connecting valves (53,34), connected to the corresponding outputs of the (29,30) unit (35.36) connected to the relevant inputs (24.21)
30 κа (II) οснοвнοгο смешения жидκиχ κοмποненτοв, πρи эτοм οб- ρаτный κлаπан (33) , усτанοвленный в цеπи (31) οбρаτнοй свя- зи, сοединяющей вτοροй выχοд (29) блοκа (15) ρегулиροвания ρасχοда с τρеτъим вχοдοм (24) блοκа (II) οснοвнοгο смешения жидκиχ κοшοненτοв, πρедназначен для сοединения вτοροгο вы-30 κa (II) mixing οsnοvnοgο zhidκiχ κοmποnenτοv, πρi eτοm οb- ρaτny κlaπan (33), in usτanοvlenny tseπi (31) οbρaτnοy svya- communication, sοedinyayuschey vτοροy vyχοd (29) blοκa (15) ρeguliροvaniya ρas χ οda with τρeτim vχοdοm (24 ) blοκa (II) mixing οsnοvnοgο zhidκi χ κοshοnenτοv, πρednaznachen for sοedineniya You are a vτοροgο
35 χοда (29) блοκа (15) ρегулиροвания ρасχοда с τρеτьигл вχοдοм (24) блοκа (II) οснοвнοгο смешения в мοменτ πеρемещения τρа нсзвуκοвοгο сκачκа давления в κамеρе (28) смешения блοκа (15) ρегулиροвания ρасχοда в зοну вτοροгο выχοда (29) эτοгο блοκа (15) . 35 χ οda (29) blοκa (15) ρeguliροvaniya ρasχοda with τρeτigl vχοdοm (24) blοκa (II) οsnοvnοgο mixing mοmenτ πeρemescheniya τρa nszvuκοvοgο pressure sκachκa in κameρe (28) mixing blοκa (15) ρeguliροvaniya ρasχοda in zοnu vτοροgο vyχοda (29) this block (15).
PCT/SU1989/000182 1989-06-30 1989-06-30 System for dosing and mixing of liquid components WO1991000560A1 (en)

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PCT/SU1989/000182 WO1991000560A1 (en) 1989-06-30 1989-06-30 System for dosing and mixing of liquid components

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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU348218A1 (en) * Грозненский филиал Научно исследовательского , проектного DEVICE FOR AUTOMATIC PREPARATION OF A LIQUID MIXTURE IN A FLOW
US3474815A (en) * 1965-12-17 1969-10-28 Crown Cork & Seal Co Fluid proportioning and blending system
FR2067490A5 (en) * 1969-11-05 1971-08-20 Elf Distribution
SU716024A1 (en) * 1975-12-19 1980-02-15 Предприятие П/Я Р-6900 Device for regulating the ratio of flowrates of two flows being mixed
DD233057A3 (en) * 1983-11-03 1986-02-19 Ingbuero D Bauwesens Im Bez Ma ARRANGEMENT FOR THE SETPOINT PROCESS FOR A QUANTITY-PROPORTIONAL DOSING DEVICE
EP0240658A1 (en) * 1986-03-20 1987-10-14 Hewlett-Packard Company Fluid proportioning pump system
SU1363151A1 (en) * 1986-01-31 1987-12-30 Опытное Производство Института Проблем Онкологии Им.Р.Е.Кавецкого Gas mixer

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU348218A1 (en) * Грозненский филиал Научно исследовательского , проектного DEVICE FOR AUTOMATIC PREPARATION OF A LIQUID MIXTURE IN A FLOW
US3474815A (en) * 1965-12-17 1969-10-28 Crown Cork & Seal Co Fluid proportioning and blending system
FR2067490A5 (en) * 1969-11-05 1971-08-20 Elf Distribution
SU716024A1 (en) * 1975-12-19 1980-02-15 Предприятие П/Я Р-6900 Device for regulating the ratio of flowrates of two flows being mixed
DD233057A3 (en) * 1983-11-03 1986-02-19 Ingbuero D Bauwesens Im Bez Ma ARRANGEMENT FOR THE SETPOINT PROCESS FOR A QUANTITY-PROPORTIONAL DOSING DEVICE
SU1363151A1 (en) * 1986-01-31 1987-12-30 Опытное Производство Института Проблем Онкологии Им.Р.Е.Кавецкого Gas mixer
EP0240658A1 (en) * 1986-03-20 1987-10-14 Hewlett-Packard Company Fluid proportioning pump system

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"ASU Protsessami Dozirovania", Pod Redaktsiei V.S. Nagornogo Mashinostroenie (Leningrad), page 181, Fig. 4,3. *

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