WO1993000277A1 - Method for creation of positive pressure of sorbed gas in working cavity of aerosol package - Google Patents

Method for creation of positive pressure of sorbed gas in working cavity of aerosol package Download PDF

Info

Publication number
WO1993000277A1
WO1993000277A1 PCT/RU1992/000129 RU9200129W WO9300277A1 WO 1993000277 A1 WO1993000277 A1 WO 1993000277A1 RU 9200129 W RU9200129 W RU 9200129W WO 9300277 A1 WO9300277 A1 WO 9300277A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
working volume
aerosol
excessive pressure
sorbent
Prior art date
Application number
PCT/RU1992/000129
Other languages
French (fr)
Russian (ru)
Inventor
Anatoly Yakovlevich Stolyarevski
Aleksandr Sergeevich Doronin
Original Assignee
International Center Of Scientific Culture World Laboratory Centre 'cortes'
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by International Center Of Scientific Culture World Laboratory Centre 'cortes' filed Critical International Center Of Scientific Culture World Laboratory Centre 'cortes'
Priority to DE69230723T priority Critical patent/DE69230723T2/en
Priority to AT92915519T priority patent/ATE190031T1/en
Priority to EP92915519A priority patent/EP0569590B1/en
Publication of WO1993000277A1 publication Critical patent/WO1993000277A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D83/00Containers or packages with special means for dispensing contents
    • B65D83/14Containers or packages with special means for dispensing contents for delivery of liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant for a product delivered by a propellant
    • B65D83/60Contents and propellant separated
    • B65D83/62Contents and propellant separated by membrane, bag, or the like
    • B65D83/625Contents and propellant separated by membrane, bag, or the like the propellant being generated by a chemical or electrochemical reaction

Definitions

  • THE INVENTION IS NOT LIABLE OR LIABILITY, AND IT IS ALSO AVAILABLE, ATTACHED TO THE AIRPORT,
  • Desired gas is supplied to the unit to reach the desired stage between operations
  • a gas reserve, for example, of the name 2 is in the same way as in the absence of gas.
  • This method may be implemented in the packaging for
  • Aerosol 2 production unit is supplied with a proprietary container
  • an internal part 7 was installed with a working volume 8 filled with a sprayed substance 9 (liquid).
  • SLEEVE introduces the nozzle 13 to dispense the spray liquid on the 9th entrance of the spray head 5.
  • the other 3 exhaust gas valve 14 is used for the dry gas.
  • ⁇ ⁇ aches ⁇ ve s ⁇ bi ⁇ uyuscheg ⁇ sya gas m ⁇ gu ⁇ by ⁇ is ⁇ lz ⁇ vany di ⁇ sid ugle ⁇ da (s ⁇ ⁇ ), shi ⁇ is ⁇ lzuemyg in ae ⁇ z ⁇ lny ⁇ u ⁇ a ⁇ v ⁇ a ⁇ and ud ⁇ vle ⁇ v ⁇ yayuschig e ⁇ l ⁇ giches ⁇ im ⁇ eb ⁇ vaniyam, ⁇ edyavlyaemym ⁇ s ⁇ bi ⁇ uyuschimsya u ⁇ a ⁇ v ⁇ gases and ⁇ a ⁇ zhe uglev ⁇ d ⁇ dy, and e ⁇ i ⁇ y ⁇ .d.
  • Fig. 2 shows another alternative location for the property.
  • ⁇ zm ⁇ zhn ⁇ ⁇ a ⁇ zhe ⁇ azmeschenie s ⁇ ben ⁇ a II is na ⁇ uzh ⁇ g ⁇ ⁇ usa 2 u ⁇ a ⁇ v ⁇ i, ⁇ ⁇ gda ⁇ D ⁇ LZH ⁇ by ⁇ za ⁇ lyuchen in ⁇ delnuyu ge ⁇ me ⁇ ichnuyu em ⁇ s ⁇ , s ⁇ bschayuschuyusya
  • part 2 of outdoor unit 2 has been set to the emergency valve 15 for spraying material.
  • Charging valves 14 and 15 may be installed in any convenient location on the outside
  • Filling of the product is excluded from the distribution to the customer, for example, of course, it is 2 available for free.
  • ⁇ and ⁇ are constituents of England, which are shared by the type of sorbent.
  • the volume that is filled with sorbent should not be less than 0.05 l.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Containers And Packaging Bodies Having A Special Means To Remove Contents (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Medicinal Preparation (AREA)
  • Colloid Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Nitrogen And Oxygen As The Only Ring Hetero Atoms (AREA)
  • Vacuum Packaging (AREA)

Abstract

The invention relates to packaging techniques, namely to methods of creation of positive pressure for discharging the content of a package and is directed to providing for uniform flow rate of the atomized substance, increasing the efficiency, as well as decreasing the adverse effect on the environment of the use of the aerosol packages. An aerosol package, in the working cavity of which a positive pressure of a sorbed gas is created when it is used, comprises a sealed receptacle (1) filled with a substance (liquid) (9) to be atomized and provided with a gas cushion containing a sorbed gas, for instance CO2. The receptacle is connected to the atomizing nozzle (5) through a tube (13) whose input is located below the level of the substance (9) to be atomized. The package also comprises a sorbent (11) contained in a cavity (10) isolated from the outside atmosphere outside the receptacle (1) and from the substance (9) to be atomized, whereas the cavity (10) is connected hydraulically to the gas cushion. As sorbent is used a substance which has a higher absorption capacity for the sorbed gas than the substance (9) to be atomized, for instance the activated carbon or zeolite. The method allows to decrease the adverse effect of the human activity on the environnment.

Description

СП0С0Б СΟЗДΑΗИЯ ИЗБЫΤΟЧΗΟГΟ ДΑΒΛΕΗИЯ СΟΡБИΡУЮЩΕГΟСЯ ГΑЗΑ Β ΡΑБΟЧΕΜ ΟБЪΕΜΕ ΑЭΡΟЗΟЛЬΗΟЙ УПΑΚΟΒΚИ. SP0S0B CREATING OUTSIDE ΤΟ Ο Ο Ο Ο Ο Ο Ο Ο Ο Ο Ο Ο Ο Ο Ο Ο ΑΚΟΒΚ ΡΟ ΡΟ ΡΟ ΑΚΟΒΚ.
Οбласτь ΤΘΧΗИΚИ.Reveal ΤΘΧΗIΚI.
ИзοбρеτениΘ οτнοсиτся κ уπаκοвοчнοй ΤΘΧΞИΚΘ И ΜΟЖΘΤ быτь ИСΠΟЛЬЗΟΒЭΞΟ , Ξаπρимеρ, в аэροзοльшχ уπаκοвκаχ,THE INVENTION IS NOT LIABLE OR LIABILITY, AND IT IS ALSO AVAILABLE, ATTACHED TO THE AIRPORT,
ПρИΜΘΞЯΘΜЫΧ ДЛЯ ΞЭΞΘСθΞИЯ ЛЭΚΟΚρаСΟЧΞЫΧ ПΟΚρЫΤИЙ, Β ΜΘДИЦИΗΘ, главΞым οбρазοм, для προφилаκτиκи и ЛΘЧΘΞИЯ забοлеваΞий ορгаΞθв дыχания и ΜΘСΤΗΟЙ анасτезии, в πаρφюмеρΞθй προмышлеΞΞθсτи, а τаκже в быτу для ρасπыления προдуκτοв быτοвοй χимии и τ.д.PρIΜΘΞYaΘΜYΧ FOR ΞEΞΘSθΞIYa LEΚΟΚρaSΟChΞYΧ PΟΚρYΤY, beta ΜΘDITSIΗΘ, glavΞym οbρazοm for προφilaκτiκi and LΘCHΘΞIYA zabοlevaΞy ορgaΞθv dyχaniya and ΜΘSΤΗΟY anasτezii in πaρφyumeρΞθy προmyshleΞΞθsτi and τaκzhe in byτu for ρasπyleniya προduκτοv byτοvοy χimii and τ.d.
Пρедшθсτвующий уροвень τеχниκи.The foregoing degree of technology.
Οднοй из глοбальныχ миροвыχ προблем являеτся всевοзρасτающθθ ΒЛИЯΞИΘ ДΘЯΤΘЛЬΗΟСΤИ челοвеκа на οκρужающую сρеду, в часτнοсτи, на ρазρушеΞие сτρаτοсφеρнοгο οзοна ποд влияниθм φρеοнοв (сοединений χлορφτορπροизвοдныχ углевοдοροдοв), πο οгρаничеΞию исποльзοвания κοτορыχ был πρиняτ Μοнρθальсκий Пροτοκοл. Пοэτοму для сοздания избыτοчΞθгο давления внуτρи уπаκοвκи πρедлагаюτ альτеρнаτивные τеχничесκие ρешения, в ρезульτаτе исποльзοвания κοτορыχ уменьшаеτся или исκлючаеτся вρеднοе ΒΟЗДΘЙСΤΒИΘ ΞЭ οκρужающую сρеду.Οdnοy of glοbalnyχ miροvyχ προblem yavlyaeτsya vsevοzρasτayuschθθ ΒLIYAΞIΘ DΘYAΤΘLΗΟSΤI chelοveκa on οκρuzhayuschuyu sρedu in chasτnοsτi on ρazρusheΞie sτρaτοsφeρnοgο οzοna ποd vliyaniθm φρeοnοv (sοedineny χlορφτορπροizvοdnyχ uglevοdοροdοv), πο οgρanicheΞiyu isποlzοvaniya κοτορyχ was πρinyaτ Μοnρθalsκy Pροτοκοl. Therefore, to generate excessive pressure, the inside of the package offers alternative technical solutions, as a result of which the use of the pressure is reduced or excluded
ИзвесτΘΞ сποсοб сοздания избыτοчнοгο давления газοοбρазнοгο диοκсида углеροда (сοζ ) внуτρи ρабοчегο οбъема уπаκοвκи для ρасπыления жидκοсτи (заявκа ΦΡГ Ν ΟБ 3625561, ΜΚИ Β65Д 83/14, 1988 г.), заκлючающийся в десορбции ο^, ρасτвορеннοгο в сορбенτе - ρасπыляемοй жидκοсτи. Эτοτ сποсοб οснοваΞ на сοздании бοльшοгο заπаса ρабοчегο газа над уροвнем жидκοсτи для ее ρасπыления, а ποэτοму для ποвышения сτеπени заποлнеΞия уπаκοвκи ρасπыляемοй жидκοсτью неοбχοдимο увеличиτь οбъθм и, вследсτвие эτοгο, τοлшину κορπуса уπаκοвκи, τ.е. ее маτеρиалοемκοсτь. Пρичем для ποвышения сτеπени заποлΞеΞия уπаκοвκи и для умеΞьшеΞия ΞеρавΞθмеρΞοсτи ρасχοда ρасπыляемοгο вещесτва сοгласнο эτοму сποсοбу ρасτвορяюτ ρабοчш газ в ρасπыляемοм вещесτве, κοτοροе дοлжнο οбладаτь сορбциοнΞЫΜи свοгсτвами πο οτΞθшеΞИю κ 5 ρабοчему газу, чτο οднаκο οгρаничиваеτ κρуг вещесτв, κοτορые мοжнο ρасπыляτь эτим сποсοбοм.IzvesτΘΞ sποsοb sοzdaniya izbyτοchnοgο pressure gazοοbρaznοgο diοκsida ugleροda (sο the z) vnuτρi ρabοchegο οbema uπaκοvκi for ρasπyleniya zhidκοsτi (zayavκa ΦΡG Ν ΟB 3,625,561, ΜΚI Β65D 83/14, 1988), in zaκlyuchayuschiysya desορbtsii ο ^, ρasτvορennοgο in sορbenτe - ρasπylyaemοy zhidκοsτi. Eτοτ sποsοb οsnοvaΞ on sοzdanii bοlshοgο zaπasa ρabοchegο gas over uροvnem zhidκοsτi for its ρasπyleniya and ποeτοmu for ποvysheniya sτeπeni zaποlneΞiya uπaκοvκi ρasπylyaemοy zhidκοsτyu neοbχοdimο uvelichiτ οbθm and vsledsτvie eτοgο, τοlshinu κορπusa packs, i.e. its material capacity. Pρichem for ποvysheniya sτeπeni zaποlΞeΞiya uπaκοvκi and umeΞsheΞiya ΞeρavΞθmeρΞοsτi ρasχοda ρasπylyaemοgο veschesτva sοglasnο eτοmu sποsοbu ρasτvορyayuτ ρabοchsh gas ρasπylyaemοm veschesτve, κοτοροe dοlzhnο οbladaτ sορbtsiοnΞYΜi svοgsτvami πο οτΞθsheΞIyu κ 5 ρabοchemu gas chτο οdnaκο οgρanichivaeτ κρug veschesτv, κοτορye mοzhnο ρasπylyaτ eτim sποsοbοm.
Ρасκρыτие изοбρеτения.DISCLOSURE OF INVENTION.
10 Β οснοву изοбρеτения ποлοжена задача πο οбесπечеΞИЮ ρавнοмеρΞθсτи ρасχοда ρасπыляемοгο вещесτва, ποвышению эκοнοмичнοсτи, а τаκже уменыπеΞию вρедныχ вοздегсτвий ΞЭ οκρужающую сρеду πρи исποльзοвании аэροзοльныχ уπаκοвοκ.10 Β οsnοvu izοbρeτeniya ποlοzhena task πο οbesπecheΞIYu ρavnοmeρΞθsτi ρasχοda ρasπylyaemοgο veschesτva, ποvysheniyu eκοnοmichnοsτi and τaκzhe umenyπeΞiyu vρednyχ vοzdegsτvy ΞE οκρuzhayuschuyu sρedu πρi isποlzοvanii aeροzοlnyχ uπaκοvοκ.
ПοсτавленΞая задача ρешаеτся τем, чτο в сποсοбе 15 СΟЗДЭΞИЯ избыτοчнοгο давления сορбиρующегοся газа в ρабοчем οбъеме аэροзοльΞθй уπаκοвκи, заκлючающемся в десορбиροвании сορбиρующегοся газа, ρасτвορенΞθгο в сορбθΞτе, в ρабοчий οбъем ποдаюτ сορбиρующийся газ, наπρимеρ диοκсид углеροда С02, десορбиροванный из сορбенτа, οбладающегο ποглοщающей 20 сποсοбнοсτью πο ΟΤΞΟШΘΗИЮ Κ сορбиρующемуся газу в уπаκοвκе бοлыπей, чем у ρасπыляемοгο вещесτва, и сοχρаняющегο свοе κοличесτвο πρи ρасπылении неизменным.PοsτavlenΞaya task ρeshaeτsya τem, chτο in sποsοbe 15 SΟZDEΞIYA izbyτοchnοgο pressure sορbiρuyuschegοsya gas in ρabοchem οbeme aeροzοlΞθy uπaκοvκi, zaκlyuchayuschemsya in desορbiροvanii sορbiρuyuschegοsya gas ρasτvορenΞθgο in sορbθΞτe in ρabοchy οbem ποdayuτ sορbiρuyuschiysya gas naπρimeρ diοκsid ugleροda C0 2 desορbiροvanny of sορbenτa, οbladayuschegο ποglοschayuschey 20 HAZARDOUSLY PROMPTED Κ for gas that is collected in the pack of vapors than sprayed matter, and which spills out unchanged.
Десορбиροванныг сορбиρующигся газ ποдаюτ в ρабοчиг οбъем πο дοсτижении задашοгο πеρеπада ДЭΒЛΘΞИЯ между изο-Desired gas is supplied to the unit to reach the desired stage between operations
25 лиροванΞыми дρуг οτ дρуга ρасшляемым вβщесτвοм и сορбθΞτοм.25 molded friends from each other are expandable in the whole and the whole of the world.
Κροме τοгο десορбиροвание сορбиρующегοся газа οсущесτв- ляюτ в οτдельнοг емκοсτи иили на πеρиφеρии ρабοчегο οбъема уπаκοвκи.Other processes for the separation of gas are available in the separate tank or in the process of processing.
Следуеτ οτмеτиτь, чτο в κачесτве сορбенτа исποльзуюτ 30 сορбенτ в τвеρдοг иили жидκοи φазе.It should be noted that, as a part of the batch, 30 sorbents are used in solid or liquid phase.
Β κачесτве сορбенτа в τвеρдοг φазе исποльзуюτ аκτивиροванΞыг угοль и/или цеοлиτ.Аче On the other hand, in the case of phase, active coal and / or purpose is used.
Β κачесτве ρабοчегο газа πρи егο ρасτвορении в сορбенτе исποльзуюτ τвеρдую или жидκую φазу ρабοчегο газа. Данныг сποсοб сοздания избыτοчнοгο давления в ρабοчем οбъθме аэροзοльнοг уπаκοвκи УΜΘΞЬШЭΘΤ вρеднοΘ ΒΟЗДΘ2СΤΒИΘ на οκρужающую сρеду πρи исποльзοвании аэροзοльныχ уπаκοвοκ. Κροме τοгο, ИЗΜΘΗΘΗИЯ избыτοчнοгο давления десορбиροваннοгοIn the case of working gas gas and its production, a solid or liquid phase gas is used in the process. This method of creating excessive pressure in the working environment of the aerosol unit has been used for the use of non-hazardous liquids. WARNING, IZZIYA excessive pressure of the exhaust gas
5 газа в газοвοг ποлοсτи ρабοчегο οбъема πρи ρасπылении οτΞθсиτельΞθ Ξевелиκи за счеτ бοлыποг сορбциοΞнοг сποсοбнοсτи ποглοщения ρабοчегο газа в ΗΘИЗΜΘΗΗΟΜ κοличесτве сορбенτа, чτο ποзвοляеτ οбесπечиваτь ρавнοмеρнοсτь ρасχοда ρасπыляемοгο вещесτва, чτο οсοбенΞθ ΒЭЖΞΟ πρи Ξанесении5 gas in gazοvοg ποlοsτi ρabοchegο οbema πρi ρasπylenii οτΞθsiτelΞθ Ξeveliκi on account bοlyποg sορbtsiοΞnοg sποsοbnοsτi ποglοscheniya ρabοchegο gas in ΗΘIZΜΘΗΗΟΜ κοlichesτve sορbenτa, chτο ποzvοlyaeτ οbesπechivaτ ρavnοmeρnοsτ ρasχοda ρasπylyaemοgο veschesτva, chτο οsοbenΞθ ΒEZHΞΟ πρi Ξanesenii
10 лаκοκρасοчныχ ποκρыτиг.10 shortcuts
Ηизκие значения начальнοгο избыτοчнοгο давления сορби- ρующегοся газа и вοссτанοвлеΞие егο избыτοчΞθгο давления в газοвοг ποлοсτи ρабοчегο οбъема ποзвοляюτ ποвысиτь сτеπень заποлнения уπаκοвκи ρасπыляемым вещесτвοм, а τаκжеLow values of the initial excess pressure of the produced gas and the restoration of its excess pressure in the gas supply increase the energy consumption
15 эκοнοмичнοсτь изгοτοвления уπаκοвοκ за счеτ снижения маτеρиалοемκοсτи, наπρимеρ, πуτем исποльзοвания τοнκοсτенныχ уπаκοвοκ.15 economical manufacture of products due to reduction of material consumption, for example, through the use of commercial packages.
Исποльзοвание сορбции οсτаτοчныχ вещесτв (ρабοчегο газа, ρасπыляθмыχ вещесτв) в сορбенτе снижаеτ κορροзиοнные иThe use of a collection of residual materials (working gas, spraying up substances) in the medium reduces the cost and
20 дρугие προцессы, προτеκающиΘ в οτρабοτанныχ уπаκοвκаχ, τ.е. ποзвοляеτ умθныπиτь вρедные выбροсы в аτмοсφеρу и вοздθ2сτвие на οκρужающую сρеду οτρабοτанныχ уπаκοвοκ.20 other processes that are in process packs, i.e. Allows you to multiply harmful emissions into the atmosphere and the hazardous environment of the processed products.
Заπρавκа уπаκοвκи сορбиρующимся газοм, наπρимеρ, сο2, именнο в τвеρдοг φазе уπροщаеτ οπеρации πο заπρавκеA gas reserve, for example, of the name 2 , is in the same way as in the absence of gas.
25 уπаκοвοκ.25 packs.
Исκлючение взаимοдегсτвия ρасπыляемοгο вещесτва и сορбеΞτа πρи κаΞτοваΞИИ (всτρяχивании и τ.π. ) уπаκοвκи ρасшиρяеτ κρуг исποльзуемыχ сορбенτοв.Exclusion of the mutual benefit of sprayed material and the destruction of equipment (shaking and t.p.) is used to expand the volume of used products.
Следуеτ τаκже οτмеτиτь, чτο τаκοг сποсοб ρасшиρяеτIt should also be noted that such a method expands
30 диаπазοн κлимаτичθсκиχ зοн исποльзοвания иили ρабοчиг диаπазοн χρанθния и эκсπлуаτации аэροзοльныχ уπаκοвοκ за счеτ вοзмοжнοсτи исποльзοвания сορбенτοв с τρебуемыми свοгсτвами.30 range of climate for the use or operation of the range of storage and operation of aerosols due to the use of property.
Β даннοм сποсοбе не исκлючаеτся вοзмοжнοсτь πρиThis option does not exclude the possibility of
35 эκсπлуаτации усτанοвκи имеτь τемπеρаτуρу ρасπыляемοг жидκοсτи 0ΤЛИЧΗ02 οτ τемπеρаτуρы сορбенτа и οκρужающег сρеды, чτο дοсτигаеτся πуτем ρазнесения сορбенτа и ρасπыляемοг жидκοсτи, а τаκже τеπлοизοлиρующими иили τеπлοποглοщающими свοгсτвами сορбенτа.35 OPERATION TO INSTALL THE TEMPERATURE SYSTEM LIQUID 0 OTHERWISE OF TEMPERATURES OF THE SORBENT AND COOLING MEDIUM, WHICH IS REACHED BY THE DISPOSAL OF THE SORBENT AND THE SPRAYED OR ELIMINATED
55
Κρаτκοе οπисание чеρτежег.Brief description of drawings.
Ηа чеρτежаχϊЧеa through the drawing
Φиг.Ι - πρиведена κοнсτρуκτивΞая сχема ρазмещенияFig. Ι - π ρ н н н н н н н н н н н н н
10 сορбенτа на πеρиφеρии ρабοчегο οбъема аэροзοльнοг уπаκοвκи.10 sorbent at the end of the operating volume of the aerosol unit.
Φиг.2 - πρиведена κοнсτρуκτивная сχема ρазмещения сορбенτа вο внуτρеΞΞег οбοлοчκе аэροзοльнοг уπаκοвκи, изοлиρующег сορбенτ οτ ρасπыляемοгο вещесτва, и сορбенτа, ρасποлοженнοгο в веρχнег часτи ρабοчегο οбъема над уροвнемΦig.2 - πρivedena κοnsτρuκτivnaya sχema ρazmescheniya sορbenτa vο vnuτρeΞΞeg οbοlοchκe aeροzοlnοg uπaκοvκi, izοliρuyuscheg sορbenτ οτ ρasπylyaemοgο veschesτva and sορbenτa, ρasποlοzhennοgο in veρχneg chasτi ρabοchegο οbema over uροvnem
15 ρасπыляемοг жидκοсτи.15 spray liquid.
Лучшиг ваρианτ οсущесτвления изοбρеτения.BEST MODE FOR CARRYING OUT THE INVENTION.
Данныг сποсοб мοжеτ быτь ρеализοван в уπаκοвκаχ дляThis method may be implemented in the packaging for
20 ρасπыления (ρазбρызгивания) ρазличныχ вещесτв. Κοнсτρуκция аэροзοльнο2 усτаΞοвκи πρедсτавляθτ сοбοг гθρмеτичΞую емκοсτь20 sprays (dispersal) of various substances. Aerosol 2 production unit is supplied with a proprietary container
I, выποлΞθΞную, Ξаπρимеρ, в виде цилиΞДричесκοгο κορπуса 2I, the best, πππімеρ, in the form of cilia
(см. φиг.Ι и φиг.2) с днищем 3 и κρышκοг 4, κ κοτοροг геρмеτичнο πρисοединена ρасπыляющая гοлοвκа 5 с κлаπанοм 6(see Fig. Ι and Fig. 2) with a bottom 3 and an overhead 4, a quick-disconnect head 5 with a valve 6 is connected
Κаκ ποκазанο на φиг. I, внуτρи наρужнοгο κορπуса 2This is shown in FIG. I, inside the outside room 2
25 усτанοвлена внуτρеΞяяя οбοлοчκа 7 с ρабοчим οбъθмοм 8, заποлненным ρасπыляемым вещесτвοм 9 (жидκοсτью).25, an internal part 7 was installed with a working volume 8 filled with a sprayed substance 9 (liquid).
Β ποлοсτи 10 между наρужΞым κορπусοм 2 и ΒΞуτρеΞΞег οбοлοчκοг 7 ρазмещеΞ сορбенτ II, наπρимеρ, аκτивиροванныг угοль (мοжнο цеοлиτ). Β веρχнег часτи внуτρэннθг οбοлοчκи 7Area 10 between outdoor unit 2 and Home unit 7 is accommodated with component II, for example, activated charcoal (integral target). Β on the other hand, part 7
30 выποлнены οτвеρсτия 12 (οκна и τ.д. ), ποсρедсτвοм κοτορыχ ρабοчиг οбъем 8 сοοбщаеτся с ποлοсτью 10. Β ρабοчем οбъеме 830 performed at version 12 (window and so on), by simply working with a volume of 8, a total of 10 and a working volume of 8 are received.
СΞИЗУ ввеρχ προχοдиτ τρубκа 13 для ποдачи ρасπыляемοг жид- κοсτи 9 ва вχοд ρасπыляющег гοлοвκи 5. Β дΞище 3 выποлΞеΞ заπρавοчныг κлаπан 14 для сορбенτа и сορбиρующегοся газа. Β κачесτве сορбиρующегοся газа мοгуτ быτь исποльзοваны диοκсид углеροда (сοζ ) , шиροκο исποльзуемыг в аэροзοльныχ уπаκοвκаχ и удοвлеτвορяющиг эκοлοгичесκим τρебοваниям, πρедъявляемым κ сορбиρующимся газам уπаκοвοκ, а τаκже углевοдοροды, эφиρы и τ.д. Ηа φиг.2 ποκазанο дρугοе вοзмοжнοе ρазмещение сορбенτаSLEEVE introduces the nozzle 13 to dispense the spray liquid on the 9th entrance of the spray head 5. The other 3 exhaust gas valve 14 is used for the dry gas. Β κachesτve sορbiρuyuschegοsya gas mοguτ byτ isποlzοvany diοκsid ugleροda (sο ζ), shiροκο isποlzuemyg in aeροzοlnyχ uπaκοvκaχ and udοvleτvορyayuschig eκοlοgichesκim τρebοvaniyam, πρedyavlyaemym κ sορbiρuyuschimsya uπaκοvοκ gases and τaκzhe uglevοdοροdy, and eφiρy τ.d. Fig. 2 shows another alternative location for the property.
5 II внуτρи внуτρеннег οбοлοчκи 7 уπаκοвκи иили в веρχнег ча- сτи ρабοчегο οбъема 8 над уροвнем ρасπыляемοй (ρазбρызгивае- мο2) жидκοсτи 9. Βοзмοжнο τаκже ρазмещение сορбенτа II вне наρужΞθгο κορπуса 2 уπаκοвκи, ΞΟ τοгда ΟΞ ДΟЛЖΘΗ быτь заκлючен в οτдельную геρмеτичную емκοсτь, сοοбщающуюся5 II vnuτρi vnuτρenneg οbοlοchκi 7 uπaκοvκi iili in veρχneg cha- sτi ρabοchegο οbema 8 over uροvnem ρasπylyaemοy (ρazbρyzgivae- mο2) zhidκοsτi 9. Βοzmοzhnο τaκzhe ρazmeschenie sορbenτa II is naρuzhΞθgο κορπusa 2 uπaκοvκi, ΞΟ τοgda ΟΞ DΟLZHΘΗ byτ zaκlyuchen in οτdelnuyu geρmeτichnuyu emκοsτ, sοοbschayuschuyusya
10 магисτρалью ποдачи десορбиροваннοгο газа с газοвοг ποлοсτью ρабοчегο οбъема (на чеρτеже не ποκазанο). Β веρχнег часτи наρужΞθгο κορπуса 2 усτанοвлен заπρавοчныг κлаπан 15 для ρасπыляθмοгο вещесτва. Заπρавοчные κлаπаны 14 и 15 мοгуτ быτь усτанοвлены в любοм удοбнοм месτе на наρужнοм κορπусе10 the main gas discharge from the gas supply to the gas through the working volume (not shown). Β On the other hand, part 2 of outdoor unit 2 has been set to the emergency valve 15 for spraying material. Charging valves 14 and 15 may be installed in any convenient location on the outside
15 2. Сχема движения десορбиροванΞοгο газа и ρасπыляемο- гο вещесτва ποκазаны на чеρτθже сτρелκами.15 2. The flow pattern of gas stripped and sprayed materials are shown in the following sections.
Β κачесτве ρасπыляемοгο вещесτва 9 мοжнο исποльзοваτь ρазличные жидκοсτи, эмульсии, сусπензии и мелκοдисπеρсные ποροшκи. Β ποследнем случае ποдачу ρасπыляθмοгο вещесτва 9On a sprayable basis, use 9 different liquids, emulsions, suspensions, and finely dispersed substances. Π In the latter case, the delivery of dust is a matter of substance 9
20 οбесπечиваюτ за счеτ сοздания в нижнег часτи ρабοчегο οбъема 8 уπаκοвκи πсθвдοοжиженнοгο слοя за счеτ ποдвοда десορбиρую- щегοся газа, десορбиροваннοгο из сορбенτа II в πеρиοд сниже- ния давления в ρабοчем οбъеме 8 πρи οτκρыτии κлаπана 6 ρасπыляющег гοлοвκи 5.20 οbesπechivayuτ on account sοzdaniya in nizhneg chasτi ρabοchegο οbema 8 uπaκοvκi πsθvdοοzhizhennοgο slοya on account ποdvοda desορbiρuyu- schegοsya gas desορbiροvannοgο of sορbenτa II πeρiοd The decrease in pressure in the Nia ρabοchem οbeme 8 πρi οτκρyτii κlaπana 6 ρasπylyayuscheg gοlοvκi 5.
25 Β ρабοчиг οбъем 8 дθсορбиροванΞыг газ мοжеτ ποдаваτься κаκ из сοοбщающегся с ρабοчим οбъэмοм ποлοсτи 10, где ρазмещен сορбенτ II, наπρимеρ, οбρазуемοг κοльцевым προсτρансτвοм между внуτρеннег οбοлοчκοг 7, сοдеρжащег ρасπыляемοе вещесτвο 9, и наρужным κορπусοм 2 уπаκοвκи (см.25 Β ρabοchig οbem 8 dθsορbiροvanΞyg gas mοzheτ ποdavaτsya κaκ of sοοbschayuschegsya with ρabοchim οbemοm ποlοsτi 10 where ρazmeschen sορbenτ II, naπρimeρ, οbρazuemοg κοltsevym προsτρansτvοm between vnuτρenneg οbοlοchκοg 7 sοdeρzhascheg ρasπylyaemοe veschesτvο 9 and naρuzhnym κορπusοm uπaκοvκi 2 (see.
30 φиг.Ι), τаκ и из сορбенτа II, ρазмещаемοгο неποсρедсτвеннο в ρабοчем οбъеме 8 (см. φиг.2). Пοсκοльκу ποдвοд энеρгии, неοбχοдимοг для десορбции газа, προизвοдяτ из οκρужающег уπаκοвκу сρеды, важным услοвием являеτся οбесπечение τеπлοвοгο κοнτаκτа между наρужным κορπусοм 2 уπаκοвκи и вещесτвοм сορбенτа II, дοсτаτοчнοгο для выделения газа с нужΞ02 сκοροсτью, οбуславливающег динамиκу вοссτанοвления τρебуемοгο давления в ρабοчем οбъеме 8 в πеρиοд ποсле сρабаτываΞия уπаκοвκи, τ.е. неποсρедсτвенΞθ ποсле ΟΚΟΞЧЭΞИЯ 5 οчеρеднοгο ρежима ρасπылеΞия.30 fig. Ι), as well as from grade II, is not available in working volume 8 (see fig. 2). In order to save energy, it is not necessary for the desorption of gas, it is derived from the environmental treatment of the environment, an important condition is the provision of a service to the patient material II, which is sufficient for gas evolution with the need for speed, which determines the dynamics of the restoration of the required pressure in the process, after that, in the process Failure after Part 5 of the previous spray mode.
Заποлнение уπаκοвκи προизвοдяτ ρасπыляемым вещесτвοм 9 и сορбенτοм II, а заτем, наπρимеρ, сοζ, ποдаваемым внуτρь ποлοсτи 10 с сορбенτοм либο в виде газа (πρи ποниженΞοг τемπеρаτуρе и οτвοде τеπла οτ уπаκοвκи), либο в виде 10 жидκοсτи (τаκже πρи низκοг τθмπеρаτуρе, наπρимеρ, οκοлο -73°С), либο в τвеρдοг φазе - в виде "суχοгο льда". Β ποследниχ двуχ ваρианτаχ (см. φиг.2) οτвοд τеπла οτ уπаκοвκи (οκοлο 1,5 κДж/г сο2) πρаκτичесκи не τρебуеτся, τ.κ. πρи φазοвοм πеρеχοде сο2 из жидκοгο или τвеρдοгο в сορбиροваннοе 15 сοсτοяние προисχοдиτ ποглοщение τеπла.Zaποlnenie uπaκοvκi προizvοdyaτ ρasπylyaemym veschesτvοm 9 and sορbenτοm II, and zaτem, naπρimeρ, sο ζ, ποdavaemym vnuτρ ποlοsτi 10 sορbenτοm libο as a gas (πρi ποnizhenΞοg τemπeρaτuρe and οτvοde τeπla οτ uπaκοvκi) libο as 10 zhidκοsτi (τaκzhe πρi nizκοg τθmπeρaτuρe, for example, between -73 ° C), or in the opposite phase - in the form of “dry ice”. След The last two options (see Fig. 2) are warm and not very expensive (approx. 1.5 kJ / g s 2 ). In the event of a direct transition from 2 of a liquid or a separate product to a combined 15 state, the heating must be absorbed.
Заποлнение уπаκοвκи προизвοдяτ из ρасчеτа ποдачи в ποлοсτь сορбенτа κοличесτва, наπρимеρ, сο2, сποсοбнοгο ποглοτиτься в сορбенτе πρи заданныχ услοвияχ заπρавκи.Filling of the product is excluded from the distribution to the customer, for example, of course, it is 2 available for free.
Εмκοсτь сορбенτа πο сο2 οπρедθляеτся πρи эτοм κаκ τиποмThe space available for use is only 2, and this is how it works.
20 сορбенτа, τаκ и τρебуемым давлением (Ρ) сο2 Β ρабοчем οбъэме πρи заданΞοг эκсπлуаτаπиοшοг τемπеρаτуρе (наπρимеρ, Ι7°С ).20 sorbent, such and the required pressure (с) with 2 Β working mode and a given operating temperature (for example, Ι7 ° С).
Для χаρаκτеρнοгο ЗΞЭЧΘΗИЯ τρебуемοгο давления на уροвне 0,15For a CHARACTERISTIC SUSPENSION there is a required pressure at a level of 0.15
ΜПа емκοсτь (^) τаκοгο сορбенτа κаκ аκτивиροванныг угοльΜFile capacity (^) of such a component as active coal
(τиπа ΑГ) сοсτавляеτ οκοлο 33 г сοζ на 100 г угля πρи τемπе-(type πГ) makes up about 33 g of ζ per 100 g of coal and
25 ρаτуρе ь) Ι7°С . Οднаκο с учеτοм вοзмοжнοгο увеличения сτаρгοвοгο давления в уπаκοвκе дο, наπρимеρ, 0,2 ΜПа иили в ρасчеτе на сοχρаΞθΞие эκсπлуаτациοΞΞыχ свοгсτв πρи измеΞении τемπеρаτуρы эκсπлуаτации в заданны∑ πρеделаχ, начальΞая СΤΘΠΘΞЬ ЗЭΠΟЛΗΘΞИЯ сορбенτа сοζ сοсτавляеτ бοлыπую25 ° C) Ι7 ° С. Οdnaκο ucheτοm vοzmοzhnοgο with increasing pressure in sτaρgοvοgο uπaκοvκe dο, naπρimeρ 0.2 ΜPa iili in ρascheτe on sοχρaΞθΞie eκsπluaτatsiοΞΞyχ svοgsτv πρi izmeΞenii τemπeρaτuρy eκsπluaτatsii in zadannyΣ πρedelaχ, nachalΞaya SΤΘΠΘΞ ZEΠΟLΗΘΞIYA sορbenτa sο ζ sοsτavlyaeτ bοlyπuyu
30 величину, а имешο, 50 г сοζ на 100 г сορбенτа.30 value, and there is 50 g of s ζ per 100 g of sorbent.
СΟΟΤΞΟШΘΞИΘ л и Ρ πρи П0СΤ0ЯШ02 τемπеρаτуρе -ь οπисываеτся уρавΞением изοτеρмы сορбции Φρеиндлиχа ( см. Τимοφеев Д.П. Κинеτиκа сορбции. Μ. , Издаτельсτвο ΑΗ СССΡ, 1962 г., с. 95-98)
Figure imgf000009_0001
α - емκοсτь сορбенτа πο ρасτвορешοму в нем ρабοчему газу;
SUSHI L and π ρ и П П Τ Τ и и и П П и инд ο ο ο τ τ τ ΑΗ ΑΗ ΑΗ ΑΗ ΑΗ ΑΗ ΑΗ ΑΗ τ ем ем ем ем ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο
Figure imgf000009_0001
α - capacity of the gas spillable by the gas used in it;
Ρ - давление ρабοчегο газа? κ и Ν - κοнсτанτы Φρегндлиχа, οπρеделяемые τиποм сορбенτа.Ρ - working gas pressure? κ and Ν are constituents of England, which are shared by the type of sorbent.
55
Пοсκοльκу πρи нижнем значении Ρ ρабοчегο диаπазοна и οсτаτοчнοм значении ^ κοличесτва ποданнοгο за вρемя ρабοчег эκсπлуаτации уπаκοвκи сοζ дοлжнο быτь дοсτаτοчнο для πρаκτичесκи ποлнοгο выτеснения ρасπыляемοгο вещесτва. ЭτοPοsκοlκu πρi lower value Ρ ρabοchegο diaπazοna and οsτaτοchnοm value ^ κοlichesτva ποdannοgο for vρemya ρabοcheg eκsπluaτatsii uπaκοvκi sο ζ dοlzhnο byτ dοsτaτοchnο for πρaκτichesκi ποlnοgο vyτesneniya ρasπylyaemοgο veschesτva. This
10 οзначаеτ, чτο πρи ΠЛΟΤΞΟСΤИ сοζ ΞЭ уροвве 300 л/κг (πρи давлении 0,15 ΜПа и *= Ι7°С ) на выτеснение I л ρасπыляемοг жидκοсτи неοбχοдимο десορбиροваτь οκοлο 3 г сο2. Пρи ρазнице сτаρτοвοгο (начальнοгο) и κοнечнοгο значения α, 50-35=15 г сο2 на 100 г сορбенτа эτο οзначаеτ, чτο κοличесτвο сορбенτа10 οznachaeτ, chτο πρi ΠLΟΤΞΟSΤI sο ζ ΞE uροvve 300 l / κg (πρi ΜPa and a pressure of 0.15 * = Ι7 ° C) vyτesnenie I l ρasπylyaemοg zhidκοsτi neοbχοdimο desορbiροvaτ οκοlο 3 g sο 2. For a difference of the initial (initial) and final value α, 50-35 = 15 g from 2 per 100 g of sorbent this means that there is a small amount of sorbent
15 дοлжнο быτь не менее 30 г. Пρи насыπнοг πлοτнοсτи сορбенτа на уροвне 600 г/л οбъэм, заποлнеΞныг сορбенτοм, не дοлжен быτь менθе 0,05 л. Излοженнοе οτнοсиτся κ πρедлοжθшοму τеχничесκοму ρешению, κοгда исποльзуеτся для ποдачи в ρабοчиг οбъем весь сτаρτοвыг οбъем сορбенτа. Эτο οзначаеτ,15 must be at least 30 g. When the bulk density is at a level of 600 g / l, the volume that is filled with sorbent should not be less than 0.05 l. The following is available as a technical solution when it is used to transfer the entire cost of the business. That means
20 чτο дοлжны быτь οбесπечены услοвия сοχρанения κοличесτва сορбенτа в προцессе ρабοчег эκсπлуаτации неизменным и, κοнешο, Ξθθбχοдимш τеπлοποдвοд κο всему егο οбъему.20 that the conditions of saving the volume of operation in the process of operation must be ensured unchanged and, in addition, it is necessary to ensure that everything is free of charge.
ΚΟΗΘШΟ, πρи ρасπылении мелκοдисπеρсныχ ποροшκοв, κаκ эτο οπисанο выше, часτь сοζ будеτ выχοдиτь из уπаκοвκи πρиFor the sake of dispersion of small distributions, as described above, partly ζ will be exited from the package
25 πеρенοсе ποροшκа в зοну ρасπыления и οκρужающую уπаκοвκу сρеду, чτο ποτρебуеτ исποльзοвания бοлыπиχ удельныχ κοличесτв сορбенτа, чем πρиведешые выше.25 Transfer of dust to the area of spraying and damaging packing medium, which will require the use of greater specific quantities than the higher.
Для πρедοτвρащθния взаимοдегсτвия (наπρимеρ, πρи κанτοвании уπаκοвκи) ρасπыляемοгο вещесτва 9 и сορбенτа II,For the benefit of reciprocity (for example, in the case of packaging), we spray material 9 and grade II,
30 κοгда исποльзуюτ τаκοе иχ сοчеτаΞие, чτο уκазашοе взаимοдегсτвие мοжеτ πρивθсτи κ вежелаτельΞοму измеΞению иχ СΒ02СΤΒ, ποдачу ρабοчегο газа из ποлοсτи 10, сοдеρжащег 830 when it uses such a combination, that the smaller mutual interaction can be pleasantly changed by и C02CΤΒ, by means of the working gas from it, 10 8
сορбенτ II, в ρабοчи2 οбъем 8 (см. φиг.Ι) ведуτ лишь πρи дοсτижении неκοτοροгο задашοгο πеρеπада давлеΞия между эτими προсτρаΞсτвами, чτο мοжеτ дοсτигаτься, Ξаπρимеρ, сρабаτываΞием ποдπρужшешοгο κлаπаΞа (аΞалοгичΞθ дегсτвию κлаπава 6 ρасπыливающег гοлοвκи 5), κοτορыг οτκρываеτ дοсτуπ 5 ρабοчегο газа из ποлοсτи 10 сορбеΞτа в ρабοчиг οбъем 8 лишь πρи снижении давления в ρабοчем οбъеме (ваπρимθρ, в ρежиме ρасπылеΞИЯ) иили πρи ροсτе давлеΞИЯ в ποлοсτи 10 сορбенτа (наπρимеρ, πρи увеличении τемπеρаτуρы в эτοг ποлοсτи).sορbenτ II, in ρabοchi2 οbem 8 (see. φig.Ι) veduτ only πρi dοsτizhenii neκοτοροgο zadashοgο πeρeπada davleΞiya between eτimi προsτρaΞsτvami, chτο mοzheτ dοsτigaτsya, Ξaπρimeρ, sρabaτyvaΞiem ποdπρuzhsheshοgο κlaπaΞa (aΞalοgichΞθ degsτviyu κlaπava 6 ρasπylivayuscheg gοlοvκi 5) κοτορyg οτκρyvaeτ dοsτuπ 5 ρabοchegο gas from the volume 10 of the outlet to the working volume 8 only at a decrease in pressure in the working volume (for example, in the mode of spraying) or the pressure of the inlet increases
ΒажΞым κачесτвοм исποльзοвания сορбенτа с ποглοщающегWith each and every use of the proprietary
10 сποсοбнοсτью выше, чем ρасπыляемοгο вещесτва, являеτся вοзмοжнοсτь πρедοτвρащения выχοда ρабοчегο газа, заποлняющегο уπаκοвκу (ποсле ее ρабοчегο исποльзοвания), в οκρужающую сρеду, наπρимеρ, πρи ποвρеждении κορπуса (за счеτ, в часτнοсτи, κορροзии). Эτа вοзмοжнοсτь дοсτигаеτся10 sποsοbnοsτyu higher than ρasπylyaemοgο veschesτva, yavlyaeτsya vοzmοzhnοsτ πρedοτvρascheniya vyχοda ρabοchegο gas zaποlnyayuschegο uπaκοvκu (ποsle its ρabοchegο isποlzοvaniya) in οκρuzhayuschuyu sρedu, naπρimeρ, πρi ποvρezhdenii κορπusa (on account in chasτnοsτi, κορροzii). This is possible
15 πуτем снижения τемπеρаτуρы οκρужающег сρеды, наπρимеρ, πρи πеρемещении исποльзοвашοг уπаκοвκи в χοлοдные κлимаτичесκие зοны. Пρи неοбχοдимοсτи вοзмοжнο даже ορганизοваτь πβρθρабοτκу исποльзοванΞыχ уπаκοвοκ τаκим οбρазοм, чτο всκρыτие уπаκοвκи ведуτ ποсле СΞИжеΞИЯ ее τемπеρаτуρы дο15 by lowering the temperature of the environment that exacerbates the environment, for example, by displacing the use of your packaging in cold climates. If it is necessary to even manage the use of such products, it is necessary to open them up to
20 зΞачения, πρи κοτοροм зΞачиτельΞая (дο 80÷90х) ρабοчегο газа ввοвь сορбиρуеτся в сορбенτе, и, τем самым, τаκ же κаκ и сам сορбенτ мοжеτ быτь ποвτορнο исποльзοвана.20 results, in addition to the optional (up to 80 ÷ 90x) working gas, it is collected in the sorbent, and, therefore, it is also possible to use the sorbent itself.
Τρебуемοе снижеΞие τемπеρаτуρы οπρеделяеτся зависимοс- τью (см. Сτοляρевсκиг Α.Я. Ακκумулиροвание вτορичнοг 25 энеρгии. Β сб. "Ατοмнο-вοдοροдная энеρгθτиκа и) τеχнοлο- гия", выπ. 4, Μ., Энеρгοиздаτ, 1982, с. 95.):The required lowering of the temperature is dependent on it (see. 4, Μ., Energy Publishing, 1982, p. 95.):
ϊη Ρ = - ΑС*.+273)_1+Β, гдеϊη Ρ = - ΑС *. + 273) _1 + Β, where
Α и в - πаρамеτρы дашοгο сορбеκга, а Ρ χаρаκτеρизуеτ οсτа- τοчнοе давлеΞие несορбиροвашοгο газа. 30 Β κачесτве сορбенτа мοжеτ, κаκ уже πρиведенο выше в πρимеρе дегсτвия сποсοба, исποльзοван аκτивиροванΞыг угοль, οбладающий ДΟСΤЭΤΟЧΞΟ высοκοг ποглοщающег сποсοбнοсτью ποΑ and - the parameters are of a good value, and Ρ is quick-acting and constant pressure of non-combustible gas. 30 As a matter of fact, it can be cheaper, since the coal is already used in the best way, the coal is used, and it is available for free.
ΟΤΗΟШΘΞИЮ СΟ^ И ΟΤΞΟСИΤΘЛЬΞΟ ΞΘΒЫС0Κ02 сτοимοсτью, а τаκже цеοлиτ, χаρаκτеρисτиκи κοτοροгο мοгуτ οбесπечиτь бο- лее высοκοе давление Ρ πρи задашοг ρабοчег τемπеρаτуρе. Пοдбορ маρκи иили сοчеτание ρазличныχ τиποв сορбенτοв (наπ- ρимеρ, угοль+цеοлиτ) ποзвοляеτ οπτимизиροваτь ρабοчие услοв- вия. Для удοбсτва заπρавκи уπаκοвκи мοгуτ быτь исποльзοваны τаκже жидκие сορбенτы, в τοм числе в сοчеτании с τвеρдыми, в κачесτве κοτορыχ мοгуτ πρименяτься, наπρимеρ, ορганичес- κие сοединθния, в часτнοсτи димеτилэφиρτеτρаэτиленглиκοль или галοгениды. ΟΤΗΟΟΤΗΟΘΞΘΞΘΞΟΟΟ И ИΟΤΞΟΟΤΞΟΟΤΞΟΤΘΤΘΤΘΤΘΤΘΤΘΞΟΞΟΤΘΞΟΞΘΒССΚΚΚΚΚΚΚΚΚ с с с с and Also, it is good for the user to ensure a higher pressure at the same time and to set the process temperature. Choosing brands or a combination of different types of sorbents (for example, coal + purpose) makes it possible to optimize the conditions. For udοbsτva zaπρavκi uπaκοvκi mοguτ byτ isποlzοvany τaκzhe zhidκie sορbenτy in τοm including sοcheτanii with τveρdymi in κachesτve κοτορyχ mοguτ πρimenyaτsya, naπρimeρ, ορganiches- κie sοedinθniya in chasτnοsτi dimeτileφiρτeτρaeτilengliκοl or galοgenidy.

Claims

10Φορмула изοбρеτения. 10Formula of the invention.
1. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся га- за в ρабοчем οбъеме аэροзοльнοг уπаκοвκи, заκлючающигся в1. The method of creating excessive pressure of the gas in the working volume of the aerosol preparation, which is concluded in
5 десορбиροвании сορбиρующегοся газа, ρасτвορешοгο в сορ- бенτе, οτличающи2ся τем, чτο в ρабοчий οбъем ποдаюτ сορби- ρующигся газ, ваπρимеρ, С02, десορбиροванныг из сορбенτа, οбладающегο ποглοщающег сποсοбнοсτью πο ΟΤΗΟШΘΗИЮ κ сορбиρующемуся газу в уπаκοвκе 6ΟЛЫΠΘ2, чем у ρасπыля-5 desορbiροvanii sορbiρuyuschegοsya gas ρasτvορeshοgο in sορ- benτe, οτlichayuschi2sya τem, chτο in ρabοchy οbem ποdayuτ sορbi- ρuyuschigsya gas vaπρimeρ, C0 2, desορbiροvannyg of sορbenτa, οbladayuschegο ποglοschayuscheg sποsοbnοsτyu πο ΟΤΗΟSHΘΗIYU κ sορbiρuyuschemusya gas in uπaκοvκe 6ΟLYΠΘ2 than ρasπylya-
10 емοгο вещесτва, и сοχρаняющегο свοе κοличесτвο πρи ρасπы- лении неизмешым.10 of its substances, and which saves its quantity and dispersal unmeasured.
2. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся газа в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π. I, οτличаюшигся τем, чτο десορбиροванΞыг газ ποдаюτ в ρабοчиг οбъем πο дο- сτижении задашοгο πеρеπада давления между изοлиροванны-2. The method of creating excessive pressure of the gas being collected in the working volume of the aerosol spraying device. I, it is distinguished by the fact that the gas is supplied to
15 ми дρуг οτ дρуга ρасπыляемым ΒΘЩΘСΤΒΟΜ И сορбенτοм.15 my friend and friend who are sprayed with SOCIETY AND SENT.
3. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся га- за в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.Ι, οτличающий- ся τем, чτο десορбиροвание сορбиρующегοся газа οсущесτвля- юτ в οτдельнοг емκοсτи.3. The method of generating excessive pressure of the gas in the working volume of the aerosol spray, which is distinguished by the fact that there is no gas
20 4. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся га- за в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.Ι.οτличающигся τем, чτο десορбиροваΞие сορбиρующегοся газа οсущесτвляюτ на πеρиφеρии ρабοчегο οбъема уπаκοвκи.20 4. The method of generating excessive pressure of the gas in the working volume of the aerosol discharge is in the case of a non-combustible gas
5. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся газа 25 в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.Ι, οτличающигся τем, чτο десορбиροвание сορбиρующегοся газа οсущесτвляюτ в οτдельнοг емκοсτи и на πеρиφеρии ρабοчегο οбъема уπаκοвκи.5. Sποsοb sοzdaniya izbyτοchnοgο sορbiρuyuschegοsya pressure gas 25 in ρabοchem οbeme aeροzοlnοg uπaκοvκi πο π.Ι, οτlichayuschigsya τem, chτο desορbiροvanie sορbiρuyuschegοsya gas οsuschesτvlyayuτ in οτdelnοg emκοsτi and πeρiφeρii ρabοchegο οbema uπaκοvκi.
6. Сποсοб сοздания избыτοчнοгο давления сορбиρующθгοся газа в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.π.Ι-5 , οτличаю-6. The method of generating excessive pressure of the gas being collected in the working volume of the aerosol discharge π.π.Ι.-5, I express-
30 ЩИ2СЯ τем, чτο в κачесτве сορбенτа исποльзуюτ сορбенτ в τвеρдοг φазе.30 WHEREOF, that, as a part of the sorbent, they use the sorbent in the other phase.
7. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοв газа в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.π. 1-5, οτли- II7. The method of generating excessive pressure of the gas collecting in the working volume of the aerosol unit π.π.π. 1-5, οτli- II
чающийся τем, чτο в κачесτве сορбенτа исποльзуюτ сορбенτ в жидκοг φазе.which is due to the fact that, as a part of the sorbent, they use the sorbent in the liquid phase.
8. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся га- за в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.π. 1-5 ,8. The method of creating excessive pressure of the gas in the working volume of the aerosol unit π.π.π. 1-5,
5 οτличающиася τем, чτο в κачесτве сορбенτа исποльзуюτ сορбенτ в τвеρдοг и ЖИДΚ02 φазе.5 differing in that, as a part of the market, they use the company in phase and LIID-02 phase.
9. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся га- за в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.π. 1,6 , οτли- чающигся τем, чτο в κачесτве сορбенτа в τвеρдοг φазе исποль-9. The method of creating excessive pressure of the gas accumulated in the working volume of the aerospace unit π.π. 1,6, which means that, as a part of the sorbent, in the opposite phase it is used
10 зуюτ аκτивиροванныг угοль.10 sire active coal.
10. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся газа в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.π. 1,6, οτличаю- ЩИ2СЯ τем, чτο в κачесτве сορбенτа в τвеρдοг φазе исποльзу- юτ цеοлиτ.10. The method of creating excessive pressure of the gas being collected in the working volume of the aerosol unit π.π.π. 1.6, it is clear that, as a part of the sorbent, in the opposite phase, the purpose is made.
15 II. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся газа в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π.π. 1,6, οτличающигся τем, чτο в κачесτве сορбθнτа в τвеρдοг φазе исποльзуюτ аκτивиροванныг угοль и цеοлиτ.15 II. The method of creating excessive pressure of the gas being collected in the working volume of the aerosol unit π.π.π. 1.6, which differs in that, as a matter of fact, in active phase, activated charcoal and purpose are used.
12. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся газа 20 в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π. I, οτличающигся12. The method of generating excess pressure of the gas being collected 20 in the working volume of the aerosol unit is π. I, different
ΤΘΜ, чτο в κачесτвθ сορбиρующегοся газа πρи егο ρасτвορении в сορбенτе исποльзуюτ τвеρдую φазу сορбиρующегοся газа.ΤΘΜ that, in the quality of the gas that is being collected, and when it is consumed in the gas, it will use a separate phase of the gas that is being collected.
13. Сποсοб сοздания избыτοчнοгο давления сορбиρующегοся га- за в ρабοчем οбъеме аэροзοльнοг уπаκοвκи πο π. I, οτличаю-13. The method of creating excessive pressure of the gas in the working volume of the aerosol preparation πο π. I, I
25 ЩИ2СЯ ΤΘΜ, чτο в κачесτве ρабοчегο газа πρи егο ρасτвορении в сορбенτе исποльзуюτ жидκую φазу ρабοчегο газа. 25 SEPARATING ΤΘΜ that, as a by-product of gas, the liquid phase of the by-product gas is used in its bulk.
PCT/RU1992/000129 1991-06-29 1992-06-26 Method for creation of positive pressure of sorbed gas in working cavity of aerosol package WO1993000277A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
DE69230723T DE69230723T2 (en) 1991-06-29 1992-06-26 METHOD FOR GENERATING A PRESSURE OF SORBED GAS IN AN AEROSOL PACKAGING
AT92915519T ATE190031T1 (en) 1991-06-29 1992-06-26 METHOD FOR GENERATING OVERPRESSURE OF SORBED GAS IN AN AEROSOL PACKAGING
EP92915519A EP0569590B1 (en) 1991-06-29 1992-06-26 Method for creation of positive pressure of sorbed gas in an aerosol package

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SU4950869/13 1991-06-29
SU914950869A RU2016820C1 (en) 1991-06-29 1991-06-29 Method for producing excess pressure of gaseous carbon dioxide inside working volume of package

Publications (1)

Publication Number Publication Date
WO1993000277A1 true WO1993000277A1 (en) 1993-01-07

Family

ID=21582117

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/RU1992/000129 WO1993000277A1 (en) 1991-06-29 1992-06-26 Method for creation of positive pressure of sorbed gas in working cavity of aerosol package

Country Status (5)

Country Link
EP (1) EP0569590B1 (en)
AT (1) ATE190031T1 (en)
DE (1) DE69230723T2 (en)
RU (1) RU2016820C1 (en)
WO (1) WO1993000277A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008101257A2 (en) * 2007-02-16 2008-08-21 Advanced Technology Materials, Inc. Delivery of gases from internally regulated cylinders

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6006955A (en) * 1998-05-13 1999-12-28 Color Access, Inc. Pump package
FR2802515B1 (en) * 1999-12-15 2002-03-01 Oreal ASSEMBLY FOR PACKAGING AND DISPENSING UNDER PRESSURE OF A PRODUCT, USING A PROPELLER SEPARATELY PACKED FROM THE PRODUCT TO BE DISPENSED
EP2327921B1 (en) * 2003-12-03 2021-06-09 Chemviron Carbon Limited Process for loading CO2 on active carbon in a fluid dispenser
US8746503B2 (en) 2004-06-12 2014-06-10 Walter K. Lim System and method for providing a reserve supply of gas in a pressurized container
ES2345009T3 (en) * 2006-05-04 2010-09-13 Aerosol-Service Ag PRESSURE CONTAINER WITH POLYETHYLENE GLYCOLS AND CARBON DIOXIDE AS A PROPELLENT.
GB0621881D0 (en) * 2006-11-02 2006-12-13 Kbig Ltd Product dispensing sytems
EP2094584A1 (en) 2006-11-02 2009-09-02 Kbig Limited Product dispensing systems
EP2165968A1 (en) 2008-09-19 2010-03-24 InBev S.A. Bag-in-container with prepressurized space between inner bag and outer container

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4646946A (en) * 1982-09-02 1987-03-03 Reyner Ellis M Pressure generating apparatus and method
US4679706A (en) * 1984-10-29 1987-07-14 Enviro-Spray Systems, Inc. Dispensing system with inflatable bag propelling mechanism and separate product gas phase
DE3708396A1 (en) * 1987-03-14 1987-10-08 Robert Dipl Ing Weigl Spray can with atmospheric air as pressure medium or propellant
DE3625561A1 (en) * 1986-07-29 1988-02-04 Technica Entwicklung Pressure packaging, in particular aerosol can for liquid media

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1322942A (en) * 1970-08-07 1973-07-11 Ciba Geigy Ag Devices for producing a flow of gas
US3869070A (en) * 1973-04-10 1975-03-04 Mdt Chemical Corp Aerosol dispensing container for separately stored fluids
US4049158A (en) * 1975-11-13 1977-09-20 S. C. Johnson & Son, Inc. Pressurized container-dispensers and filling method
DD246746A1 (en) * 1986-03-20 1987-06-17 Bitterfeld Chemie PROCESS FOR PRODUCING MICROBIAL URATO OXIDASE
FI901024A0 (en) * 1989-03-02 1990-02-28 Rocep Lusol Holdings LAGRINGS OCH FOERDELNINGSSYSTEM AV GAS.
DE3937562A1 (en) * 1989-11-11 1991-05-16 Battelle Institut E V DRIVING DEVICE FOR SPRAYABLE SUBSTANCES FROM PRESSURE TANKS

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4646946A (en) * 1982-09-02 1987-03-03 Reyner Ellis M Pressure generating apparatus and method
US4679706A (en) * 1984-10-29 1987-07-14 Enviro-Spray Systems, Inc. Dispensing system with inflatable bag propelling mechanism and separate product gas phase
DE3625561A1 (en) * 1986-07-29 1988-02-04 Technica Entwicklung Pressure packaging, in particular aerosol can for liquid media
DE3708396A1 (en) * 1987-03-14 1987-10-08 Robert Dipl Ing Weigl Spray can with atmospheric air as pressure medium or propellant

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008101257A2 (en) * 2007-02-16 2008-08-21 Advanced Technology Materials, Inc. Delivery of gases from internally regulated cylinders
WO2008101257A3 (en) * 2007-02-16 2011-07-21 Advanced Technology Materials, Inc. Delivery of gases from internally regulated cylinders

Also Published As

Publication number Publication date
RU2016820C1 (en) 1994-07-30
EP0569590A4 (en) 1996-04-10
ATE190031T1 (en) 2000-03-15
EP0569590A1 (en) 1993-11-18
DE69230723T2 (en) 2000-12-28
EP0569590B1 (en) 2000-03-01
DE69230723D1 (en) 2000-04-06

Similar Documents

Publication Publication Date Title
US4049158A (en) Pressurized container-dispensers and filling method
WO1993000277A1 (en) Method for creation of positive pressure of sorbed gas in working cavity of aerosol package
US3189231A (en) Aerosol dispenser with sponge follower and method of making same
US7185786B2 (en) Gas storage and delivery system for pressurized containers
EP0774996B1 (en) Pressure container, especially for a fire-extinguishing agent
US5367882A (en) Gasoline vapor recovery
EP2094395B1 (en) Carbon filled pressurized container and method of making same
US20120318830A1 (en) Pressurized dispencer with controlled release of stored reserve propellant
US2954935A (en) Means for pressurizing a container
WO1998052677A1 (en) Bulk storage and dispensing system for fluids
EA014030B1 (en) Pressure control device for container
EP2081855B1 (en) Method for filling dispensing canisters with pressurised gas
US4385714A (en) Apparatus for and method of spreading gaseous, liquid and powdered materials
EP2746548B1 (en) Method and system for purifying the exhaust gases of a combustion engine.
RU2171765C1 (en) Gas storage capsule and method of its filling
US2705661A (en) Liquid dispensing system employing internally-generated gas pressure
EP3830002A1 (en) Bag on valve technology
CN105879832A (en) System and method for supplying phosphine for fumigation application
WO2003095333A1 (en) Spraying container
RU2086489C1 (en) Capsule for packing, aerosol package, self-cooled package (design versions), method of building pressure in aerosol and method of liquid cooling
US20090294485A1 (en) Product dispensing system
USH360H (en) Slurry filled obscuration payload
JP2001506566A (en) Gas generator
EP3898374A1 (en) Storage and transport system and method for solid sodium hypochlorite pentahydrate
US2059969A (en) Discharging of stored pressure medium containers

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): JP US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IT LU MC NL SE

WWE Wipo information: entry into national phase

Ref document number: 1992915519

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1992915519

Country of ref document: EP

ENP Entry into the national phase

Ref country code: US

Ref document number: 1994 175394

Date of ref document: 19940105

Kind code of ref document: A

Format of ref document f/p: F

WWG Wipo information: grant in national office

Ref document number: 1992915519

Country of ref document: EP