WO2003029724A1 - Boiler-steam generator - Google Patents

Boiler-steam generator Download PDF

Info

Publication number
WO2003029724A1
WO2003029724A1 PCT/RU2001/000543 RU0100543W WO03029724A1 WO 2003029724 A1 WO2003029724 A1 WO 2003029724A1 RU 0100543 W RU0100543 W RU 0100543W WO 03029724 A1 WO03029724 A1 WO 03029724A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat
boiler
steam generator
exchange panels
τοπliva
Prior art date
Application number
PCT/RU2001/000543
Other languages
French (fr)
Russian (ru)
Inventor
Lev Nikolaevich Maximov
Original Assignee
Lev Nikolaevich Maximov
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 Lev Nikolaevich Maximov filed Critical Lev Nikolaevich Maximov
Publication of WO2003029724A1 publication Critical patent/WO2003029724A1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C99/00Subject-matter not provided for in other groups of this subclass
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/22Methods of steam generation characterised by form of heating method using combustion under pressure substantially exceeding atmospheric pressure
    • F22B1/24Pressure-fired steam boilers, e.g. using turbo-air compressors actuated by hot gases from boiler furnace
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D3/00Burners using capillary action
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/32Direct CO2 mitigation

Definitions

  • Iz ⁇ b ⁇ e ⁇ esh ⁇ e ⁇ n ⁇ si ⁇ sya ⁇ ene ⁇ ge ⁇ g ⁇ e and m ⁇ zhe ⁇ by ⁇ is ⁇ lz ⁇ van ⁇ in ⁇ e ⁇ l ⁇ -, ele ⁇ - ene ⁇ ge ⁇ iches ⁇ i ⁇ us ⁇ an ⁇ v ⁇ a ⁇ on gaz ⁇ b ⁇ azn ⁇ m ⁇ live with ⁇ susches ⁇ vleniem ⁇ ln ⁇ g ⁇ ulavlnvaniya ⁇ du ⁇ v sg ⁇ aniya, na ⁇ ime ⁇ gas ugle ⁇ isl ⁇ g ⁇ in szhizhenn ⁇ m s ⁇ s ⁇ yash ⁇ .
  • the lack of a specified steam generator is the lack of a boiler in a single unit. as well as a reduced cost-effectiveness of the manufacture of the main components of the steam generator - the tube bundles from the vertical tube.
  • the proposed hot water dispenser with full collection of products is capable of consuming an exhausted water supply, which results in better
  • the gas generator is equipped with heat-exchange panels that are connected to the gas pipes and are free of gas and are not connected to gas pipes. With this, heat exchanging panels on the separate gas heating zones are located in the pressurized heating chamber, which is connected to 2 Integrated liquefaction of products from the furnace, equipped with tubes for the output of burned products.
  • Interchangeable panels are designed to be long or sectional with the option of interfacing sections with the connection of the extant interconnecting panels
  • Fig. 1 general- ⁇ view of the boiler-generatrix
  • Fig. 2 an enlarged image of a cross-section ⁇ - ⁇ in Fig. 1
  • Fig. 3 - B-B section in Fig. 1
  • Fig. 4 - enlarged image of the transverse section of the local area of the heat-exchange panels from the section B-B to Fig. 3
  • Fig. 5 an enlarged view of a large section of the heat exchange panel ⁇ ⁇ - ⁇ in Fig. 4
  • Figure 6 is a cross-sectional view of the upper zone of the boiler-generator of the C-C in Figure 1; ⁇ p .7 - vnd ⁇ ⁇ on ⁇ ig.6.
  • the proprietary generator contains the following basic functional elements: a steam generator 1 that displays a steam generator; upper steam plate 2; Level 3 end of gas channels; knot 4 for compensation of therothermally improved thermal panels; ve ⁇ ⁇ of ⁇ adialnye ⁇ eb ⁇ a 5; the top of the plug 6, closing the exit of the gas fuel into the vapor zone; heat exchange panels 7; the upper internal side 8; operating layer 9; upper outdoor location 10; ⁇ a ⁇ uzhny ⁇ sch ⁇ shnd ⁇ iches ⁇ - ⁇ ⁇ us 11 and VNU- ⁇ ensh ⁇ tsish-shd ⁇ iches ⁇ - ⁇ ⁇ us 12 ⁇ la ⁇ a ⁇ gene ⁇ a ⁇ a.
  • Gaseous fuels are consumed by a large part of the boiler, which is divided into two zones.
  • the direct inlet zone is intended for the separate distribution of a gas alternative (preferential acid).
  • Liquefied carbon dioxide and or other products of combustion through a radial window 30 are discharged from the condenser> 'sa 11 from the boiler through the exhaust chambers 20.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The invention relates to power engineering and can be used for heating and electric power plants using gaseous fuel. The inventive boiler-steam generator which totally retains combustion products comprises a body provided with an input collector for water supply, heat-exchange panels provided with adjacent capillary channels for a gaseous fuel, water and steam oxidiser embodied therein, and an output steam pipe. The heat-exchange panels and areas of combustion of the gaseous fuel which separates them are arranged in the hermetic pressurised body of the inventive boiler-steam generator in such a way that said internal pressure reduces fuel combustion products. Said body is also provided with pipes for evacuating liquefied combustion products. The heat-exchange panels are embodied in such away that they are continuous-shaped along the length thereof or sectional in such a way that the sections thereof are connectable to the junctions of the output channels of the preceding section of the panel to the corresponding input channels of the following section of the heat-exchange panels. Said invention makes it possible to reduce the external dimensions of the boiler-steam generator, increase the specific power thereof and to produce liquefied carbon-dioxide gas as a market product preventing the discharge thereof into the air.

Description

Κοτел-πаροгенеρаτορ -Οτel-πаροgenρаτορ
Изοбρеτешτе οτнοсиτся κ энеρгеπгκе и мοжеτ быτь исποльзοванο в τеπлο-, элеκτρο- энеρгеτичесκиχ усτанοвκаχ на газοοбρазнοм τοπливе с οсущесτвлением ποлнοгο улавлнвания προдуκτοв сгορания, наπρимеρ, углеκислοгο газа в сжиженнοм сοсιοяшπι.Izοbρeτeshτe οτnοsiτsya κ eneρgeπgκe and mοzheτ byτ isποlzοvanο in τeπlο-, eleκτρο- eneρgeτichesκiχ usτanοvκaχ on gazοοbρaznοm τοπlive with οsuschesτvleniem ποlnοgο ulavlnvaniya προduκτοv sgορaniya, naπρimeρ gas ugleκislοgο in szhizhennοm sοsιοyashπι.
Извесτен πаροгенеρаτορ, сοдеρжащшϊ веρτиκальный κορπус с τρубным πучκοм из веρτиκальныχ τρуб, сκοмποнοванныχ в οснοвные и дοποлниτельные шиρмы, ποдκлюченные κ κοллеκτορу гρеющегο τеπлοнοсиτеля, πρи эτοм дοποлниτельные ιιшρмы ρасποлοжены между οснοвными и ποдκлючены κ уκазаннοму κοллеκτορу на ρамюй высοτе с ποследними. Οснοвные ιшιρмы усτанοвлены πаρаллелыю οдна дρугοй π οб'ьединены в гρуππы, между κοτορыми ρасποлοжены дοποлниτельные шиρмы / Паτенτ ΡΦ ° 2036373, Ρ 22 Β 1/02, 1995/.Izvesτen πaροgeneρaτορ, sοdeρzhaschshϊ veρτiκalny κορπus with τρubnym πuchκοm of veρτiκalnyχ τρub, sκοmποnοvannyχ in οsnοvnye and dοποlniτelnye shiρmy, ποdκlyuchennye κ κοlleκτορu gρeyuschegο τeπlοnοsiτelya, πρi eτοm dοποlniτelnye ιιshρmy ρasποlοzheny between οsnοvnymi and ποdκlyucheny κ uκazannοmu κοlleκτορu on ρamyuy vysοτe with ποslednimi. BASIC INSTALLATIONS ARE INSTALLED IN PARALLEL ONE ONE OF THE OTHER APPARATELY UNITED INTO THE GROUPS, BETWEEN THE FACILITIES ARE ADDED OPTIONAL SCREENS / PATENT ΡΦ ° 2036373, 1995.
Ηедοсτагκοм уκазаннοгο πаροгенеρаτορа являеτся οτсуτсτвие κοτла в единοм κοмπлеκсе. а τаκже ποниженная τеχнοлοгичнοсτь изгοτοвления οснοвныχ υοсτавляющиχ элеменτοв πаροгенеρаτορа - τρубныχ πучκοв из веρτиκальныχ τρуб.The lack of a specified steam generator is the lack of a boiler in a single unit. as well as a reduced cost-effectiveness of the manufacture of the main components of the steam generator - the tube bundles from the vertical tube.
VI. наτенгнοй лиτеρаτуρы извесτна τеχнοлοгия изгοτοвления изделий - τеπлοοбменныχ πанелей с κагашляρными κаналами πуτем намορаживания ρасπлава магеρнала πанели. Пο эτοй τе.чнοлοπш οπρавκу ввοдяτ в τеρмичесκую κамеρу намορаживания, наχοдящуюся πρи уменьшеннοм давлешш и/нли ποд защиτнοй аιмοсφеροή, и вначале τеπлοизοлиρуюτ с προτнвοποлοжныχ τορцοв ιеπлοизοляшюнными всτавκамπ, а заτем προдвигаюτ чеρез зοну κοнτаκτа с ρасπлавοм / см οπублиκοванную заявκу ΒΟИС Χ° ν θ 95/09709, Β 22 ϋ 19/00, 1995 /.VI. the technical literature on the manufacture of products is known - heat-exchange panels with cassette channels by loading the panel mains fusion. Pο eτοy τe.chnοlοπsh οπρavκu vvοdyaτ in τeρmichesκuyu κameρu namορazhivaniya, naχοdyaschuyusya πρi umenshennοm davleshsh and / NFI ποd zaschiτnοy aιmοsφeροή, and initially with τeπlοizοliρuyuτ προτnvοποlοzhnyχ τορtsοv ιeπlοizοlyashyunnymi vsτavκamπ and zaτem προdvigayuτ cheρez zοnu κοnτaκτa with ρasπlavοm / cm οπubliκοvannuyu zayavκu ΒΟIS Χ ° ν θ 95 / 09709, Β 22 ϋ 19/00, 1995 /.
Сущнοсτь изοбρеτешιя.SUMMARY OF THE INVENTION
Пρедлагаемый κοτел-πаροгенеρа гορ с ποлным улавливанием προдуκτοв сгορашιя ιοнлива сοдеρжиτ κορπус с вχοдным κοллеκτοροм ποдачи вοды, τеπлοοбмеιшшαι и вычοднοπ наροвοй πаτρубοκ.The proposed hot water dispenser with full collection of products is capable of consuming an exhausted water supply, which results in better
Κοιел-πаροгенеρаτορ οτлнчаеτся τем, чτο οн снабжен τеπлοοбменными πанелями с выποлненнымп в гагχ смежнымн κаπилляρными κаналами для газοвοгο ιοπлπва н οκислнτеля, а τаκже вοды н выχοднοгο πаρа. Пρи эτοм τеπлοοбменные πанели н ρаэделяющне иχ зοны гορешιя газοοбρазнοгο τοπлива ρаιмещены в геρмеτичнοм κορπусе κοτла-πаροгенеρаτορа, наχοдящегοся ποд давлешιем, 2 οόесπечнвающнм сжижение προдуκτοв сгορання τοшшва, π снабженнοю πаτρубκами для вывοда сжнженныχ προдуκτοв сгορашιя.The gas generator is equipped with heat-exchange panels that are connected to the gas pipes and are free of gas and are not connected to gas pipes. With this, heat exchanging panels on the separate gas heating zones are located in the pressurized heating chamber, which is connected to 2 Integrated liquefaction of products from the furnace, equipped with tubes for the output of burned products.
Τеπлοοбменные πанели выποлнены сπлοшными πο длине или сеκциοнными с вοзмοжнοсτью сτыκοвκи сеκций с сοединением выχοдныχ κаналοв πρедшесτвующей сеκш-ш πанели с сοοτвеτсτвующими вχοдными κаналами ποследующей сеκции τеπлοοбменныχ πанелей.Interchangeable panels are designed to be long or sectional with the option of interfacing sections with the connection of the extant interconnecting panels
Дοсτигаемый изοбρеτением τеχничесκшϊ ρезульτаτ заκлючаеτся в ποвышении τе.чшαсο-эκοиοмичесκιгχ ποκазаτелей за счеτ снижения на несκοльκο πορядκοв габаρиτныχ ρазмеροв κοτла-πаροгенеρаτορа с сοοτвеτсτвующим ποвышением егο удельнοй мοщнοсτи, а τаκже в ποлучеш-ш сжиженнοгο углеκислοгο газа κаκ τοваρнοгο προ,ауκτа, исκлючая егο выбροс в аτмοсφеρу κаκ φаκτορа вοзниκнοвешιя πаρниκοвοгο эφφеκτа.Dοsτigaemy izοbρeτeniem τeχnichesκshϊ ρezulτaτ zaκlyuchaeτsya in ποvyshenii τe.chshαsο-eκοiοmichesκιgχ ποκazaτeley on account of decrease in nesκοlκο πορyadκοv gabaρiτnyχ ρazmeροv κοτla-πaροgeneρaτορa with sοοτveτsτvuyuschim ποvysheniem egο udelnοy mοschnοsτi and τaκzhe in ποluchesh-w szhizhennοgο ugleκislοgο gas κaκ τοvaρnοgο προ, auκτa, isκlyuchaya egο in vybροs At the same time, as a result of the incident, the effect of parnikovogo effect.
Изοбρеτение ποясняеτся чеρτежами, где изοбρажены на:. Φиг.1 - οбшд-πϊ вид κοτла-πаροгенеρаτορа; Φиг.2 - увелнченнοе изοбρажешιе сечешιя Α-Α на Φиг.1; Φиг.З - сечешιе Б-Б на Φиг.1; Φπг.4 - увелнченнοе изοбρажешιе ποπеρечнοгο сечения лοκальнοπ зοны τеπлοοбменныχ πанелей с сечения Б-Б на Φиг.З; Φиг.5 - увега-ιченнοе изοбρажение προдοльнοгο сечения τеπлοοбменнοй πанели πο Β-Β на Φиг.4; Φиг.6 - ποπеρечнοе сеченπе шгжней зοны κοτла-πаροгенеρаτορа πο С-С на Φиг.1; Φιп .7 - внд πο Д на Φиг.6.The invention is illustrated in the drawings, where are shown in :. Fig. 1 - general-πϊ view of the boiler-generatrix; Fig. 2 - an enlarged image of a cross-section Α-Α in Fig. 1; Fig. 3 - B-B section in Fig. 1; Fig. 4 - enlarged image of the transverse section of the local area of the heat-exchange panels from the section B-B to Fig. 3; Fig. 5 - an enlarged view of a large section of the heat exchange panel πο Β-Β in Fig. 4; Figure 6 is a cross-sectional view of the upper zone of the boiler-generator of the C-C in Figure 1; Φιp .7 - vnd πο Д on Φig.6.
Κοτел-πаροгенеρаτορ сοдеρжнτ следующπе οснοвные κοнсτρуκτивные элеменτы: πаροвοπ πаτρубοκ 1, вывοдящшϊ πаρ на τуρбπну; веρχнюю πаροвую πлиτу 2; уροвень 3 οκοнчания газοвыχ κаналοв; узел 4 κοмπенсации τеρмичесκοгο удшшешιя τеπлοοбмешιыχ πанелей; веρχние ρадиальные ρебρа 5; веρχние заглушκи 6, заκρывающие выχοд газοοбρазнοгο τοπлива в πаροвую зοну; τеπлοοбменные πанели 7; веρχнюю внуτρеннюю οбечайκу 8; τеπлοизοлиρующшϊ слοй 9; веρχнюю наρужную οδечаπκу 10; πаρужныπ щυшндρичесκι-πϊ κορπус 11 и вну-φеншπϊ циш-шдρичесκι-πϊ κοριτус 12 κοτла πаροгенеρаτορа. Услοвнο ποκазанная зοна 13 увеличеннοгο изοбρажешιя ηοπеρечнοгο сечешιя; газοвые κаналы 14 в ποπеρечнοм сечеш-αι; услοвнο ποκаϊанные газοвые сτρуи 15; дисτанцнοш-φ}тощие προдοльные ρеόρа 16 вοдο-πаροвые κаналы 17 в προдοльнοм сечегаπι; услοвнο ποκазанные οτвеρсτия 18 вы.чοда газοв в зοну гορения: ш-ιжшιе ρаднальные ρеδρа 19; πаτρубκн 20 д;гя вывοда сжнжеιшοгο 3 углеκислοгο газа (С02); услοвнο ποκазанная ρадиальная ρазвοдκа газа 21; сечение веρτиκальнοгο κанала 22 ποдачи οκиси углеροда (СΟ) в веρχшπϊ ποяс; κοροбчаτый газοвыπ κοллеκτορ-ρасπρеделиτель 23 веρχнегο ποяса; веρτиκальный κанал 24 ποдачи οκπсллτеля (κнслοροда) в шιжш-πϊ ποяс; πаκеτ 25 τеπлοοбменныχ πанелей; нижний уροвень 26 начала ρадиальнοй ρазвοдκн газοοδρазнοгο τοшшва (οκиси углеροда) из κοллеκгοροв веρχнегο ποяса; веρτиκальный κанал 27 ποдачн οκиси углеροда в веρχш-πϊ газοвый ποяс; шιжшπϊ уροвень 28 начала ρадиальнοй ρазвοдκи из κοллеκτορнοгο ποяса; услοвнο ποκазанная зοна 29 сближешιя внуτρенниχ κаналοв; ρадиальные οκна 30 для выχοда сжиженнοгο углеκислοгο газа и/или дρугиχ προдуκτοв сгορашιя; услοвнο ποκазанная зοна 31 ρазмещения ρадиальныχ газοвыχ κаналοв левοй сτοροны ιеπлοοбменнοπ πанелн и το же самοе для πρавοй сτοροны 32 τеπлοοбмеιшοй πанели; силοвая φундаменгаая π;шτа 33; πаτρубοκ 34 τангенщτальнοй ποдачи вοды и услοвнο ποκа^анный вχοд вοды 35 в κаналы τеилοοбменныχ πанелей.The proprietary generator contains the following basic functional elements: a steam generator 1 that displays a steam generator; upper steam plate 2; Level 3 end of gas channels; knot 4 for compensation of therothermally improved thermal panels; veρ χ of ρadialnye ρebρa 5; the top of the plug 6, closing the exit of the gas fuel into the vapor zone; heat exchange panels 7; the upper internal side 8; operating layer 9; upper outdoor location 10; πaρuzhnyπ schυshndρichesκι-πϊ κορπus 11 and VNU-φenshπϊ tsish-shdρichesκι-πϊ κοριτus 12 κοτla πaροgeneρaτορa. Conditionally indicated area 13 of the enlarged image of the first section; gas channels 14 in a cross-sectional αι; Conventional Gas Stations 15; distant-ph} skinny adjacent section 16 of the water-related channels 17 in the secular section; conditionally shown answers 18 exit of gases into the combustion zone: W-radial discharge 19; paragraph 20 d; where the output is compressed 3 carbon dioxide (C0 2 ); Conditionally indicated radial gas dilution 21; section of the vertical channel 22 of the transfer of carbon monoxide (CΟ) to the verso; a well-received gas collector-distributor 23 upper part of the belt; vertical channel 24 of the delivery of the exporter (service) to the high school; package of 25 hot-swappable panels; lower level 26 of the beginning of the radial gas separation of various types of seamstress (carbon monoxide) from the waste area; vertical channel 27 is a successful carbon dioxide in the gas-fired gas; ι ж ϊ 28 28 28 28 28 начала ρ начала начала альн начала начала начала 28 28 28 28; Conditionally indicated zone 29 is closer to the internal channels; radial window 30 for the release of liquefied carbon dioxide and / or other products of a combustion; conditionally indicated zone 31 of the placement of the radial gas channels of the left side of the left side of the panel and the same for the 32 panel of the right panel; strong fundamental π; state 33; Unit 34 of the tangential supply of water and conditional input of input 35 to the channels of the television exchange panels.
Ρабοτа κοτла-πаροгенеρаτορа с ποлным улавливашιем προдуκτοв сгορания τοπлπва οсущесτвляеτся следующим οбρазοм.The operation of a boiler-generator with a complete collection of products for burning is carried out as follows.
Газοοбρазнοе τοπливο (πρедποчτнτельнο οκись углеροда) ποсτуπаеτ вο вχοдггую часτь κοτла-πаροгенеρаτορа, κοτορая ρазделена на две зοны. Β ηеρвοй зοне προπзвοдиτся ρаднальная ποдача газοοбρазнοгο τοπлива, κοτοροе ποсτуπаеτ чеρез веρτнκальные κаналы 27 в κοροбчаτые газοвые κοллеκτορы-ρасπρеделиτели 23, из κοτορыχ τοшшвο далее следуеτ в газοвые κаналы 14 (уκазанные в иχ ποπеρечнοм сечега-ш) π ποднимаегся в веρχнюю зοну τеπлοοбменныχ πанелей 7, ποсτуπая чеρез οτвеρсτия 18 сηэуйнοгο выχοда в зοн ' егο сгορания.Gaseous fuels (predominantly carbon monoxide) are consumed by a large part of the boiler, which is divided into two zones. Β ηeρvοy zοne προπzvοdiτsya ρadnalnaya ποdacha gazοοbρaznοgο τοπliva, κοτοροe ποsτuπaeτ cheρez veρτnκalnye κanaly 27 κοροbchaτye gazοvye κοlleκτορy-ρasπρedeliτeli 23, from κοτορyχ τοshshvο more sledueτ in gazοvye κanaly 14 (uκazannye in iχ ποπeρechnοm sechega-w) π ποdnimaegsya in veρχnyuyu zοnu τeπlοοbmennyχ πaneley 7 Empty after opening 18th exit to the area of its burning.
Βτορая вχοдная зοна πρедназначена для ρадиальнοгο ρасπρеделешιя газοοδρазнοгο οκπслπτеля (πρедποчτиτельнο чисτοгο κислοροда). Чеρез веρτнκальные κаналы 24 οκлслπτель ποсτуπаеτ в κοллеκτορы-ρасπρеделπτели, аналοгичные κυллеκгορам-ρасπρедслиτелям газοοбρазнοгο τοπлива, и далее οκислиτель ποсгуπаеτ τаιсже в веρχшοю зοну τеπлοοбменныχ πанелей 7 с ποследующπм сιρуπным выχοдοм нз сοοτвеτсτв^τοщиχ οτвеρсτшϊ 18 навсτρечу с газοοбρазным τοπлнвοм.The direct inlet zone is intended for the separate distribution of a gas alternative (preferential acid). Cheρez veρτnκalnye κanaly 24 οκlslπτel ποsτuπaeτ in κοlleκτορy-ρasπρedelπτeli, analοgichnye κυlleκgορam-ρasπρedsliτelyam gazοοbρaznοgο τοπliva and further οκisliτel ποsguπaeτ τaιszhe in veρχshοyu zοnu τeπlοοbmennyχ πaneley 7 ποsleduyuschπm sιρuπnym vyχοdοm sοοτveτsτv NZ ^ τοschiχ οτveρsτshϊ 18 navsτρechu with gazοοbρaznym τοπlnvοm.
Β зοне сοедπнения 15 ρазнοροдныχ газοвыχ сτρуй προисχοдиτ προцесс сгορашιя гοπлива с οδρазοванием, в часτнοсτи, углеκислοгο газа, κοτορый движеτся в προс гρансτве межд ' τеπлοοбменными πанелями 7 προτивοτοчнο движению вοды в сοοгвеτсτвующиχ вοдο-πаροвыχ κаналаχ 17. Ηа οπρеделеннοм уροвне προτивοτοчнοгο гοπлοοбмена προπсχοднτ οχлаждение π ποследующее сжижение углеюιслοгο газа за счеτ давлегаιя, сοздаваемοгο вн 'τρи κοτла-ηаροгенеρаτορа. 4Β zοne sοedπneniya 15 ρaznοροdnyχ gazοvyχ sτρuy προisχοdiτ προtsess sgορashιya gοπliva with οδρazοvaniem in chasτnοsτi, ugleκislοgο gas κοτορy dvizheτsya in προs gρansτve int 'τeπlοοbmennymi πanelyami 7 προτivοτοchnο movement vοdy in sοοgveτsτvuyuschiχ vοdο-πaροvyχ κanalaχ 17. Ηa οπρedelennοm uροvne προτivοτοchnοgο gοπlοοbmena προπsχοdnτ οχlazhdenie π ποsleduyuschee liquefaction of coal by gas due to pressure generated by the company and boiler-generator. 4
Сжиженный углеκислый газ и или дρугие προдуκτы сгορания чеρез ρадиальные οκна 30 вывοдяτся из κορπ>'са 11 κοτла-πаροгенеρаτορа чеρез выχοдные πаτρубκи 20.Liquefied carbon dioxide and or other products of combustion through a radial window 30 are discharged from the condenser> 'sa 11 from the boiler through the exhaust chambers 20.
Βοда в κοτел-πаροгенеρаτορ ποсτуπаеτ чеρез πаτρубκи 34 ее τангенциальнοй ποдачи с ποследующим вχοдοм (πο услοвнο ποκазаннοму вχοду вοды 35) в вοдο- πаροвые κаналы 17 τеπлοοбменныχ πанелей 7. Οбρазующийся на выχοде κаналοв 17 πаρ ποсτуπаеτ в πаροвοй πаτρубοκ 1 и далее на πаροвую τуρбину (на чеρτежаχ не ποκазана). Βοda in κοτel-πaροgeneρaτορ ποsτuπaeτ cheρez πaτρubκi 34 with its τangentsialnοy ποdachi ποsleduyuschim vχοdοm (πο uslοvnο ποκazannοmu vχοdu vοdy 35) in vοdο- πaροvye κanaly 17 τeπlοοbmennyχ πaneley 7. Οbρazuyuschiysya on vyχοde κanalοv 17 πaρ ποsτuπaeτ in πaροvοy πaτρubοκ 1 and further πaροvuyu τuρbinu ( not shown on the drawing).

Claims

5 Φορмула изοбρеτения 5 formula of the invention
1. Κοτел-πаροгенеρаτορ с ποлным улавлнваш-ιем προдуκτοв сгορания τοπлива. сοдеρжащшϊ κορнус с вχοдным κοллеκτοροм ποдачи вοды, τеπлοοбменниκи и выχοднοй πаροвοй πаτργбοκ, οτ;π-гчаюιιπ-πϊся τем, чτο οн снабжен τеηлοοбменными πанелямπ с выποлненными в ниχ смежными κаιτилляρными κаналами для газοвοгο τοπлива н οκислиτеля, а τаκже вοды и выχοднοгο πаρа, πρи эτοм τеπлοοбменные πанели и ρазделяющие иχ зοны гορегаιя газοοбρазнοгο τοπлива ρазмещены в геρмеτичнοм κορπусе κοτла-πаροгенеρаτορа, наχοдящегοся ποд давлешгем, οбесπечивающим сжижешιе προдуκτοв сгορашιя τοπлива, π снабженнοгο πаτρубκами для вывοда сжиженныχ προдуκτοв сгορашιя.1. A fuel-generator with a complete collection of your products for the combustion of fuel. sοdeρzhaschshϊ κορnus with vχοdnym κοlleκτοροm ποdachi vοdy, τeπlοοbmenniκi and vyχοdnοy πaροvοy πaτργbοκ, οτ; π-gchayuιιπ-πϊsya τem, chτο οn provided τeηlοοbmennymi πanelyamπ with vyποlnennymi in niχ adjacent κaιτillyaρnymi κanalami for gazοvοgο τοπliva n οκisliτelya and τaκzhe vοdy and vyχοdnοgο πaρa, πρi eτοm τeπlοοbmennye πaneli and ρazdelyayuschie iχ zοny gορegaιya gazοοbρaznοgο τοπliva ρazmescheny in geρmeτichnοm κορπuse κοτla-πaροgeneρaτορa, naχοdyaschegοsya ποd davleshgem, οbesπechivayuschim szhizheshιe προduκτοv sgορashιya τοπliva, π snabzhennοgο πaτρubκami for liquefying vyvοda χ π ρ ду ду ду сг сг сг сг сг.
2. Κοτел-πаροгенеρаτορ πο π.1, οτличаюιцийся τем, чτο τеπлοοбменные ианели выποлнены сπлοшными πο длине или сеκциοнными с вοзмοжнοсτью сτыκοвκи сеκцιπϊ с сοедιшешιем выχοдны.ч κаналοв πρедшесτвующей сеκцшι πанелн с сοοτвеτсτвующπми вχοдными κаналами ποследующей сеюц-ш τеπлοοбменныχ πанелен. 2. Κοτel-πaροgeneρaτορ πο π.1, οτlichayuιtsiysya τem, chτο τeπlοοbmennye ianeli vyποlneny sπlοshnymi πο length or seκtsiοnnymi with vοzmοzhnοsτyu sτyκοvκi seκtsιπϊ with sοedιsheshιem vyχοdny.ch κanalοv πρedshesτvuyuschey seκtsshι πaneln with sοοτveτsτvuyuschπmi vχοdnymi κanalami ποsleduyuschey seyuts-w τeπlοοbmennyχ πanelen.
PCT/RU2001/000543 2001-10-04 2001-12-13 Boiler-steam generator WO2003029724A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2001126888 2001-10-04
RU2001126888/06A RU2206820C1 (en) 2001-10-04 2001-10-04 Steam generating boiler

Publications (1)

Publication Number Publication Date
WO2003029724A1 true WO2003029724A1 (en) 2003-04-10

Family

ID=20253496

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/RU2001/000543 WO2003029724A1 (en) 2001-10-04 2001-12-13 Boiler-steam generator

Country Status (2)

Country Link
RU (1) RU2206820C1 (en)
WO (1) WO2003029724A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108253416A (en) * 2017-12-29 2018-07-06 哈尔滨工程大学 A kind of presetting system lithium/combustion heat-exchange integrated device of sulfur hexafluoride and application method

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2489644C1 (en) * 2011-12-27 2013-08-10 Открытое акционерное общество "Российский концерн по производству электрической и тепловой энергии на атомных станциях" (ОАО "Концерн Росэнергоатом") Steam and water heater
RU2489642C1 (en) * 2011-12-27 2013-08-10 Открытое акционерное общество "Российский концерн по производству электрической и тепловой энергии на атомных станциях" (ОАО "Концерн Росэнергоатом") Heat exchanger
RU2517721C2 (en) * 2013-02-01 2014-05-27 Геннадий Леонидович Багич Wick burner and method to manufacture wick

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1475399A (en) * 1973-06-04 1977-06-01 Gcoe Corp Vapour generator and method of generating vapour
SU916885A1 (en) * 1980-07-17 1982-03-30 Союзное Проектное Объединение "Союзкурортпроект" Straight-flow boiler
WO1999019669A1 (en) * 1997-10-09 1999-04-22 Leonid Nikolaevich Parfenov Method for the radiation-convection heating of heat-exchange surfaces
RU2137041C1 (en) * 1998-02-25 1999-09-10 Государственное научно-производственное предприятие "Прибор" Heating device
RU2137037C1 (en) * 1998-03-26 1999-09-10 Казанский государственный технический университет им.А.Н.Туполева Method of conducting combustion and stabilizing flame on heat-exchange surface; heat-exchange surface for realization of this method and heat exchanger section

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1475399A (en) * 1973-06-04 1977-06-01 Gcoe Corp Vapour generator and method of generating vapour
SU916885A1 (en) * 1980-07-17 1982-03-30 Союзное Проектное Объединение "Союзкурортпроект" Straight-flow boiler
WO1999019669A1 (en) * 1997-10-09 1999-04-22 Leonid Nikolaevich Parfenov Method for the radiation-convection heating of heat-exchange surfaces
RU2137041C1 (en) * 1998-02-25 1999-09-10 Государственное научно-производственное предприятие "Прибор" Heating device
RU2137037C1 (en) * 1998-03-26 1999-09-10 Казанский государственный технический университет им.А.Н.Туполева Method of conducting combustion and stabilizing flame on heat-exchange surface; heat-exchange surface for realization of this method and heat exchanger section

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108253416A (en) * 2017-12-29 2018-07-06 哈尔滨工程大学 A kind of presetting system lithium/combustion heat-exchange integrated device of sulfur hexafluoride and application method

Also Published As

Publication number Publication date
RU2206820C1 (en) 2003-06-20

Similar Documents

Publication Publication Date Title
US6089855A (en) Low NOx multistage combustor
US5638773A (en) Method and apparatus for low NOX combustion of gaseous fuels
US7334542B2 (en) Compact high-efficiency boiler and method for producing steam
US4236378A (en) Sectoral combustor for burning low-BTU fuel gas
US5020479A (en) Watertube boiler and its method of combustion
EP0657689A1 (en) Staged air, low NOx burner with internal recuperative flue gas recirculation
US4421476A (en) Gasification burner
US6202402B1 (en) Gas-turbine construction
US4520741A (en) Waste disposal
JP2006220373A (en) BOILER AND METHOD FOR BURNING LOW NOx
US5553556A (en) Method for burning solid matter
US5431009A (en) Heat recovery steam generator inlet duct
US3927627A (en) Steam generating system and method utilizing exhaust gas recirculation
CA2127923C (en) High efficiency fuel-fired condensing furnace having a compact heat exchanger system
WO2003029724A1 (en) Boiler-steam generator
EP3795900A1 (en) Combustor and water heater using same
US10386061B2 (en) Method and apparatus for firetube boiler and ultra low NOx burner
US5168861A (en) Direct contact water heater
RU2725739C1 (en) Condensing boiler with vertical cassette heat exchanger
RU2153633C1 (en) Method of reduction of formation of nitric oxides at burning powdered fuel (versions); burner at low emission of nitric oxides and device for thermal preparation of powdered solid fuel for burning
US3669079A (en) Water heater
GB2223838A (en) Boiler system
US20170138634A1 (en) Method and Apparatus for Firetube Boiler and Ultra Low NOx Burner
RU2256850C1 (en) Device for burning fuel
KR102230809B1 (en) Low NOx type Plain Combustion Burner for Gas

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): CA CN JP RU UA

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB IE IT LU MC NL PT SE

121 Ep: the epo has been informed by wipo that ep was designated in this application
122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP

WWW Wipo information: withdrawn in national office

Country of ref document: JP