HRP20120691A2 - Marine flue gases purifier with sox removing and dry separation of solid particles - Google Patents
Marine flue gases purifier with sox removing and dry separation of solid particles Download PDFInfo
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- HRP20120691A2 HRP20120691A2 HRP20120691AA HRP20120691A HRP20120691A2 HR P20120691 A2 HRP20120691 A2 HR P20120691A2 HR P20120691A A HRP20120691A A HR P20120691AA HR P20120691 A HRP20120691 A HR P20120691A HR P20120691 A2 HRP20120691 A2 HR P20120691A2
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- Croatia
- Prior art keywords
- solid particles
- separator
- fan
- dry separation
- flue gas
- Prior art date
Links
- 239000002245 particle Substances 0.000 title claims abstract description 18
- 239000007787 solid Substances 0.000 title claims abstract description 18
- 238000000926 separation method Methods 0.000 title claims description 13
- 239000003546 flue gas Substances 0.000 title claims 12
- 239000007789 gas Substances 0.000 claims abstract description 41
- 239000004071 soot Substances 0.000 claims abstract description 16
- 239000013535 sea water Substances 0.000 claims abstract description 6
- 238000006477 desulfuration reaction Methods 0.000 claims description 7
- 230000023556 desulfurization Effects 0.000 claims description 7
- 238000005192 partition Methods 0.000 claims description 5
- -1 polypropylene Polymers 0.000 claims description 4
- 239000004743 Polypropylene Substances 0.000 claims description 3
- 229920001155 polypropylene Polymers 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 10
- 238000009736 wetting Methods 0.000 claims 1
- 238000000746 purification Methods 0.000 abstract description 2
- 239000000567 combustion gas Substances 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 238000010276 construction Methods 0.000 description 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 5
- 229910052815 sulfur oxide Inorganic materials 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000002803 fossil fuel Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 230000008520 organization Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/0214—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters with filters comprising movable parts, e.g. rotating filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/037—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of inertial or centrifugal separators, e.g. of cyclone type, optionally combined or associated with agglomerators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/06—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being an inertial, e.g. centrifugal, device
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2290/00—Movable parts or members in exhaust systems for other than for control purposes
- F01N2290/02—Movable parts or members in exhaust systems for other than for control purposes with continuous rotary movement
- F01N2290/06—Movable parts or members in exhaust systems for other than for control purposes with continuous rotary movement driven by auxiliary drive
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2590/00—Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines
- F01N2590/08—Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines for heavy duty applications, e.g. trucks, buses, tractors, locomotives
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Treating Waste Gases (AREA)
Abstract
Tehnički problem koji se mora riješiti ovim izumom je pronaći rješenje za odsumporavanje i uklanjanje čađi iz ispušnih plinova izgaranja u brodskim primjenama zbog zaštite okoliša kao i u svrhu štednje energije te povećanje sigurnosti broda, te izbjegavanja rizika od izbijanja požara kod kotlova na ispušne plinove motora. Ovaj problem je riješen brodskim uređajem za pročišćavanje ispušnih plinova koji se sastoji od ventilator - separatora (1) s rotorom aksijalno -radijalnog tipa koji je opremljen aksijalnim lopaticama (1.7) zakrivljenim u radijalne dio (1.8) za centrifugalno izbacivanje krutih čestica kroz slobodni presjek (1.12) a koje imaju savinuti kraj da dio krutih čestica iz centrifugalnog separatorskog dijela (1.8) ne pobjegne u tlačno centrifugalne lopatice (1.6) te centrifugalni dio za izbacivanje primljenih ispušnih plinova koji sadrže odvojenu čađu kroz slobodni presjek (1.12), uređaja za odsumporavanje koji je spojen s ventilatorom - separatorom koji sadrži mokre filtere (5) sa sapnicama (6) za raspršivanje morske vode, izmjenjivača topline (2) koji je spojen između ventilatora - separatora i uređaja za odsumporavanje za izmjenjivanje topline između djelomično pročišćenih ispušnih plinova iz ventilatora - separatora i pročišćenih ispušnih plinova iz uređaja za odsumporavanje.The technical problem that must be solved by the present invention is to find a solution for desulphurization and removal of soot from combustion gases in marine applications for environmental protection as well as to save energy and increase ship safety, and avoid the risk of fire in engine exhaust boilers. This problem is solved by a marine exhaust gas purification device consisting of a fan-separator (1) with an axial-radial type rotor equipped with axial blades (1.7) curved into radial part (1.8) for centrifugal ejection of solid particles through the free cross section ( 1.12) which have a bent end so that part of the solid particles from the centrifugal separator part (1.8) does not escape into the pressure centrifugal blades (1.6) and the centrifugal part for expelling the received exhaust gases containing separate soot through the free cross section (1.12). is connected to a fan-separator containing wet filters (5) with nozzles (6) for spraying seawater, a heat exchanger (2) which is connected between the fan-separator and a desulphurisation device for heat exchange between partially purified exhaust gases from the fan - separators and purified exhaust gases from the desulphurisation plant.
Description
Područje na koje se izum odnosi The field to which the invention relates
Izum se odnosi na ekologiju, odnosno pročišćavanje ispušnih plinova od štetnih tvari nastalih izgaranjem fosilnih goriva u brodskim motorima i kotlovima. The invention relates to ecology, that is, the purification of exhaust gases from harmful substances created by the combustion of fossil fuels in marine engines and boilers.
Tehnički problem Technical problem
Izgaranjem fosilnih goriva koje sadrže sumpor nastaju sumporni oksidi (SOX) i krute čestice u obliku čađe, pepela i neizgorenih ugljikovodika. Svi su ovi produkti izgaranja štetni za okoliš. IMO organizacija (International Maritime Organisation) je počela uvoditi ograničenja upotrebe teških goriva (mazuta) s velikim sadržajem sumpora u lukama i nekim zaštićenim zonama, a koje će se 2015.g.znatno proširiti, dok će do 2020.g.biti obuhvaćena sva svjetska mora. Brodovi imaju mogućnost upotrebljavati bez sumporna skupa goriva (euro dizel), ili teška jeftina goriva s velikim sadržajem sumpora, ali sa ugrađenim uređajem za odsumporavanjem i filtriranjem krutih čestica. Combustion of fossil fuels containing sulfur produces sulfur oxides (SOX) and solid particles in the form of soot, ash and unburned hydrocarbons. All these combustion products are harmful to the environment. The IMO organization (International Maritime Organization) has begun to introduce restrictions on the use of heavy fuel (fuel oil) with a high sulfur content in ports and some protected zones, which will be significantly expanded in 2015, while by 2020 all the world's must. Ships have the option of using sulfur-free fuel (euro diesel), or heavy cheap fuel with a high sulfur content, but with a built-in device for desulfurization and filtering of solid particles.
Stanje tehnike State of the art
Postoji nekoliko proizvođača brodskih uređaja za odsumporavanje ispušnih plinova (marine SOX scrubber) kao što su Wartsila, Aalborg - Alfalaval, Hamworthy, koji su započeli proizvodnju. Kod svih je princip rada sličan, a sastoji se u tome da se ispušni plinovi iz motora ili kotlova u kanalima ili mlaznicama miješaju sa vodom radi hlađenja, dovode u dno uređaja za odsumporavanje i vode vertikalno prema gore (mokrom filtru) gdje sada teža mokra čađa pada na dno uređaja. Začađena voda se u separatorima čisti od čađe koja se potom sprema u tankovima. Nakon prolaska kroz mokre filtere, gdje se sumporni oksidi kemijski vežu sa vodom i tvore sumpornu kiselinu, neutralizacija iste vrši se doziranjem natrijeve lužine (NaOH). There are several manufacturers of marine SOX scrubbers such as Wartsila, Aalborg - Alfalaval, Hamworthy, which have started production. The principle of operation is similar for all of them, and it consists in the fact that exhaust gases from engines or boilers are mixed with water in channels or nozzles for cooling, fed to the bottom of the desulphurization device and led vertically upwards (to the wet filter), where the wet soot is now heavier falls to the bottom of the device. Sooty water is cleaned of soot in separators, which is then stored in tanks. After passing through wet filters, where sulfur oxides chemically bond with water and form sulfuric acid, its neutralization is done by dosing sodium lye (NaOH).
Na kraju uređaja ugrađen je parni zagrijač koji sada ohlađene ispušne plinove zagrijava na određenu temperaturu, kako bi se izbjeglo stvaranje bijelog oblaka kondenzata na izlazu iz brodskog dimnjaka. Ovo predstavlja veliki utrošak energije. A steam heater is installed at the end of the device, which heats the now cooled exhaust gases to a certain temperature, in order to avoid the formation of a white cloud of condensate at the exit of the ship's chimney. This represents a large expenditure of energy.
Izlaganje suštine izuma Presentation of the essence of the invention
Cilj izuma je iznalaženje novog rješenja odsumporavanja ispušnih plinova u svrhu uštede energije i povećanja sigurnosti broda, izbjegavanja rizika od izbijanja požara kod kotlova na ispušne plinove motora. The goal of the invention is to find a new solution for exhaust gas desulphurization for the purpose of saving energy and increasing the safety of the ship, avoiding the risk of fire outbreaks in engine exhaust gas boilers.
Ispušni plinovi se čiste od čađe i drugih krutih čestica u posebno konstruiranom ventilator - separatoru i vode u gornji dio uređaja za odsumporavanja, gdje je smješten unakrsni izmjenjivač topline plin - plin, tj. vrući ispušni plinovi koji ulaze u uređaj se hlade, te pritom zagrijavaju ohlađene plinove na izlasku iz uređaja. Ovakvom konstrukcijom izmjenjivača topline, uređaj sam sebe hladi, odnosno zagrijava energijom koja se kod drugih sustava baca u okoliš. Kada se uređaj primjenjuje za odsumporavanje ispušnih plinova brodskog motora, a iza kojeg je u pravilu uvijek ugrađen kotao na ispušne plinove 12, koji služi za utilizaciju energije, ventilator - separator, kao sastavni dio pročistača, ugrađuje se prije kotla na ispušne plinove 12 (prikazano na slici 2). Ovim rješenjem kotao na ispušne plinove je zaštićen od stvaranja naslaga čađe, te je izbjegnut rizik od nastanka požara u kotlu na ispušne plinove, što predstavlja povećanje sigurnosti broda te efikasnosti samoga kotla na ispušne plinove jer nema pada kapaciteta uslijed zaprljanja. The exhaust gases are cleaned of soot and other solid particles in a specially designed fan-separator and lead to the upper part of the desulphurization device, where the gas-gas cross heat exchanger is located, i.e. the hot exhaust gases entering the device are cooled, and at the same time heated cooled gases at the exit from the device. With this design of the heat exchanger, the device cools itself, that is, it heats itself with energy that is thrown into the environment by other systems. When the device is used to desulphurize the exhaust gases of a marine engine, and behind which, as a rule, an exhaust gas boiler 12 is always installed, which serves for energy utilization, the fan - separator, as an integral part of the purifier, is installed before the exhaust gas boiler 12 (shown in Figure 2). With this solution, the exhaust gas boiler is protected from the formation of soot deposits, and the risk of fire in the exhaust gas boiler is avoided, which increases the safety of the ship and the efficiency of the exhaust gas boiler itself, since there is no drop in capacity due to contamination.
Kratki popis crteža A short list of drawings
Slika 1: Presjek uređaja Figure 1: Section of the device
Slika 2: Položaj ventilator - separatora u odnosu na motor i kotao na ispušne plinove Figure 2: Position of the fan - separator in relation to the engine and the exhaust gas boiler
Slika 3: Uzdužni presjek ventilatora - separatora Figure 3: Longitudinal section of fan - separator
Slika 3a: Poprečni presjek (A-A) ventilatora - separatora Figure 3a: Cross section (A-A) of fan - separator
Slika 4: Konstrukcija izmjenjivača topline na vrhu uređaja za odsumporavanje Figure 4: Construction of the heat exchanger on top of the desulfurization device
Slika 5: Konstrukcija mokrih filtera Figure 5: Construction of wet filters
Detaljan opis najmanje jednog od načina ostvarivanja izuma A detailed description of at least one way of realizing the invention
Ispušni plinovi se pomoću ventilator - separatora 1 čiste od čađe koja se kroz cijev 10 iz separatorskog kanala uvodi u vrećasti filter 11 i skuplja u posudu. U ovom slučaju imamo suhu separaciju čađe i drugih krutih čestica za razliku od ostalih postojećih uređaja koji imaju mokru separaciju. Očišćeni plinovi ulaze u izmjenjivač topline 2, čija je konstrukcija vidljiva na slici 4, koji se nalazi na vrhu uređaja za odsumporavanje, a koji je sastavljen od velikog broja pravokutnih cijevi oigličenih i sa unutrašnje i sa vanjske strane, u svrhu povećanja ogrjevne površine. The exhaust gases are cleaned of soot using the fan - separator 1, which is introduced through the pipe 10 from the separator channel into the bag filter 11 and collected in the container. In this case, we have dry separation of soot and other solid particles, unlike other existing devices that have wet separation. The cleaned gases enter the heat exchanger 2, the construction of which can be seen in Figure 4, which is located on top of the desulphurization device, and which is composed of a large number of rectangular tubes that are polished on both the inside and the outside, in order to increase the heating surface.
Vrući plinovi ulaze u unutarnje kanale pravokutne cijevi, te se hlade pomoću plinova prethodno ohlađenih u samom uređaju za odsumporavanje, a koji prolaze kroz vanjske kanale pravokutne oigličene cijevi. Kao što je vidljivo, riječ je o unakrsnom izmjenjivaču topline. Ohlađeni plinovi ulaze u kanal 3, u kojemu se pomoću morske vode, koja se dovodi kroz sapnice 4, koje su postavljene u kontra struji, plinovima dodatno spušta temperatura. U kanalu istovremeno počinje proces odsumporavanja, odnosno kemijsko vezivanje sumpornih oksida sa morskom vodom, te stvaranje sumporne kiseline. Sumporna kiselina se istodobno neutralizira zbog lužnate karakteristike morske vode. Iz kanala 3, sada već potpuno ohlađeni ispušni plinovi ulaze u donji dio pročistača te prolaze prema gore kroz prvi mokri filter 5, konstrukcija vidljiva na slici 5, oplakujući se raspršenim more iz sapnica 6. U prvom stupnju se odvija glavnina odsumporavanja. U drugom mokrom filteru 5, konstrukcija vidljiva na slici 5, odvija se dodatno odsumporavanje do vrlo visokog postotka. Mokri filteri 5 su sastavljeni od vrlo velikog broja polipropilenskih ploča koje na sebi imaju velik broj izdanaka, a u svrhu ostvarivanja velike izmjenjivačke površine. Nakon prolaska kroz drugi stupanj, ispušni plinovi prolaze kroz unakrsni izmjenjivač, koji je opisan na početku, a konstrukcija vidljiva na slici 4, gdje se zagrijavaju te prolaze kroz brodski dimnjak u atmosferu. Raspršeno more se skuplja na dnu pročistača, te se kroz cijev 8 izbacuje van broda. More koje se izbacuje iz broda bistro je, jer se čađa izdvojila u ventilator - separator, a sadrži samo sulfate kao produkte neutralizacije sumporne kiseline. Sulfate, tj.gips, je dozvoljeno otpuštati u more jer su u potpunosti neškodljivi. Priključak 9 služi za, po potrebi, potpuno pražnjenje pročistača. The hot gases enter the inner channels of the rectangular tube, and are cooled by the gases previously cooled in the desulphurization device itself, which pass through the outer channels of the rectangular tube. As you can see, it is a cross heat exchanger. The cooled gases enter the channel 3, in which the temperature of the gases is further lowered with the help of sea water, which is supplied through the nozzles 4, which are installed in a counter current. At the same time, the desulphurization process begins in the channel, that is, the chemical bonding of sulfur oxides with seawater, and the formation of sulfuric acid. Sulfuric acid is simultaneously neutralized due to the alkaline nature of seawater. From channel 3, the now completely cooled exhaust gases enter the lower part of the purifier and pass upwards through the first wet filter 5, a structure visible in Figure 5, being sprayed with sea spray from nozzles 6. In the first stage, the bulk of desulfurization takes place. In the second wet filter 5, construction visible in Figure 5, additional desulphurization takes place to a very high percentage. Wet filters 5 are composed of a very large number of polypropylene plates that have a large number of shoots on them, in order to achieve a large exchange surface. After passing through the second stage, the exhaust gases pass through the cross exchanger, which was described at the beginning, and the construction is visible in Figure 4, where they are heated and pass through the ship's chimney into the atmosphere. The dispersed sea is collected at the bottom of the purifier, and it is thrown out of the ship through pipe 8. The sea that is ejected from the ship is clear, because the soot was separated in the fan - separator, and contains only sulfates as products of neutralization of sulfuric acid. Sulfates, i.e. gypsum, are allowed to be released into the sea because they are completely harmless. Connection 9 serves for, if necessary, complete emptying of the purifier.
Ventilator - separator 1 kao jedan od najznačajnijih dijelova pročistača sastavljen je na slijedeći način: Fan - separator 1, as one of the most important parts of the purifier, is assembled as follows:
Rotor je pomoću glavčine 1.1 konzolno ovješen na elektromotor. Na glavčinu se pomoću vijaka pričvršćuje temeljna ploča 1.2 na koju je zavarena cijev 1.3, koja služi kao nosač lopatica 1.6, 1.7 i 1.8. Između temeljne ploče 1.2 i cijevi 1.3 zavarena je konusa cijev 1.4 oblikovana sa radijusom u svrhu minimiziranja otpora strujanja. Rotor je aksijalno - radijalnog tipa. Na ulasku u rotor su postavljene aksijalne lopatice 1.7 koje su zavarene za radijalne lopatice 1.8, koje su u ovom slučaju separatorske lopatice. Broj lopatica 1.7 i 1.8 je odabran tako da lopatice hvataju čađu iz ispušnih plinova prije nego ispušni plinovi napuste separatorski dio. Separatorske lopatice 1.8 su na svome kraju savinute kako bi hvatale čađu i centrifugalno je izbacivale kroz kanal 1.12. Iz presjeka A - A na slici 3 je vidljivo da je između separatorskih lopatica 1.8 zavarena pregrada 1.10 i pregrada 1.11 u svrhu smanjenja slobodnog presjeka 1.12 kroz kojeg na ovaj način istječe mala količina ispušnih plinova pomiješanih sa separiranom čađom. The rotor is cantilever-suspended on the electric motor using hub 1.1. The base plate 1.2 is attached to the hub with screws, to which the pipe 1.3 is welded, which serves as a support for the vanes 1.6, 1.7 and 1.8. Between the base plate 1.2 and the tube 1.3, a cone-shaped tube 1.4 is welded with a radius in order to minimize flow resistance. The rotor is axial-radial type. At the entrance to the rotor, axial blades 1.7 are placed, which are welded to radial blades 1.8, which in this case are separator blades. The number of blades 1.7 and 1.8 is chosen so that the blades capture soot from the exhaust gases before the exhaust gases leave the separator section. Separator blades 1.8 are bent at their end to catch soot and centrifugally eject it through channel 1.12. From the section A - A in Figure 3, it can be seen that a partition 1.10 and a partition 1.11 are welded between the separator blades 1.8 in order to reduce the free section 1.12 through which a small amount of exhaust gases mixed with separated soot flows.
Način primjene izuma Method of application of the invention
Na taj način izum omogućava novu tehnologiju odsumporavanja ispušnih plinova koja pojednostavljuje sustav i čini ga konkurentnim. In this way, the invention enables a new exhaust gas desulfurization technology that simplifies the system and makes it competitive.
Popis upotrijebljenih pozivnih oznaka List of used call signs
1 Ventilator - separator 1 Fan - separator
1.1 Glavčina rotora 1.1 Rotor hub
1.2 Temeljna ploča rotora 1.2 Rotor base plate
1.3 Nosač lopatica 1.3 Blade holder
1.4 Konusni lim rotora 1.4 Conical rotor sheet
1.5 Konusni ulaz rotora 1.5 Conical rotor inlet
1.6 Glavne centrifugalne lopatice 1.6 Main centrifugal blades
1.7 Aksijalne lopatice 1.7 Axial vanes
1.8 Separatorske lopatice 1.8 Separator vanes
1.9 Bočni konusni poklopci separatorskih lopatica 1.9 Lateral conical covers of separator blades
1.10 Pregradni limovi separatorskih lopatica 1.10 Partition sheets of separator blades
1.11 Pregradni limovi separatorskih lopatica 1.11 Partition sheets of separator blades
1.12 Slobodni presjek za istjecanje ispušnog plina pomiješanog sa separiranom čađom 1.12 Free cross-section for the outflow of exhaust gas mixed with separated soot
2 Oigličeni izmjenjivač topline, slika 4 2 A simplified heat exchanger, Figure 4
3 Spojni kanal gornjeg i donjeg dijela pročistača 3 Connecting channel of the upper and lower parts of the purifier
4 Sapnice u kanalu 4 Nozzles in the channel
5 Polipropilenske igličaste ploče mokrih filtera, slika 5 5 Polypropylene needle plates of wet filters, picture 5
6 Sapnice mokrih filtera 6 Wet filter nozzles
7 Izlaz plinova iz pročistača 7 Gas outlet from the purifier
8 Izlazna cijev mora 8 The outlet pipe of the sea
9 Ispušno - drenažni otvor 9 Exhaust - drainage hole
10 Izlaz separirane čađe 10 Output of separated carbon black
11 Vrećasti filter 11 Bag filter
12 Kotao na ispušne plinove motora 12 Engine exhaust gas boiler
Claims (10)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HRP20120691AA HRP20120691A2 (en) | 2012-08-31 | 2012-08-31 | Marine flue gases purifier with sox removing and dry separation of solid particles |
EP13771057.0A EP2912286A1 (en) | 2012-08-31 | 2013-09-02 | Exhaust gas purifying device and method |
PCT/EP2013/002631 WO2014032814A1 (en) | 2012-08-31 | 2013-09-02 | Exhaust gas purifying device and method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HRP20120691AA HRP20120691A2 (en) | 2012-08-31 | 2012-08-31 | Marine flue gases purifier with sox removing and dry separation of solid particles |
Publications (1)
Publication Number | Publication Date |
---|---|
HRP20120691A2 true HRP20120691A2 (en) | 2014-03-14 |
Family
ID=49293575
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
HRP20120691AA HRP20120691A2 (en) | 2012-08-31 | 2012-08-31 | Marine flue gases purifier with sox removing and dry separation of solid particles |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2912286A1 (en) |
HR (1) | HRP20120691A2 (en) |
WO (1) | WO2014032814A1 (en) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4840645A (en) * | 1983-04-15 | 1989-06-20 | Allied-Signal Inc. | Rotary separator with a porous shroud |
BRPI0506637A (en) * | 2004-02-07 | 2007-12-18 | Jangshik Yun | air purifier using centrifuge rotor liquid |
-
2012
- 2012-08-31 HR HRP20120691AA patent/HRP20120691A2/en not_active Application Discontinuation
-
2013
- 2013-09-02 EP EP13771057.0A patent/EP2912286A1/en not_active Withdrawn
- 2013-09-02 WO PCT/EP2013/002631 patent/WO2014032814A1/en active Application Filing
Also Published As
Publication number | Publication date |
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EP2912286A1 (en) | 2015-09-02 |
WO2014032814A1 (en) | 2014-03-06 |
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