HRP20191705T1 - Kontrola plinskog sastava postrojenja za odvajanje plina s membranama - Google Patents
Kontrola plinskog sastava postrojenja za odvajanje plina s membranama Download PDFInfo
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- HRP20191705T1 HRP20191705T1 HRP20191705T HRP20191705T1 HR P20191705 T1 HRP20191705 T1 HR P20191705T1 HR P20191705 T HRP20191705 T HR P20191705T HR P20191705 T1 HRP20191705 T1 HR P20191705T1
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- permeate
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- retentate
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- 239000000203 mixture Substances 0.000 title claims 16
- 239000012528 membrane Substances 0.000 title claims 13
- 239000012466 permeate Substances 0.000 claims 60
- 239000012465 retentate Substances 0.000 claims 47
- 238000000926 separation method Methods 0.000 claims 35
- 239000007789 gas Substances 0.000 claims 27
- 238000000034 method Methods 0.000 claims 14
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 7
- 238000011088 calibration curve Methods 0.000 claims 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 4
- 239000004642 Polyimide Substances 0.000 claims 4
- 230000002596 correlated effect Effects 0.000 claims 4
- 229920001721 polyimide Polymers 0.000 claims 4
- 230000001105 regulatory effect Effects 0.000 claims 4
- -1 polysiloxanes Polymers 0.000 claims 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 2
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 2
- 230000001276 controlling effect Effects 0.000 claims 2
- 229910052739 hydrogen Inorganic materials 0.000 claims 2
- 239000001257 hydrogen Substances 0.000 claims 2
- 239000000463 material Substances 0.000 claims 2
- 239000000047 product Substances 0.000 claims 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims 1
- 239000004952 Polyamide Substances 0.000 claims 1
- 239000004721 Polyphenylene oxide Substances 0.000 claims 1
- 239000001569 carbon dioxide Substances 0.000 claims 1
- 229910002091 carbon monoxide Inorganic materials 0.000 claims 1
- 229920002301 cellulose acetate Polymers 0.000 claims 1
- 238000004140 cleaning Methods 0.000 claims 1
- 230000006835 compression Effects 0.000 claims 1
- 238000007906 compression Methods 0.000 claims 1
- 229920001887 crystalline plastic Polymers 0.000 claims 1
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000000855 fermentation Methods 0.000 claims 1
- 230000004151 fermentation Effects 0.000 claims 1
- 239000012510 hollow fiber Substances 0.000 claims 1
- 238000005259 measurement Methods 0.000 claims 1
- 239000004941 mixed matrix membrane Substances 0.000 claims 1
- 239000003345 natural gas Substances 0.000 claims 1
- 229920002492 poly(sulfone) Polymers 0.000 claims 1
- 229920002647 polyamide Polymers 0.000 claims 1
- 229920000642 polymer Polymers 0.000 claims 1
- 229920006380 polyphenylene oxide Polymers 0.000 claims 1
- 229920001451 polypropylene glycol Polymers 0.000 claims 1
- 229920001296 polysiloxane Polymers 0.000 claims 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D53/225—Multiple stage diffusion
- B01D53/226—Multiple stage diffusion in serial connexion
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D53/228—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
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- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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- C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
- C12M47/18—Gas cleaning, e.g. scrubbers; Separation of different gases
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D2053/221—Devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/14—Pressure control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2317/00—Membrane module arrangements within a plant or an apparatus
- B01D2317/02—Elements in series
- B01D2317/027—Christmas tree arrangements
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D71/06—Organic material
- B01D71/58—Other polymers having nitrogen in the main chain, with or without oxygen or carbon only
- B01D71/62—Polycondensates having nitrogen-containing heterocyclic rings in the main chain
- B01D71/64—Polyimides; Polyamide-imides; Polyester-imides; Polyamide acids or similar polyimide precursors
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- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
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Claims (17)
1. Uređaj za odvajanje plinova, koji kao membranske stupnjeve odvajanja sadrži najmanje stupanj odvajanja dovodne struje (1), stupanj odvajanja retentata (2) i stupanj odvajanja permeata (3) i također najmanje jedan kompresor (4) smješten na strani napajanja navedenog stupnja odvajanja dovodne struje (1) i/ili najmanje jednu, poželjno jednu ili dvije, vakuumske pumpe postavljene nizvodno od navedenog stupnja odvajanja dovodne struje (1), poželjno na strani permeata navedenog stupnja odvajanja retentata (2) u drugoj struji permeata (9a + 9b) i/ili na strani permeata navedenog stupnja odvajanja permeata (3) u trećoj struji permeata (11),
pri čemu
navedeni stupanj odvajanja dovodne struje (1) odvaja dovodnu struju (5), koja se sastoji od dvije ili više komponenti, u prvu struju permeata (6) i prvu struju retentata (7),
navedeni stupanj odvajanja retentata (2) dijeli navedenu prvu struju retentata (7) u drugu struju permeata (9a + 9b) i drugu struju retentata (8) koja se uklanja kao proizvod ili se dalje obrađuje, a navedena druga struja permeata se dovodi u navedenu dovodnu struju (5),
navedeni stupanj odvajanja permeata (3) dijeli navedenu prvu struju permeata (6) u treću struju retentata (10a + 10b) i treću struju permeata (11), koja se uklanja kao proizvod ili se dalje obrađuje ili se odbacuje, a navedena treća struja retentata se dovodi u navedenu dovodnu struju (5), naznačen time što
- navedena druga struja permeata (9a + 9b) sadrži najmanje jedna sredstva za kontrolu permeata (18) s kojima se tlak permeata navedenog stupnja odvajanja retentata (2) može povisiti ili sniziti i koji se kontrolira na temelju izmjerenih vrijednosti iz jednog ili više sredstava za mjerenje (20a) u navedenoj prvoj struji retentata (7) i/ili jednog ili više sredstava za mjerenje (20b) u navedenoj drugoj struji retentata (8) radi određivanja sastava određene smjese plina i navedena druga struja permeata (9b) se dovodi u navedenu dovodnu struju (5) nizvodno od navedenih sredstava za kontrolu permeata (18),
i
- navedena treća struja retentata (10a + 10b) sadrži najmanje jedna sredstva za kontrolu retentata (19) s kojima se tlak retentata navedenog stupnja odvajanja permeata (3) može podići ili spustiti i koji se kontrolira na temelju izmjerenih vrijednosti iz jednog ili više mjerača protoka (21a) u navedenoj prvoj struji permeata (6) i/ili jednog ili više sredstva za mjerenje (21b) u navedenoj trećoj struji permeata (11) radi određivanja sastava određene smjese plina.
2. Uređaj prema patentnom zahtjevu 1,
naznačen time što
navedena prva struja permeata (6) nije podvrgnuta rekompresiji
i/ili
najmanje jedan od navedenih koraka membranskog odvajanja (1) do (3) sadrži više od jednog modula membrane za odvajanje plina međusobno spojenih paralelno i/ili serijski,
i/ili
modul(i) membrane za odvajanje plina se sastoje od membrana od šupljih vlakana i/ili ravnih membrana.
3. Uređaj prema patentnom zahtjevu 1 ili 2, naznačen time što
se navedena druga struja permeata (9b) i navedena treća struja retentata (10b) vode do usisne strane navedenog kompresora (4),
i/ili time što
se koristi više stupanjski kompresor (4), pri čemu poželjno navedena druga struja permeata (9b) i/ili navedena treća struja retentata (10b) se uvode u navedeni kompresor (4) između dva stupnja kompresije,
i/ili time što je navedeni kompresor (4) smješten u navedeni uređaj tako da stvara gradijent tlaka u navedenom stupnju odvajanja dovodne struje (1).
4. Uređaj prema bilo kojem od patentnih zahtjeva 1 do 3, naznačen time što
navedeni uređaj sadrži sredstva za regulaciju (24) koja prilagođavaju kapacitet navedenog kompresora (4), poželjno njegovu brzinu rotacije, prema promjenama u navedenoj drugoj struji permeata (9b) i/ili navedenoj trećoj struji retentata (10b) i/ili navedenoj struji sirovog plina (17), pri čemu je navedena struja sirovog plina strujanje najmanje dva plina koji se dovode u uređaj u skladu sa izumom da bi se tamo odvojili i koji se zajedno s navedenom drugom strujom permeata (9b) i strujom retentata (10b) dovode u navedenu dovodnu struju (5), i/ili time što
je navedeni uređaj konfiguriran tako da se kompenzira mijenjanje količina recikliranog plina iz navedene druge struje permeata (9b) i/ili navedene treće struje retentata (10b), poželjno automatski, regulacijom količine isporučenog sirovog plina, poželjno putem sredstva za regulaciju sirovog plina (25), poželjno bez promjene brzine rotacije navedenog kompresora (4).
5. Uređaj prema bilo kojem od patentnih zahtjeva 1 do 4, naznačen time što se online ili offline sredstva za mjerenje (20b) i/ili (21b) koriste u navedenoj drugoj struji retentata (8) i/ili u navedenoj trećoj struji permeata (11) kako bi se odredio sastav određene smjese plina.
6. Uređaj prema bilo kojem od patentnih zahtjeva 1 do 5, naznačen time što
su materijali koji se upotrebljavaju za separacijski aktivni sloj membrana amorfne ili djelomično kristalne plastike kao što su, na primjer ali ne isključivo, poliimidi, poliamidi, polisulfoni, celulozni acetati i derivati, polifenilen oksidi, polisiloksani, polimeri s intrinzičnom mikroporozom, membrane miješanih matrica, membrane s olakšanim transportom, polietilen oksidi, polipropilen oksidi ili njihove smjese.
7. Uređaj prema patentnom zahtjevu 6,
naznačen time što
materijal koji se koristi za separacijski aktivni sloj membrana je poliimid s općom formulom
gdje 0 ≤ x ≤ 0.5 i 1 ≥ y ≥ 0.5 i R odgovara jednom ili više, identičnih ili različitih radikala R odabranih iz skupine koju čine radikali L1, L2, L3 i L4,
poželjno poliimid s CAS brojem 9046-51-9 i/ili poliimid s CAS brojem 134119-41-8.
8. Postupak za kontrolu postrojenja za odvajanje plina prema bilo kojem patentnom zahtjevu od 1 do 7, naznačen time što
i. kada koncentracija manje permeirajuće komponente B, po izboru također određene iz parametra koji je s njom u vezi, navedene druge struje retentata (8) pada ispod unaprijed određene zadane vrijednosti, tlak navedene druge struje permeata (9a) se snižava pomoću navedenih sredstava za kontrolu permeata (18) sve dok se navedena koncentracija/parametar ne vrati u raspon zadanih vrijednosti,
ii. kada koncentracija manje permeirajuće komponente B, po izboru također određene iz parametra koji je s njom u vezi, navedene druge struje retentata (8) raste iznad unaprijed određene zadane vrijednosti, tlak navedene druge struje permeata (9a) se povećava pomoću navedenih sredstava za kontrolu permeata (18) sve dok se navedena koncentracija/parametar ne vrati u raspon zadanih vrijednosti,
i
iii. kada koncentracija manje permeirajuće komponente B, po izboru također određene iz parametra koji je s njom u vezi, navedene treće struje permeata (11) pada ispod unaprijed određene zadane vrijednosti, tlak navedene treće struje retentata (10a) se povećava pomoću navedenih sredstava za kontrolu retentata (19) sve dok se navedena koncentracija/parametar ne vrati u raspon zadanih vrijednosti,
iv. kada koncentracija manje permeirajuće komponente B, po izboru također određene iz parametra koji je s njom u vezi, navedene treće struje permeata (11) raste iznad unaprijed određene zadane vrijednosti, tlak navedene treće struje retentata (10a) se snižava pomoću navedenih sredstava za kontrolu retentata (19) sve dok se navedena koncentracija/parametar ne vrati u raspon zadanih vrijednosti.
9. Postupak prema patentnom zahtjevu 8,
naznačen time što
se koncentracija određuje online i/ili offline.
10. Postupak za kontrolu postrojenja za odvajanje plina prema bilo kojem patentnom zahtjevu od 1 do 7,
naznačen time što
v. kada se povećava volumenski protok navedene prve struje retentata (7), tlak navedene druge struje permeata (9a) se snižava pomoću navedenih sredstava za kontrolu permeata (18) sve dok se svojstvo navedene druge struje retentata (8) koja je korelirana s kalibracijskom krivuljom s navedenim volumenskim protokom navedene prve struje retentata (7), poželjno sastavom navedene druge struje retentata (8), ne vrati u raspon zadanih vrijednosti,
vi. kada se smanjuje volumenski protok navedene prve struje retentata (7), tlak navedene druge struje permeata (9a) se povećava pomoću navedenih sredstava za kontrolu permeata (18) sve dok se svojstvo navedene druge struje retentata (8) koja je korelirana s kalibracijskom krivuljom s navedenim volumenskim protokom navedene prve struje retentata (7), poželjno sastavom navedene druge struje retentata (8), ne vrati u raspon zadanih vrijednosti,
i/ili
vii. kada se povećava volumenski protok navedene prve struje permeata (6), tlak navedene treće struje retentata (10a) se povećava pomoću navedenih sredstava za kontrolu retentata (19) sve dok se svojstvo navedene treće struje permeata (11) koja je korelirana s kalibracijskom krivuljom s navedenim volumenskim protokom navedene prve struje permeata (6), poželjno sastavom navedene treće struje permeata (11), ne vrati u raspon zadanih vrijednosti,
viii. kada se smanjuje volumenski protok navedene prve struje permeata (6), tlak navedene treće struje retentata (10a) se snižava pomoću navedenih sredstava za kontrolu retentata (19) sve dok se svojstvo navedene treće struje permeata (11) koja je korelirana s kalibracijskom krivuljom s navedenim volumenskim protokom navedene prve struje permeata (6), poželjno sastavom navedene treće struje permeata (11), ne vrati u raspon zadanih vrijednosti.
11. Postupak prema patentnom zahtjevu 10,
naznačen time što
se kalibracijska krivulja koja sadrži korelaciju između brzine protoka i tlaka koristi kao kontrolna krivulja za održavanje koncentracije u nekoj drugoj struji plina.
12. Postupak prema bilo kojem od patentnih zahtjeva 8 do 11, naznačen time što
je pad tlaka kroz navedeni stupanj odvajanja dovodne struje (1) postavljen na od 1 do 30 bar, poželjno na od 2 do 20 bar i poželjnije na 3 i 10 bar,
i/ili time što
je pad tlaka kroz navedeni stupanj odvajanja dovodne struje (1) i navedeni stupanj odvajanja retentata (2) postavljen na od 1 do 100 bar, poželjno na od 5 do 80 bar i poželjnije na od 10 do 70 bar.
13. Postupak prema bilo kojem od patentnih zahtjeva 8 do 12, naznačen time što
pokretačka sila koja se koristi za zadatak odvajanja je razlika parcijalnog tlaka između strane retentata i strane permeata u određenim stupnjevima membranskog odvajanja, pri čemu je navedena razlika parcijalnog tlaka generirana kompresorom (4), koji je postavljen na strani dovoda od navedenog stupnja odvajanja dovodne struje (1), te po izboru pomoću najmanje jedne, poželjno jedne ili dvije vakuumske pumpe u navedenoj drugoj i/ili trećoj struji permeata (9a + 9b) i/ili (11) i/ili pomoću struje plina za čišćenje na strani permeata,
i/ili time što
je tlak permeata od navedenog stupnja odvajanja dovodne struje (1) u jednakom ili povišenom stanju u odnosu na tlak okoline, tako da još uvijek postoji razlika parcijalnog tlaka između retentata i permeata navedenog stupnja odvajanja permeata (3) i stoga postoji pokretačka sila u slučaju da se navedeni permeat iz navedenog stupnja odvajanja permeata (3) nalazi pod tlakom okoline ili se primjenjuje negativni tlak.
14. Postupak prema bilo kojem od patentnih zahtjeva 8 do 13, naznačen time što
sredstva za regulaciju (24) prilagođavaju kapacitet navedenog kompresora (4), poželjno njegovu brzinu rotacije, promjenama u drugoj struji permeata (9b) i/ili navedenoj trećoj struji retentata (10b) i/ili navedenoj struji sirovog plina (17),
ili time što
se mijenjanje količina recikliranog plina iz navedene druge struje permeata (9b) i/ili navedene treće struje retentata (10b) kompenzira, poželjno automatski, regulacijom isporučene količine sirovog plina, poželjno putem navedenog sredstva za regulaciju sirovog plina (25), poželjno bez promjene brzine rotacije navedenog kompresora
ili time što
učinkovitost postrojenja prema ovom izumu se povećava ili smanjuje promjenom volumenskog protoka navedenog kompresora (4), pri čemu se
rezultirajuća promjena u koncentraciji navedene manje permeirajuće komponente B u navedenoj drugoj struji retentata (8) suprotstavlja u skladu s alternativama postupka i/ii,
i/ili
rezultirajuća promjena u koncentraciji navedene manje permeirajuće komponente B u navedenoj trećoj struji permeata (11) se suprotstavlja u skladu s alternativama postupka iii/iv
i/ili
rezultirajuća promjena u brzini protoka navedene prve struje retentata (7) se suprotstavlja u skladu s alternativama postupka v/vi,
i/ili
rezultirajuća promjena u brzini protoka navedene prve struje permeata (6) se suprotstavlja u skladu s alternativama postupka vii/viii.
15. Postupak prema bilo kojem od patentnih zahtjeva 8 do 14, naznačen time što
navedeni postupak se primjenjuje u radu postrojenja za bioplin i time što se rotacijska brzina kompresora i a samim tim i volumenski protok navedenog kompresora (4) kontrolira u skladu s navedenom razinom punjenja postrojenja za bioplin, poželjno se određuje putem tlaka fermentacije ili srednjom razinom punjenja spremnika, kako bi se razina punjenja u fermentatoru i/ili međuprostoru spremnika mogla mijenjati ili održavati konstantnom,
i/ili time što
plinska smjesa koja se koristi je smjesa pretežno, ali ne isključivo ugljikovog dioksida i metana ili smjesa pretežno, ali ne isključivo vodika i metana ili smjesa pretežno, ali ne isključivo ugljikovog monoksida i vodika ili sirovog bioplina ili sirovog prirodnog plina.
16. Postupak prema bilo kojem od patentnih zahtjeva 8 do 15, naznačen time što
membranski moduli za odvajanje plina koji imaju mješovitu selektivnost plina CO2/CH4 od ne manje od 30, poželjno ne manje od 35, poželjnije ne manje od 40 i najpoželjnije ne manje od 45 se koriste barem u navedenom stupnju odvajanja dovodne struje (1), ali poželjno u sva tri stupanja membranskog odvajanja (1) do (3),
i/ili time što
volumen plina koji se reciklira u navedenoj drugoj struji permeata (9b) i u navedenoj trećoj struji retentata (10b) iznosi ukupno manje od 60 volumenskih % volumena struje sirovog plina (17),
i/ili time što
koncentracija najmanje jednog plina permeata navedenog stupnja odvajanja dovodne struje (1), nakon povrata navedene druge struje permeata (9b) i navedene treće struja retentata (10b), se povećava u navedenoj dovodnoj struji (5), poželjno za ne manje od 2%, poželjnije za ne manje od 3% i još poželjnije za 3 do 40%, sve u usporedbi s koncentracijom u navedenoj struji sirovog plina (17).
17. Postrojenje za bioplin, naznačeno time što sadrži uređaj prema bilo kojem od patentnih zahtjeva 1 do 7.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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EP12192571 | 2012-11-14 | ||
EP13167835 | 2013-05-15 | ||
PCT/EP2013/071039 WO2014075850A1 (de) | 2012-11-14 | 2013-10-09 | Steuerung der gaszusammensetzung einer gasseparationsanlage mit membranen |
EP13774181.5A EP2919888B1 (de) | 2012-11-14 | 2013-10-09 | Steuerung der gaszusammensetzung einer gasseparationsanlage mit membranen |
Publications (1)
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HRP20191705T1 true HRP20191705T1 (hr) | 2019-12-13 |
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HRP20191705 HRP20191705T1 (hr) | 2012-11-14 | 2019-09-19 | Kontrola plinskog sastava postrojenja za odvajanje plina s membranama |
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US (1) | US9770687B2 (hr) |
EP (1) | EP2919888B1 (hr) |
JP (1) | JP6400017B2 (hr) |
KR (1) | KR102097480B1 (hr) |
CN (1) | CN104797322B (hr) |
AU (1) | AU2013347150B2 (hr) |
BR (1) | BR112015010492B8 (hr) |
CA (1) | CA2891492C (hr) |
DK (1) | DK2919888T3 (hr) |
EA (1) | EA032909B1 (hr) |
ES (1) | ES2746099T3 (hr) |
HR (1) | HRP20191705T1 (hr) |
HU (1) | HUE045214T2 (hr) |
IL (1) | IL238397B (hr) |
LT (1) | LT2919888T (hr) |
MX (1) | MX2015006129A (hr) |
MY (1) | MY185177A (hr) |
PH (1) | PH12015501063B1 (hr) |
PL (1) | PL2919888T3 (hr) |
PT (1) | PT2919888T (hr) |
RS (1) | RS59147B1 (hr) |
SG (1) | SG11201503826RA (hr) |
SI (1) | SI2919888T1 (hr) |
WO (1) | WO2014075850A1 (hr) |
ZA (1) | ZA201503318B (hr) |
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2013
- 2013-10-09 RS RS20191107A patent/RS59147B1/sr unknown
- 2013-10-09 US US14/442,804 patent/US9770687B2/en active Active
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2015
- 2015-04-21 IL IL238397A patent/IL238397B/en active IP Right Grant
- 2015-05-13 PH PH12015501063A patent/PH12015501063B1/en unknown
- 2015-05-13 ZA ZA2015/03318A patent/ZA201503318B/en unknown
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2019
- 2019-09-19 HR HRP20191705 patent/HRP20191705T1/hr unknown
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