HRP20150090T1 - Postupak za sušenje mokrih äśestica, gdje su mokre äśestice bijeli mineral sa svjetlinom ry od barem 65%, kroz sušenje u direktnom supergrijanom parnom sušioniku - Google Patents
Postupak za sušenje mokrih äśestica, gdje su mokre äśestice bijeli mineral sa svjetlinom ry od barem 65%, kroz sušenje u direktnom supergrijanom parnom sušioniku Download PDFInfo
- Publication number
- HRP20150090T1 HRP20150090T1 HRP20150090TT HRP20150090T HRP20150090T1 HR P20150090 T1 HRP20150090 T1 HR P20150090T1 HR P20150090T T HRP20150090T T HR P20150090TT HR P20150090 T HRP20150090 T HR P20150090T HR P20150090 T1 HRP20150090 T1 HR P20150090T1
- Authority
- HR
- Croatia
- Prior art keywords
- calcium carbonate
- particles
- steam
- drying chamber
- drying
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims 22
- 238000001035 drying Methods 0.000 title claims 21
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims 9
- 239000011707 mineral Substances 0.000 title claims 9
- 239000013618 particulate matter Substances 0.000 title 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims 32
- 239000002245 particle Substances 0.000 claims 26
- 229910000019 calcium carbonate Inorganic materials 0.000 claims 15
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims 4
- 238000004519 manufacturing process Methods 0.000 claims 4
- 239000000203 mixture Substances 0.000 claims 4
- 229920006395 saturated elastomer Polymers 0.000 claims 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims 2
- 239000000920 calcium hydroxide Substances 0.000 claims 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims 2
- 239000007788 liquid Substances 0.000 claims 2
- 239000007787 solid Substances 0.000 claims 2
- 239000005995 Aluminium silicate Substances 0.000 claims 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims 1
- 235000012211 aluminium silicate Nutrition 0.000 claims 1
- 239000000440 bentonite Substances 0.000 claims 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims 1
- 229910000281 calcium bentonite Inorganic materials 0.000 claims 1
- BAJCNPGPHMFYJP-UHFFFAOYSA-L calcium oxygen(2-) titanium(4+) carbonate Chemical compound [O-2].[O-2].[Ca+2].[Ti+4].[O-]C([O-])=O BAJCNPGPHMFYJP-UHFFFAOYSA-L 0.000 claims 1
- 239000004927 clay Substances 0.000 claims 1
- 229910052570 clay Inorganic materials 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 239000010459 dolomite Substances 0.000 claims 1
- 229910000514 dolomite Inorganic materials 0.000 claims 1
- 239000000835 fiber Substances 0.000 claims 1
- 238000005188 flotation Methods 0.000 claims 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims 1
- 239000000347 magnesium hydroxide Substances 0.000 claims 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims 1
- 230000014759 maintenance of location Effects 0.000 claims 1
- 229940088417 precipitated calcium carbonate Drugs 0.000 claims 1
- 239000002893 slag Substances 0.000 claims 1
- 239000000454 talc Substances 0.000 claims 1
- 229910052623 talc Inorganic materials 0.000 claims 1
- 239000004408 titanium dioxide Substances 0.000 claims 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F11/00—Compounds of calcium, strontium, or barium
- C01F11/18—Carbonates
- C01F11/185—After-treatment, e.g. grinding, purification, conversion of crystal morphology
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/12—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
- F26B11/16—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a vertical or steeply-inclined plane
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/18—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotating helical blades or other rotary conveyors which may be heated moving materials in stationary chambers, e.g. troughs
- F26B17/20—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotating helical blades or other rotary conveyors which may be heated moving materials in stationary chambers, e.g. troughs the axis of rotation being horizontal or slightly inclined
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/001—Heating arrangements using waste heat
- F26B23/002—Heating arrangements using waste heat recovered from dryer exhaust gases
- F26B23/004—Heating arrangements using waste heat recovered from dryer exhaust gases by compressing and condensing vapour in exhaust gases, i.e. using an open cycle heat pump system
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/18—Sludges, e.g. sewage, waste, industrial processes, cooling towers
-
- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Microbiology (AREA)
- Drying Of Solid Materials (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
Claims (20)
1. Postupak za sušenje mokrih čestica, naznačen time da su suhe čestice minerali koji imaju svjetlinu Ry od barem 65% mjerenu u skladu s DIN 53163, postupak koji sadrži sljedeće korake
a) omogućavanje barem jednog toka za napajanje (1) mokrih čestica,
b) omogućavanje barem jednog recirkulacijskog kruga koji sadrži barem jednu komoru za sušenje (40), barem jedan cirkulacijski ventilator (41) i barem jedan izmjenjivač topline (42), pri čemu barem jedna komora za sušenje(40) obuhvaća sustav za miješanje i miješane čestice, barem jedan ulaz toka za napajanje vlažnih čestica, barem jedan ulaz vruće pare i barem jedan izlaz ispušne pare
c) dovođenje, bilo stalno ili povremeno, barem jednog toka za napajanje (1) vlažnih čestica u miješane čestice u barem jednoj komori za sušenje (40) putem barem jednog ulaza toka za napajanje,
d) dovođenje vruće pare (6) u barem jednu komoru za sušenje (40) putem barem jednog ulaza vruće pare,
e) izravno kontaktiranje miješanih čestica s vrućom parom u barem jednoj komori za sušenje (40) radi sušenja miješanih čestica i ispuštanje navedene pare putem barem jednog izlaza ispušne pare (3), bez odvajanja od ispušne pare (3) bilo koje prenesene čestice,
f) dovođenje ispušne pare u kojoj se nalaze čestice (3, 4, 5) u barem jedan izmjenjivač topline (42) u kojemu se ispušna para sa česticama ponovno zagrijava kako bi se dobila vruća para (6), pri čemu ispušna para u kojoj se nalaze čestice prolazi kroz barem jedan cirkulacijski ventilator (41) prije ili nakon barem jednog izmjenjivača topline (42) i dovođenje navedene vruće pare natrag u barem jednu komoru za sušenje (40) putem barem jednog ulaza vruće pare,
g) podjela viška pare (7) s barem jednog položaja unutar recirkulacijskog kruga,
h) dovođenje viška pare (7) u barem jedan mehanički kompresor (43), pri čemu se višak pare komprimira kako bi se podigla zasićena temperatura viška pare, koristeći komprimirani višak pare (8) kao izvor topline u barem jednom izmjenjivaču topline (42) i odvodeći višak pare kao tekući kondenzat (9), i
i) ispuštanje, bilo stalno ili povremeno, suhih čestica kao barem jednog proizvodnog toke putem barem jednog izlaza kako bi se dobile suhe čestice
2. Postupak u skladu s patentnim zahtjevom 1, naznačen time da barem jedna komora za sušenje (40) ima barem jedan izlaz za suhe čestice i da se barem jedan proizvodni tok ispušta putem barem jednog izlaza za suhe čestice iz barem jedne komore za sušenje i/ili da preostali recirkulacijski krug bez barem jedne komore sa sušenje ima barem jedan otvor za suhe čestice i da se barem jedan proizvodni tok ispušta putem barem jednog otvora za suhe čestice iz recirkulacijskog kruga bez barem jedne komore za sušenje.
3. Postupak u skladu s patentnim zahtjevom 1 ili 2, naznačen time da je sustav za miješanje u komori za sušenje odabran od jedne, dviju ili više miješalica osovine, ili jedne, dviju ili više miješalica kombiniranih s osovinama i mehanički fluidizirane osnove za ležaj, pri čemu je sustav za miješanje po mogućnosti mješalica sa dvije kombinirane osovine i mehanički fluidizirana osnova za ležaj.
4. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da je tlak u barem jednoj komori za sušenje od 0 do 5 bar, poželjno od 0.1 do 1,5 bar, a još poželjnije od 0,1 do 0,95 bar ili od 1,05 do 1,2 bar.
5. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da je vruća para vruća vodena para i da je pad tlaka kroz recirkulacijski krug od 500 do 3000 Pa, po mogućnosti 1000 do 2000 Pa, pri čemu je tlak u barem jednoj komori za sušenje od 0,8 do 1,2 bar.
6. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da se višak pare (7) dijeli iz barem jednog položaja unutar recirculacijskog kruga, pri čemu se utvrđuje da je prenesena količina čestica najniža, pri čemu se po mogućnosti višak pare (7) dijeli iz ispušne pare (3) nakon izlaska iz barem jedne komore za sušenje (40), a prije izlaska iz barem jednog circulacijskog ventilatora (41).
7. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da je barem jedan izmjenjivač topline (42) omotač i cijevni izmjenjivač topline.
8. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time, da je barem jedan mehanički kompresor centrifugalni kompresor, visokotlačni centrifugalni ventilator ili volumetrička pumpa, po mogućnosti visokotlačni centrifugalni ventilator.
9. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da se temperatura vruće pare (6) i temperatura ispušne pare (3) koja izlazi iz barem jedne komore za sušenje razlikuje temperaturnom razlikom ΔTR, pri čemu je ΔTRod 5 do 100°C, poželjno od 10 do 50°C, poželjnije od 15 do 30°C, još poželjnije od 15 do 25°C i najpoželjnije oko 22°C.
10. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da se zasićena temperatura viška pare (7) i zasićena temperatura komprimiranog viška pare (8) razlikuje temperaturnom razlikom ΔTE, pri čemu je ΔTE od 6 do 130°C, poželjno 11 do 80°C, poželjnije od 15 do 60°C i najpoželjnije od 20 do 45°C.
11. Postupak u skladu s patentnim zahtjevom 9 ili 10, naznačen time da je razlika između ΔTE i ΔTR od 1 do 30°C, poželjno od 4 do 20°C, još poželjnije od 6 do 15°C i najpoželjnije 6 do 10°C.
12. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da višak pare (7) prolazi barem kroz jedan separator (44) kako bi se uklonile bilo koje prenesene čestice iz viška pare prije nego se dovede kao pročišćeni ili ponovno prokuhani višak pare (17) u barem jedan mehanički kompresor (43).
13. Postupak u skladu s patentnim zahtjevom 12, naznačen time da se uklonjene prenesene čestice dovode kao reciklirajući tok (13) u barem jednu komoru za sušenje (40) ili u barem jedan tok za napajanje (1, 2).
14. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da je barem jedan tok za napajanje (1) prethodno zagrijan prije nego se dovede u barem jednu komoru za sušenje (40), pri čemu je poželjno da tok za napajanje (1) bude prethodno zagrijan barem jednim izmjenjivačem topline (46), pri čemu se tekući kondenzat (9, 19), i/ili ispušni tok iz barem separatora (44) koristi kao izvor topline.
15. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da dobivene suhe čestice sadrže manje od 15 tež.-% ukupne vlage, poželjno manje od 5 tež.-%, poželjnije manje od 2 tež.-% te najpoželjnije manje od 1 tež.-%, na temelju ukupne težine suhih čestica.
16. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da je prosječno vrijeme zadržavanja suhih čestica unutar recirkulacijskog kruga barem 10 minuta, barem 30 minuta ili barem 60 minuta.
17. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da je bijel mineral odabran iz minerala na bazi kalcijeva karbonata ili kalcijeva hidroksida ili kalcijeva sulfata, poželjno kalcijeva karbonata, još poželjnije mljevenog kalcijeva karbonata, modificiranog kalcijeva karbonata ili precipitiranog kalcijeva karbonata ili odabran iz minerala koji sadrže kalcijev karbonat pri čemu minerali koji sadrže kalcijev karbonat po mogućnosti sadrže dolomit ili ostatke iz flotacije kalcijevog karbonata ili njihovih smjese.
18. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da je bijeli mineral mineral na bazi kalcijeva karbonata pomiješan s glinom ili talkom ili kalcijevim hidroksidom ili kalcijevim sulfatom, ili se radi o smjesama kalcijeva karbonata i kaolina ili smjesama kalcijeva karbonata i bentonita, ili smjesama prirodnog kalcijeva karbonata i aluminijeva hidroksida, magnezijeva hidroksida, tinjca ili sintetičkih ili prirodnih vlakana ili je kostruktura minerala, ponajprije kostruktura talk-kalcijeva karbonata ili talk-titanijeva dioksida ili kalcijeva karbonat-titanija dioksida.
19. Postupak u skladu s bilo kojim od prethodnih zahtjeva, naznačen time da su dobivene suhe čestice kalcijev karbonat sa sadržajem čvrste tvari od više od 95 tež.-%, u odnosu na ukupnu težinu kalcijeva karbonata.
20. Uporaba postupka u skladu s bilo kojim od patentnih zahtjeva 1 do 19 za proizvodnju kalcijeva karbonata sa sadržajem čvrste tvari od više od 95 tež.-%, u odnosu na ukupnu težinu mokrog kalcijeva karbonata, naznačena time da je kalcijev karbonat po mogućnosti proizveden bez prisutnosti klasifikatora.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP11162729.5A EP2511637B1 (en) | 2011-04-15 | 2011-04-15 | Method for drying wet particulate matter, wherein the dried particulate matter is a white mineral having a brightness Ry of at least 65%, through drying in a direct superheated steam dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| HRP20150090T1 true HRP20150090T1 (hr) | 2015-04-24 |
Family
ID=44501777
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| HRP20150090TT HRP20150090T1 (hr) | 2011-04-15 | 2015-01-26 | Postupak za sušenje mokrih äśestica, gdje su mokre äśestice bijeli mineral sa svjetlinom ry od barem 65%, kroz sušenje u direktnom supergrijanom parnom sušioniku |
Country Status (21)
| Country | Link |
|---|---|
| US (1) | US10190820B2 (hr) |
| EP (2) | EP2511637B1 (hr) |
| JP (1) | JP5791781B2 (hr) |
| KR (2) | KR101750078B1 (hr) |
| CN (1) | CN103534545B (hr) |
| AU (1) | AU2012241989B2 (hr) |
| BR (1) | BR112013026493A2 (hr) |
| CA (1) | CA2831859C (hr) |
| CL (1) | CL2013002913A1 (hr) |
| CO (1) | CO6801699A2 (hr) |
| DK (1) | DK2511637T3 (hr) |
| ES (1) | ES2528741T3 (hr) |
| HR (1) | HRP20150090T1 (hr) |
| MX (1) | MX336705B (hr) |
| PL (1) | PL2511637T3 (hr) |
| PT (1) | PT2511637E (hr) |
| RS (1) | RS53755B1 (hr) |
| RU (1) | RU2559409C2 (hr) |
| SI (1) | SI2511637T1 (hr) |
| TW (1) | TWI457525B (hr) |
| WO (1) | WO2012140028A1 (hr) |
Families Citing this family (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2913125C (en) | 2013-05-22 | 2021-11-09 | Multivector As | A method, a system and devices for processing at least one substance into a dried, fragmented, fluidized end product |
| NO339255B1 (no) * | 2013-05-22 | 2016-11-21 | Multivector As | Anordning for virvling av minst ett fragmentert stoff |
| NO339253B1 (no) * | 2013-05-22 | 2016-11-21 | Multivector As | Fremgangsmåte og system for behandling av minst ett stoff til et tørket, fragmentert, virvlet sluttprodukt |
| CN105085423B (zh) * | 2014-05-21 | 2019-03-12 | 欧洲技术设于伊特根的三聚氰氨-卢森堡-分支机构 | 用于干燥三聚氰胺晶体的工艺和相关设备 |
| CN105218469B (zh) * | 2014-06-25 | 2020-05-01 | 欧洲技术设于伊特根的三聚氰氨-卢森堡-分支机构 | 用于干燥三聚氰胺晶体的装置 |
| CN104448938A (zh) * | 2014-11-18 | 2015-03-25 | 江苏群鑫粉体材料有限公司 | 胶粘剂用超细活性重质碳酸钙的生产方法 |
| CN105000582B (zh) * | 2015-08-28 | 2016-08-24 | 沈阳鑫博工业技术股份有限公司 | 一种焙烧氢氧化铝回收水蒸汽的系统及方法 |
| FR3043165B1 (fr) * | 2015-10-29 | 2018-04-13 | CRYODIRECT Limited | Dispositif de transport d'un gaz liquefie et procede de transfert de ce gaz a partir de ce dispositif |
| US10151060B2 (en) * | 2015-11-24 | 2018-12-11 | Water-Gen Ltd | Steam compression dryer |
| EP3393973B1 (en) * | 2015-12-23 | 2022-08-24 | Mineral Carbonation International PTY Ltd | Dehydroxylation of magnesium silicate minerals for carbonation |
| CN105674694B (zh) * | 2016-01-07 | 2017-12-26 | 南昌理工学院 | 一种过热蒸汽干燥设备 |
| KR20170109912A (ko) * | 2016-03-22 | 2017-10-10 | 삼성에스디아이 주식회사 | 극판 건조 장치 |
| BR102016008739A2 (pt) * | 2016-04-19 | 2017-10-24 | Nunes Claristoni | Grain drying process |
| WO2018109144A1 (en) * | 2016-12-15 | 2018-06-21 | Hsl Energy Holding Aps | Plant and process for production of a dried product from a humid product |
| EP3361198A1 (en) | 2017-02-13 | 2018-08-15 | Danmarks Tekniske Universitet | A slurry drying plant, a method for drying slurry and use of a slurry drying plant |
| CA2973708C (en) * | 2017-07-18 | 2024-01-02 | Jorge Diaz | Method for efficient and effective drying. |
| CN108548389A (zh) * | 2018-04-17 | 2018-09-18 | 张静雯 | 一种抖动敲打式谷物烘干装置 |
| CN108759442A (zh) * | 2018-04-18 | 2018-11-06 | 浙江理工大学 | 过热蒸汽加热干燥装置及方法 |
| CN108741750A (zh) * | 2018-05-24 | 2018-11-06 | 国网山东省电力公司济南市章丘区供电公司 | 一种智能化电力施工二次接线图纸查看装置 |
| CN109011664A (zh) * | 2018-08-06 | 2018-12-18 | 昆山中能工业设备有限公司 | 加热物料的热交换装置 |
| CN109173321B (zh) * | 2018-08-21 | 2021-01-26 | 无锡华翔化纤有限公司 | 一种涤纶化纤生产用切片沸腾结晶干燥机 |
| JP7322367B2 (ja) * | 2018-09-13 | 2023-08-08 | 王子ホールディングス株式会社 | 粉体の乾燥装置ならびに粉体の乾燥方法 |
| CN109442965B (zh) * | 2018-11-12 | 2024-04-05 | 国能龙源环保有限公司 | 一种基于蒸汽再压缩技术的褐煤干燥收水系统 |
| CN210602572U (zh) * | 2019-07-02 | 2020-05-22 | 江苏集创原子团簇科技研究院有限公司 | 纳米材料干燥装置 |
| AR119243A1 (es) | 2019-07-08 | 2021-12-01 | Omya Int Ag | Composición seca cosmética y/o para el cuidado de la piel |
| CA3149734A1 (en) * | 2019-08-30 | 2021-03-04 | Jan Foeke KIKSTRA | Energy recovery from contact dryers |
| EP4157202A1 (en) | 2020-05-29 | 2023-04-05 | Omya International AG | Use of a mineral blend as cosmetic agent for wet cosmetic compositions |
| CN115265024B (zh) * | 2022-06-14 | 2023-11-24 | 浙江中控技术股份有限公司 | 一种循环冷却水系统集成控制优化的方法 |
Family Cites Families (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2622342A (en) | 1949-05-23 | 1952-12-23 | Goulounes Noel | Apparatus for the drying of granular and powdery materials |
| US4242808A (en) | 1978-11-22 | 1981-01-06 | Ingersoll-Rand Company | Paper web drying system and process |
| US4223452A (en) | 1979-02-12 | 1980-09-23 | Chambers John M | Drying process and apparatus for accomplishing the same |
| SE442023B (sv) | 1981-02-11 | 1985-11-25 | Svensk Exergiteknik Ab | Forfarande for upparbetning av betmassa fran sockerbetor och anordning for genomforandet av forfarandet |
| FR2510736B1 (fr) | 1981-07-28 | 1986-07-18 | Beghin Say Sa | Procede de sechage par recompression de vapeur |
| SE8405982L (sv) * | 1984-11-27 | 1986-05-28 | Hans Theliander | Sett att torka partikelformigt material |
| DE3443762A1 (de) | 1984-11-30 | 1986-06-05 | Uhde Gmbh, 4600 Dortmund | Verfahren und anlage zur kondensation von ueberschussdampf |
| DE58905358D1 (de) | 1988-05-24 | 1993-09-30 | Siemens Ag | Verfahren und Einrichtung zum Trocknen von Klärschlamm. |
| DE4234376A1 (de) * | 1992-10-12 | 1994-04-14 | Henkel Kgaa | Wertstoffe und Wertstoffgemische für Netz-, Wasch- und/oder Reinigungsmittel in neuer Zubereitungsform |
| US5291668A (en) | 1992-04-03 | 1994-03-08 | Tecogen, Inc. | Steam atmosphere drying exhaust steam recompression system |
| US5291688A (en) * | 1993-02-08 | 1994-03-08 | Pederson Robert D | Adjustable door assembly |
| US5632102A (en) * | 1994-11-14 | 1997-05-27 | Glatt Gmbh | Process and apparatus for the production and/or treatment of particles |
| TW562700B (en) * | 2000-11-28 | 2003-11-21 | Takamo Ind Co Ltd | Garbage processing machine |
| EP1466131B1 (en) | 2001-12-17 | 2006-12-27 | HOLM CHRISTENSEN BIOSYSTEMER ApS | Apparatus for drying a particulate product with superheated steam |
| DE10211292A1 (de) * | 2002-03-14 | 2003-09-25 | Basf Ag | Verfahren zur Herstellung von gefälltem Calciumcarbonat mit hohem Weißgrad |
| DE10323774A1 (de) * | 2003-05-26 | 2004-12-16 | Khd Humboldt Wedag Ag | Verfahren und Anlage zur thermischen Trocknung eines nass vermahlenen Zementrohmehls |
| US20050158225A1 (en) * | 2004-01-20 | 2005-07-21 | Mcgill Patrick D. | Structure level of silica from silica slurry method |
| ATE501090T1 (de) * | 2005-11-29 | 2011-03-15 | Trading Engineering Technologies Llc | Trockner und verfahren zur trocknung von gefälltem calciumcarbonat |
| CN201122041Y (zh) * | 2007-10-19 | 2008-09-24 | 林荣郎 | 具有热交换器的干燥机 |
| EP2158813A1 (en) * | 2008-08-28 | 2010-03-03 | Omya Development AG | Stabilisation of aqueous mineral preparations by reuterin |
| JP5446284B2 (ja) * | 2009-01-27 | 2014-03-19 | 王子ホールディングス株式会社 | 無機粒子の製造方法 |
-
2011
- 2011-04-15 PL PL11162729T patent/PL2511637T3/pl unknown
- 2011-04-15 ES ES11162729.5T patent/ES2528741T3/es active Active
- 2011-04-15 EP EP11162729.5A patent/EP2511637B1/en active Active
- 2011-04-15 SI SI201130354T patent/SI2511637T1/sl unknown
- 2011-04-15 DK DK11162729.5T patent/DK2511637T3/en active
- 2011-04-15 RS RS20150021A patent/RS53755B1/en unknown
- 2011-04-15 PT PT111627295T patent/PT2511637E/pt unknown
-
2012
- 2012-04-06 TW TW101111968A patent/TWI457525B/zh not_active IP Right Cessation
- 2012-04-11 CN CN201280018491.1A patent/CN103534545B/zh active Active
- 2012-04-11 MX MX2013011764A patent/MX336705B/es unknown
- 2012-04-11 WO PCT/EP2012/056494 patent/WO2012140028A1/en active Application Filing
- 2012-04-11 EP EP12712683.7A patent/EP2697586A1/en not_active Withdrawn
- 2012-04-11 KR KR1020137029177A patent/KR101750078B1/ko active IP Right Grant
- 2012-04-11 AU AU2012241989A patent/AU2012241989B2/en not_active Ceased
- 2012-04-11 CA CA2831859A patent/CA2831859C/en not_active Expired - Fee Related
- 2012-04-11 US US14/008,679 patent/US10190820B2/en active Active
- 2012-04-11 KR KR1020167002623A patent/KR20160018845A/ko not_active Application Discontinuation
- 2012-04-11 JP JP2014504286A patent/JP5791781B2/ja active Active
- 2012-04-11 RU RU2013150808/06A patent/RU2559409C2/ru active
- 2012-04-11 BR BR112013026493A patent/BR112013026493A2/pt not_active Application Discontinuation
-
2013
- 2013-10-11 CL CL2013002913A patent/CL2013002913A1/es unknown
- 2013-10-16 CO CO13245710A patent/CO6801699A2/es active IP Right Grant
-
2015
- 2015-01-26 HR HRP20150090TT patent/HRP20150090T1/hr unknown
Also Published As
| Publication number | Publication date |
|---|---|
| CA2831859C (en) | 2017-05-16 |
| RU2559409C2 (ru) | 2015-08-10 |
| CN103534545B (zh) | 2016-03-02 |
| AU2012241989B2 (en) | 2015-09-17 |
| PL2511637T3 (pl) | 2015-04-30 |
| SI2511637T1 (sl) | 2015-02-27 |
| PT2511637E (pt) | 2015-02-05 |
| US20140310979A1 (en) | 2014-10-23 |
| TW201245647A (en) | 2012-11-16 |
| BR112013026493A2 (pt) | 2016-12-27 |
| KR20160018845A (ko) | 2016-02-17 |
| ES2528741T3 (es) | 2015-02-12 |
| DK2511637T3 (en) | 2015-02-02 |
| KR20140006051A (ko) | 2014-01-15 |
| MX2013011764A (es) | 2013-11-04 |
| EP2511637A1 (en) | 2012-10-17 |
| EP2511637B1 (en) | 2014-10-29 |
| RU2013150808A (ru) | 2015-05-20 |
| CA2831859A1 (en) | 2012-10-18 |
| WO2012140028A1 (en) | 2012-10-18 |
| CL2013002913A1 (es) | 2014-10-17 |
| JP2014512507A (ja) | 2014-05-22 |
| MX336705B (es) | 2016-01-28 |
| EP2697586A1 (en) | 2014-02-19 |
| JP5791781B2 (ja) | 2015-10-07 |
| KR101750078B1 (ko) | 2017-06-22 |
| US10190820B2 (en) | 2019-01-29 |
| RS53755B1 (en) | 2015-06-30 |
| TWI457525B (zh) | 2014-10-21 |
| CN103534545A (zh) | 2014-01-22 |
| AU2012241989A1 (en) | 2013-12-05 |
| CO6801699A2 (es) | 2013-11-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| HRP20150090T1 (hr) | Postupak za sušenje mokrih äśestica, gdje su mokre äśestice bijeli mineral sa svjetlinom ry od barem 65%, kroz sušenje u direktnom supergrijanom parnom sušioniku | |
| JP6048778B2 (ja) | パーム油の生産加工工程から最終的に排出される排出水とパーム副産物とを利用した処理設備及び処理方法 | |
| FI124836B (fi) | Prosessi ja laitos metallioksidin valmistamiseksi metallisuoloista | |
| EA021211B1 (ru) | Способ и установка для получения оксида алюминия из гидроксида алюминия | |
| KR20150048438A (ko) | 산업폐열을 이용한 유기성폐기물 복합건조장치 | |
| CN102200379A (zh) | 一种节能喷雾干燥工艺 | |
| WO2018109144A1 (en) | Plant and process for production of a dried product from a humid product | |
| SE1050032A1 (sv) | System och förfarande för behandling av bulkmaterial i en pneumatisk ångtork | |
| RU2535559C2 (ru) | Способ управления процессом получения сыпучей формы холинхлорида на основе сухого свекловичного жома | |
| RU2653019C1 (ru) | Способ сушки пульпы фосфорной кислоты в сушильном барабане при производстве минеральных удобрений | |
| CN106418273A (zh) | 一种（鸡蛋）蛋黄粉的生产方法 | |
| CA2877629C (en) | Method of drying salt and similar materials through the use of heat engine waste heat | |
| NL8200830A (nl) | Werkwijze voor de vervaardiging van droog rookgasgips. | |
| CN116322351A (zh) | 用于生产高度可消化的水解角蛋白材料的改进方法 | |
| RU2178867C1 (ru) | Установка для сушки жома | |
| CN103058488B (zh) | 用窄筛分高温颗粒热载体干燥污泥的流化床干燥器 | |
| CN105794976A (zh) | 一种生产奶粉的方法 | |
| TH12887A3 (th) | กรรมวิธีการผลิตน้ำตาลมะพร้าวผงด้วยการทำแห้งแบบพ่นฝอย | |
| TH12887C3 (th) | กรรมวิธีการผลิตน้ำตาลมะพร้าวผงด้วยการทำแห้งแบบพ่นฝอย | |
| RU2014151325A (ru) | Способ получения сферического пороха |