ES2528741T3 - Método para secar materia particulada húmeda, en el que la materia particulada secada es un mineral blanco que tiene un brillo Ry de al menos el 65%, a través de secado en un secador de vapor sobrecalentado directo - Google Patents

Método para secar materia particulada húmeda, en el que la materia particulada secada es un mineral blanco que tiene un brillo Ry de al menos el 65%, a través de secado en un secador de vapor sobrecalentado directo Download PDF

Info

Publication number
ES2528741T3
ES2528741T3 ES11162729.5T ES11162729T ES2528741T3 ES 2528741 T3 ES2528741 T3 ES 2528741T3 ES 11162729 T ES11162729 T ES 11162729T ES 2528741 T3 ES2528741 T3 ES 2528741T3
Authority
ES
Spain
Prior art keywords
particulate matter
steam
drying chamber
excess
superheated steam
Prior art date
Legal status (The legal status 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 status listed.)
Active
Application number
ES11162729.5T
Other languages
English (en)
Inventor
Olav Bergset
Alain Cremaschi
Robert Gutsche
Ludovic Hautcoeur
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Omya International AG
Original Assignee
Omya International AG
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 Omya International AG filed Critical Omya International AG
Application granted granted Critical
Publication of ES2528741T3 publication Critical patent/ES2528741T3/es
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (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)

Abstract

Método para secar materia particulada húmeda, en el que la materia particulada secada es un mineral blanco que tiene un brillo Ry de al menos el 65% medido según la norma DIN 53163, comprendiendo el método las etapas de a) proporcionar al menos una corriente (1) de alimentación de materia particulada húmeda, b) proporcionar un circuito de recirculación que comprende al menos una cámara (40) de secado, al menos un ventilador (41) de circulación y al menos un intercambiador (42) de calor, en el que la al menos una cámara (40) de secado comprende un sistema de mezclado y materia particulada mezclada, al menos una entrada para la corriente de alimentación de materia particulada húmeda, al menos una entrada para el vapor sobrecalentado y al menos una salida para el vapor de escape, c) alimentar, o bien de manera continua o bien discontinua, la al menos una corriente (1) de alimentación de materia particulada húmeda al interior de la materia particulada mezclada en la al menos una cámara (40) de secado por medio de la al menos una entrada para la corriente de alimentación, d) alimentar vapor (6) sobrecalentado al interior de la al menos una cámara (40) de secado por medio de la al menos una entrada para vapor sobrecalentado, e) poner en contacto directamente la materia particulada mezclada con vapor sobrecalentado dentro de la al menos una cámara (40) de secado para secar la materia particulada mezclada y dejar escapar dicho vapor por medio de la al menos una salida para el vapor (3) de escape sin separar del vapor (3) de escape ninguna materia particulada transportada, f) alimentar el vapor (3, 4, 5) de escape que transporta materia particulada al interior del al menos un intercambiador (42) de calor, en el que el vapor de escape que transporta materia particulada se recalienta para proporcionar vapor (6) sobrecalentado, en el que el vapor de escape que transporta materia particulada pasa por el al menos un ventilador (41) de circulación antes o después del al menos un intercambiador (42) de calor y alimentar dicho vapor sobrecalentado de nuevo al interior de la al menos una cámara (40) de secado por medio de la al menos una entrada para vapor sobrecalentado, g) separar un vapor (7) en exceso de al menos una posición dentro del circuito de recirculación, h) alimentar el vapor (7) en exceso al interior de al menos un compresor (43) mecánico, en el que el vapor en exceso se comprime para elevar la temperatura saturada del vapor en exceso, usar dicho vapor (8) en exceso comprimido como fuente de calor en el al menos un intercambiador (42) de calor y descargar el vapor en exceso como un condensado (9) líquido, e i) descargar, o bien de manera continua o bien discontinua, la materia particulada secada como al menos una corriente de producto por medio de al menos una salida para obtener la materia particulada secada.

Description

imagen1
imagen2
imagen3
imagen4
imagen5
imagen6
imagen7
imagen8
imagen9
imagen10
imagen11
imagen12
imagen13
imagen14
imagen15
imagen16

Claims (1)

  1. imagen1
    imagen2
    imagen3
ES11162729.5T 2011-04-15 2011-04-15 Método para secar materia particulada húmeda, en el que la materia particulada secada es un mineral blanco que tiene un brillo Ry de al menos el 65%, a través de secado en un secador de vapor sobrecalentado directo Active ES2528741T3 (es)

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
ES2528741T3 true ES2528741T3 (es) 2015-02-12

Family

ID=44501777

Family Applications (1)

Application Number Title Priority Date Filing Date
ES11162729.5T Active ES2528741T3 (es) 2011-04-15 2011-04-15 Método para secar materia particulada húmeda, en el que la materia particulada secada es un mineral blanco que tiene un brillo Ry de al menos el 65%, a través de secado en un secador de vapor sobrecalentado directo

Country Status (21)

Country Link
US (1) US10190820B2 (es)
EP (2) EP2511637B1 (es)
JP (1) JP5791781B2 (es)
KR (2) KR101750078B1 (es)
CN (1) CN103534545B (es)
AU (1) AU2012241989B2 (es)
BR (1) BR112013026493A2 (es)
CA (1) CA2831859C (es)
CL (1) CL2013002913A1 (es)
CO (1) CO6801699A2 (es)
DK (1) DK2511637T3 (es)
ES (1) ES2528741T3 (es)
HR (1) HRP20150090T1 (es)
MX (1) MX336705B (es)
PL (1) PL2511637T3 (es)
PT (1) PT2511637E (es)
RS (1) RS53755B1 (es)
RU (1) RU2559409C2 (es)
SI (1) SI2511637T1 (es)
TW (1) TWI457525B (es)
WO (1) WO2012140028A1 (es)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108548389A (zh) * 2018-04-17 2018-09-18 张静雯 一种抖动敲打式谷物烘干装置

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10260803B2 (en) 2013-05-22 2019-04-16 Waister As Method, a system and devices for processing at least one substance in 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
US10780393B2 (en) * 2015-12-23 2020-09-22 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.
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
US20220333863A1 (en) * 2019-08-30 2022-10-20 Cargill, Incorporated 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)

* Cited by examiner, † Cited by third party
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
WO2003052336A1 (en) 2001-12-17 2003-06-26 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
DE602005026829D1 (de) * 2005-11-29 2011-04-21 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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108548389A (zh) * 2018-04-17 2018-09-18 张静雯 一种抖动敲打式谷物烘干装置

Also Published As

Publication number Publication date
EP2511637A1 (en) 2012-10-17
CN103534545A (zh) 2014-01-22
AU2012241989B2 (en) 2015-09-17
CO6801699A2 (es) 2013-11-29
CN103534545B (zh) 2016-03-02
CA2831859C (en) 2017-05-16
US10190820B2 (en) 2019-01-29
US20140310979A1 (en) 2014-10-23
MX336705B (es) 2016-01-28
RU2559409C2 (ru) 2015-08-10
SI2511637T1 (sl) 2015-02-27
HRP20150090T1 (hr) 2015-04-24
KR20140006051A (ko) 2014-01-15
PL2511637T3 (pl) 2015-04-30
PT2511637E (pt) 2015-02-05
TW201245647A (en) 2012-11-16
WO2012140028A1 (en) 2012-10-18
JP5791781B2 (ja) 2015-10-07
KR101750078B1 (ko) 2017-06-22
RS53755B1 (en) 2015-06-30
EP2697586A1 (en) 2014-02-19
JP2014512507A (ja) 2014-05-22
DK2511637T3 (en) 2015-02-02
EP2511637B1 (en) 2014-10-29
CL2013002913A1 (es) 2014-10-17
RU2013150808A (ru) 2015-05-20
AU2012241989A1 (en) 2013-12-05
BR112013026493A2 (pt) 2016-12-27
TWI457525B (zh) 2014-10-21
KR20160018845A (ko) 2016-02-17
CA2831859A1 (en) 2012-10-18
MX2013011764A (es) 2013-11-04

Similar Documents

Publication Publication Date Title
ES2528741T3 (es) Método para secar materia particulada húmeda, en el que la materia particulada secada es un mineral blanco que tiene un brillo Ry de al menos el 65%, a través de secado en un secador de vapor sobrecalentado directo
CN107076513B (zh) 糊状产品的热干燥方法和设备
EP2775028A3 (en) Laundry treating apparatus
EA201290376A1 (ru) Способ и устройство для сушки листов гипсокартона
FI3733615T3 (fi) Monitoiminen märän jätteen käsittelyjärjestelmä
BR112012031704A2 (pt) dispositivo e método para a secagem e torrefação de pelo menos um fluxo de material contendo carbono em um forno de múltiplas lareiras
TR201104078A1 (tr) Isı pompalı çamaşır kurutucu.
KR20130097402A (ko) 습윤한 물질의 건조기
BRPI0603944A (pt) aparelho e método de secar roupas
AR086226A1 (es) Secadora de granos con flujo de aire de doble paso
CA2998660A1 (en) Continuous-flow dryer comprising a heat exchanger
EA202091532A1 (ru) Способ и устройство для сушки гипсовой плиты
CA3002087A1 (en) Continuous-flow dryer comprising an exhaust air recirculation device
PH12016502494A1 (en) Dispersing and flattening apparatus for uniform drying of transportation coals in coal dryer using reheat steam
PL405932A1 (pl) Instalacja do suszenia, w szczególności do suszenia drewna i sposób suszenia w takiej instalacji
PH12020500634A1 (en) Clothes dryer
GB201106891D0 (en) Biomass plant
JP2011220593A (ja) 連続式箱型乾燥機が具えられた乾燥設備
AR098353A1 (es) Aparato de lecho fluidizado
TR201818635T4 (tr) Bir Çamaşır Kurutucu
CA3002089A1 (en) Continuous-flow dryer comprising a first and a second section
RS20100203A2 (en) LOW TEMPERATURE CONDENSER DRYER WITH FULL AIR RECIRCULATION SUPPORTED BY HEAT PUMP OPERATION
CN102435053A (zh) 一种利用自身蒸发气体进行热循环的干燥方法
RU2010123609A (ru) Система сушки осадка
ES2564520T3 (es) Procedimiento y dispositivo de tratamiento de productos con una corriente de gas