CL2017000409A1 - Método y dispositivo para separar dos fases - Google Patents

Método y dispositivo para separar dos fases

Info

Publication number
CL2017000409A1
CL2017000409A1 CL2017000409A CL2017000409A CL2017000409A1 CL 2017000409 A1 CL2017000409 A1 CL 2017000409A1 CL 2017000409 A CL2017000409 A CL 2017000409A CL 2017000409 A CL2017000409 A CL 2017000409A CL 2017000409 A1 CL2017000409 A1 CL 2017000409A1
Authority
CL
Chile
Prior art keywords
phase
heavy
light
impurities
fraction
Prior art date
Application number
CL2017000409A
Other languages
English (en)
Inventor
Anders Göran Hofstedt
Original Assignee
Anders Göran Hofstedt
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=56020122&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=CL2017000409(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Anders Göran Hofstedt filed Critical Anders Göran Hofstedt
Publication of CL2017000409A1 publication Critical patent/CL2017000409A1/es

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B5/00—Other centrifuges
    • B04B5/10—Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/04—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
    • B04B1/08—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B13/00—Recovery of fats, fatty oils or fatty acids from waste materials
    • C11B13/005—Recovery of fats, fatty oils or fatty acids from waste materials of residues of the fabrication of wood-cellulose (in particular tall-oil)
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C11/00—Regeneration of pulp liquors or effluent waste waters
    • D21C11/0007—Recovery of by-products, i.e. compounds other than those necessary for pulping, for multiple uses or not otherwise provided for
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C11/00—Regeneration of pulp liquors or effluent waste waters
    • D21C11/0042—Fractionating or concentration of spent liquors by special methods
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
    • H05B6/00—Heating by electric, magnetic or electromagnetic fields
    • H05B6/02—Induction heating
    • H05B6/10—Induction heating apparatus, other than furnaces, for specific applications
    • H05B6/101—Induction heating apparatus, other than furnaces, for specific applications for local heating of metal pieces
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Electromagnetism (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Centrifugal Separators (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

<p>MÉTODO PARA SEPARAR AL MENOS UNA MEZCLA DE UNA FASE LÍQUIDA O SÓLIDA LIGERA Y UNA FASE LÍQUIDA PESADA. LA INVENCIÓN SE CARACTERIZA EN LOS PASOS DE A) REALIZAR UNA PRIMERA SEPARACIÓN DE LA MEZCLA EN UN PRIMER SEPARADOR CENTRÍFUGO, LO QUE DA POR RESULTADO UNA PRIMERA FRACCIÓN PESADA COMPRENDIDA DE LA FASE PESADA CON SÓLO PEQUEÑAS CANTIDADES DE IMPUREZAS EN LA FORMA DE LA FASE LIGERA Y UNA PRIMERA FRACCIÓN LIGERA COMPRENDIDA DE LA FASE LIGERA CON IMPUREZAS EN LA FORMA DE LA FASE PESADA; Y B) REALIZAR UNA SEGUNDA SEPARACIÓN DE LA PRIMERA FRACCIÓN LIGERA EN UN SEGUNDO SEPARADOR CENTRÍFUGO HERMÉTICO DEL TIPO PURIFICADOR, LO QUE DA POR RESULTADO UNA SEGUNDA FRACCIÓN PESADA COMPRENDIDA DE LA FASE PESADA CON IMPUREZAS EN LA FORMA DE LA FASE LIGERA Y UNA SEGUNDA FRACCIÓN LIGERA COMPRENDIDA DE LA FASE LIGERA CON SOLO PEQUEÑAS CANTIDADES DE IMPUREZAS EN LA FORMA DE LA FASE PESADA. LA INVENCIÓN TAMBIÉN SE REFIERE A UN DISPOSITIVO.</p>
CL2017000409A 2014-08-21 2017-02-20 Método y dispositivo para separar dos fases CL2017000409A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE1450971A SE539191C2 (sv) 2014-08-21 2014-08-21 Förfarande och anordning för att separera två faser

Publications (1)

Publication Number Publication Date
CL2017000409A1 true CL2017000409A1 (es) 2017-08-18

Family

ID=56020122

Family Applications (1)

Application Number Title Priority Date Filing Date
CL2017000409A CL2017000409A1 (es) 2014-08-21 2017-02-20 Método y dispositivo para separar dos fases

Country Status (7)

Country Link
US (1) US10486169B2 (es)
EP (1) EP3183064B1 (es)
CA (1) CA2958679C (es)
CL (1) CL2017000409A1 (es)
RU (1) RU2698875C1 (es)
SE (1) SE539191C2 (es)
WO (1) WO2016028214A1 (es)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK4015088T3 (da) * 2019-08-19 2023-09-11 Alfa Laval Corp Ab Centrifugeseparationssystem og fremgangsmåde til anvendelse af en centrifugeseparator
CN113004940B (zh) * 2021-03-02 2022-07-15 西安近代化学研究所 一种非均相三组元液体燃料的快速分离系统及方法

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2200468A (en) 1938-08-08 1940-05-14 Francis J Cirves Recovery of by-products from black liquor
NL113586C (es) * 1956-04-26 1900-01-01
US3963219A (en) * 1974-04-30 1976-06-15 Amico Anthony J D Fence
SU532396A1 (ru) * 1974-06-11 1976-10-25 Карагандинский политехнический институт Центробежный сепаратор
SE528537C2 (sv) * 2003-11-24 2006-12-12 Biovelop Internat Bv Löslig dietfiber från havre- och kornsädeskorn
SE530024C2 (sv) * 2006-06-20 2008-02-12 Alfa Laval Corp Ab Centrifugalseparator där den mekaniska tätningsanordningen innefattar ett förspänningselement
EP2181744A1 (en) 2008-10-29 2010-05-05 Citec Engineering Oy AB Method and arrangement for separating water and particular material from heavy fuel oil
SE534386C2 (sv) * 2009-10-29 2011-08-02 Alfa Laval Corp Ab Centrifugalseparator samt metod för separering av fasta partiklar
SE536019C2 (sv) 2009-11-06 2013-04-02 Alfa Laval Corp Ab Hermetisk centrifugalseparator
SE534404C2 (sv) 2009-12-30 2011-08-09 Anders Goeran Hofstedt Förfarande för att från en blandning av svartlut och råsåpa låta separera och spjälka råsåpa
US9308473B2 (en) 2011-04-20 2016-04-12 Hatch Pty Ltd Phase splitter
AU2012271578B2 (en) 2011-06-14 2016-05-12 Oat Tech Incorporated Oat-derived sweetener
EP3178565B1 (en) 2012-05-14 2018-06-27 Alfa Laval Corporate AB Disc stack for centrifugal separator

Also Published As

Publication number Publication date
US10486169B2 (en) 2019-11-26
RU2698875C1 (ru) 2019-08-30
EP3183064B1 (en) 2020-10-21
SE539191C2 (sv) 2017-05-09
SE1450971A1 (sv) 2016-02-22
WO2016028214A1 (en) 2016-02-25
CA2958679A1 (en) 2016-02-25
US20170246646A1 (en) 2017-08-31
CA2958679C (en) 2023-09-12
EP3183064A4 (en) 2017-12-27
EP3183064A1 (en) 2017-06-28

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