ES2079981T3 - Procedimiento para la evacuacion mejorada de vahos en el secado de vapor caliente. - Google Patents

Procedimiento para la evacuacion mejorada de vahos en el secado de vapor caliente.

Info

Publication number
ES2079981T3
ES2079981T3 ES93917376T ES93917376T ES2079981T3 ES 2079981 T3 ES2079981 T3 ES 2079981T3 ES 93917376 T ES93917376 T ES 93917376T ES 93917376 T ES93917376 T ES 93917376T ES 2079981 T3 ES2079981 T3 ES 2079981T3
Authority
ES
Spain
Prior art keywords
exhaust
current
liquid phase
partial
vapour condensate
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.)
Expired - Lifetime
Application number
ES93917376T
Other languages
English (en)
Inventor
Wilfried Rahse
Johann Fues
Reiner Vogler
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.)
Henkel AG and Co KGaA
Original Assignee
Henkel AG and Co KGaA
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
Priority claimed from DE4204035A external-priority patent/DE4204035A1/de
Priority claimed from DE19924204090 external-priority patent/DE4204090A1/de
Priority claimed from DE19924206050 external-priority patent/DE4206050A1/de
Priority claimed from DE4206521A external-priority patent/DE4206521A1/de
Priority claimed from DE19924206495 external-priority patent/DE4206495A1/de
Priority claimed from DE19924208773 external-priority patent/DE4208773A1/de
Priority claimed from DE19924209432 external-priority patent/DE4209432A1/de
Application filed by Henkel AG and Co KGaA filed Critical Henkel AG and Co KGaA
Application granted granted Critical
Publication of ES2079981T3 publication Critical patent/ES2079981T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • 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
    • F26B3/10—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 the gas or vapour carrying the materials or objects to be dried with it
    • F26B3/12—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 the gas or vapour carrying the materials or objects to be dried with it in the form of a spray, i.e. sprayed or dispersed emulsions or suspensions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0033—Other features
    • B01D5/0036—Multiple-effect condensation; Fractional condensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
    • B01D5/009—Collecting, removing and/or treatment of the condensate
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00—Special methods for preparing compositions containing mixtures of detergents
    • C11D11/02—Preparation in the form of powder by spray drying
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00—Special methods for preparing compositions containing mixtures of detergents
    • C11D11/04—Special methods for preparing compositions containing mixtures of detergents by chemical means, e.g. by sulfonating in the presence of other compounding ingredients followed by neutralising
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/005—Treatment of dryer exhaust gases
    • F26B25/006—Separating volatiles, e.g. recovering solvents from dryer exhaust gases

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Wood Science & Technology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Processing Of Solid Wastes (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

LA CORRIENTE PARCIAL DE VAPORES DE EXHAUSTACION CARGADA CON SUSTANCIAS INERTES Y/O SUSTANCIAS DE VALOR ARRASTRADAS SE TRANSFIERE COMO UNA CORRIENTE DE PRODUCTO VAPOR A PARTIR DE LAS PLACAS DE SECADO OPERATIVAS CON VAPOR SOBRECALENTADO COMO GAS DE SECADO, A CONTINUACION ES AL MENOS CONDENSADO PARCIALMENTE MEDIANTE INTERCAMBIO DE CALOR INDIRECTO CON UN MEDIO REFRIGERANTE. EL VAPOR DE EXHAUSTACION CONDENSADO ES LIMPIADO DE FORMA SUBSECUENTE MEDIANTE AL MENOS UNA ETAPA DE DESTILACION. MEDIANTE RECIRCULACION DE UNA CORRIENTE PARCIAL A PARTIR DE LA FASE LIQUIDA DE LA PLANTA (5) DE DESTILACION, EL CONDENSADO DE VAPOR DE EXHAUSTACION SE UTILIZA PARA LA ABSORCION DE LA ENERGIA DE CONDENSACION DE LA CORRIENTE GASEOSA DEL VAPOR DE EXHAUSTACION DE UN INTERCAMBIADOR (2) DE CALOR INDIRECTO. EL CONDENSADO DE VAPOR DE EXHAUSTACION ASI PRODUCIDO SE SUMINISTRA A LA PLANTA (5) DE DESTILACION, DE DONDE ES LLEVADO A UN INTERCAMBIO DE ENERGIA DIRECTA CON LA CORRIENTE PARCIAL RECICLADA DEL CONDENSADO DE VAPOR DEEXHAUSTACION ARRASTRADO A PARTIR DE LA FASE LIQUIDA. UN VAPOR LIQUIDO PARCIAL, DISPONIENDO DE UNA CONCENTRACION ALTA DE SUSTANCIAS INERTES Y/O SUSTANCIAS DE VALOR ARRASTRADAS, PUEDE SER DE ESTA FORMA ARRASTRADO A PARTIR DE LA FASE LIQUIDA DE LA PLANTA (5) DE DESTILACION. LA FASE DE VAPOR A PARTIR DEL DESTILADOR (5) ES TRATADA ADEMAS EN UNA FORMA APROPIADA.
ES93917376T 1992-02-12 1993-02-04 Procedimiento para la evacuacion mejorada de vahos en el secado de vapor caliente. Expired - Lifetime ES2079981T3 (es)

Applications Claiming Priority (7)

Application Number Priority Date Filing Date Title
DE4204035A DE4204035A1 (de) 1992-02-12 1992-02-12 Verbessertes verfahren zur trocknung von wertstoffen fuer wasch- und reinigungsmittel mit ueberhitztem wasserdampf
DE19924204090 DE4204090A1 (de) 1992-02-12 1992-02-12 Vereinfachtes trocknungsverfahren fuer wertstoffe und wertstoffgemische aus dem bereich der wasch- und reinigungsmittel mit ueberhitztem wasserdampf
DE19924206050 DE4206050A1 (de) 1992-02-27 1992-02-27 Neuartige staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem aufloesevermoegen in waessrigen medien
DE4206521A DE4206521A1 (de) 1992-03-02 1992-03-02 Verfahren zur herstellung von granulaten, die als netz-, wasch- und/oder reinigungsmittel geeignet sind
DE19924206495 DE4206495A1 (de) 1992-03-02 1992-03-02 Verfahren zum herstellen von granulaten, die als netz-, wasch und/oder reinigungsmittel geeignet sind
DE19924208773 DE4208773A1 (de) 1992-03-19 1992-03-19 Verfahren zur trocknung von wertstoffen oder deren gemischen, die als netz-, wasch- und/oder reinigungsmittel geeignet sind
DE19924209432 DE4209432A1 (de) 1992-03-24 1992-03-24 Verfahren zur verbesserten Brüdenentsorgung bei der Heißdampftrocknung

Publications (1)

Publication Number Publication Date
ES2079981T3 true ES2079981T3 (es) 1996-01-16

Family

ID=27561562

Family Applications (1)

Application Number Title Priority Date Filing Date
ES93917376T Expired - Lifetime ES2079981T3 (es) 1992-02-12 1993-02-04 Procedimiento para la evacuacion mejorada de vahos en el secado de vapor caliente.

Country Status (10)

Country Link
EP (1) EP0625924B1 (es)
JP (1) JPH07503890A (es)
KR (1) KR950700105A (es)
AT (1) ATE130208T1 (es)
AU (1) AU3453193A (es)
BR (1) BR9305862A (es)
CA (1) CA2130005A1 (es)
DE (1) DE59300962D1 (es)
ES (1) ES2079981T3 (es)
WO (1) WO1993015816A1 (es)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4340093A1 (de) * 1993-11-24 1995-06-01 Cognis Bio Umwelt Verfahren zur vereinfachten Trennung von Mehrstoffgemischen wenigstens anteilig organischen Ursprungs
KR100864980B1 (ko) * 2002-06-11 2008-10-23 엘지디스플레이 주식회사 액정표시장치의 잔상방지장치
EP1719549A1 (en) * 2005-04-25 2006-11-08 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk Onderzoek TNO Method for purifying steam
DE102010025206A1 (de) 2010-06-22 2011-12-22 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren zur Rückgewinnung flüchtiger Bestandteile aus einem Feststoff
CN102967121B (zh) * 2012-11-30 2014-12-10 山东科院天力节能工程有限公司 废热蒸汽热量可回收利用的过热蒸汽褐煤干燥工艺
SE543500C2 (en) * 2020-02-20 2021-03-09 Valmet Oy Recovery of energy and chemicals from a steam explosion process
CN113735209A (zh) * 2021-09-09 2021-12-03 北京泾渭环境科技有限公司 一种全量化垃圾渗滤液处理装置及工艺

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1233709B (de) * 1962-12-03 1967-02-02 Rosenblads Patenter Ab Verfahren zum Kondensieren von beim Abblasen von Sulfatzellstoffkochern frei gewordenem Abblasedampf
DE2746927A1 (de) * 1976-10-25 1978-04-27 Erich Pagendarm Verfahren zum betrieb eines durchlauftrockners und trocknungsanlage fuer die ausuebung dieses verfahrens
JPS54151677A (en) * 1978-05-16 1979-11-29 Toyo Boseki Concentrator for polyvinylalcohol
DE2948541A1 (de) * 1979-12-03 1981-06-04 Nukem Gmbh, 6450 Hanau Verfahren und vorrichtung zur mehrstufigen verdampfung

Also Published As

Publication number Publication date
CA2130005A1 (en) 1993-08-13
JPH07503890A (ja) 1995-04-27
ATE130208T1 (de) 1995-12-15
EP0625924A1 (de) 1994-11-30
DE59300962D1 (de) 1995-12-21
KR950700105A (ko) 1995-01-16
WO1993015816A1 (de) 1993-08-19
BR9305862A (pt) 1997-02-18
EP0625924B1 (de) 1995-11-15
AU3453193A (en) 1993-09-03

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