ES308623A1 - Process and device for the continuous concentration-crystallization of sugar syrups - Google Patents

Process and device for the continuous concentration-crystallization of sugar syrups

Info

Publication number
ES308623A1
ES308623A1 ES0308623A ES308623A ES308623A1 ES 308623 A1 ES308623 A1 ES 308623A1 ES 0308623 A ES0308623 A ES 0308623A ES 308623 A ES308623 A ES 308623A ES 308623 A1 ES308623 A1 ES 308623A1
Authority
ES
Spain
Prior art keywords
syrup
crystallizations
concentrations
crystallization
treated
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
Application number
ES0308623A
Other languages
Spanish (es)
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.)
MALEK JEAN MICHE
Original Assignee
MALEK JEAN MICHE
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 MALEK JEAN MICHE filed Critical MALEK JEAN MICHE
Publication of ES308623A1 publication Critical patent/ES308623A1/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
    • C13B30/02—Crystallisation; Crystallising apparatus
    • C13B30/022—Continuous processes, apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D9/00—Crystallisation
    • B01D9/0018—Evaporation of components of the mixture to be separated
    • B01D9/0031—Evaporation of components of the mixture to be separated by heating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D9/00—Crystallisation
    • B01D9/0036—Crystallisation on to a bed of product crystals; Seeding
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D9/00—Crystallisation
    • B01D9/005—Selection of auxiliary, e.g. for control of crystallisation nuclei, of crystal growth, of adherence to walls; Arrangements for introduction thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
    • C13B30/02—Crystallisation; Crystallising apparatus
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
    • H05H1/00—Generating plasma; Handling plasma
    • H05H1/24—Generating plasma
    • H05H1/26—Plasma torches
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S159/00—Concentrating evaporators
    • Y10S159/03—Fluidized bed

Landscapes

  • Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Plasma & Fusion (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Spectroscopy & Molecular Physics (AREA)
  • Jellies, Jams, And Syrups (AREA)
  • Confectionery (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

Process and device for continuous concentration-crystallization of liquids such as sugar syrups, characterized in that the process consists in carrying continuously and subjecting the syrup to a series of successive heating and evaporation-concentrations-unit crystallizations, to be incorporated directly, in the syrup treated, each of these concentrations-unit crystallizations, except for the first, a gaseous phase and preferably air saturated with water vapor, in order to ensure intense circulation and agitation of this syrup in several circuits successively closed, in separating the gaseous phase fired in front of the circuit by the treated syrup, so that each of these closed circuits forms two liquid columns joined to their heads and their bases, the syrup constituting the first of these liquid columns, gilded of an upward movement caused by the thermal currents that prov They have the heating of the syrup, and the rise of the bubbles of the gas phase in this liquid column, the syrup representing the other column that is in a downward slide of recirculation, and in extracting, at the end of this series of successive concentrations-crystallizations , the product composed of substantially uniform crystalline grains in suspension in the mother liquor. (Machine-translation by Google Translate, not legally binding)
ES0308623A 1964-02-14 1965-01-27 Process and device for the continuous concentration-crystallization of sugar syrups Expired ES308623A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR963824A FR1393567A (en) 1964-02-14 1964-02-14 Method and device for the continuous concentration-crystallization of liquid solutions such as sweet syrups

Publications (1)

Publication Number Publication Date
ES308623A1 true ES308623A1 (en) 1965-06-16

Family

ID=8823194

Family Applications (1)

Application Number Title Priority Date Filing Date
ES0308623A Expired ES308623A1 (en) 1964-02-14 1965-01-27 Process and device for the continuous concentration-crystallization of sugar syrups

Country Status (6)

Country Link
US (1) US3505111A (en)
CH (1) CH440175A (en)
DE (1) DE1300880B (en)
ES (1) ES308623A1 (en)
FR (2) FR1393567A (en)
NL (1) NL6501748A (en)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE739031A (en) * 1968-09-21 1970-03-18
US3891395A (en) * 1970-12-17 1975-06-24 Escher Wyss Ltd Crystalliser with intergral pumping means
US3859052A (en) * 1972-08-15 1975-01-07 Joh A Benckiser Chem Fab Gmbh Crystallization apparatus having pressure-liquid level control means
US4168211A (en) * 1975-08-18 1979-09-18 Pottharst Jr John E Distillation apparatus and method
NL187770C (en) * 1980-11-12 1992-01-02 Esmil Bv FLOW-UP DEVICE FOR A LIQUID MEDIUM CONTAINING A FLUIDISABLE GRAIN MASS.
NL8102308A (en) * 1981-05-12 1982-12-01 Esmil Bv DEVICE FOR OPERATING PHYSICAL AND / OR CHEMICAL PROCESSES, IN PARTICULAR A HEAT EXCHANGER.
ES8302100A1 (en) * 1981-12-22 1983-02-01 Moreno Pedro Alamo Method for the agitation of liquid masses under vacuum by means of pneumatic injection
IT1163795B (en) * 1983-07-18 1987-04-08 Montedison Spa APPARATUS FOR THE STRIPPING OF AMMONIA FROM SOLUTIONS COMING FROM THE SYNTHESIS OF UREA
US5230742A (en) * 1987-02-02 1993-07-27 A. E. Staley Manufacturing Co. Integrated process for producing crystalline fructose and high-fructose, liquid-phase sweetener
US5350456A (en) * 1987-02-02 1994-09-27 A. E. Staley Manufacturing Company Integrated process for producing crystalline fructose and a high fructose, liquid-phase sweetener
US5656094A (en) * 1987-02-02 1997-08-12 A.E. Staley Manufacturing Company Integrated process for producing crystalline fructose and a high-fructose, liquid phase sweetener
US5234503A (en) * 1987-02-02 1993-08-10 A.E. Saley Manufacturing Co. Integrated process for producing crystalline fructose and a high-fructose, liquid-phase sweetener
US5523064A (en) * 1994-11-02 1996-06-04 Swenson Process Equipment, Inc., A Delaware Corp. Crystallization apparatus
US7731822B2 (en) * 2004-02-19 2010-06-08 Smith Strom W High capacity angled tower
EP2308576B1 (en) * 2009-09-25 2015-11-04 Stefan Ebner Vaporiser
US9732068B1 (en) 2013-03-15 2017-08-15 GenSyn Technologies, Inc. System for crystalizing chemical compounds and methodologies for utilizing the same

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE77205C (en) * G. HEYDECKE, Meine, Hann Process for conveying the crystallization out of the sugar from the filling masses of the sugar factories and refineries, called foam crystallization
DE115256C (en) *
DE90071C (en) * 1896-02-16 1897-01-06
US880629A (en) * 1907-06-14 1908-03-03 C Christianson Harry Method of crystallizing sugar.
FR524427A (en) * 1915-01-04 1921-09-03 Leon Naudet Method and device for the evaporation of sweet juices
NL10124C (en) * 1918-12-24
US1860741A (en) * 1927-02-14 1932-05-31 Jeremiassen Finn Crystallization apparatus
US1945281A (en) * 1930-05-15 1934-01-30 Koppers Co Delaware Evaporating apparatus
US2042488A (en) * 1932-08-12 1936-06-02 Chem Ind Basel Process for evaporating liquids
US2426839A (en) * 1943-05-29 1947-09-02 Alexander B Morris Method and apparatus for cleaning or grading sand or the like
FR1104869A (en) * 1954-05-14 1955-11-24 Fr De Const Mecaniques Soc Cooking device, continuously operating, variable speed and adjustable for crystallization of sweet solutions
DE1148524B (en) * 1957-04-01 1963-05-16 Gerhard Weidenfeld Standing evaporator with self-regulating liquid flow
FR81168E (en) * 1962-02-14 1963-08-09 Improvements to boilers, evaporators and boilers

Also Published As

Publication number Publication date
US3505111A (en) 1970-04-07
NL6501748A (en) 1965-08-16
CH440175A (en) 1967-07-15
FR86441E (en) 1966-02-04
DE1300880B (en) 1969-08-07
FR1393567A (en) 1965-03-26

Similar Documents

Publication Publication Date Title
ES308623A1 (en) Process and device for the continuous concentration-crystallization of sugar syrups
GB1415699A (en) Evaporative method
ES289247A1 (en) An apparatus to cause a heat exchange between very fine particles and a gas (Machine-translation by Google Translate, not legally binding)
ES351087A1 (en) Crystallization method and device
Elliot et al. LABORATORY STUDIES IN THE THERMAL BAR
GB1445354A (en) Process and apparatus for concentrating a dilute solution of corrosive products
ES306649A1 (en) A procedure for continuous recovery of p-xylene from liquid mixtures containing p-xylene. (Machine-translation by Google Translate, not legally binding)
GB911638A (en) Separation of at least one component from a mixture of substances
GB630884A (en) Improvements in and relating to the absorption and separation of vapours and gases
CH377784A (en) Device for evenly removing liquid from column trays
ES386356A1 (en) Continuous process for crystallization
GB1135063A (en) Process for the purification of malic acid
SE334429B (en)
GB1111207A (en) Purification of dimethyl sulphoxide
Tamura et al. Nutritional Studies on Chlorella VII Digestibility of the Protein of Chlorella in Vitro
GB1090273A (en) An improved boiling process and apparatus for producing crystals in mother liquors
GB1079429A (en) A process for purifying impure acrolein
FR1280904A (en) Device for degassing liquids by the degassing process with circulation of the liquid
SU142988A1 (en) Continuous heating apparatus for heating crushed starch raw materials
SU506803A1 (en) Device for heat press zromatography
ES375194A1 (en) Method and apparatus for distilling liquid. (Machine-translation by Google Translate, not legally binding)
GB884617A (en) Evaporator for producing a supersaturated solution
FR1264970A (en) Fruit juice concentration process
GB1061708A (en) An evaporator crystalliser,particularly for use in the sugar industry
BE592572A (en) Process and apparatus for preserving fruit juices in tanks