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AR240862A2 - Un procedimiento y un aparato de fabricacion de un condimento. - Google Patents

Un procedimiento y un aparato de fabricacion de un condimento.

Info

Publication number
AR240862A2
AR240862A2 AR30597686A AR30597686A AR240862A2 AR 240862 A2 AR240862 A2 AR 240862A2 AR 30597686 A AR30597686 A AR 30597686A AR 30597686 A AR30597686 A AR 30597686A AR 240862 A2 AR240862 A2 AR 240862A2
Authority
AR
Argentina
Prior art keywords
condiment
sequariar
manufacture
hydrolyzed
comprised
Prior art date
Application number
AR30597686A
Other languages
English (en)
Other versions
AR240862A1 (es
Original Assignee
Maggi 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 Maggi Ag filed Critical Maggi Ag
Application granted granted Critical
Publication of AR240862A1 publication Critical patent/AR240862A1/es
Publication of AR240862A2 publication Critical patent/AR240862A2/es

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L27/00Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/10Natural spices, flavouring agents or condiments; Extracts thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S203/00Distillation: processes, separatory
    • Y10S203/19Sidestream

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Seasonings (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PROCEDIMIENTO PARA PREPARAR UN CONDIMENTO SUSTANCIALMENTE LIBRE DE CLORHIDRINAS, EN ESPECIAL DEL DICLORO-1, 3-PROPANOL-2, QUE COMPRENDE HIDROLIZAR PROTEINAS VEGETALES CON ACIDO CLORHIDRICO CONCENTRADO NEUTRALIZAR DICHO HIDROLIZADO Y SEPARAR LOS PRIMEROS INSOLUBLES, DEJAR REPOSAR Y SEPARAR LOS SEGUNDOS INSOLUBLES, DESTILAR CON VAPOR DICHO HIDROLIZADO BAJO UNA PRESION REDUCIDA COMPRENDIDA ENTRE 100 Y 320 MBAR, A UNA TEMPERATURA COMPRENDIDA ENTRE 40 Y 70{C, MANTENIENDO DURANTE LA OPERACION DE DESTILACION LA DENSIDAD DEL HIDROLIZADO ENTRE 1,250 Y 1,265 G/CM3.
AR305976A 1985-11-25 1986-11-21 Un procedimiento y un aparato de fabricacion de un condimento. AR240862A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH5013/85A CH668163A5 (fr) 1985-11-25 1985-11-25 Procede de fabrication d'un condiment.

Publications (2)

Publication Number Publication Date
AR240862A1 AR240862A1 (es) 1991-03-27
AR240862A2 true AR240862A2 (es) 1991-03-27

Family

ID=4286435

Family Applications (1)

Application Number Title Priority Date Filing Date
AR305976A AR240862A1 (es) 1985-11-25 1986-11-21 Un procedimiento y un aparato de fabricacion de un condimento.

Country Status (29)

Country Link
US (2) US4759944A (es)
EP (1) EP0226769B1 (es)
JP (1) JPH0614847B2 (es)
KR (1) KR910002663B1 (es)
CN (1) CN1019732B (es)
AR (1) AR240862A1 (es)
AT (1) ATE52892T1 (es)
AU (1) AU590352B2 (es)
BR (1) BR8605889A (es)
CA (1) CA1307972C (es)
CH (1) CH668163A5 (es)
DD (1) DD252535A5 (es)
DE (1) DE3671355D1 (es)
DK (1) DK163952C (es)
ES (1) ES2015249B3 (es)
FI (1) FI86684C (es)
GB (1) GB2183659B (es)
GR (1) GR3000629T3 (es)
IE (1) IE59094B1 (es)
IN (1) IN164293B (es)
MX (1) MX168697B (es)
MY (1) MY100339A (es)
NO (1) NO169042C (es)
NZ (1) NZ218386A (es)
OA (1) OA08489A (es)
PT (1) PT83802B (es)
RU (1) RU1773229C (es)
YU (2) YU43902B (es)
ZA (1) ZA868667B (es)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE68910771T2 (de) * 1988-09-26 1994-03-31 Unilever Nv Verfahren zur Herstellung von verbessertem Proteinhydrolysat.
ES2034593T3 (es) * 1988-09-26 1993-04-01 Unilever N.V. Procedimiento para la preparacion de proteinas hidrolizadas mejoradas.
DE68905561T2 (de) * 1988-09-26 1993-07-29 Unilever Nv Verfahren zur herstellung von verbessertem proteinshydrolysat.
US5102987A (en) * 1988-10-14 1992-04-07 Nestec S.A. Preparation of hydrolyzed protein having reduced α-chlorohydrin content
DE68901456D1 (de) * 1989-02-03 1992-06-11 Nestle Sa Verfahren zur herstellung eines gewuerzmittels.
US4944953A (en) * 1989-05-19 1990-07-31 A. E. Staley Manufacturing Company Purification of hydrolysed protein with crystalline zeolite
CA2020461A1 (en) * 1989-07-14 1991-01-15 Donald J. Hamm Process for the production of hydrolyzed vegetable proteins and the product therefrom
IT1238663B (it) * 1989-10-24 1993-09-01 Panzani Ponte Liebig S P A Procedimento di idrolisi acida di proteine vegetali per la produzione di estratto proteico con basso tenore in 3 monocloropropandiolo e con 1,2 dicloropropanolo in quantita' non rilevabile.
USH989H (en) 1990-07-13 1991-11-05 A. E. Staley Manufacturing Co. Purification of hydrolyzed protein by extraction
US5151503A (en) * 1991-03-28 1992-09-29 Nestec S.A. Process for reducing hydrolysed protein chlorohydrin content
CA2066378C (en) * 1991-04-24 2000-09-19 David J. Hardman Dehalogenation of organohalogen-containing compounds
US5532389A (en) * 1993-11-23 1996-07-02 The Dow Chemical Company Process for preparing alkylene oxides
US5972691A (en) * 1995-06-07 1999-10-26 Hercules Incorporated Dehalogenation of polyamine, neutral curing wet strength resins
FR2779447A1 (fr) * 1998-06-04 1999-12-10 Angevine Biotech Production d'hydrolysats de proteines vegetales
AU1525301A (en) * 1999-12-02 2001-06-12 Dsm N.V. Process for preparing improved protein hydrolysates
FR2817547B1 (fr) * 2000-12-01 2003-08-22 Total Raffinage Distribution Procede et dispositif pour le traitement en continu d'eaux usees d'origine industrielle par strippage a la vapeur d'eau
JP7541406B1 (ja) * 2023-09-14 2024-08-28 株式会社コスモテック 蒸留処理装置

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2251771A (en) * 1939-06-17 1941-08-05 Mid Continent Petroleum Corp Method of and apparatus for selecting fractions from fractionating condensers
US2364341A (en) * 1941-04-24 1944-12-05 Eastman Kodak Co Distillation control
DE1057437B (de) * 1953-08-20 1959-05-14 Tech Art Inc Maschine zum Falten von Schachtelzuschnitten
US2873799A (en) * 1956-01-09 1959-02-17 Allied Chem Method and apparatus for dehydrating aqueous caustic solutions
DE1057435B (de) * 1956-11-12 1959-05-14 C H Knorr A G Verfahren zum Entfernen von ueberschuessiger Salzsaeure bei der Eiweisshydrolyse
US2991309A (en) * 1957-12-30 1961-07-04 Internat Minerals & Chemicals Protein hydrolysis
DE1159901B (de) * 1959-09-16 1963-12-27 Leybold Hochvakuum Anlagen Vorrichtung zur fraktionierenden Destillation unter Vakuum
US3322650A (en) * 1964-01-03 1967-05-30 Phillips Petroleum Co Control of ratio of rate of heat flow to rate of feed in distillation responsive to bottoms analysis
US3503854A (en) * 1967-08-22 1970-03-31 Blaw Knox Co Dual stage steam stripping of vegetable oils at dual pressures
US3458404A (en) * 1967-12-11 1969-07-29 Shell Oil Co Apparatus for distilling liquids
US3542653A (en) * 1968-04-22 1970-11-24 Procter & Gamble Apparatus and process for continuous heat-bleaching and high temperature steam deodorization of edible oils
AU441069B2 (en) * 1968-04-24 1973-10-03 Blaw-Knox Company Process and apparatus for removing the remaining volatile substances from plant materials
US3692538A (en) * 1970-07-14 1972-09-19 Mayer & Co Inc O Method of preparing meaty-flavored protein hydrolyzates from meat carcass components
US3660247A (en) * 1970-07-31 1972-05-02 Du Pont Process and apparatus for controlling with a computer a distillation column product and heat fluid rates of flow
DE2212816C3 (de) * 1972-03-16 1974-12-12 Wiegand Karlsruhe Gmbh, 7505 Ettlingen Vorrichtung zur gleichmäßigen Verteilung einzudampfender Flüssigkeit in einem Fallstromverdampfer
US3952109A (en) * 1973-02-13 1976-04-20 Far-Mar-Co., Inc. Low salt protein hydrolyzates
CH602023A5 (es) * 1975-08-26 1978-07-14 Maggi Ag
US4194017A (en) * 1975-08-26 1980-03-18 Societe D'assistance Technique Pour Produits Nestle S.A. Flavored bouillon base
US4342624A (en) * 1976-04-05 1982-08-03 Eaton Corporation Vapor compression liquid treating system
US4165391A (en) * 1976-06-08 1979-08-21 Stauffer Chemical Company Agent for providing meaty flavor in foods
CH620347A5 (es) * 1977-03-17 1980-11-28 Maggi Ag
SU725684A1 (ru) * 1978-01-09 1980-04-05 Предприятие П/Я В-8296 Устройство дл автоматического управлени процессом ректификации
DE2914101A1 (de) * 1979-04-07 1980-10-23 Schmidding Wilh Gmbh & Co Verfahren zum desodorieren und/oder entsaeuern von hochsiedenden organischen verbindungen, insbesondere von speiseoelen
JPS6038001A (ja) * 1983-08-09 1985-02-27 Nippon Zeon Co Ltd 蒸溜塔の制御方法
US4731175A (en) * 1986-07-07 1988-03-15 Phillips Petroleum Company Preheat control for a fractional distillation process

Also Published As

Publication number Publication date
EP0226769A1 (fr) 1987-07-01
NZ218386A (en) 1989-04-26
PT83802B (pt) 1989-05-12
GR3000629T3 (en) 1991-09-27
AU6518186A (en) 1987-05-28
PT83802A (fr) 1986-12-01
GB2183659A (en) 1987-06-10
YU43902B (en) 1989-12-31
BR8605889A (pt) 1987-08-25
CN1019732B (zh) 1992-12-30
FI864489L (fi) 1987-05-26
DK562486A (da) 1987-05-26
KR910002663B1 (ko) 1991-05-03
YU47048B (sh) 1994-12-28
DK163952C (da) 1992-09-21
MY100339A (en) 1990-08-28
AR240862A1 (es) 1991-03-27
DK163952B (da) 1992-04-27
CA1307972C (en) 1992-09-29
RU1773229C (ru) 1992-10-30
EP0226769B1 (fr) 1990-05-23
JPH0614847B2 (ja) 1994-03-02
YU201486A (en) 1988-04-30
FI86684C (fi) 1992-10-12
DK562486D0 (da) 1986-11-24
KR870004665A (ko) 1987-06-01
NO169042B (no) 1992-01-27
US4759944A (en) 1988-07-26
OA08489A (fr) 1988-07-29
ES2015249B3 (es) 1990-08-16
YU112587A (en) 1988-08-31
GB2183659B (en) 1989-11-22
DE3671355D1 (de) 1990-06-28
CN86107674A (zh) 1987-06-10
FI864489A0 (fi) 1986-11-05
NO169042C (no) 1992-05-06
GB8627515D0 (en) 1986-12-17
US4869785A (en) 1989-09-26
AU590352B2 (en) 1989-11-02
CH668163A5 (fr) 1988-12-15
MX168697B (es) 1993-06-04
ATE52892T1 (de) 1990-06-15
ZA868667B (en) 1987-06-24
NO864697D0 (no) 1986-11-24
DD252535A5 (de) 1987-12-23
JPS62224256A (ja) 1987-10-02
FI86684B (fi) 1992-06-30
IN164293B (es) 1989-02-11
IE862985L (en) 1987-05-25
IE59094B1 (en) 1994-01-12

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