MX168697B - Procedimiento de fabricacion de un condimento - Google Patents

Procedimiento de fabricacion de un condimento

Info

Publication number
MX168697B
MX168697B MX004344A MX434486A MX168697B MX 168697 B MX168697 B MX 168697B MX 004344 A MX004344 A MX 004344A MX 434486 A MX434486 A MX 434486A MX 168697 B MX168697 B MX 168697B
Authority
MX
Mexico
Prior art keywords
hydrolyzate
head
column
insoluble
duct
Prior art date
Application number
MX004344A
Other languages
English (en)
Inventor
Roland Faesi
Giancarlo Werner
Ursula Wolfensberger
Original Assignee
Nestle Sa
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 Nestle Sa filed Critical Nestle Sa
Publication of MX168697B publication Critical patent/MX168697B/es

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • 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

La presente invención se refiere a procedimiento de fabricación de un condimento, en el que se hidrolizan proteínas vegetales con ácido clorhídrico concentrado, se neutraliza el hidrolizado, se separan los primeros insolubles, se le deja reposar y se separan los segundos insolubles caracterizado por el hecho de que despues de la separación de dichos primeros o dichos segundos insolubles, se somete al hidrolizado a una destilación al vapor bajo presión reducida a la vez que se mantiene la densidad del hidrolizado a un valor sensiblemtne constante, de fin de eliminar el dicloro-1-3-propano-2-ol. Aparato de destilación comprendiendo una columan de destilación (1) compeusta de un cabezal (4), un cuerpo cilíndrico (2) provisto de elementos de contacto (3), y un fondo (5); un dispositivo de bombeo de gas (8, 9) conectado a dicho cabezal; un conducto de introducción (7) del hidrolizado conectado a dicha columna entre dicho cuerpo y el citado cabezal; un conducto de inyección (6) de vapor conectado a dicha columna entre el citado fondo y dicho cuerpo, y un conducto de evacuación (10) del hidrolizado, conectado a dicho fondo, caracterizado por el hecho de que además comprende un dispositivo de regulación (11) de la temperatura del hidrolizado conectado a dicho conducto de introducción (7) y por el hecho de que el diámetro del citado cabezal (4) es sensiblemente mayor que el diámetro de dicho cuerpo (2).
MX004344A 1985-11-25 1986-11-13 Procedimiento de fabricacion de un condimento MX168697B (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 (1)

Publication Number Publication Date
MX168697B true MX168697B (es) 1993-06-04

Family

ID=4286435

Family Applications (1)

Application Number Title Priority Date Filing Date
MX004344A MX168697B (es) 1985-11-25 1986-11-13 Procedimiento 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 (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0361595B1 (en) * 1988-09-26 1993-11-18 Unilever N.V. Process for preparing improved hydrolysed protein
EP0361597B1 (en) * 1988-09-26 1993-03-24 Unilever N.V. Process for preparing improved hydrolysed protein
EP0361596B1 (en) * 1988-09-26 1992-08-05 Unilever N.V. Process for preparing improved hydrolysed protein
US5102987A (en) * 1988-10-14 1992-04-07 Nestec S.A. Preparation of hydrolyzed protein having reduced α-chlorohydrin content
ES2030923T3 (es) * 1989-02-03 1992-11-16 Societe Des Produits Nestle S.A. Procedimiento de fabricacion de un condimento.
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
WO2001039607A1 (en) * 1999-12-02 2001-06-07 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

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
DK163952B (da) 1992-04-27
GB2183659A (en) 1987-06-10
DK562486D0 (da) 1986-11-24
ATE52892T1 (de) 1990-06-15
YU201486A (en) 1988-04-30
FI86684B (fi) 1992-06-30
IE59094B1 (en) 1994-01-12
PT83802B (pt) 1989-05-12
KR910002663B1 (ko) 1991-05-03
DK562486A (da) 1987-05-26
OA08489A (fr) 1988-07-29
KR870004665A (ko) 1987-06-01
ZA868667B (en) 1987-06-24
ES2015249B3 (es) 1990-08-16
DD252535A5 (de) 1987-12-23
NZ218386A (en) 1989-04-26
YU47048B (sh) 1994-12-28
NO169042B (no) 1992-01-27
CA1307972C (en) 1992-09-29
GB2183659B (en) 1989-11-22
CN86107674A (zh) 1987-06-10
US4759944A (en) 1988-07-26
YU43902B (en) 1989-12-31
GR3000629T3 (en) 1991-09-27
EP0226769A1 (fr) 1987-07-01
IN164293B (es) 1989-02-11
CN1019732B (zh) 1992-12-30
JPS62224256A (ja) 1987-10-02
BR8605889A (pt) 1987-08-25
RU1773229C (ru) 1992-10-30
AU590352B2 (en) 1989-11-02
NO864697D0 (no) 1986-11-24
DK163952C (da) 1992-09-21
FI86684C (fi) 1992-10-12
FI864489A (fi) 1987-05-26
FI864489A0 (fi) 1986-11-05
AU6518186A (en) 1987-05-28
EP0226769B1 (fr) 1990-05-23
DE3671355D1 (de) 1990-06-28
US4869785A (en) 1989-09-26
JPH0614847B2 (ja) 1994-03-02
CH668163A5 (fr) 1988-12-15
GB8627515D0 (en) 1986-12-17
NO169042C (no) 1992-05-06
IE862985L (en) 1987-05-25
AR240862A1 (es) 1991-03-27
YU112587A (en) 1988-08-31
MY100339A (en) 1990-08-28
PT83802A (fr) 1986-12-01
AR240862A2 (es) 1991-03-27

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