SE417328B - PROCEDURE FOR THE DEODORIZATION OF COCOA MOTHER IN A THIN LAYER INDUSTRIES WHICH WERE FAT CONTINUOUSLY CONTINUOUSLY HOMOGENIZED TOGETHER WITH DEONIZED OR DISTILLED WATER - Google Patents

PROCEDURE FOR THE DEODORIZATION OF COCOA MOTHER IN A THIN LAYER INDUSTRIES WHICH WERE FAT CONTINUOUSLY CONTINUOUSLY HOMOGENIZED TOGETHER WITH DEONIZED OR DISTILLED WATER

Info

Publication number
SE417328B
SE417328B SE7800463A SE7800463A SE417328B SE 417328 B SE417328 B SE 417328B SE 7800463 A SE7800463 A SE 7800463A SE 7800463 A SE7800463 A SE 7800463A SE 417328 B SE417328 B SE 417328B
Authority
SE
Sweden
Prior art keywords
continuously
cocoa butter
evaporator
thin
deodorization
Prior art date
Application number
SE7800463A
Other languages
Swedish (sv)
Other versions
SE7800463L (en
Inventor
K-E P Thuren
Original Assignee
Fazer Ab
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 Fazer Ab filed Critical Fazer Ab
Priority to SE7800463A priority Critical patent/SE417328B/en
Priority to GB791256A priority patent/GB2012801B/en
Priority to DE19792901093 priority patent/DE2901093A1/en
Priority to NL7900316A priority patent/NL7900316A/en
Publication of SE7800463L publication Critical patent/SE7800463L/en
Publication of SE417328B publication Critical patent/SE417328B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B3/00Refining fats or fatty oils
    • C11B3/12Refining fats or fatty oils by distillation
    • C11B3/14Refining fats or fatty oils by distillation with the use of indifferent gases or vapours, e.g. steam

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Confectionery (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Dairy Products (AREA)

Description

7v80Q463-? ett deodoriserat kakaosmör, som kontinuerligt avlägsnas från tunnskiktsindunstaren. 7v80Q463-? a deodorized cocoa butter, which is continuously removed from the thin layer evaporator.

Vid förfarandet enligt uppfinningen homogeniseras kakao- smör kontinuerligt tillsammans med ca 10 vikt% destillerat eller avjoniserat vatten vid 65fl5°C. Detta homogenisat drives i ett tunt skikt av ca O,l mm genom en tunnskiktsindunstare under ett vakuum av ca 10-30 mm Hg och ett ångtryck av ca 2-3 atm.In the process of the invention, cocoa butter is continuously homogenized together with about 10% by weight of distilled or deionized water at 65 ° C. This homogenate is driven in a thin layer of about 0.1 mm through a thin layer evaporator under a vacuum of about 10-30 mm Hg and a vapor pressure of about 2-3 atm.

Vid passagen genom indunstaren avgår, förutom vatten, de flyktiga ämnensom skall avlägsnas för erhållande av deodoriserat kakaosmör. Driftsparametrarna är inte kritiska för förfarandet, men de ovan angivna_värdena är de som för närvarande anses ge de bästa resultaten. Vid en föredragen utföringsform av uppfinningen erhålles 4 liter av produkten per minut, och förlusterna är endast 0,3 %, vilket skall jämföras med ca 1,5 % förluster för det kända satsvisa förfarandet. Fördelarna med etta kontinuerliga förfarande är uppenbara.In the passage through the evaporator, in addition to water, the volatile substances are removed which must be removed to obtain deodorized cocoa butter. The operating parameters are not critical to the process, but the above values are the ones currently considered to give the best results. In a preferred embodiment of the invention, 4 liters of the product are obtained per minute, and the losses are only 0.3%, which is to be compared with about 1.5% losses for the known batch process. The advantages of this continuous process are obvious.

Produkten utsättas under en mycket kort tid (bråkdelen av en sekund) för'förhöjd temperatur, varför man undviker försämring av produkten genom bl a ökat peroxidtal. I och med att vattnet redan från början är jämnt fördelat 1 råvaran, när den upphettas i vakuum, kommer alla delar av den under behandling varande rå- varan att väsentligen samtidigt utsättas för ångdestillation, så att man erhåller en produkt med mycket jämn sammansättning.The product is exposed for a very short time (fraction of a second) to elevated temperature, so that deterioration of the product is avoided by, among other things, increased peroxide numbers. Since the water is evenly distributed in the raw material from the beginning, when it is heated in vacuum, all parts of the raw material under treatment will be subjected to steam distillation substantially simultaneously, so that a product with a very even composition is obtained.

Förlusterna av de naturligt förekommande antioxidationsmedlen, tokoferolerna, främst u-tokoferol, är ringa på grund av den synnerligen korta värmebehandlingstiden.The losses of the naturally occurring antioxidants, the tocopherols, mainly u-tocopherol, are small due to the extremely short heat treatment time.

Allmänt kan sägas att föreliggande uppfinning åstadkommer ett skonsamt, snabbt och smidigt sätt att deodorisera kakaosmör i anslutning till övriga kakao- och chokladtillverkning.In general it can be said that the present invention provides a gentle, fast and flexible way of deodorizing cocoa butter in connection with other cocoa and chocolate production.

Uppfinningen skall nu närmare beskrivas, och för att under- lätta förståelsen har ett blockschema bifogats.The invention will now be described in more detail, and in order to facilitate understanding, a block diagram has been attached.

Först renas råvaran genom att den filtreras i ett platt- filter, varefter den pumpas till ett mätkärl med bladomrörare, där ca 200 kg av det filtrerade kakaosmöret förblandas med ca 20 kg avjoniserat eller destillerat vatten. Denna blandning leds sedan till nästa kärl med turbomixomröring för homogenisering och föruppvärmning. Efter en temperaturjustering pumpas det förupp- värmda homogenisatet medelst en kontinuerlig doseringspump till. 'en tunnskiktsindunstare, vars driftsparametrar justeras till lämpliga värden med avseende pâ skikttjocklek, vakuum, ångtryckFirst, the raw material is purified by filtering it in a plate filter, after which it is pumped to a measuring vessel with a stirrer, where about 200 kg of the filtered cocoa butter is premixed with about 20 kg of deionized or distilled water. This mixture is then passed to the next vessel with turbomix stirring for homogenization and preheating. After a temperature adjustment, the preheated homogenate is pumped by means of a continuous dosing pump. a thin-layer evaporator, the operating parameters of which are adjusted to appropriate values with respect to layer thickness, vacuum, vapor pressure

Claims (3)

1. 78ÛO¿163~7 och temèeratur. Den använda indunstningsanordningen,~Liprocæherm- -Evaporator, har beskrivits i US-patent 3 921 709. Från tunn- skiktsindunstaren avgår det kondenserade ångor med de ämnen, främst pyrroler och pyraziner, som skall avlägsnas vid deodori- seringen. Den deodoriserade produkten, som avlägsnas från tunn- skiktsindunstaren, är helt fri från vatten och är av hög kvali- tet, varför den direkt kan användas vid exempelvis chokladfram- ställning. Uppfinningen skall nu närmare beskrivas med hänvisning till ett konkret utföringsexempel. EXEMPEL 100 kg filtrerat kakaosmör, pressmör, med ett aromindex av 50-70 enligt W Rostagno et al (Rev. Int. Choc. (RIC) 25 (1970) lO, oktober) homogeniserades tillsammans med lOil,0 kg avjoni- serat vatten vid 60i5°C. Homogenisatet inmatades med en doserings- pump i den ovan angivna deodoriseringsanordningen (Lipro-Therm- -Evaporator). Ångtrycket i anordningen justerades till 2,5i0,3 atm, vakuumet till 10-30 mm Hg och rotationshastigheten till 1000-1500 r/min. Beroende på inmatningshastigheten erhölls deodoriserat kakaosmör av olika deodoriseringsgrad, och uttryckt som aromindex var värdena från 6,5 till 15,0. PATENTKRAV l. Förfarande för kontinuerlig deodorisering av kakaosmör medelst ånga under förhöjt tryck och förhöjd temperatur i vakuum, k ä n n e t e c k n a t därav, att kakaosmöret kontinuerligt homogeniseras tillsammans med avjoniserat eller destillerat vat- ten till ett homogenisat, vilket i ett kontinuerligt förlopp ut- sättes för ångdestillation i en tunnskiktsindunstare för avdriv- ning av vattnet och flyktiga aromämnen och för bildande av ett deodoriserat kakaosmör, som kontinuerligt avlägsnas från tunn- skiktsindunstaren.1. 78ÛO¿163 ~ 7 and temèeratur. The evaporation device used, Liprocæherm -Evaporator, has been described in U.S. Pat. The deodorized product, which is removed from the thin-layer evaporator, is completely free of water and is of high quality, which is why it can be used directly in, for example, chocolate production. The invention will now be described in more detail with reference to a concrete embodiment. EXAMPLE 100 kg of filtered cocoa butter, press butter, with an aroma index of 50-70 according to W Rostagno et al (Rev. Int. Choc. (RIC) 25 (1970) 10, October) was homogenized together with 10 60 ° C. The homogenate was fed with a dosing pump into the above-mentioned deodorizer (Lipro-Therm-Evaporator). The vapor pressure in the device was adjusted to 2.5i0.3 atm, the vacuum to 10-30 mm Hg and the rotational speed to 1000-1500 r / min. Depending on the feed rate, deodorized cocoa butter of different degrees of deodorization was obtained, and expressed as aroma index, the values were from 6.5 to 15.0. CLAIM 1. A process for the continuous deodorization of cocoa butter by means of steam under elevated pressure and elevated temperature in vacuum, characterized in that the cocoa butter is continuously homogenized together with deionized or distilled water to a homogenized, which in a continuous process is subjected to steam distillation in a thin-film evaporator to evaporate the water and volatile flavorings and to form a deodorized cocoa butter, which is continuously removed from the thin-layer evaporator. 2. Förfarande enligt kravet l, k ä n n e t e c k n a t där- av, att det avjoniseradeealler destillerade vattnet inblandas i en mängd av lOÉl,0 vikt%, beräknat på homogenisatet.2. A process according to claim 1, characterized in that the deionized or distilled water is mixed in an amount of 10 000, 0% by weight, calculated on the homogenate. 3. Förfarande enligt kravet 1 eller 2, k ä n n e t e c k - n a t därav, att tunnskiktsindunstningen utföres vid ett ång- 4 Manas-v tryck av 2,5i0,5 atm, en temperatur av 65il5°C och ett vakuum av 10-30 mm Hg. ~ ANFÖRDÅ PUBLIKATIONER: Sverige putentunsökun 7410267-4 US 3 921 709 (165-88) Andra publikationer: Fette-Seifen-Anstrichmittel 64 Jahrgang, Nr 2, 1962 p. 145-1503. A process according to claim 1 or 2, characterized in that the thin-layer evaporation is carried out at a vapor pressure of 2.5 x 0.5 atm, a temperature of 65 ° C and a vacuum of 10-30 mm. Hg. ~ BEFORE PUBLICATIONS: Sweden putentunsökun 7410267-4 US 3 921 709 (165-88) Other publications: Fette-Seifen-Anstrichmittel 64 Jahrgang, Nr 2, 1962 p. 145-150
SE7800463A 1978-01-16 1978-01-16 PROCEDURE FOR THE DEODORIZATION OF COCOA MOTHER IN A THIN LAYER INDUSTRIES WHICH WERE FAT CONTINUOUSLY CONTINUOUSLY HOMOGENIZED TOGETHER WITH DEONIZED OR DISTILLED WATER SE417328B (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
SE7800463A SE417328B (en) 1978-01-16 1978-01-16 PROCEDURE FOR THE DEODORIZATION OF COCOA MOTHER IN A THIN LAYER INDUSTRIES WHICH WERE FAT CONTINUOUSLY CONTINUOUSLY HOMOGENIZED TOGETHER WITH DEONIZED OR DISTILLED WATER
GB791256A GB2012801B (en) 1978-01-16 1979-01-12 Continuous deodorization of cocoa butter in thin layers
DE19792901093 DE2901093A1 (en) 1978-01-16 1979-01-12 PROCESS FOR CONTINUOUS DEODORIZATION OF COCOA BUTTER IN A THIN FILM EVAPORATOR
NL7900316A NL7900316A (en) 1978-01-16 1979-01-15 PROCEDURE FOR CONTINUOUSLY DEODORIZING COCOA BUTTER IN A THIN-LAYER EVAPORATOR.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE7800463A SE417328B (en) 1978-01-16 1978-01-16 PROCEDURE FOR THE DEODORIZATION OF COCOA MOTHER IN A THIN LAYER INDUSTRIES WHICH WERE FAT CONTINUOUSLY CONTINUOUSLY HOMOGENIZED TOGETHER WITH DEONIZED OR DISTILLED WATER

Publications (2)

Publication Number Publication Date
SE7800463L SE7800463L (en) 1979-07-17
SE417328B true SE417328B (en) 1981-03-09

Family

ID=20333674

Family Applications (1)

Application Number Title Priority Date Filing Date
SE7800463A SE417328B (en) 1978-01-16 1978-01-16 PROCEDURE FOR THE DEODORIZATION OF COCOA MOTHER IN A THIN LAYER INDUSTRIES WHICH WERE FAT CONTINUOUSLY CONTINUOUSLY HOMOGENIZED TOGETHER WITH DEONIZED OR DISTILLED WATER

Country Status (4)

Country Link
DE (1) DE2901093A1 (en)
GB (1) GB2012801B (en)
NL (1) NL7900316A (en)
SE (1) SE417328B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5174956A (en) * 1989-04-26 1992-12-29 Suntory Limited Method for deodorization of cork
PT93857B (en) * 1989-04-26 1996-10-31 Suntory Ltd PROCESS AND APPARATUS FOR CORODE DEODORIZATION
JP3844513B2 (en) * 1992-02-20 2006-11-15 株式会社Adeka Oil composition for confectionery and method for producing the same

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1737731A (en) * 1925-02-14 1929-12-03 Rogstone Chemical Res Inc Method of deodorizing animal and vegetable oils
US2478089A (en) * 1945-10-10 1949-08-02 Clayton Benjamin Process of refining glyceride oils

Also Published As

Publication number Publication date
GB2012801A (en) 1979-08-01
DE2901093A1 (en) 1979-07-19
SE7800463L (en) 1979-07-17
NL7900316A (en) 1979-07-18
GB2012801B (en) 1982-07-21

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