DE2047504B2 - - Google Patents
Info
- Publication number
- DE2047504B2 DE2047504B2 DE2047504A DE2047504A DE2047504B2 DE 2047504 B2 DE2047504 B2 DE 2047504B2 DE 2047504 A DE2047504 A DE 2047504A DE 2047504 A DE2047504 A DE 2047504A DE 2047504 B2 DE2047504 B2 DE 2047504B2
- Authority
- DE
- Germany
- Prior art keywords
- pentosans
- extraction
- naoh
- bread
- temperature
- 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.)
- Granted
Links
Classifications
-
- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D2/00—Treatment of flour or dough by adding materials thereto before or during baking
- A21D2/08—Treatment of flour or dough by adding materials thereto before or during baking by adding organic substances
- A21D2/14—Organic oxygen compounds
- A21D2/18—Carbohydrates
- A21D2/183—Natural gums
-
- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D2/00—Treatment of flour or dough by adding materials thereto before or during baking
- A21D2/08—Treatment of flour or dough by adding materials thereto before or during baking by adding organic substances
- A21D2/14—Organic oxygen compounds
- A21D2/18—Carbohydrates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
- C08B37/0057—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Xylans, i.e. xylosaccharide, e.g. arabinoxylan, arabinofuronan, pentosans; (beta-1,3)(beta-1,4)-D-Xylans, e.g. rhodymenans; Hemicellulose; Derivatives thereof
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Molecular Biology (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Health & Medical Sciences (AREA)
- Compounds Of Unknown Constitution (AREA)
- Bakery Products And Manufacturing Methods Therefor (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Cosmetics (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Description
Zwar ist es auch bekannt (vgl. Zeitschrift »Chemi- untergetaucht liegen bleiben; das Extrakt ist zu »cb.es Zentralblatt «Bd. 137/1966, Nr. 4-3054), daß ein verwerfen. Danach wird das Ausgangsmaterial inIt is also known (see the journal »Staying under chemical conditions; the extract is closed "Cb.es Zentralblatt" vol. 137/1966, No. 4-3054) that a discard. Then the starting material is in
n_
10 n_
10
°48° 48
IVIV
bekannte Verfahren jedoch in gleicher Weise. kann auch in mehreren Stufen mit abnehmenderknown methods, however, in the same way. can also be in several stages with decreasing
Der Erfindung liegt die Aufgabe zugrunde, ein NaOH-Konzentration bis zur vollständigen Erschöp-The invention is based on the object of a NaOH concentration up to complete exhaustion
industriell anwendbares Verfahren zur Isolierung fung des Ausgangsmaterials durchgeführt werden.industrially applicable method for isolating fung of the starting material can be carried out.
wasserunlöslicher Pentosane mit wesentlich gesteigerter 65 Bei der Extraktion muß der pH-Wert zwischen 8 undwater-insoluble pentosans with significantly increased 65. During the extraction, the pH value must be between 8 and
Effektivität zu finden. 13, besser zwischen 11 und 12,5, gehalten werden.Find effectiveness. 13, better between 11 and 12.5, can be kept.
Die Erfindung besteht darin, daß die Extrahierung Es empfiehlt sich, die Extraktion in einer inertenThe invention consists in that the extraction It is advisable to carry out the extraction in an inert
der Pentosane bei einer Temperatur zwischen 53 und Atmosphäre durchzuführen. Die erhaltene Extrakt-perform the pentosans at a temperature between 53 and atmosphere. The extract obtained
phase ist abzugießen und gegebenenfalls bei zu hoher Viskosität zu verdünnen.phase must be poured off and, if necessary, diluted if the viscosity is too high.
Danach wird ungelöste Stärke aus der Extraktphase abzentrifugiert oder mittels eines adsorbierenden Materials, vorzugsweise aktive Holzkohle oder Steinwolle im alkalischen Milieu abfiltriert. Das Abfiltrieren kann auch nach Elektrodialysierung in neutralem Milieu erfolgen.After that, undissolved starch is made from the extract phase centrifuged or by means of an adsorbent material, preferably active charcoal or rock wool filtered off in an alkaline medium. The filtration can also be carried out after electrodialysis in neutral Environment.
Alsdann ist die Extraktphase bei einer Temperatur zwischen 20 und 1000C der Elektrodialyse zu unterwerfen, wobei das in der Extraktphase vorhandene Alkali entfernt wird. Bei der Elektrodialyse ist darauf zu achten, daß das pH nicht unter 6 sinkt Danach ist einzutrocknen, beispielsweise durch Zerstäubungstrocknung. The extract phase is then to be subjected to electrodialysis at a temperature between 20 and 100 ° C., the alkali present in the extract phase being removed. During electrodialysis, care must be taken that the pH does not drop below 6. Then it is dried, for example by spray drying.
Zur zumindest teilweisen Hydrolisierung von Proteinen kann die auf eine Konzentration von 1 bis 5 % gebrachte Extraktphase vor der Elektrodiaiysierung unter Stickstoff für zwei bis acht Stunden auf eine Temperatur von 80 bis 85° C erwärmt werden. Nach der Elektrodialysierung noch vorhandene hydrolisierte Proteine können durch Niederschlagen der Pentosane in Form von weißen Fasern mit Äthanol od. dgl. entfernt werden.For at least partial hydrolysis of proteins, the concentration of 1 to 5% brought extract phase to one under nitrogen for two to eight hours before electrodialysis Temperature of 80 to 85 ° C can be heated. Hydrolyzed ones still present after electrodialysis Proteins can od by precipitating the pentosans in the form of white fibers with ethanol. removed.
Claims (3)
Pentosane, weil die Extraktion der Pentosane minde- Das Ausgangsmaterial sollte zunächst einen halben »tens einen Monat dauert und die Effektivität der - . . -. ari ™™(,,,ηηκί,ΐΛ·η ;„ " Monu Pentosane unzureichend ist. 55 Tag ^ Zimmertemperatur (20 bis 30 C) in ^ NaOHwhen added to bread dough in an amount of starting materials for the production of water-1 or 2% to a B r otvolumenvergrößerung of insoluble pentosans are grasses or Gramineae, 6 or 7% and give a better crumb structure, ie, members of the grass family, whereby the overall better coloration and better freshness of the plant or only parts of the plant, such as. B. Broteo. This known method does not yet open up any grains, stems or stalks, leaves, roots, husks, economical presentation and use of these etc. can be used.
Pentosans, because the extraction of the pentosans min- The starting material should initially take half a month and the effectiveness of the -. . -. ari ™ Bäumen ( ,,, ηηκί, ΐΛ · η; „" Mo nu Pentosane is insufficient. 55 day ^ room temperature (20 to 30 C) in ^ NaOH
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
LU59598 | 1969-10-09 | ||
LU59598 | 1969-10-09 | ||
LU61573 | 1970-08-25 | ||
LU61573 | 1970-08-25 |
Publications (3)
Publication Number | Publication Date |
---|---|
DE2047504A1 DE2047504A1 (en) | 1971-06-16 |
DE2047504B2 true DE2047504B2 (en) | 1975-10-09 |
DE2047504C3 DE2047504C3 (en) | 1976-05-13 |
Family
ID=
Also Published As
Publication number | Publication date |
---|---|
EG10264A (en) | 1977-09-30 |
DK142853C (en) | 1981-09-28 |
AT315104B (en) | 1974-05-10 |
NL162917C (en) | 1980-07-15 |
NL162917B (en) | 1980-02-15 |
OA03491A (en) | 1971-03-30 |
RO58834A (en) | 1975-09-15 |
JPS5420581B1 (en) | 1979-07-24 |
SE386688B (en) | 1976-08-16 |
CS159781B2 (en) | 1975-01-31 |
NO136717B (en) | 1977-07-18 |
IL35326A0 (en) | 1971-04-28 |
DK142853B (en) | 1981-02-09 |
FI52593B (en) | 1977-06-30 |
CH520166A (en) | 1972-03-15 |
DE2047504A1 (en) | 1971-06-16 |
FI52593C (en) | 1977-10-10 |
NL7013792A (en) | 1971-04-14 |
IL35326A (en) | 1974-06-30 |
CA927826A (en) | 1973-06-05 |
IT1055515B (en) | 1982-01-11 |
NO136717C (en) | 1977-10-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE69622990T2 (en) | FLAT PROCESSING, ITS USE AND PRODUCTION | |
DE2908186A1 (en) | CHEWING GUM WITH A LIQUID, FLAVORED FILLING AND METHOD FOR THE PRODUCTION THEREOF | |
EP0387649A2 (en) | Process for making a soluble cacao product | |
DE1517335B1 (en) | Process for the manufacture of ribbon tobacco | |
DE2719297A1 (en) | EMULSIONS AND PROCESS FOR THEIR PRODUCTION | |
DE2751570A1 (en) | CARBOXYMETHYLATED BETA-1,3-GLUCANES, METHOD FOR MANUFACTURING THEREOF AND ANTITUMOR AGENTS | |
DE3855758T2 (en) | VEGETABLE RUBBER SUBSTANCE AND THEIR USE IN FOODSTUFFS | |
DE2822540A1 (en) | PROCESS FOR MANUFACTURING A NON-THYGROSCOPIC LACTULOSE POWDER | |
DE2047504C3 (en) | Process for the isolation of water-insoluble pentosans | |
DE2047504B2 (en) | ||
DE2251339A1 (en) | NEW TOBACCO COMPOSITION AND PROCESS FOR ITS MANUFACTURING | |
DD291469A5 (en) | METHOD FOR PRODUCING A LACTOPROTEIN-FREE, ENERGY-RELATED STRIP FAT | |
DE1517305C3 (en) | Process for the production of tobacco foils | |
DE2529088C3 (en) | Shaped articles of tobacco and process for their manufacture | |
DE1467970A1 (en) | Process for the production of anti-carcinogenic substances | |
DE582522C (en) | Toothpaste and process for making the same | |
DE652236C (en) | Treatment of plant phosphatides with alcohol and water | |
DE693333C (en) | r plants | |
DE906754C (en) | Process for the production of light- and heat-stable condensation products (acetals) of polyvinyl alcohol with aliphatic aldehydes | |
DE2546008A1 (en) | PROCESS FOR MANUFACTURING A FLAVORING AGENT | |
DE907293C (en) | Process for the preparation of polysulfuric acid esters and salts thereof | |
DE852938C (en) | Process for the treatment of grain germs and for the production of strengthening agents therefrom | |
DE2335251C3 (en) | Free-flowing and binder-free pentaerythritol tetranitrate and process for its production and its use for the production of detonating cords | |
DE2026626C3 (en) | 1 isopropenyl 2 benzoylacetylene and process for its preparation | |
DE10135060A1 (en) | Galactomannan with changed mannose to galactose ratio |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C3 | Grant after two publication steps (3rd publication) | ||
E77 | Valid patent as to the heymanns-index 1977 | ||
8339 | Ceased/non-payment of the annual fee |