CS210229B1 - A method for producing low-glued swelling starches - Google Patents
A method for producing low-glued swelling starches Download PDFInfo
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- CS210229B1 CS210229B1 CS197280A CS197280A CS210229B1 CS 210229 B1 CS210229 B1 CS 210229B1 CS 197280 A CS197280 A CS 197280A CS 197280 A CS197280 A CS 197280A CS 210229 B1 CS210229 B1 CS 210229B1
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Abstract
Spúaob výroby nizkoštlepených bobtnavých škrobov. Účelom vynálezu je epdaob výroby tepelne upravených škrobov a obilných atik enzýbovou úpravou* K auapenzii škrobov alebo obilných núk vo vodě alebo v nlleku ea po úprava hodndt pH přidá bakteriálna alfa-anyláza v nnožetve zabezpečujúcom požadovaný stupeň štiepenie škrobov. Súčasné nazovatenia a štiepenie škrobov prebieha na válcovéj súšiarni. Sin ea zlake výrobok požadovaných vlastnosti. Suapanziu nožno obohatit chloridon sodným a aacharózou. Výrobok je vhodný ako zahueťovadlo a enulgačnýni účinkanl pre potravinářské výrobky a ako prieada do pekárenských výrobkov.Method for the production of low-digestible swelling starches. The purpose of the invention is to produce heat-treated starches and cereal grains by enzymatic treatment. Bacterial alpha-anylase is added to a suspension of starches or cereal grains in water or in a solution after adjusting the pH value in an amount ensuring the desired degree of starch digestion. Simultaneous digestion and starch digestion take place in a roller dryer. The product has the desired properties. The suspension can be enriched with sodium chloride and acarose. The product is suitable as a thickener and emulsifying agent for food products and as an additive to bakery products.
Description
Predmetom vynálezu je apdaob výroby nlzkoStlepaných bobtnavých Skrobov anzýmovým postupom tak, to do vodnaj auspenzle Skrobov chemicky neupravených, slaťováných, oxidovaných, alabo do auepenzla obilných aúk aa přidá po úprava pH alfa-amyléza v množstva 60-18 500 jednotiek daxtrlnačnaj aktivity na 1 kg auSiny Škrobu, auepenzla aa dopraví na valcovú auSlaraň, na ktorej Škrob znazovatie, čiastočne aa naStlapí, uauSl a 3alaJ aa hotový produkt upravuje obvyklýn epčaoboa.The object of the present invention is to produce a low-shear swelling starch by an anzyse process, such as into an aqueous auspension of chemically untreated, molten, oxidized, or auepenzene cereal aukes, and adds 60-18,500 units of activity per liter of activity. The starch, auepenzla aa is conveyed to a cylindrical aulact, on which the starch marking, partially and a staggered, and a 3a, and the finished product is treated with the usual epcaoboa.
Oadnotka DA je množstvo enzýmu, ktoré za 1 mlnútu provedla 1 ag Škrobu na vysokomolakulérne dextriny.The DA is the amount of enzyme which has made 1 g of starch per millimeter per high molecular weight dextrin.
Takto získaná produkty aa použljú ako surovinová zložka pre pripravu instant potravin, napr. za studená pripravitelných pudingov, kráaov, zmrzlin ako glycldická alabo konziatenčné zložka, prlpravkov na zvýSenia stálosti chleba a pečivá, lepidiel, eaulgačných člnidiel apod.The products thus obtained are used as a raw material component for preparing instant foods, e.g. cold-prepared puddings, custards, ice creams as glycldic and / or consensus ingredients, bread and pastry enhancers, adhesives, eagling boats, etc.
Podlti doteraz znáaych poatupov aa prevádzala dagradácia Skrobov ako samostatný proces prad auSanlm, čo je alce velmi výhodná pri stradnom a hlbSom naStloponl Škrobu a Škrobových surovin, nevyhovuje vSak pra pripravu nízko naStiepaných Skrobov, ktorá eSte vykazujú značné vysokú vlakozitu mazov, ťažko aa tranaportujú, rozotlarajú a nanáSajú na valcovú euSiareň.According to previously known processes, and the degradation of Starches as a separate process of auSanlm, which is very advantageous for straddling and deepening of Starch and Starch raw materials, however, it does not suit the preparation of low-chopped Starch, which still has a high and applied to a cylindrical e-room.
Tento nedostatek odstraňuje nový postup podlá vynálezu, ktorý umožňuje lahků výrobu a požadovaným stupňom naStiepenia Škrobu. DalSou výhodou navrhovaného apAeobu jo jednoduché regulovateZnoať procesu dagradácia Škrobu a regulovatelnoeť výroby filmu, spojené ao zvýSenýa využitím tepelnáj energie auSania, zniženim lnvaetičných nákladov na plénovanú kapacitu, ako 1 znlženlm celkových výrobných nákladov.This drawback is overcome by the novel process according to the invention, which allows the bottles to be produced and the desired degree of starch cleavage. Another advantage of the proposed apAeob is the simple control of the starch degradation process and the control of film production, associated with and increased use of thermal energy and suction, by reducing the cost of the plenum capacity as a result of reducing the total cost of production.
Okrem toho navrhovaný apdaob výroby umožňuje na pripravu euapenzil okrem vody použltia mliaka a iných prlaad, ktoré ulahčujú mechanické spracovania usuSaného produktu, ako aú napr. chlorid sodný, aaeharóza a iné prlaady.In addition, the proposed production process allows the preparation of euapenzil in addition to water using milk and other additives which facilitate the mechanical processing of the dried product, such as e.g. sodium chloride, aaeharose, and other ingredients.
Přiklad 1Example 1
V narazovaj nádrži, ktoré mé obsah 1 500 litrov ea pripravl auapanzia z 600 litrov vody a 300 kg zamiakového Škrobu, pH ea upraví za atéleho mia&enla uhličitanem eodným na hodnotu 6,0, Do prlpravanaj auapanzia aa přidá anzýmový preparát alfa-amyléza v množstva 750 jednotiek OA na 1 kg euSlny Škrobu. Po dokonalen zhoaoganizoyanl aa Škrobové mlleko čerpá na valcovú auSlaraň. Tu dochádza k zmazovateniu, enzýnovénu Stiepeniu vytvořeného mazu a usuSanlu. Získaný uauSený film aa zrazuje a po rozdrtanl na préSok aa situja a balí.In an impact tank, which contains 1,500 liters of ea and prepared auapanzia from 600 liters of water and 300 kg of starch starch, pH ea is adjusted to 6.0 with sodium carbonate at the same time. To the prepared auapanzia aa adds anamyl preparation alpha-amylase in 750 units of OA per 1 kg of starch eu. After finished zhoaoganizoyanl aa Starch milk draws on the cylindrical auSlaran. Here, the lubrication, the enzyme cleavage of the sebum and the usuSanl are erased. The obtained, coated film aa is betrayed and after crushing to aa sieve and sieves and packs.
Přiklad 2Example 2
Oo narazovaj nádrži opatrenej alaSadlom aa napustí 750 litrov odstředěného mliaka.Oo impact the alaSadloma tank and fill 750 liters of skimmed milk.
Do allaka aa za stálého miaSanla přidá 200 kg alaťovaného kukuřičného Škrobu a hodnota pH sa upraví uhličitanem sodným na 5,6, Potom aa přidá 1 kg chloridu sodného a 60 kg rafinovaného cukru. Po dokonala] homogenlzécll následuje prldavok anzýmového preparátu alfa-amylézy v množstva 230 jednotiek OA na 1 kg auSiny Škrobu a auapanzia je vedené na valcovú auSlaraň. UsuSený produkt aa drti rta jemný préSok a balí.To allaca aa, while still stirring, add 200 kg of alated corn starch and adjust the pH to 5.6 with sodium carbonate. Then aa add 1 kg of sodium chloride and 60 kg of refined sugar. After complete homogenization, the addition of the alpha-amylase anzyme preparation was carried out in an amount of 230 OA units per kg of starch and the auapanzia was fed to a cylindrical aulaman. The dried product and crushed the fine powder and packs.
Příklad 3Example 3
V nádrži sa připraví suspenzia z 1 090 litrov vody a S8S kg pšenlčnaj hladkej aúky. Po úprava pH na 6,2 hydroxldoa sodným aa přidá anzýaový preparát alfa-aayláze v anožstve 12 000 jednotiek na 1 kg sušiny Škrobu. Zhoaogenizovaná suspenzia ea přečerpává na valcovú suilaren, kde ea usuší. Křehký film ea šnekoa dopravuje do drtiče e po sitovanl sa balí.A suspension is prepared in a tank of 1,090 liters of water and S8S kg of wheat smooth wheat. After adjusting the pH to 6.2 with sodium hydroxide aa, the α-alaselase anzyme preparation added 12,000 units per kg of starch dry matter. The homogenized suspension ea is pumped to a cylindrical suilarene where ea is dried. The fragile film ea is conveyed to the crusher after the screening is wrapped.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS197280A CS210229B1 (en) | 1980-03-22 | 1980-03-22 | A method for producing low-glued swelling starches |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS197280A CS210229B1 (en) | 1980-03-22 | 1980-03-22 | A method for producing low-glued swelling starches |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CS210229B1 true CS210229B1 (en) | 1982-01-29 |
Family
ID=5355464
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS197280A CS210229B1 (en) | 1980-03-22 | 1980-03-22 | A method for producing low-glued swelling starches |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS210229B1 (en) |
-
1980
- 1980-03-22 CS CS197280A patent/CS210229B1/en unknown
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