CS231759B1 - Manufacturing process of steamed curd - Google Patents
Manufacturing process of steamed curd Download PDFInfo
- Publication number
- CS231759B1 CS231759B1 CS816776A CS677681A CS231759B1 CS 231759 B1 CS231759 B1 CS 231759B1 CS 816776 A CS816776 A CS 816776A CS 677681 A CS677681 A CS 677681A CS 231759 B1 CS231759 B1 CS 231759B1
- Authority
- CS
- Czechoslovakia
- Prior art keywords
- cheese
- curd
- steamed
- heated
- production
- Prior art date
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- 235000013351 cheese Nutrition 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 230000005484 gravity Effects 0.000 claims description 8
- 238000003801 milling Methods 0.000 claims description 5
- 238000009835 boiling Methods 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 238000004898 kneading Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 238000010025 steaming Methods 0.000 description 13
- 239000006188 syrup Substances 0.000 description 4
- 235000020357 syrup Nutrition 0.000 description 4
- 239000005862 Whey Substances 0.000 description 3
- 102000007544 Whey Proteins Human genes 0.000 description 3
- 108010046377 Whey Proteins Proteins 0.000 description 3
- 230000013011 mating Effects 0.000 description 3
- 240000002129 Malva sylvestris Species 0.000 description 2
- 235000006770 Malva sylvestris Nutrition 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 235000014121 butter Nutrition 0.000 description 1
- 235000021105 fermented cheese Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 235000014059 processed cheese Nutrition 0.000 description 1
- 229940108461 rennet Drugs 0.000 description 1
- 108010058314 rennet Proteins 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Dairy Products (AREA)
Description
Vynález rieši spósob výroby paren,ej syroviny na kontinuálnych zmaselňovačoch KM 1000, 2000, 3000 československej výroby. Takýmto sposobom spařená syrovina je použitá na výrobu pařených syrov vyrábaných v tuzemsku i v zahraničí.The invention solves a method of production of steam and cheese in continuous butter-making machines KM 1000, 2000, 3000 of Czechoslovak production. This kind of steamed cheese is used for the production of steamed cheeses produced in the Czech Republic and abroad.
Doposial používané zariadenie na parenie syroyiny je dovážané z Maďarska a Taliapska. Uvedené zariadenie dovážané z Maďarska má tú nevýhodu, že je nie vyhrievaný miesič syroviny a tým dochádza k rozdielnej konzistencii v syře a neštandardnej aikosti. Uvedené zariadenie dovážané z Táli,anska má tú nevýhodu, že pariaca horúca voda necirkuluje, ale s vyplaveným tukom a bielkovinou tečie do odpadu. Týmto sa zvyšuje i energetická spotřeba paliv na výrobu parenej syroviny. Nákup pariacich zariadení zo zahraničia zhoršuje platolbnú bilanciu zahraničného obchodu a tieto sú nižšieho nedostatečného výkonu.The syroyine steaming equipment used so far is imported from Hungary and Italy. The above-mentioned equipment imported from Hungary has the disadvantage that the cheese mixer is not heated and thus there is a different consistency in cheese and non-standard quality. Said device imported from Talia, has the disadvantage that the steaming hot water does not circulate but flows out of the waste with the washed out fat and protein. This also increases the energy consumption of fuels for the production of steamed cheese. Purchase of steaming equipment from abroad worsens the balance of payments of foreign trade and these are of lower performance.
Hoře uvedené nedostatky odstraňuje sposob výroby parenej syroviny na kontinuálnych zmaselňovačoch KM 1000, 2000, 3000 českoslovensikej výroby, ktorého podstata spočívá v tom, že pariaca voda, pariaci roztok s obsahom 6 až 15 %-nej soli o teplotě 60 až 95 °C cirkuluje a je vytláčaný čerpadlom do výšky 10 cm nad zmaselňovač do lievika, kde splachuje pridávanú rozdrobenu syrovinu a samospádom v potrubí tečie do mútiaceho valca, ktorého plášť cirkulujúcou horúcou vodou je vyhriaty na 60 až 95 °C, ktorého rotor má frekvenciu otáČok 5 až 35 min-1 a ďalej preteká zmes do odlučovacieho valca, který má frekvenciu otáčok 3 až 35 min-1 a syrovina padá do miesiča, v kitorom miesiace závitovky majú frekvenciu otáčok 38 až 70 min-1 a v plášti cirkuluje horúca voda o teplote 60 až 75 Stupňov Celsia.The aforementioned drawbacks are eliminated by the method of production of steamed rennet on continuous butter-making machines KM 1000, 2000, 3000 of Czechoslovak production, which consists in that the boiling water, the boiling solution containing 6 to 15% salt at 60 to 95 ° C circulates and it is pushed by a pump up to 10 cm above the butterburizer into the funnel, where it flushes the added shredded cheese and gravity flows in the pipeline into a milling cylinder whose jacket is heated to 60 to 95 ° C with a circulating hot water . 1 and then the mixture flows into a separator cylinder having a speed of 3 to 35 min -1 and the cheese falls into a kneader, in which the kneading screws have a speed of 38 to 70 min -1 and hot water at a temperature of 60 to 75 degrees Celsius circulates in the jacket. .
Spósob výroby parenej syroviny podlá vynálezu zlepšuje akosť syrov, zvyšuje produktivitu práce a celkovú hospodárnost. Cirkulujúca horúca pariaca voda a pariaci roztok znižuje straty na tuku, bielkovín a zničuje spotřebu energie. Umožňuje všestrannejšie využitie kontinuálnych zmaselňovačov a tým zvyšuje hospodárnost strojárenskej výroby. Zlepšuje platobnú bilanciu zahrainičného obchodu v dósledku obmedzenia dovozu zariadení na parenie syroviny.The method of making steamed cheese according to the invention improves the quality of the cheeses, increases labor productivity and overall economy. Circulating hot steaming water and steaming solution reduce fat, protein losses and destroy energy consumption. It allows for more versatile use of continuous buttermakers and thus increases the economy of engineering production. It improves the balance of payments of foreign trade due to restrictions on imports of cheese-steaming equipment.
Příklad 1Example 1
Vykysnutá syrovina bola pokrájaná a nasypaná do lievika, Zároveň do lievika vtékal pariaci roztok s 15% obsahom soli o teplote 95 °C, který pridávanú rozdrobená syrovinu splachoval do potrubia ústiaceho samospádom do mútiaceho valca, ktorého plášť bol zohrievaný cirkulujúcou horúcou vodou na 95 °C a v ktorom rotor mat frekvenciu otáčok 35 min-1. Z mútiaceho valca pariaci roztok so syrovinou tiekol samospádom do odlučovača, ktorý mal frekvenciu otáčok 35 min-1, kde syrovina bola zbavovaná pariaceho roztoku. Spařená syrovina padala do miesiča, ktorého plášť bol zohrievaný cirkulujúcou horúcou vodou na teplotu 60 °C a závitovky miesiča malý frekvenciu otáčok 38 min-1. Takto vypracovaná spařená syrovina bola plněná do duplikátorových lisovacích vání a po vyzretí bola použitá na výrobu tavených syrov.At the same time, a steaming solution with a 15% salt content at 95 ° C flowed into the funnel, which flushed the added crumbled cheese into a pipe flowing by gravity into a milling cylinder whose jacket was heated to 95 ° C with circulating hot water. and in which the rotor have a frequency of 35 revolutions min -1. Mútiaceho from the roll of the paste Pipin solution flowed by gravity into the separator, which had a frequency of 35 revolutions min-1, wherein the cheese curd was drained of the solution brewing. Mating curd fell into the mixer, the jacket was heated by circulating hot water at 60 DEG C. and the screw speed mixer low frequency of 38 min-1. The thus prepared steamed cheese was filled into duplicator pressing trays and after maturing it was used for the production of processed cheese.
Příklad 2Example 2
Vykysnutá syrovina bola pokrájaná a nasýpaná do lievika. Zároveň do lievika vtékal pariaci roztok s obsahom 6 °/o-nej soli o teplote 72 aC, ktorý rozdrobená syrovinu splachoval do potrubia ústiaceho samospádom do mútiaceho valca, ktorého plášť bol zohrievaný cirkulujúcou horúcou vodou na 72 °C a v ktorom rotor mal frekvenciu otáčok 20 min-1. Z mútiaceho valca pariaci roztok so syrovinou tiekol samospádom do odlučovača, ktorý mal frekvenciu otáček 15 min-1, kde syrovina bola zbavená pariaceho roztoku. Spařená syrovina padala do miesiča, ktorého plášť bol zohrievaný cirkulujúcou horúcou vodou na teplotu 72 °C a závitovky miesiča malý frekvenciu otáčok 45 min-1. Takto spařená syfovina bola plněná do kaškavalových foriem. Syr Kaškaval takto vyrobený po vyzretí bol daný na konzum.The fermented cheese was cut and poured into a funnel. At the same time the funnel flowed Pipin solution containing 6 ° / o salt therein at a temperature of 72, and C is fragmented curd flushed down the pipe is flowing by gravity into the mútiaceho cylinder, the jacket was heated by circulating hot water at 72 ° C and in which the rotor is controlled rate of revolutions 20 min -1 . From the milling cylinder, the steaming solution with the syrup flowed by gravity to a separator having a rotational speed of 15 min -1 , where the syrup was freed of the steaming solution. Mating curd fell into the mixer, the jacket was heated by circulating hot water at 72 DEG C. and the screw speed mixer low frequency of 45 min-1. The soaked syphovina was filled into kashkaval forms. Kashkaval cheese produced after maturing was put on consumption.
Příklad 3Example 3
Vo výrobníku syrové zrno prekysávalo za neustálého premiešavania, aby nenastalo jeho zlepovanie. Po dosiahnutí 140 SH srvátky bolo so srvátkou vypuštěné do lisovacej váni, z ktoreij boli vyhřáté formy. Po vypuštění do lisovácej váni bola syrovina premiešaná a rýchle vypuštěná srvátka. Do syrového zrna bola napuštěná studená voda a zároveň bolo premiešané pod vodou. Týmto sa zrno schladilo a přestalo kysnut. Potom bolo syrové zrno vo vodě přečerpávané do odlučovača, z ktorého padalo do lieviak umiestneného 10 cm nad zmaselňovačo.m. Zároveň do lievika vtékala horúca pariaca voda o teplote 60 °C, ktorá syrové zmá splachovala do potrubia ústiaceho samospádom do mútiaceho valca, ktorého plášť bol zohrievaný cirkulujúcou horúcou vodou na teplotu 60 °C a v ktorom mal rotor frekvenciu otáčok 5 min-1. Z mútiaceho valca pariaca voda so syrovinou tiekla samospádom do odlučovača, ktorý mal frekvenciu otáčok 3 s-1, kde syrovina bola zbavená pariacej vody. Spařená syrovina padala do miesiča, ktorého plášť bol zohrievaný cirkulujúcou horúcou vodou na teplotu 75 °C a závitovky miesiča malý frekvenciu otáčok 70 min-1. Vytlačená spařená syrovina z miesiča bola vytahovaná v stuhy a tak spracovaná do tvaru parenie.In the machine, the cheese grain was acidified with constant stirring to avoid sticking. After reaching 14 0 GA whey, whey was discharged into a molding bathtubs, the ktoreij was heated mold. After being discharged into the pressing line, the cheese was mixed and the whey was drained rapidly. Cold water was impregnated into the raw grain while being stirred under water. This allowed the grain to cool and to stop rising. Then the raw grain in water was pumped into a separator from which it fell into a funnel placed 10 cm above the butter. Simultaneously, hot steaming water at 60 ° C flowed into the funnel and flushed the cheese into a pipe flowing by gravity into a milling cylinder whose jacket was heated to 60 ° C with circulating hot water and where the rotor had a rotational speed of 5 min -1 . From the kneading cylinder the steaming water with the syrup flowed by gravity to a separator having a speed of 3 s -1 , where the syrup was freed of the steaming water. Mating curd fell into the mixer, the jacket was heated by circulating hot water at 75 DEG C. and the screw speed mixer low frequency of 70 min-1. The extruded steamed cheese from the kneader was pulled into ribbons and thus processed into a steaming shape.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS816776A CS231759B1 (en) | 1981-09-15 | 1981-09-15 | Manufacturing process of steamed curd |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS816776A CS231759B1 (en) | 1981-09-15 | 1981-09-15 | Manufacturing process of steamed curd |
Publications (2)
Publication Number | Publication Date |
---|---|
CS677681A1 CS677681A1 (en) | 1984-05-14 |
CS231759B1 true CS231759B1 (en) | 1984-12-14 |
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ID=5415543
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CS816776A CS231759B1 (en) | 1981-09-15 | 1981-09-15 | Manufacturing process of steamed curd |
Country Status (1)
Country | Link |
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CS (1) | CS231759B1 (en) |
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1981
- 1981-09-15 CS CS816776A patent/CS231759B1/en unknown
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Publication number | Publication date |
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CS677681A1 (en) | 1984-05-14 |
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