SI9820005A - Method for producing cold-filtered beer - Google Patents
Method for producing cold-filtered beer Download PDFInfo
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- SI9820005A SI9820005A SI9820005A SI9820005A SI9820005A SI 9820005 A SI9820005 A SI 9820005A SI 9820005 A SI9820005 A SI 9820005A SI 9820005 A SI9820005 A SI 9820005A SI 9820005 A SI9820005 A SI 9820005A
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- beer
- filtered
- filter
- membrane filter
- aqueous medium
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- 235000013405 beer Nutrition 0.000 title claims abstract description 40
- 238000004519 manufacturing process Methods 0.000 title abstract description 3
- 239000012528 membrane Substances 0.000 claims abstract description 29
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 claims abstract description 21
- 229910001424 calcium ion Inorganic materials 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 19
- 230000002378 acidificating effect Effects 0.000 claims abstract description 14
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 239000012736 aqueous medium Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000002360 preparation method Methods 0.000 claims description 7
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical group CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000004952 Polyamide Substances 0.000 claims description 5
- 229920002647 polyamide Polymers 0.000 claims description 5
- 238000005374 membrane filtration Methods 0.000 claims description 4
- 235000008694 Humulus lupulus Nutrition 0.000 claims description 3
- 239000004310 lactic acid Substances 0.000 claims description 3
- 235000014655 lactic acid Nutrition 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- GXCLVBGFBYZDAG-UHFFFAOYSA-N N-[2-(1H-indol-3-yl)ethyl]-N-methylprop-2-en-1-amine Chemical compound CN(CCC1=CNC2=C1C=CC=C2)CC=C GXCLVBGFBYZDAG-UHFFFAOYSA-N 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims description 2
- 150000007524 organic acids Chemical class 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 description 8
- 239000004094 surface-active agent Substances 0.000 description 8
- 239000007864 aqueous solution Substances 0.000 description 7
- 238000000746 purification Methods 0.000 description 6
- 239000008399 tap water Substances 0.000 description 6
- 235000020679 tap water Nutrition 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 108090000790 Enzymes Proteins 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 102000035195 Peptidases Human genes 0.000 description 2
- 108091005804 Peptidases Proteins 0.000 description 2
- 239000004365 Protease Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000249 desinfective effect Effects 0.000 description 2
- 238000005108 dry cleaning Methods 0.000 description 2
- 230000002255 enzymatic effect Effects 0.000 description 2
- -1 fatty acids Chemical class 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000008237 rinsing water Substances 0.000 description 2
- 108700038091 Beta-glucanases Proteins 0.000 description 1
- 108010001817 Endo-1,4-beta Xylanases Proteins 0.000 description 1
- 101710121765 Endo-1,4-beta-xylanase Proteins 0.000 description 1
- 206010017533 Fungal infection Diseases 0.000 description 1
- 208000031888 Mycoses Diseases 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000007942 carboxylates Chemical group 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000003891 oxalate salts Chemical class 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000009928 pasteurization Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001184 polypeptide Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H1/00—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H1/00—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages
- C12H1/02—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages combined with removal of precipitate or added materials, e.g. adsorption material
- C12H1/06—Precipitation by physical means, e.g. by irradiation, vibrations
- C12H1/063—Separation by filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/16—Use of chemical agents
- B01D2321/162—Use of acids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/16—Use of chemical agents
- B01D2321/164—Use of bases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/16—Use of chemical agents
- B01D2321/168—Use of other chemical agents
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Genetics & Genomics (AREA)
- Food Science & Technology (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Toxicology (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
Description
BRAU-UNION Osterreich AktiengesellschaftBRAU-UNION Osterreich Aktiengesellschaft
Postopek za pripravo hladno filtriranega pivaProcess for the preparation of cold filtered beer
Predloženi izum se nanaša na postopek za pripravo hladno filtriranega piva, pri čemer pivo filtriramo skozi membranski filter, ki lahko absorbira kalcijeve ione, ter ga po filtraciji čistimo in speremo z vodnimi mediji, nakar očiščeni in sprani membranski filter uporabimo za novo filtracijo.The present invention relates to a process for the preparation of cold filtered beer, whereby the beer is filtered through a membrane filter that can absorb calcium ions, and after filtration it is purified and washed with aqueous media, and then the purified and washed membrane filter is used for new filtration.
Pivo je treba zaradi dolgih poti prodaje razkužiti, da bi ga naredili sposobnega za skladiščenje. Dandanes pivo za razkuževanje v prvi vrsti pasterizirajo. Za to pivo, polnjeno npr. v steklenicah ali pločevinkah, segrejejo na temperaturo med 62 in 68 °C, s čimer uničijo klice.Beer has to be disinfected because of its long sales routes in order to be able to store it. Today, disinfecting beer is primarily pasteurized. For this beer stuffed e.g. in bottles or cans, heated to a temperature between 62 and 68 ° C, thus destroying the germs.
To pasteriziranje pa porabi veliko energije. Nadalje ima pomanjkljivost, da lahko dovedena energija sproži kemične reakcije, ki poslabšajo produkt in ki so le težko obvladljive. Zaradi teh reakcij se lahko npr. okus produkta neugodno spremeni (Pasteurjev okus) in poleg tega obstoji nevarnost, da se tvorijo neželene snovi. Pasteriziranje je torej relativno drag postopek razkuževanja, ki porabi veliko energije in zato obremenjuje okolje ter zmanjša kvaliteto.However, this pasteurizing consumes a lot of energy. Furthermore, it has the disadvantage that the energy supplied can trigger chemical reactions that degrade the product and which are only difficult to control. Due to these reactions, e.g. the taste of the product changes unfavorably (Pasteur's taste) and there is also the risk of the formation of unwanted substances. Pasteurization is, therefore, a relatively expensive disinfecting process that consumes a lot of energy and therefore burdens the environment and reduces quality.
Nadaljni postopek razkuževanja je hladna filtracija skozi membranske filtre. Hladno filtrirana piva ponujajo npr. v Združenih državah Amerike, na Japonskem in v Koreji kot t.i. draft beers. V Evropi so ta piva prepovedana, ker vsebujejo tehnične encime. S temi tehničnimi encimi preprečijo pomanjkljivost hladne filtracije, ki je inherentna tej tehniki: hitra zamašitev filtra. To zamašitev pripisujejo usedlinam snovi, ki se filtrirajo iz piva, na strani membranskega filtra po toku navzgor. Usedline se dajo le težko ali pa se sploh ne dajo več odstraniti s filtra in zmanjšajo življenjsko dobo filtra. To podraži proizvodnjo piva, ker so membranski filtri dragi.A further disinfection process is cold filtration through membrane filters. Cold filtered beers offer e.g. in the United States, Japan, and Korea as t.i. draft beers. In Europe, these beers are banned because they contain technical enzymes. These technical enzymes counteract the disadvantage of cold filtration inherent in this technique: rapid filter clogging. This clogging is attributed to the sedimentation of beer-filtered substances on the membrane filter side upstream. Sediments are only difficult to remove or can no longer be removed from the filter and reduce the filter life. This increases the cost of beer production because membrane filters are expensive.
p/lz/26841pr.docp / lz / 26841pr.doc
Da bi zvišali življenjsko dobo filtra, priporočajo izdelovalci membranskih filtrov, da se uporabljene membrane čistijo z obdelavo s proteazami, glukanazami in ksilanazami kot tudi s kemikalijami, kot tenzidi, kislinami/bazami in oksidacijskimi sredstvi, in s tem postanejo zopet primerne za uporabo. To čiščenje lahko npr. poteče v dveh stopnjah, pri čemer v prvi stopnji čistijo z navedenimi encimi in nato po želji dodatno z navedenimi kemikalijami.In order to increase the filter life, membrane filter makers recommend that the membranes used be cleaned by treatment with proteases, glucanases and xylanases as well as chemicals such as surfactants, acids / bases and oxidizing agents, thus making them suitable for use again. This cleaning may e.g. it proceeds in two stages, the first stage being purified with said enzymes and then optionally with the specified chemicals.
ΛΛ
Kot primer predvideva postopek čiščenja npr. pri filtrski površini okoli 320 m po filtracijski količini vsakokrat 5000 hektolitrov (hi) encimatsko čiščenje in po vsakokrat 20000 hi dodatno kemično čiščenje. Tipična življenjska doba tako očiščenih filtrov z navedeno filtrsko površino okoli 320 m2 je okoli 100000 hi.As an example, it envisages a cleaning process e.g. at a filter surface of about 320 m, at a filtration rate of 5,000 hectoliters (hi) each year, enzymatic purification and 20000 hi each additional dry cleaning. The typical life span of such purified filters with a filter area of about 320 m 2 is about 100,000 hi.
Znano je, da mnoge vrste membranskih filtrov po tem, ko so jih podvrgli prvemu postopku čiščenja, neposredno po čiščenju filtrirajo pivo, ki, polnjeno v steklenicah ali pločevinkah, teži k t.i. prekipevanju (gushing).Many types of membrane filters, after being subjected to the first purification process, are known to filter beer directly after purification, which, when bottled or bottled, tends to so-called. gushing.
Pod izrazom gushing je znano spontano prekipevanje piva pri odprtju steklenice oz. pločevinke. Pri tem pride do nenadnega izhajanja ogljikovega dioksida, ki ga spremlja tako močna tvorba pene, da pride do bolj ali manj močnega spraznjenja steklenice oz. pločevinke. Na dlani je, da porabniki smatrajo tendenco za gushing kot napako produkta, ki lahko vodi do resnih gospodarskih pomanjkljivosti pivovarja.The term gushing is known for spontaneous pouring of beer when opening a bottle or. cans. This results in the sudden release of carbon dioxide, which is accompanied by a strong foam formation that results in a more or less strong emptying of the bottle or. cans. It is on the palm of the hand that consumers tend to think of gushing as a product defect that can lead to serious economic disadvantages for the brewer.
Točen vzrok za nastop gushinga ni znan. Domnevajo, da je gushing v zvezi z uporabljenimi surovinami za proizvodnjo piva. Kot t.i. promotorji gushinga veljajo nižje molekulske spojine, npr. maščobne kisline, grenke hmeljne snovi, polipeptidi, oksalna kislina in snovi iz glivične okužbe. Nadalje je znano, da lahko membranska filtracija zmanjša tendenco za gushing. Vsekakor pa vodijo membranski filtri z različnimi velikostmi por do različnih rezultatov.The exact cause of the onset of gushing is unknown. It is alleged that it is gushing in relation to the raw materials used to make the beer. Like you. gushing promoters are considered to be lower molecular compounds, e.g. fatty acids, bitter hops, polypeptides, oxalic acid and fungal infections. It is further known that membrane filtration can reduce the tendency for gushing. However, membrane filters with different pore sizes lead to different results.
Po izkušnjah prijavitelja je tendenca za gushing zlasti izrazita pri pivih, ki jih filtrirajo skozi določene sveže očiščene membranske filtre. Posebno izrazito je to pri membranskih filtrih, ki vsaj deloma obstoje iz poliamida. Zato je naloga izuma, dati na p/lz/2684 lpr.doc razpolago postopek za pripravo hladno filtriranega piva, pri katerem filtriramo skozi membranske filtre in je kljub temu tendenca piva za gushing, ki ga filtriramo neposredno po postopku čiščenja, vsaj zmanjšana.In the experience of the applicant, the tendency for gushing is particularly pronounced in beers that are filtered through certain freshly purified membrane filters. This is especially pronounced for membrane filters that are at least partly made of polyamide. Therefore, it is an object of the invention to provide at p / lz / 2684 lpr.doc a process for the preparation of cold filtered beer, which is filtered through membrane filters and, nevertheless, the tendency of gushing beer to be filtered directly after the purification process is at least reduced.
Postopek v smislu izuma za pripravo hladno filtriranega piva, pri katerem pivo filtriramo skozi membranski filter, ki lahko absorbira kalcijeve ione in ga po filtraciji čistimo in spiramo z vodnimi mediji, nakar očiščeni in sprani membranski filter uporabimo za novo filtracijo, je označen s tem, da za spiranje uporabimo kisel vodni medij, ki ima pH manj kot 5,0, ali da za spiranje uporabljeni medij podvržemo obdelavi za zmanjšanje vsebnosti kalcijevih ionov.The process of the invention for the preparation of cold filtered beer, in which the beer is filtered through a membrane filter that can absorb calcium ions and after filtration is cleaned and washed with aqueous media, and then the purified and washed membrane filter is used for new filtration, to use an acidic aqueous medium having a pH of less than 5.0 or to undergo treatment to reduce the calcium ion content.
Izum temelji na spoznanju, daje tendenca za gushing zlasti izrazita takrat, kadar pivo filtriramo skozi membranski filter, ki lahko absorbira kalcijeve ione. To je npr. primer takrat, kadar filter vsaj deloma obstoji iz poliamida. Če tak filter po čiščenju spiramo z vodnim medijem, npr. vodovodno vodo, ki vsebuje kalcijeve ione, se ti absorbirajo, tako da je filter obložen s kalcijevimi ioni. Če tak filter, obložen s kalcijevimi ioni, uporabimo za novo filtriranje piva, se ti kalcijevi ioni sprostijo s filtra pri začetku filtracije zaradi kisle vrednosti pH piva, ki gaje treba filtrirati. Ti kalcijevi ioni pridejo torej v pivo. Prijavitelj smatra, da sproščeni kalcijevi ioni s karboksilatnimi ioni, npr. oksalatom, prisotnimi v pivu, tvorijo fine kristale, ki učinkujejo kot kali za tvorbo mehurčkov plinskega CO2.The invention is based on the realization that the tendency to gushing is particularly pronounced when beer is filtered through a membrane filter that can absorb calcium ions. This is e.g. an example where the filter is at least partly made of polyamide. If such a filter is rinsed after cleaning with an aqueous medium, e.g. tap water containing calcium ions is absorbed so that the filter is coated with calcium ions. If such a calcium ion-coated filter is used to filter the beer again, these calcium ions are released from the filter at the start of the filtration due to the acidic pH of the beer to be filtered. So these calcium ions get into the beer. The Applicant considers that the released calcium ions with carboxylate ions, e.g. The oxalates present in the beer form fine crystals, which act as pellets to form gas CO 2 bubbles.
Sedaj se je pokazalo, da je treba tendenco za gushing pripisati začetnemu oddajanju kalcijevih ionov s sveže očiščenih filtrov. Kislo spiranje v smislu izuma služi torej za to, da kalcijeve ione, ki jih absorbira membranski filter med postopkom čiščenja, spet izperemo.It has now emerged that the tendency for gushing should be attributed to the initial release of calcium ions from freshly purified filters. The acidic wash according to the invention therefore serves to rinse the calcium ions absorbed by the membrane filter during the purification process.
Če za čiščenje in spiranje uporabimo vodne medije, ki jih podvržemo obdelavi za zmanjšanje vsebnosti kalcijevih ionov, torej dekalcifikaciji, npr. z ionskimi izmenjalci, kislo spiranje v smislu izuma ni potrebno. Tudi v tem primeru pivo, ki ga filtriramo skozi sveže očiščen filter, ne kaže tendence za gushing.If aqueous media are used for cleaning and washing, they are subjected to treatment to reduce the calcium ion content, ie decalcification, e.g. with ion exchangers, no acidic washing according to the invention is required. Even in this case, the beer filtered through a freshly cleaned filter shows no tendency to gushing.
p/lz/26841pr.docp / lz / 26841pr.doc
Kisel vodni medij ima smotrno pH manj kot 4,5, prednostno med 3,0 in 4,0 in zlasti manj kot 3,5.An acidic aqueous medium has a pH of less than 4.5, preferably between 3.0 and 4.0, and especially less than 3.5.
Za naravnavo vrednosti pH uporabimo smotrno organsko kislino, zlasti mlečno kislino.Useful organic acid, especially lactic acid, is used to adjust the pH.
Izum se nanaša nadalje na postopek za pripravo hladno filtriranega piva, pri čemer pivo, pripravljeno iz slada, hmelja in vode, podvržemo membranski filtraciji, in je označen s tem, da za pripravo piva uporabimo vodo, ki smo jo podvrgli obdelavi za zmanjšanje vsebnosti kalcijevih ionov.The invention further relates to a process for the preparation of cold filtered beer, whereby beer made from malt, hops and water is subjected to membrane filtration and is characterized by the use of water which has been subjected to treatment to reduce the calcium content of beer ions.
Izum lahko izvajamo pri vseh membranskih filtrih, ki vežejo kalcijeve ione. To je primer npr. pri membranskem filtru, ki vsaj deloma obstoji iz poliamida. Smatramo, da ima polimer proste karboksilatne skupine ali podobne reaktivne skupine, ki lahko vežejo kalcijeve ione.The invention can be carried out on all calcium ion-binding membrane filters. This is an example, for example. with a membrane filter that is at least partly made up of polyamide. The polymer is believed to have free carboxylate groups or similar reactive groups that can bind calcium ions.
V nadaljevanju bomo izum še podrobneje opisali.The invention will be described in further detail below.
Za membransko filtracijo smo uporabili poliamidni membranski filter, ki se običajno uporablja v stanju tehnike. Po filtraciji smo filter čistili najprej encimatsko in nato kemično, kot sledi.For membrane filtration, we used a polyamide membrane filter commonly used in the art. After filtration, the filter was first purified enzymatically and then chemically as follows.
Za encimatsko čiščenje smo zamašeni filter 1 uro obdelovali z 1 %-no vodno raztopino zmesi beta-glukanaz in ksilanaz (P3-Ultrasil 65; proizvajalec: Henkel) s pH 5 (naravnan s pomočjo 0,05 %-ne vodne raztopine zmesi tenzidov in kisle komponente (P3-Ultrasil 75; proizvajalec: Henkel) pri temperaturi 50 °C. Nato smo to obdelavo še enkrat izvedli.For enzymatic purification, the clogged filter was treated for 1 hour with a 1% aqueous solution of a mixture of beta-glucanases and xylanases (P3-Ultrasil 65; manufacturer: Henkel) with pH 5 (adjusted with a 0.05% aqueous solution of the surfactant mixture and acidic components (P3-Ultrasil 75; manufacturer: Henkel) at 50 ° C. This treatment was then repeated.
Potem smo filter obdelovali z 0,5 %-no vodno raztopino zmesi tenzidov, glukanaz in proteaz (P3-Ultrasil 62; proizvajalec: Henkel) s pH 9-9,5 (naravnan s pomočjo 0,15 %-ne vodne raztopine zmesi tenzidov in alkalne komponente (P3-Ultrasil 91;The filter was then treated with a 0.5% aqueous solution of a mixture of surfactants, glucanases and proteases (P3-Ultrasil 62; manufacturer: Henkel) with a pH of 9-9.5 (adjusted with 0.15% aqueous solution of a mixture of surfactants and alkaline components (P3-Ultrasil 91;
p/lz/26841pr.doc proizvajalec: Henkel) 3 ure pri temperaturi 50 °C in nato sprali z vodovodno vodo (50 °C).p / lz / 26841pr.doc manufacturer: Henkel) for 3 hours at 50 ° C and then rinsed with tap water (50 ° C).
Za kemično čiščenje smo filter obdelovali z 1 %-no vodno raztopino zmesi tenzidov in kisle komponente (P3-Ultrasil 75; proizvajalec: Henkel) 30 minut pri 60 °C in nato spirali s svežo vodovodno vodo. Nato smo filter obdelovali z vodno raztopino, ki je vsebovala 1 % zmesi tenzidov in alkalne komponente (P3-Ultrasil 91; proizvajalec Henkel) in 1 % zmesi tenzidov in donorja kisika (P3-Ultrasil 0,5; proizvajalec: Henkel), 30 minut pri temperaturi 60 °C in nato spirali s svežo vodovodno vodo. Nato smo filter še enkrat obdelovali z 0,5 %-no vodno raztopino zmesi tenzidov in kisle komponente (P3-Ultrasil 75; proizvajalec: Henkel) 30 minut in nato toliko časa spirali s svežo vodovodno vodo, dokler izpiralna voda ni dosegla električne prevodnosti sveže vode.For dry cleaning, the filter was treated with a 1% aqueous solution of a mixture of surfactants and acidic component (P3-Ultrasil 75; manufacturer: Henkel) for 30 minutes at 60 ° C and then washed with fresh tap water. The filter was then treated with an aqueous solution containing 1% surfactant and alkaline component mixture (P3-Ultrasil 91; manufacturer Henkel) and 1% surfactant and oxygen donor mixture (P3-Ultrasil 0.5; manufacturer: Henkel) for 30 minutes. at 60 ° C and then rinsed with fresh tap water. The filter was then treated again with a 0.5% aqueous solution of a mixture of surfactants and acidic component (P3-Ultrasil 75; manufacturer: Henkel) for 30 minutes and then rinsed with fresh tap water until the rinsing water reached electrical conductivity fresh water.
Voda, uporabljena za čiščenje in spiranje uporabljenega membranskega filtra, je bila vsakokrat ne-dekalcificirana vodovodna voda.The water used to clean and rinse the membrane filter used was non-decalcified tap water.
Pokazalo se je, da je imelo pivo, ki smo ga v začetku filtrirali skozi ta membranski filter, čiščen po vodnem postopku, tendenco za gushing. Sele od količine filtrata okoli 0,8 hi piva na m2 filtrske površine, ko je bilo končano oddajanje kalcija, smo lahko spet filtrirali pivo brez tendence za gushing.The beer, which we initially filtered through this membrane filter, purified by water, was shown to have a tendency to gushing. Only from the amount of filtrate of about 0.8 h of beer per m 2 of filter surface, when the calcium release was complete, we were able to filter the beer again without the tendency to gushing.
Če smo enak filter, očiščen po gornjem postopku, sprali z vodo, ki smo jo z dodatkom mlečne kisline spravili na pH 4,5, seje pokazalo, daje bila izpiralna voda obogatena s kalcijevimi ioni, ki so očitno izvirali s sveže očiščenega membranskega filtra. Pivo, ki smo ga filtrirali skozi ta membranski filter, spran s kislo izpiralno vodo, ni imel tendence za gushing.If the same filter, purified by the above procedure, was washed with water, which was brought to pH 4.5 with the addition of lactic acid, it was shown that the rinsing water was enriched with calcium ions, which apparently originated from a freshly cleaned membrane filter. The beer filtered through this membrane filter washed with acidic rinse water had no tendency to gushing.
p/lz/2684Ipr.docp / lz / 2684Ipr.doc
Enak učinek smo lahko opazovali, če smo za čiščenje in spiranje uporabili dekalcificirano vodo.The same effect could be observed if decalcified water was used for cleaning and rinsing.
ZaFor
BRAU-UNION OsterreichBRAU-UNION Osterreich
AktiengesellsAktiengesells
PA’PA '
UU
PISARJA 4.0.0. ANA, ČOPOVA 14 βWRITERS 4.0.0. ANA, CHOPOVA 14 β
p/lz/26841pr.docp / lz / 26841pr.doc
Claims (7)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT0081797A AT405291B (en) | 1997-05-13 | 1997-05-13 | METHOD FOR PRODUCING COLD-FILTERED BEER |
| PCT/AT1998/000125 WO1998051776A1 (en) | 1997-05-13 | 1998-05-13 | Method for producing cold-filtered beer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SI9820005A true SI9820005A (en) | 1999-08-31 |
Family
ID=3500432
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SI9820005A SI9820005A (en) | 1997-05-13 | 1998-05-13 | Method for producing cold-filtered beer |
Country Status (13)
| Country | Link |
|---|---|
| EP (1) | EP0920489A1 (en) |
| JP (1) | JP2000515026A (en) |
| KR (1) | KR20000023736A (en) |
| CN (1) | CN1230985A (en) |
| AT (1) | AT405291B (en) |
| BG (1) | BG103059A (en) |
| BR (1) | BR9804908A (en) |
| HU (1) | HUP0100325A3 (en) |
| ID (1) | ID21517A (en) |
| PL (1) | PL331218A1 (en) |
| SI (1) | SI9820005A (en) |
| TR (1) | TR199900060T1 (en) |
| WO (1) | WO1998051776A1 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CZ302041B6 (en) * | 2009-02-25 | 2010-09-15 | Výzkumný ústav pivovarský a sladarský, a. s. | Method for determining final re-foaming of packaged beer due to barley |
| CZ308152B6 (en) * | 2018-10-23 | 2020-01-22 | Výzkumný ústav pivovarský a sladařský, a.s. | A method of treating cereal to prepare malt and / or malt prepared therefrom to reduce the foaming potential of malt |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS51125958A (en) * | 1974-11-19 | 1976-11-02 | Ebara Infilco Co Ltd | Method for removing membrane- contaminating matters |
| US4357254A (en) * | 1981-01-12 | 1982-11-02 | Chemical Sciences, Inc. | Cleaning composition |
| FR2660211A1 (en) * | 1990-03-27 | 1991-10-04 | Ceramiques Tech Soc D | Process for cleaning semipermeable membranes |
| US5230804A (en) * | 1991-03-19 | 1993-07-27 | Hoechst Ag | Process for separating catalysts from suspensions by filtration |
| US5277819A (en) * | 1992-06-03 | 1994-01-11 | Pall Corporation | Cold draft beer filter membrane cleaning process |
| DE4401456A1 (en) * | 1994-01-19 | 1995-07-20 | Wissenschaftsfoerderung Der De | Process for clarifying beer using crossflow microfiltration |
| DE19503060A1 (en) * | 1995-02-01 | 1996-08-08 | Henkel Ecolab Gmbh & Co Ohg | Cleaning procedure for membrane filters |
| JPH09262444A (en) * | 1996-03-29 | 1997-10-07 | Toray Ind Inc | Cleaning method of membrane module |
| JP3538203B2 (en) * | 1997-04-08 | 2004-06-14 | ポール・コーポレーション | Beer production method |
| AT405183B (en) * | 1997-04-08 | 1999-06-25 | Steirerbrau Ag | METHOD FOR PRODUCING COLD-FILTERED BEER |
-
1997
- 1997-05-13 AT AT0081797A patent/AT405291B/en not_active IP Right Cessation
-
1998
- 1998-05-13 SI SI9820005A patent/SI9820005A/en unknown
- 1998-05-13 BR BR9804908-9A patent/BR9804908A/en not_active IP Right Cessation
- 1998-05-13 WO PCT/AT1998/000125 patent/WO1998051776A1/en not_active Ceased
- 1998-05-13 ID IDW990007A patent/ID21517A/en unknown
- 1998-05-13 HU HU0100325A patent/HUP0100325A3/en unknown
- 1998-05-13 JP JP10548605A patent/JP2000515026A/en active Pending
- 1998-05-13 EP EP98918966A patent/EP0920489A1/en not_active Withdrawn
- 1998-05-13 TR TR1999/00060T patent/TR199900060T1/en unknown
- 1998-05-13 CN CN98800965A patent/CN1230985A/en active Pending
- 1998-05-13 PL PL98331218A patent/PL331218A1/en unknown
-
1999
- 1999-01-07 BG BG103059A patent/BG103059A/en unknown
- 1999-01-12 KR KR1019997000200A patent/KR20000023736A/en not_active Withdrawn
Also Published As
| Publication number | Publication date |
|---|---|
| WO1998051776A1 (en) | 1998-11-19 |
| HUP0100325A2 (en) | 2001-05-28 |
| TR199900060T1 (en) | 1999-07-21 |
| PL331218A1 (en) | 1999-07-05 |
| ID21517A (en) | 1999-06-24 |
| AT405291B (en) | 1999-06-25 |
| KR20000023736A (en) | 2000-04-25 |
| BR9804908A (en) | 2000-01-25 |
| EP0920489A1 (en) | 1999-06-09 |
| CN1230985A (en) | 1999-10-06 |
| HUP0100325A3 (en) | 2003-03-28 |
| JP2000515026A (en) | 2000-11-14 |
| BG103059A (en) | 1999-09-30 |
| ATA81797A (en) | 1998-11-15 |
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