NO124053B - - Google Patents
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- Publication number
- NO124053B NO124053B NO0477/69A NO47769A NO124053B NO 124053 B NO124053 B NO 124053B NO 0477/69 A NO0477/69 A NO 0477/69A NO 47769 A NO47769 A NO 47769A NO 124053 B NO124053 B NO 124053B
- Authority
- NO
- Norway
- Prior art keywords
- mask
- weight
- dry
- binder
- effluent
- Prior art date
Links
- 239000011230 binding agent Substances 0.000 claims description 15
- 244000005700 microbiome Species 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 9
- 239000002243 precursor Substances 0.000 claims description 8
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 7
- 239000011575 calcium Substances 0.000 claims description 7
- 229910052791 calcium Inorganic materials 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 7
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 claims description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 5
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 5
- 239000012452 mother liquor Substances 0.000 claims description 5
- 230000002538 fungal effect Effects 0.000 claims description 4
- 239000002699 waste material Substances 0.000 claims description 4
- 241000235646 Cyberlindnera jadinii Species 0.000 claims description 3
- 241000228245 Aspergillus niger Species 0.000 claims description 2
- 241000222178 Candida tropicalis Species 0.000 claims 1
- 239000002994 raw material Substances 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000005469 granulation Methods 0.000 description 6
- 230000003179 granulation Effects 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 239000001913 cellulose Substances 0.000 description 5
- 229920002678 cellulose Polymers 0.000 description 5
- 241000006364 Torula Species 0.000 description 4
- 235000018102 proteins Nutrition 0.000 description 4
- 102000004169 proteins and genes Human genes 0.000 description 4
- 108090000623 proteins and genes Proteins 0.000 description 4
- 235000014633 carbohydrates Nutrition 0.000 description 3
- 150000001720 carbohydrates Chemical class 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 244000025254 Cannabis sativa Species 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000010411 cooking Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241000218631 Coniferophyta Species 0.000 description 1
- 239000005696 Diammonium phosphate Substances 0.000 description 1
- 241000250507 Gigaspora candida Species 0.000 description 1
- 229920001732 Lignosulfonate Polymers 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 240000004658 Medicago sativa Species 0.000 description 1
- 235000017587 Medicago sativa ssp. sativa Nutrition 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229920005551 calcium lignosulfonate Polymers 0.000 description 1
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 1
- RYAGRZNBULDMBW-UHFFFAOYSA-L calcium;3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Ca+2].COC1=CC=CC(CC(CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O RYAGRZNBULDMBW-UHFFFAOYSA-L 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- ONCZQWJXONKSMM-UHFFFAOYSA-N dialuminum;disodium;oxygen(2-);silicon(4+);hydrate Chemical compound O.[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Na+].[Na+].[Al+3].[Al+3].[Si+4].[Si+4].[Si+4].[Si+4] ONCZQWJXONKSMM-UHFFFAOYSA-N 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 229910000388 diammonium phosphate Inorganic materials 0.000 description 1
- 235000019838 diammonium phosphate Nutrition 0.000 description 1
- 239000002706 dry binder Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011121 hardwood Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- WRUGWIBCXHJTDG-UHFFFAOYSA-L magnesium sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Mg+2].[O-]S([O-])(=O)=O WRUGWIBCXHJTDG-UHFFFAOYSA-L 0.000 description 1
- 229940061634 magnesium sulfate heptahydrate Drugs 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000012460 protein solution Substances 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229940080314 sodium bentonite Drugs 0.000 description 1
- 229910000280 sodium bentonite Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/28—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic using special binding agents
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/10—Animal feeding-stuffs obtained by microbiological or biochemical processes
- A23K10/12—Animal feeding-stuffs obtained by microbiological or biochemical processes by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K40/00—Shaping or working-up of animal feeding-stuffs
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K40/00—Shaping or working-up of animal feeding-stuffs
- A23K40/10—Shaping or working-up of animal feeding-stuffs by agglomeration; by granulation, e.g. making powders
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Food Science & Technology (AREA)
- Biotechnology (AREA)
- Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- Physiology (AREA)
- Animal Husbandry (AREA)
- Biomedical Technology (AREA)
- Biochemistry (AREA)
- Sustainable Development (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Fodder In General (AREA)
Description
Fremgangsmåte ved granulering av en forstoffblanding. Procedure for granulating a precursor mixture.
Foreliggende oppfinnelse angår en'.ny og forbedret metode for The present invention relates to a new and improved method for
granulering av dyrefor.,--dvs^. i folge foreliggende oppfinnelse kan man .granulere dyrefor ved som bindemiddel å anvende, en blanding av pro-teiner, vitaminer, mineraler samt carbohydrat og lignosulfonat, som erholdes ved dyrkning av gjær eller andre lettfordoyelige sopp-mikroorganismer i avlut fra ammonium-, magnesium- eller kalsiumbaserte sulfittkok. granulation of animal fodder.,--ie^. according to the present invention, animal fodder can be granulated by using, as a binder, a mixture of proteins, vitamins, minerals as well as carbohydrate and lignosulfonate, which is obtained by growing yeast or other easily digestible fungal microorganisms in effluent from ammonium, magnesium or calcium-based sulphite boils.
I lopet av de siste år har mange forsok vært gjort på å forene forskjellige typer av forbestanddeler til granulater og andre på kunstig vis sammensatte forstoffer for a erholde mest mulig vel-smakende og letthåndterlige .produkter. De bindemidler som har vært forenet med disse på kunstig vei sammensatte forstoffer har i hoved-saken vært natrlumbentonitt og, særlig i lopet av den senere tid, In the course of recent years, many attempts have been made to combine different types of pre-ingredients into granules and other artificially compounded pre-substances in order to obtain the best possible good-tasting and easy-to-handle products. The binders that have been combined with these artificially composed precursors have mainly been sodium bentonite and, especially in recent times,
avlut fra kalsiumbaserte sulfittkok. leachate from calcium-based sulphite boils.
Ammonium-, magnesium- og kalsiumbasert avlut eller'blandinger av disse er ferdige biprodukter, som erholdes fra tilsvarende konvensjonelle sulfittmasseprosesser i de industrier som fremstiller papir og cellulose. Angjeldende avlut inneholder betydelige mengder carbohydrat og andre gjæringsmidler, som som kjent anvendes ved den kommersielle fremstilling av forgjærog andre mikroorganismer. Man kan nevne f.eks. Waldhof- og Schollermetodene for dyrkning av Torula utilis. Også ved dyrkning av andre sopp-mikroorganismer, f.eks. Candida tropicalis, Aspergillus niger og Saccharomyces- Ammonium-, magnesium- and calcium-based leachate or mixtures of these are finished by-products, which are obtained from corresponding conventional sulphite pulp processes in the industries that manufacture paper and cellulose. The waste liquor in question contains significant amounts of carbohydrate and other fermenting agents, which are known to be used in the commercial production of pre-fermenters and other microorganisms. One can mention e.g. The Waldhof and Scholler methods for the cultivation of Torula utilis. Also when cultivating other fungal microorganisms, e.g. Candida tropicalis, Aspergillus niger and Saccharomyces-
arter får man- passende proteinholdige produkter som i det folgende kalles for mikroorganismematerialer. species get man-suitable protein-containing products, which in the following are called microorganism materials.
Fra det norske patentskrift nr. 105.792 er det kjent at ligno-proteiner som oppnåes ved utfellning av avfallsproteinlosninger ved hjelp av en sulfittavlutlbsning, er produkter velegnet for anvendelse som bindemiddel i forstoffer, og at Torula-forgjæret avlut, også 'slik som inneholder resterende Torula-gjær, kan anvendes som middel for utfellning av proteinmateriale fra en annen proteinkilde, med den hensikt å fremstille lignoprotein. From the Norwegian patent document no. 105,792, it is known that ligno-proteins obtained by precipitation of waste protein solutions using a sulphite leaching solution are products suitable for use as binders in precursors, and that Torula pre-fermented leachate, also such as contain residual Torula -yeast, can be used as a means of precipitating protein material from another protein source, with the intention of producing lignoprotein.
Det har vist seg at man kan fremstille hårdere, mer holdbare It has been shown that it is possible to produce harder, more durable products
og mer lettfordoyelige forgranulater ifolge foreliggende oppfinnelse som kjennetegnes ved at man som bindemiddel anvender torket eller væskeformig mask, erholdt ved dyrkning av lettfordbyelig gjær eller sopp-mikroorganismer i avlut fra ammonium-, magnesium- eller kalsiumbaserte sulfittkok eller en blanding av slike, slik at den erholdte mask som er en del av.bindemidlet inneholder h - 75 vekt% mikroorganismemateriale av maskens torrvekt, idet maskens mengde i torr form utgjor minst 0,75.- 12 vekt% av foArblandin<g>en<s> torrvekt, hvorved eventuelt moderluten helt eller delvis erstattes med frisk avlut. and more easily digestible pre-granulates according to the present invention, which are characterized by the fact that dried or liquid mask is used as a binder, obtained by growing easily digestible yeast or fungal micro-organisms in effluent from ammonium-, magnesium- or calcium-based sulphite boils or a mixture thereof, so that the obtained mask which is part of the binder contains h - 75% by weight of microorganism material of the dry weight of the mask, the amount of the mask in dry form being at least 0.75 - 12% by weight of the foArblandin<g>en<s> dry weight, whereby possibly the mother liquor completely or partially replaced with fresh effluent.
Foreliggende fremgangsmåte letter granuleringen ved å oke den konvensjonelle granuleringsapparaturs produksjon og ved å minske mengden av det finmateriale som anvendes på nytt. I prinsippet kan man anvende cellulos.ekokeavlut fra hvilket som', helst treslag, og oppfinnelsen er heller ikke avhengig av om man anvender ammonium-, magnesium- eller kalsiumbasert • avlut, fremstilt ved en spesiell kokemetode elis? basert på en spesiell celluloseemnetype. Av grunner kjent for fagfolk foretrekkes det.å anvende ammonium- eller kalsiumbasert avlut, som fåes "ved tilvirkning av oppløselig cellulose fra nål- og lovtrær. The present method facilitates the granulation by increasing the production of the conventional granulation apparatus and by reducing the amount of the fine material that is reused. In principle, you can use cellulose eco-cooking liquor from any kind of wood, and the invention is also not dependent on whether you use ammonium-, magnesium- or calcium-based • liquor, produced by a special cooking method. based on a special cellulose blank type. For reasons known to those skilled in the art, it is preferred to use ammonium- or calcium-based liquors, which are obtained by the manufacture of soluble cellulose from conifers and hardwoods.
Folgende eksempel belyser fremstillingen av et i denne oppfinnelse anvendt bindemiddel. Fremstillingen baserer seg på Torula-gjær. The following example illustrates the production of a binder used in this invention. The production is based on Torula yeast.
Eksempel Example
Fra en kalsiumbasert avlut, erholdt-fra opplosningsmidlene From a calcium-based deliquor, obtained-from the solvents
ved fremstilling av rayoncellu-losemasse, fjernes . svoveldloxyd og andre lettflyktige stoffer og avluten konsentreres i et konven-sjonelt inndampningskar slik at innholdet av faststoff utgjor ca. 20%. Oppløsningen avkjoles så til ca. 25°C, pH innstilles på 5 med vandig ammoniakk og folgende mengder næringssalter pr. kg reduserende stoff tilsettes-: 28 g diammonlumfosf at, 12 g kali-umklorid, 92 g magnesiumsulfat-heptahydrat, I blandingen.innpodes så aktiv Torula utilis, som siden dyrkes ved velkjente metoder.. Den erholdte mask, som inneholder tort mikroorganismemateriale inntil 15% beregnet på torrstoff, ble fort enten- inn i- et inndampningsapparat og konsentrert til et torr stoff innhold på ca. h- 5% for det ble sproytetorket, eller ble anvendt som sådan som. et væskeformig bindemiddel. in the production of rayon cellulose pulp, is removed. sulfur dioxide and other highly volatile substances and the leachate is concentrated in a conventional evaporation vessel so that the content of solids amounts to approx. 20%. The solution is then cooled to approx. 25°C, pH is adjusted to 5 with aqueous ammonia and the following quantities of nutrient salts per kg reducing substance is added: 28 g of diammonium phosphate, 12 g of potassium chloride, 92 g of magnesium sulfate heptahydrate. Active Torula utilis is then inoculated into the mixture, which is then cultivated by well-known methods. The mask obtained, which contains dry microorganism material up to 15 % calculated for dry matter, was quickly either - into - an evaporation apparatus and concentrated to a dry matter content of approx. h- 5% for it was spray-dried, or was used as such. a liquid binder.
De erholdte .produkters analytiske -.sammensetning var i dette The analytical composition of the products obtained was in this
tilfelle (To.-rula-gjær} omtrent som folgerj case (To.-rula-yeast} much like folgerj
I det tilfelle at de andre vannopploselige stoffer i morluten., som kalsiumlignosulfonat og carbohydrater, delvis vaskes bort fra Torula-torrstoffet for torring, kan mengden av dette torrstoff bringes til å stige ved vaskning til en hvilken som helst verdi under 75%, hvorved der enda fåes et godt produkt innenfor rammen.av oppfinnelsen. Fortrinnsvis anvendes dog mask, som inneholder f.eks. 20 - h0% mikroorganismer. In the event that the other water-soluble substances in the mother liquor, such as calcium lignosulfonate and carbohydrates, are partially washed away from the Torula dry matter before drying, the amount of this dry matter can be made to rise by washing to any value below 75%, whereby there a good product is still obtained within the scope of the invention. Preferably, however, mask is used, which contains e.g. 20 - h0% microorganisms.
FSrbestanddelene^ inklusive mikroorganismesulfittavluten, enten The FSr constituents^ including the microorganism sulphite tablet, either
i tor-ret eller i væskeform, blandes i granuleringsoyemed omhyggelig in dry or liquid form, mix in the granulating oil carefully
og jevnt. Hvis man ved blandingen, anvender den torrede form, tilfores til forstoffet bindemiddel i en mengde av 0,75 - 12$ av torrvekten. Anvendes væskeformen er den dobbelte mengde nodvendig for å få samme bindevirkning. Helst tilsettes bindemidlet til forblandingen i mengder som varierer mellom 1,5 og 6$ av torrvekten. and evenly. If the dry form is used for the mixture, binder is added to the precursor material in an amount of 0.75 - 12% of the dry weight. If the liquid form is used, double the amount is required to achieve the same binding effect. Preferably, the binder is added to the premix in quantities varying between 1.5 and 6% of the dry weight.
Man kan også fremstille en torr bindemiddelblanding ved enten helt eller delvis å fjerne morluten fra mikroorganismedyrkningen og det på denne måte isolerte mikroorganismekonsentrerte mask tilsettes til fersk avlut og deretter torkes den erholdte blanding inneholdende reduserende sukker og mikroorganismemateriale. A dry binder mixture can also be prepared by either completely or partially removing the mother liquor from the microorganism cultivation and the microorganism-concentrated mask isolated in this way is added to fresh waste liquor and then the resulting mixture containing reducing sugar and microorganism material is dried.
De blandede for- og bindemidler behandles med damp for granulering, hvorved forstoffets fuktighetsinnhold stiger fra ca. 10$ The mixed precursors and binders are treated with steam for granulation, whereby the moisture content of the precursor rises from approx. 10$
til muligens 20$ og temperaturen til og med til 85°C. Den egentlige granulering kan utfores i et hvilket som helst granuleringsapparat av ringtype eller ved å anvende andre presningsmetoder, i kulemolle, knusekverner osv. Etter granuleringen avkjoles forstoffet med luft, hvilket mer eller mindre gjenoppretter det opprinnelige fuktighetsinnhold. to possibly 20$ and the temperature even to 85°C. The actual granulation can be carried out in any ring-type granulator or by using other pressing methods, in ball mills, crushers, etc. After granulation, the precursor is cooled with air, which more or less restores the original moisture content.
Oppfinnelsen kan anvendes ikke bare på det store utvalg av férblandinger, men kan også anvendes med hell ved fremstilling av hoy-, gress-, gressmel- og blåluserngranulat. Det er også åpenbart at foreliggende oppfinnelse kan tillempes og varieres på utallige måter uten å avvike fra det område og de- fordeler den byr. The invention can be applied not only to the large variety of fodder mixtures, but can also be used successfully in the production of hay, grass, grass meal and blue alfalfa granules. It is also obvious that the present invention can be applied and varied in countless ways without deviating from the area and benefits it offers.
Claims (3)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI0351/68A FI40509B (en) | 1968-02-09 | 1968-02-09 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| NO124053B true NO124053B (en) | 1972-02-28 |
Family
ID=8503984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO0477/69A NO124053B (en) | 1968-02-09 | 1969-02-07 |
Country Status (10)
| Country | Link |
|---|---|
| AT (1) | AT281574B (en) |
| BE (1) | BE727528A (en) |
| CH (1) | CH526271A (en) |
| DE (1) | DE1904363A1 (en) |
| DK (1) | DK131966C (en) |
| FI (1) | FI40509B (en) |
| FR (1) | FR2001625A1 (en) |
| GB (1) | GB1258133A (en) |
| NL (1) | NL6901685A (en) |
| NO (1) | NO124053B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI51035C (en) * | 1975-01-07 | 1978-02-14 | Otk Keskusosuusliike | |
| FI56925C (en) * | 1979-01-29 | 1980-05-12 | Serlachius Oy | FOERFARANDE FOER ATT FOERHINDRA AGGLOMERERINGEN AV LIGNOSULFONATHALTIGT BINDEMEDEL FOER GRANULERING AV FODERBLANDNINGAR |
| FR2901138A1 (en) * | 2006-05-19 | 2007-11-23 | Lesaffre & Cie | COMPOSITIONS OF PROBIOTIC MICROORGANISMS, GRANULES CONTAINING THEM, PROCESS FOR PREPARING THEM AND USES THEREOF |
-
1968
- 1968-02-09 FI FI0351/68A patent/FI40509B/fi active
-
1969
- 1969-01-28 BE BE727528D patent/BE727528A/xx not_active IP Right Cessation
- 1969-01-29 DE DE19691904363 patent/DE1904363A1/en active Pending
- 1969-01-29 AT AT88169A patent/AT281574B/en not_active Application Discontinuation
- 1969-02-03 NL NL6901685A patent/NL6901685A/xx unknown
- 1969-02-06 CH CH184669A patent/CH526271A/en not_active IP Right Cessation
- 1969-02-07 GB GB1258133D patent/GB1258133A/en not_active Expired
- 1969-02-07 FR FR6902791A patent/FR2001625A1/fr active Pending
- 1969-02-07 NO NO0477/69A patent/NO124053B/no unknown
- 1969-02-07 DK DK67069*#A patent/DK131966C/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| FI40509B (en) | 1968-10-31 |
| DK131966C (en) | 1976-03-01 |
| NL6901685A (en) | 1969-08-12 |
| DE1904363A1 (en) | 1969-09-04 |
| AT281574B (en) | 1970-05-25 |
| DK131966B (en) | 1975-10-06 |
| FR2001625A1 (en) | 1969-09-26 |
| GB1258133A (en) | 1971-12-22 |
| CH526271A (en) | 1972-08-15 |
| BE727528A (en) | 1969-07-01 |
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