NO139106B - PROCEDURE FOR TREATMENT OF RAW WHEEL - Google Patents
PROCEDURE FOR TREATMENT OF RAW WHEEL Download PDFInfo
- Publication number
- NO139106B NO139106B NO740660A NO740660A NO139106B NO 139106 B NO139106 B NO 139106B NO 740660 A NO740660 A NO 740660A NO 740660 A NO740660 A NO 740660A NO 139106 B NO139106 B NO 139106B
- Authority
- NO
- Norway
- Prior art keywords
- explosives
- barium
- explosive
- mixing
- procedure
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 8
- 239000002360 explosive Substances 0.000 claims description 38
- 239000004014 plasticizer Substances 0.000 claims description 10
- 239000004033 plastic Substances 0.000 claims description 9
- UKWUOTZGXIZAJC-UHFFFAOYSA-N 4-nitrosalicylic acid Chemical compound OC(=O)C1=CC=C([N+]([O-])=O)C=C1O UKWUOTZGXIZAJC-UHFFFAOYSA-N 0.000 claims description 7
- RAVAZXZOSFZIRB-UHFFFAOYSA-L barium(2+);hexadecanoate Chemical compound [Ba+2].CCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCC([O-])=O RAVAZXZOSFZIRB-UHFFFAOYSA-L 0.000 claims description 5
- 159000000009 barium salts Chemical class 0.000 claims description 4
- 239000002480 mineral oil Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 150000004668 long chain fatty acids Chemical class 0.000 claims description 2
- 230000035515 penetration Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000000126 substance Substances 0.000 description 5
- XTFIVUDBNACUBN-UHFFFAOYSA-N 1,3,5-trinitro-1,3,5-triazinane Chemical compound [O-][N+](=O)N1CN([N+]([O-])=O)CN([N+]([O-])=O)C1 XTFIVUDBNACUBN-UHFFFAOYSA-N 0.000 description 3
- TZRXHJWUDPFEEY-UHFFFAOYSA-N Pentaerythritol Tetranitrate Chemical compound [O-][N+](=O)OCC(CO[N+]([O-])=O)(CO[N+]([O-])=O)CO[N+]([O-])=O TZRXHJWUDPFEEY-UHFFFAOYSA-N 0.000 description 3
- 238000004898 kneading Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- DOIRQSBPFJWKBE-UHFFFAOYSA-N phthalic acid di-n-butyl ester Natural products CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical class O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 239000000026 Pentaerythritol tetranitrate Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000005422 blasting Methods 0.000 description 2
- 229960002380 dibutyl phthalate Drugs 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- 229960004321 pentaerithrityl tetranitrate Drugs 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- SNIOPGDIGTZGOP-UHFFFAOYSA-N Nitroglycerin Chemical compound [O-][N+](=O)OCC(O[N+]([O-])=O)CO[N+]([O-])=O SNIOPGDIGTZGOP-UHFFFAOYSA-N 0.000 description 1
- 239000000006 Nitroglycerin Substances 0.000 description 1
- 229920002367 Polyisobutene Polymers 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- AGXUVMPSUKZYDT-UHFFFAOYSA-L barium(2+);octadecanoate Chemical compound [Ba+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O AGXUVMPSUKZYDT-UHFFFAOYSA-L 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 239000010727 cylinder oil Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- UQXKXGWGFRWILX-UHFFFAOYSA-N ethylene glycol dinitrate Chemical compound O=N(=O)OCCON(=O)=O UQXKXGWGFRWILX-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 229960003711 glyceryl trinitrate Drugs 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000010688 mineral lubricating oil Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002828 nitro derivatives Chemical class 0.000 description 1
- BRBAEHHXGZRCBK-UHFFFAOYSA-N pentrinitrol Chemical compound [O-][N+](=O)OCC(CO)(CO[N+]([O-])=O)CO[N+]([O-])=O BRBAEHHXGZRCBK-UHFFFAOYSA-N 0.000 description 1
- 229950006286 pentrinitrol Drugs 0.000 description 1
- 235000019271 petrolatum Nutrition 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 239000010773 plant oil Substances 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000010723 turbine oil Substances 0.000 description 1
- 229940099259 vaseline Drugs 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C21/00—Whey; Whey preparations
-
- 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
- A21D2/24—Organic nitrogen compounds
- A21D2/26—Proteins
- A21D2/261—Animal proteins
- A21D2/263—Animal proteins from dairy products
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Zoology (AREA)
- Chemical & Material Sciences (AREA)
- Polymers & Plastics (AREA)
- Dairy Products (AREA)
- Chemical Treatment Of Metals (AREA)
- Paper (AREA)
Description
Fremgangsmåte til fremstilling av høybrisante plastiske sprengstoffer. Process for the production of high-explosive plastic explosives.
Plastiske sprengstoffer har vært kjent Plastic explosives have been known
i lengre tid. De høybrisante typer er for det for a longer period of time. The high-spirited types are for it
meste oppbygget således at et krystallinsk mostly structured so that a crystalline
høy-ytelsessprengstoff f- eks. nitropenta high-performance explosives e.g. nitropenta
eller heksogen er innlagret i et plastifiseringsmiddel. or hexogen is stored in a plasticizer.
Som plastifiseringsmiddel velges gela-tinaktige masser av kollodiumull med ni-troforbindelser, salpetersyreestere og ikke eksplosive gelatinerbare stoffer som poly-isobutylen, butyl- og dibutylftalat og andre. Disse plastiske sprengstoffer har den ulempe av de på grunn av gelatinstruktu-ren ikke er aldrings- og temperaturbestan-dige, og ved anvendelse av salpetersyreestere som nitroglycerin og nitroglycol, på grunn av disse stoffers fysiologiske virk-ning, ikke kan formes med hånden i upak-ket tilstand. Gelatinous masses of collodion wool with nitro compounds, nitric acid esters and non-explosive gelatinizable substances such as polyisobutylene, butyl and dibutyl phthalate and others are chosen as plasticizers. These plastic explosives have the disadvantage that, due to the gelatin structure, they are not ageing- and temperature-resistant, and when using nitric acid esters such as nitroglycerin and nitroglycol, due to the physiological effect of these substances, they cannot be shaped by hand in unpack -ket condition.
Den andre gruppen plastifiseringsmidler består av vaselin, mineralolje, voks, The second group of plasticizers consists of vaseline, mineral oil, wax,
planteoljer og lignende stoffer. Planteolje-ne har den ulempe at de er forsåpbare og vegetable oils and similar substances. Plant oils have the disadvantage that they are saponifiable and
ikke luftbestandige, da de i det vesentlige not air-resistant, as they essentially
består av fettsyreglycerider. Lagringstoe-standigheten av sprengstoffer fremstilt consists of fatty acid glycerides. The storage stability of manufactured explosives
med slike stoffer nedsettes derved. Bedre er with such substances is thereby reduced. Better is
anvendelsen av nøytralt reagerende ikke the application of neutral reacting does not
forsåpbare og bestandige oljer og pastaer saponifiable and resistant oils and pastes
på basis av mettede hydrokarboner som on the basis of saturated hydrocarbons which
vaselin og mineralske smøreoljer. En for petroleum jelly and mineral lubricating oils. One for
den praktiske anvendelse av disse spreng-stofftyper uheldig foreteelse er at disse the practical application of these types of explosives unfortunate occurrence is that these
sprengmassers konsistens er meget sterkt the consistency of explosives is very strong
avhengig av den ytre temperatur. Det be-ror på at viskositeten av fett og olje på depending on the external temperature. It depends on the viscosity of fat and oil
hydrokarbonbasis forandrer seg sterkt med hydrocarbon base changes strongly with
temperaturen og derved Influeres plastisi- the temperature and thereby influences the plasticity
teten av de herav fremstilte sprengstoffer på samme måten. Eksplosivstoffer av mi-ner aloljeholdige plastifiseringsmidler og krystalline høy-ytelsessprengstoffer som ved normale temperaturer på ca. 20° C er plastiske og godt knabare, blir ved temperaturer under frysepunktet hårde og sprøe, ved forhøyet temperatur på 50° C og mer inntrer en mykning, således at sprengmassen taper sin formtoestandighet. the head of the explosives produced from it in the same way. Explosives of mine al-oil-containing plasticizers and crystalline high-performance explosives which at normal temperatures of approx. 20° C are plastic and easily crunchable, at temperatures below freezing they become hard and brittle, at an elevated temperature of 50° C and more a softening occurs, so that the blasting mass loses its shape.
Det er nu blitt funnet at man ved plastiske formbare sprengstoffer som inneholder mineralolje som plastifiseringsmiddel og høyfølsomme brisante sprengstoffer som pentaerytritt-tetranitrat og cyklotri-metylentrinitramin, får man en forbedring i temperaturavhengigheten av disse spreng-stoffers konsistens når man til disse setter bariumsalter av langkjedede fettsyrer, spe-sielt bariumlaurat og/eller bariumpalmitat. Sprengmasser som inneholder slike tilset-ningsstoffer beholder også ved lavere og høyere temperaturer deres knabare egenskaper. It has now been found that with plastic malleable explosives that contain mineral oil as plasticizer and highly sensitive explosives such as pentaerythritol tetranitrate and cyclotrimethylenetrinitramine, an improvement in the temperature dependence of these explosives' consistency is obtained when barium salts of long-chain fatty acids are added to these , especially barium laurate and/or barium palmitate. Explosives containing such additives retain their brittle properties even at lower and higher temperatures.
Fremstillingen av de formbare sprengmasser som inneholder de nevnte barium-såper kan foregå etter de i sprengstoff-industrien kjente fremgangsmåter. Varia-sjoner som referer seg til tilsetningen av bariumsaltet er mulige. Således kan alle sprengstoffets bestannddeler ifylles i en blandingsmaskin som utøver en intens knavirkning og sammenblandes. Blandings-tiden nedsettes når det derunder foretas en oppvarmning av blandingsspannen på ca. 60° C. Bariumsaltene kan imidlertid også forblandes med mineraloljene, idet det likeledes lønner seg å foreta forblan-dingen i varmen. Det forblandede plastifiseringsmiddel blir da som vanlig fylt med de krystallinske sprengstoffer i blandever-ket og knadd. Også anvendelsen av med vann flegmatiserte høy-ytelsessprengstof-fer er mulig, da det mineralske plastifiseringsmiddel fortrenger vann. Sistnevnte kan lett helles ut fra 'blandingspannen. De siste spor av fuktighet fjerner man deretter ved oppvarmning av blandingspannen ved knaprosessen. The production of the malleable explosives containing the aforementioned barium soaps can be carried out according to methods known in the explosives industry. Variations referring to the addition of the barium salt are possible. Thus, all the components of the explosive can be filled into a mixing machine that exerts an intense kneading action and mixed together. The mixing time is reduced when the mixing pan is heated for approx. 60° C. The barium salts can, however, also be mixed with the mineral oils, as it is also worthwhile to carry out the mixing in the heat. The premixed plasticizer is then filled with the crystalline explosives in the mixing plant as usual and kneaded. The use of high-performance explosives phlegmatized with water is also possible, as the mineral plasticizer displaces water. The latter can be easily poured out of the mixing pan. The last traces of moisture are then removed by heating the mixing pan during the kneading process.
Eksempel 1: Example 1:
8,5 kg tørt pentaerytritt-tetranitrat, 1,05 kg av en glideolje med 4,5° Engler ved 20° C og 0,45 kg bariumlaurat haes i blandingskaret i en Werner-Pfleiderer-kna-maskin. Blandingskarets mantel oppvarmes med varmt vann på 70° C. Etter en blandingstid på 90 min. fåes et godt plastisk knabart sprengstoff. 8.5 kg of dry pentaerythritol tetranitrate, 1.05 kg of a lubricating oil with 4.5° Engeler at 20° C. and 0.45 kg of barium laurate are placed in the mixing vessel of a Werner-Pfleiderer kneader. The jacket of the mixing vessel is heated with hot water at 70° C. After a mixing time of 90 min. a good plastic explosive is obtained.
Eksempel 2: Example 2:
1,7 kg av en turbinolje med 5,0° Engler ved 50° C gjennomrøres med 0,3 kg bariumlaurat i varmen (ca. 50° C) så lenge inntil det oppstår en homogen masse. Dette plastifiseringsmiddel has da med 8,0 kg cykio-trimetylentrinitramin i blandingskaret og knas i 60 min. Det fremkommer et plastisk sprengstoff som lar seg godt forme. 1.7 kg of a turbine oil with 5.0° Angels at 50° C is mixed with 0.3 kg of barium laurate in the heat (approx. 50° C) until a homogeneous mass is formed. This plasticizer is then mixed with 8.0 kg of cyclotrimethylenetrinitramine in the mixing vessel and crushed for 60 minutes. A plastic explosive is produced which can be easily shaped.
Eksempel 3: Example 3:
1,3 kg av en sylinderolje med 8,0° Engler ved 100° C sammenrøres med 0,7 kg ba-riumpalmetat i varmen ved ca. 50° C til en homogen masse, og has deretter med 8,0 kg pentaerytrittetranitrat som er flegmati-sert med 1,6 kg vann i blandemaskinen. Etter 80 min. blandingstid kan ca. 1,4 kg vann helles ut av blandingspannen. De res-terende ca. 0,2 kg vann fjernes ved at blandingskaret oppvarmes ved hjelp av varmt vann på ca. 90° C og knaprosessen fortsettes ytterligere 60 min. 1.3 kg of a cylinder oil with 8.0° Angels at 100° C is mixed with 0.7 kg of barium palmitate in the heat at approx. 50° C to a homogeneous mass, and then mixed with 8.0 kg of pentaerythritol trinitrate which is phlegmatized with 1.6 kg of water in the mixing machine. After 80 min. mixing time can be approx. 1.4 kg of water is poured out of the mixing pan. The remaining approx. 0.2 kg of water is removed by heating the mixing vessel using hot water of approx. 90° C and the kneading process is continued for a further 60 min.
For å kunne sammenligne de forskjellige blandinger med hensyn til deres for-hold ved temperaturforandring ble det som mål for formbarheten valgt inntrengnings-dytoden av et stempel i sprengmassen under HøppJer konsistometer. Den ble målt ved vekslende temperaturer imidlertid ved konstant tidsvarighet og samme belastning av stemplet. Temperaturavhengigheten av sprengmassens elastiske egenskaper fremkommer da fra helningen av den rette lin-je som man får når man forbinder med hverandre de for en bestemt sprengmasse ved forskjellige temperaturer fastslåtte inntrengningsdybder. Den midlere inn-trengningsdybde er uavhengig av tilset-ningsstoffene og bare en funksjon av mengdeforholdet mellom plastifiseringsmiddel og krystallinske bestanddeler. Ved å øke delen av plastifiserende stoffer blir sprengstoffet mykere, ved nedsettelse til-svarende stivere. Likeledes kan den normale plastisitet av sprengmassene influeres ved forandring av kornifordeling av de faste bestanddeler. Plastisitetens ternpera-turavhengighet bestemmes derimot alene av inntrengningsdybdens forandring med temperaturen. In order to be able to compare the different mixtures with regard to their conditions when the temperature changes, the penetration dytode of a piston into the blasting mass under the HøppJer consistometer was chosen as the measure of formability. It was measured at varying temperatures, however, at a constant duration and the same load on the piston. The temperature dependence of the explosive's elastic properties then emerges from the slope of the straight line that is obtained when you connect the penetration depths determined for a specific explosive at different temperatures. The average penetration depth is independent of the additives and only a function of the quantity ratio between plasticizer and crystalline components. By increasing the proportion of plasticizing substances, the explosive becomes softer, by reducing it correspondingly stiffer. Likewise, the normal plasticity of the explosives can be influenced by changing the grain distribution of the solid components. The temperature dependence of plasticity, on the other hand, is determined solely by the change in penetration depth with temperature.
I tabellen er det sammenstilt en rekke av plastiske sprengstoffer med inntrengningsdybder som er fastslått ved forskjellige temperaturer. Konsistometerets belastning utgjorde i alle tilfelle 1 kg, og tiden inntil avlesning av inntrengningsdybden 1 min. Prøvelegemene var sylindre med 15 mm diameter og 15 mm høyde. Spreng-stoffene nr. 1, 2 og 3 ifølge tabellen tilsvarer de som er fremstilt ifølge de nevnte eksempler. Sprengstoff nr. 4 tilsvarer nr. 1 hvor tilsetningen av bariumlaurat ble strø-ket. Sprengstoffmassen som nevnes i nr. 5 tilsvarer sprengstoff nr. 2, bare med den forskjell at bariumlaurat er erstattet med kalsiumstearat. Ved sprengstoff nr. 6 ble det i sprengstoff nr. 3 istedenfor bariumpalmitat anvendt bariumstearat. Det ble målt ved temperaturer på -r- 10° C, + 22° C og + 60° C. Det viser seg av forsøkene at inntrengningsdybdens temperatura vhen-gighet og derved plastisitetens forandring med temperaturen er minst ved de sprengmasser som ble fremstilt ifølge oppfinnel-sen ved tilsetning av bariumlaurat og bariumpalmitat. The table shows a number of plastic explosives with penetration depths determined at different temperatures. The load on the consistometer was in all cases 1 kg, and the time until the penetration depth was read 1 min. The test specimens were cylinders with a diameter of 15 mm and a height of 15 mm. The explosives Nos. 1, 2 and 3 according to the table correspond to those produced according to the examples mentioned. Explosive No. 4 corresponds to No. 1 where the addition of barium laurate was omitted. The explosive mass mentioned in no. 5 corresponds to explosive no. 2, only with the difference that barium laurate has been replaced by calcium stearate. For explosive no. 6, barium stearate was used instead of barium palmitate in explosive no. 3. It was measured at temperatures of -r- 10° C, + 22° C and + 60° C. It appears from the experiments that the temperature dependence of the penetration depth and thereby the change in plasticity with temperature is least with the explosives that were produced according to the invention -then by adding barium laurate and barium palmitate.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NO771495A NO143781C (en) | 1973-02-28 | 1977-04-28 | APPLICATION OF AN INSOLABLE MIXTURE SOLID IN BAKERY GOODS |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US33684373A | 1973-02-28 | 1973-02-28 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| NO740660L NO740660L (en) | 1974-08-29 |
| NO139106B true NO139106B (en) | 1978-10-02 |
| NO139106C NO139106C (en) | 1979-01-10 |
Family
ID=23317913
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO740660A NO139106C (en) | 1973-02-28 | 1974-02-26 | PROCEDURE FOR TREATMENT OF RAW WHEEL |
Country Status (10)
| Country | Link |
|---|---|
| BE (1) | BE811740A (en) |
| CA (1) | CA1024812A (en) |
| CH (1) | CH604550A5 (en) |
| DE (1) | DE2406673A1 (en) |
| FR (1) | FR2218837B1 (en) |
| GB (1) | GB1424491A (en) |
| IE (1) | IE38893B1 (en) |
| IT (1) | IT1008978B (en) |
| NL (1) | NL7402522A (en) |
| NO (1) | NO139106C (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4161552A (en) * | 1978-01-12 | 1979-07-17 | Stauffer Chemical Company | Method for making comminuted meats and extenders |
| FR2425809A1 (en) * | 1978-05-18 | 1979-12-14 | Beatrice Foods Co | Stabiliser, thickening agent etc. for food - consists of non-proteinaceous colloidal whey ppte. prepd. by increasing pH of whey and heating |
| GB8622025D0 (en) * | 1986-09-12 | 1986-10-22 | Beecham Group Plc | Composition |
| US20070154607A1 (en) * | 2003-11-03 | 2007-07-05 | Ulate-Rodriguez Jorge A | Dough and method for preparing leavened food product |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE806933C (en) * | 1948-10-02 | 1951-06-21 | Dr Siegfried Huenig | Process for the simultaneous extraction of a product which can be whipped into foam and of phosphate from whey |
| US3560219A (en) * | 1968-07-01 | 1971-02-02 | Swanson Emery Carlton | Removing lipid material from whey |
-
1974
- 1974-02-12 GB GB623674A patent/GB1424491A/en not_active Expired
- 1974-02-13 DE DE19742406673 patent/DE2406673A1/en not_active Ceased
- 1974-02-14 IE IE00290/74A patent/IE38893B1/en unknown
- 1974-02-14 CA CA192,513A patent/CA1024812A/en not_active Expired
- 1974-02-18 FR FR7405334A patent/FR2218837B1/fr not_active Expired
- 1974-02-25 CH CH263474A patent/CH604550A5/xx not_active IP Right Cessation
- 1974-02-25 NL NL7402522A patent/NL7402522A/xx not_active Application Discontinuation
- 1974-02-26 NO NO740660A patent/NO139106C/en unknown
- 1974-02-28 BE BE7000497A patent/BE811740A/en not_active IP Right Cessation
- 1974-03-01 IT IT48867/74A patent/IT1008978B/en active
Also Published As
| Publication number | Publication date |
|---|---|
| GB1424491A (en) | 1976-02-11 |
| NO740660L (en) | 1974-08-29 |
| IE38893L (en) | 1974-08-28 |
| NO139106C (en) | 1979-01-10 |
| BE811740A (en) | 1974-08-28 |
| CA1024812A (en) | 1978-01-24 |
| AU6525874A (en) | 1975-08-07 |
| DE2406673A1 (en) | 1974-09-12 |
| IE38893B1 (en) | 1978-06-21 |
| NL7402522A (en) | 1974-08-30 |
| FR2218837B1 (en) | 1978-01-06 |
| FR2218837A1 (en) | 1974-09-20 |
| IT1008978B (en) | 1976-11-30 |
| CH604550A5 (en) | 1978-09-15 |
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