NO155399B - USE OF ALUMINUM CASTLE ALLOYS AND ALUMINUM KNITTED ALLOYS WASTE FOR THE MANUFACTURE OF ROLLING HALF PRODUCTS. - Google Patents

USE OF ALUMINUM CASTLE ALLOYS AND ALUMINUM KNITTED ALLOYS WASTE FOR THE MANUFACTURE OF ROLLING HALF PRODUCTS. Download PDF

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Publication number
NO155399B
NO155399B NO803675A NO803675A NO155399B NO 155399 B NO155399 B NO 155399B NO 803675 A NO803675 A NO 803675A NO 803675 A NO803675 A NO 803675A NO 155399 B NO155399 B NO 155399B
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Norway
Prior art keywords
aluminum
alloys
acid
alginic acid
castle
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NO803675A
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Norwegian (no)
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NO155399C (en
NO803675L (en
Inventor
Wolfgang Gruhl
Edgar Lossack
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Vaw Ver Aluminium Werke Ag
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Application filed by Vaw Ver Aluminium Werke Ag filed Critical Vaw Ver Aluminium Werke Ag
Publication of NO803675L publication Critical patent/NO803675L/en
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Publication of NO155399C publication Critical patent/NO155399C/en

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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/02Making non-ferrous alloys by melting
    • C22C1/026Alloys based on aluminium

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Metal Rolling (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Continuous Casting (AREA)
  • Forging (AREA)
  • Heat Treatment Of Nonferrous Metals Or Alloys (AREA)

Abstract

1. The use of mixed aluminum scrap for aluminum casting alloys selected from the group consisting of AlSi, AlSiCu and/or AlSiMg and for wrought aluminum alloys selected from the group consisting of AlMn, AlMg, AlMgMn, AlZnMg, AlZnMgCu, AlMgSi and/or AlCuMg, said casting alloys having a weight ratio to said wrought alloys of from 1:1 to 2:1, and without addition of primary aluminum for the making of rolled aluminum intermediate products, comprising from 1 to 6% Si, 1 to 3% Mg, 0.5 to 3% Zn, 0.5 to 3% Fe, 0.3 to 2% Cu as well as up to 1% Mn, up to 0.2% Ti, up to 0.5% Cr and up to 0.5% Pb, Bi, Sn, the remainder aluminum.

Description

Fremgangsmåte ved fremstilling av alginater. Procedure for the production of alginates.

Den foreliggende oppfinnelse angår i The present invention concerns i

hovedsaken et trinn i fremstillingen av alginat fra Ascophyllum nodosum, nemlig utfelling av alginsyre fra alginatekstrakten. Fremgangsmåten som skal beskrives i det følgende, medfører betydelige for-deler i forhold til tidligere kjent teknikk. essentially a step in the production of alginate from Ascophyllum nodosum, namely precipitation of alginic acid from the alginate extract. The procedure to be described in the following entails significant advantages compared to previously known technology.

Fremgangsmåten til fremstilling av The method of manufacture of

alginsyre er første gang beskrevet i britisk patent nr. 142 av Stanford i 1881, mens en rekke variasjoner er kommet senere. Av de mest kjente er Le Gloahec-Herters prosess i henhold til U.S. patent nr. 2 128 551 og alginic acid is first described in British patent no. 142 by Stanford in 1881, while a number of variations have come later. Of the best known, the Le Gloahec-Herter process according to U.S. Pat. patent no. 2 128 551 and

Greens prosess som er beskrevet i U.S. patent nr. 2 036 934. Etter Greens prosess felles alginatet etter den alkaliske ekstrak-sjon med kalsiumklorid, og etter Le Gloahec-Herters prosess utføres fellingen med syre. Ingen av disse prosessene er imidler-tid spesielt beregnet for eller egnet for Ascophyllum nodosum (grisetang). Bash-ford et al beskriver i J. Soc. Chem. Ind., 69 Green's process described in U.S. Pat. patent no. 2 036 934. According to Green's process, the alginate is precipitated after the alkaline extraction with calcium chloride, and according to Le Gloahec-Herter's process, the precipitation is carried out with acid. However, none of these processes are specifically intended for or suitable for Ascophyllum nodosum (pig seaweed). Bashford et al describe in J. Soc. Chem. Ind., 69

(1950) 337 en metode til fremstilling av alginat fra grisetang og fingertare. Her felles alginatekstrakten med en saltsur kalsiumkloridoppløsning. (1950) 337 a method for the production of alginate from pig seaweed and finger kelp. Here, the alginate extract is combined with a hydrochloric acid calcium chloride solution.

Nyere undersøkelser har vist at løse-ligheten ved lav pH er vesentlig større More recent investigations have shown that the solubility at low pH is significantly greater

for alginsyre fra grisetang enn fra laminaria-artene Laminaria digitata (fingertare) og Laminaria hyperborea (stortare). Fel-ling av alginsyre fra grisetang på vanlig måte med syre gir en løs alginsyre-gel som er praktisk talt umulig å filtrere. Denne vanskeligheten er meget fremtredende for alginsyre fra grisetang og andre tangarter, for alginic acid from pig seaweed than from the laminaria species Laminaria digitata (finger kelp) and Laminaria hyperborea (big kelp). Precipitation of alginic acid from pig seaweed in the usual way with acid gives a loose alginic acid gel which is practically impossible to filter. This difficulty is very prominent for alginic acid from pigweed and other seaweed species,

men representerer ikke noe problem ved syrefelling av alginsyre fra f. eks. tare-artene fingertare og stortare. but does not represent any problem when acid precipitation of alginic acid from e.g. the kelp species finger kelp and large kelp.

Ved hjelp av foreliggende fremgangsmåte unngåes de nevnte ulemper ved fremstilling av alginater fra grisetang og andre tangarter. With the help of the present method, the aforementioned disadvantages are avoided when producing alginates from pig seaweed and other types of seaweed.

Det har nemlig vist seg at oppløselig-heten av alginsyre fra grisetang kan ned-markert grad ved utfelling av det ekstra-settes og filtrerbarheten av den bedres i herte alginat under tilsetning av syre i en slik mengde at den erholdte alginsyresus-pensjon får en pH-verdi innenfor bestemte grenser, nemlig i området 1,6—2,5, når man før eller etter fellingen tilsetter et oppløse-lig kaliumsalt til alginatekstrakten. Namely, it has been shown that the solubility of alginic acid from pig seaweed can be reduced to a marked degree by precipitation of the extra set and its filterability is improved in hardened alginate by adding acid in such an amount that the alginic acid suspension obtained has a pH -value within certain limits, namely in the range 1.6-2.5, when a soluble potassium salt is added to the alginate extract before or after precipitation.

Ved å arbeide på denne måte får man en fibrig tungtoppløselig alginsyre som er meget lett å filtrere By working in this way, you get a fibrous, poorly soluble alginic acid which is very easy to filter

Grunnen til at alginsyre fra grisetang oppfører seg så spesielt synes å være at denne alginsyre lag seg ved fraksjonering skille i en komponent som er helt løselig i syre og små saltmengder, og en annen komponent som oppfører seg normalt (dvs. har samme løselighetsforhold som alginsyre fra fingertare). Ved å tilsette salt har det så vist seg at den løselige komponent blir saltet ut og blir uløselig. The reason why alginic acid from pig seaweed behaves in such a special way seems to be that this alginic acid separates during fractionation into a component that is completely soluble in acid and small amounts of salt, and another component that behaves normally (i.e. has the same solubility ratio as alginic acid from finger kelp). By adding salt, it has been shown that the soluble component is salted out and becomes insoluble.

De beste resultater ved fremgangsmåten ifølge oppfinnelsen oppnåes når syreutfellingen utføres ved en pH mellom 1,7 og 2,3. Etter avpressing vil den frem-stilte alginsyre direkte kunne omsettes til alginater etter vanlig kjente metoder. Det er meget overraskende at kaliumioner vir-ker langt sterkere enn andre énverdige ioner f. eks. natrium. En slik forskjell i virkning på alginsyre mellom disse ioner er ikke kjent tidligere. The best results with the method according to the invention are obtained when the acid precipitation is carried out at a pH between 1.7 and 2.3. After pressing, the produced alginic acid can be directly converted into alginates according to commonly known methods. It is very surprising that potassium ions act far more strongly than other monovalent ions, e.g. sodium. Such a difference in effect on alginic acid between these ions has not been previously known.

Ved fremgangsmåten har det vist seg særlig fordelaktig at kaliumsaltkonsentra-sjonen er minst 0,07N. In the method, it has proven particularly advantageous that the potassium salt concentration is at least 0.07N.

Det foretrekkes at fremgangsmåten utføres ved en temperatur lavere enn 30°C, og særlig foretrukket er 10—15°C. It is preferred that the method is carried out at a temperature lower than 30°C, and 10-15°C is particularly preferred.

Ved å bruke de anførte fremgangsmå-ter på ekstrakt fra grisetang, vil en oppnå alginsyre av fibrig struktur som lett lar seg filtrere. Utbyttet vil også bli bedre enn ved vanlig syrefelling. By using the listed methods on extract from pigweed, alginic acid of a fibrous structure which can be easily filtered will be obtained. The yield will also be better than with normal acid precipitation.

Eksempel. Example.

5 kg tørket Ascophyllum nodosum fra Trondheimsfjorden ble forbehandlet med svovelsyre og ekstrahert med soda. Etter frafiltrering av uløste algerester, ble alginatekstrakten tilsatt kaliumklorid til. en konsentrasjon på 0,1N og felt med svovelsyre ved pH 2,1—2,0. Det ble oppnådd en 5 kg of dried Ascophyllum nodosum from the Trondheimsfjord was pre-treated with sulfuric acid and extracted with soda. After filtering off undissolved algae residues, potassium chloride was added to the alginate extract. a concentration of 0.1N and field with sulfuric acid at pH 2.1-2.0. A was achieved

fibrig alginsyre som etter frafiltrering in-neholdt 5 pst. tørrstoff. Alginsyren ble omsatt med soda. Utbyttet ble 870 g natri-umalginat. fibrous alginic acid which, after filtration, contained 5 percent dry matter. The alginic acid was reacted with soda. The yield was 870 g of sodium alginate.

Claims (1)

Fremgangsmåte til fremstiling av alginsyre fra Ascophyllum nodosum (grisetang) ved behandling av algen med syre og alkali og utfelling av alginsyren fra det ekstraherte alginat ved tilsetning av syre i en slik mengde at den erholdte alginsyre-suspensjon får en pH-verdi i området 1,6— 2,5, karakterisert ved at alginatekstrakten før eller etter fellingen med syre tilsettes et løselig kaliumsalt, særlig kaliumklorid i en slik mengde at konsent-rasjonen blir minst 0,07N.Process for the production of alginic acid from Ascophyllum nodosum (pig seaweed) by treating the alga with acid and alkali and precipitating the alginic acid from the extracted alginate by adding acid in such a quantity that the alginic acid suspension obtained has a pH value in the range of 1, 6— 2.5, characterized in that a soluble potassium salt, especially potassium chloride, is added to the alginate extract before or after precipitation with acid in such an amount that the concentration is at least 0.07N.
NO803675A 1980-03-05 1980-12-04 USE OF ALUMINUM CASTLE ALLOYS AND ALUMINUM KNITTED ALLOYS WASTE FOR THE MANUFACTURE OF ROLLING HALF PRODUCTS. NO155399C (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE3008358A DE3008358C2 (en) 1980-03-05 1980-03-05 Use of old scrap mixed from cast aluminum alloys and wrought aluminum alloys for the production of semi-finished rolled products

Publications (3)

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NO803675L NO803675L (en) 1981-09-07
NO155399B true NO155399B (en) 1986-12-15
NO155399C NO155399C (en) 1987-03-25

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ID=6096289

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Country Status (6)

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EP (1) EP0035055B1 (en)
JP (1) JPS6014828B2 (en)
AT (1) ATE4128T1 (en)
CA (1) CA1176084A (en)
DE (1) DE3008358C2 (en)
NO (1) NO155399C (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0069026B1 (en) * 1981-05-15 1985-08-28 Cegedur Societe De Transformation De L'aluminium Pechiney Method for the extrusion characteristics of aluminium alloys of the al-mg-si-type
JPS63117606U (en) * 1987-01-27 1988-07-29
US6004409A (en) * 1997-01-24 1999-12-21 Kaiser Aluminum & Chemical Corporation Production of high quality machinable tolling plate using brazing sheet scrap
US6607615B1 (en) 1997-10-31 2003-08-19 The Furukawa Electric Co., Ltd. Extruded material of aluminum alloy for structural members of automobile body and method of manufacturing the same
JP3403333B2 (en) * 1998-05-15 2003-05-06 古河電気工業株式会社 Aluminum plate material for automobile and its manufacturing method
CN102492878A (en) * 2011-11-15 2012-06-13 徐艳 Production method for aluminum alloy bicycle frame pipe for electric bicycle
CN112210700B (en) * 2020-10-09 2021-09-17 上海华峰铝业股份有限公司 Al-Mg-Mn-Si alloy, alloy plate strip and preparation method thereof
WO2023169657A1 (en) * 2022-03-08 2023-09-14 Montanuniversität Leoben Semi-finished product made of wrought aluminium alloy, the production and use thereof, and a product produced therefrom

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2156932C3 (en) * 1971-11-16 1978-11-16 Southwire Co., Carrollton, Ga. (V.St.A.) Process for the melt-metallurgical production of conductive aluminum alloys
GB1529305A (en) * 1974-11-15 1978-10-18 Alcan Res & Dev Method of producing metal alloy products
DE2647513A1 (en) * 1976-10-21 1978-04-27 Guenther Dipl Ing Fritz Aluminium sepd. from ferrous scrap - by melting the aluminium and magnetic removal of iron below its Curie temp.
DE2701452C2 (en) * 1977-01-14 1984-06-28 The Glacier Metal Co. Ltd., London Process for the recovery of at least one metal layer from multilayer waste material
US4169728A (en) * 1978-02-09 1979-10-02 Mitsubishi Kinzoku Kabushiki Kaisha Corrosion resistant bright aluminum alloy for die-casting

Also Published As

Publication number Publication date
NO155399C (en) 1987-03-25
JPS6014828B2 (en) 1985-04-16
DE3008358B1 (en) 1980-12-04
CA1176084A (en) 1984-10-16
EP0035055B1 (en) 1983-07-13
JPS56139667A (en) 1981-10-31
DE3008358C2 (en) 1981-07-09
ATE4128T1 (en) 1983-07-15
NO803675L (en) 1981-09-07
EP0035055A1 (en) 1981-09-09

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