NO115262B - - Google Patents

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NO115262B
NO115262B NO167398A NO16739867A NO115262B NO 115262 B NO115262 B NO 115262B NO 167398 A NO167398 A NO 167398A NO 16739867 A NO16739867 A NO 16739867A NO 115262 B NO115262 B NO 115262B
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parts
volume
weight
oxy
water
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NO167398A
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Norwegian (no)
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L Jeffreys
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Amsted Ind Inc
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D18/00Pressure casting; Vacuum casting
    • B22D18/04Low pressure casting, i.e. making use of pressures up to a few bars to fill the mould
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22CFOUNDRY MOULDING
    • B22C9/00Moulds or cores; Moulding processes
    • B22C9/06Permanent moulds for shaped castings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D7/00Casting ingots, e.g. from ferrous metals
    • B22D7/06Ingot moulds or their manufacture
    • B22D7/08Divided ingot moulds

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Continuous Casting (AREA)
  • Molds, Cores, And Manufacturing Methods Thereof (AREA)
  • Steroid Compounds (AREA)
  • Casting Devices For Molds (AREA)

Description

Fremgangsmåte til partiell fjernelse av oksogrupper. Method for the partial removal of oxo groups.

En av de vanligste metoder til reduktiv One of the most common methods of reductive

fjernelse av oksogrupper er framgangsmåten ifølge Wolff-Kishner, som senere ble modifisert og forbedret av Huang-Minlon. Ved den siste reaksjon kokes karbonylfor-bindelsen i di- eller trietylenglykol sammen med 10 pst. alkalihydroksyd og et overskudd av hydrazinhydrat ca. y2 time ved tilbakeløpskjøler. Deretter destillerer man så lenge fra oppløsningsmiddelblan-dingen inntil resten har en koketemperatur på ca. 200°, og deretter kokes noen timer med tilbakeløpskjøler. removal of oxo groups is the procedure according to Wolff-Kishner, which was later modified and improved by Huang-Minlon. In the last reaction, the carbonyl compound is boiled in di- or triethylene glycol together with 10 per cent alkali hydroxide and an excess of hydrazine hydrate approx. y2 hour at reflux cooler. The solvent mixture is then distilled until the residue has a boiling temperature of approx. 200°, and then boiled for a few hours with a reflux cooler.

Også den angitte forbedrede utførelses. Also the indicated improved execution.

form for reaksjonen fører ved framstillin-gen av monooksoforbindelser av a-dioksoforbindelser fra steroidrekken henholdsvis deres enoler, særlig lM2-diketoner henholdsvis A9'1:|-ll-oksy-12-ketoner til dår-lige resultater. Således fjernes ikke bare okso-gruppen i 12-stilling, men også 11-oksogruppen reduseres til 11-oksygruppen eller elimineres fullstendig. form of the reaction leads to poor results in the production of monooxo compounds of α-dioxo compounds from the steroid series or their enols, in particular 1M2-diketones or Δ9'1:|-11-oxy-12-ketones. Thus, not only is the oxo group in the 12-position removed, but also the 11-oxo group is reduced to the 11-oxy group or eliminated completely.

Det ble nå gjort den overraskende It was now done by surprise

iakttagelse at ved omsetningen av 11,12-dioksoforbindelser fra steroidrekken, deres enoler eller enolater med hydrazin eller de_ res derivater kan den ene oksogruppe par-tielt fjernes allerede ved vesentlig lavere temperaturer. Det er altså ikke nødvendig at det opphetes til en temperatur ved hvilken alle laverekokende deler avdestillerer. Derved er det mulig å gjennomføre den partielle fjernelse av den ene oksogruppe under vesentlig mildere betingelser og opp-nå monooksoforbindelsene i godt utbytte. Den nye framgangsmåte karakteriseres ved at man oppheter de nevnte utgangsstoffer med hydrazin eller dets derivater i nær- observation that in the reaction of 11,12-dioxo compounds from the steroid series, their enols or enolates with hydrazine or their derivatives, the one oxo group can be partially removed already at significantly lower temperatures. It is therefore not necessary for it to be heated to a temperature at which all lower-boiling parts distil. Thereby, it is possible to carry out the partial removal of the one oxo group under significantly milder conditions and obtain the monooxo compounds in good yield. The new method is characterized by heating the aforementioned starting materials with hydrazine or its derivatives in close

vær av en basisk alkaliforbindelse til en temperatur ved hvilken det inntrer kvel-stof f utvikling ved høyst 160°. weather of a basic alkali compound to a temperature at which nitrogen evolution occurs at not more than 160°.

Som utgangsstoffer finner anvendelse a-dioksoforbindelser av steroidrekken, som inneholder to nabo-oksogrupper i 11- og 12-stilling, henholdsvis de tilsvarende enoler, slik som A9'11-ll-oksy-12-ketoner eller deres enolater, f. eks. metall-enolater, enolacylat eller enoleter. Steroidene kan f. eks. være avledet av østran-, androstan-, testan-, etiocholan-, pregnan-, spirostan-, furostan-, bufostan-, cholan-, cholestan-, nor. og bisnor-cholestan- eller ergostan-rekken henholdsvis deres stereoisomere, og foruten de to nabo-oksogrupper inneholde videre substituenter i de vanlige stillinger. As starting materials, α-dioxo compounds of the steroid series are used, which contain two neighboring oxo groups in the 11- and 12-position, respectively the corresponding enols, such as α9'11-11-oxy-12-ketones or their enolates, e.g. metal enolates, enolacylate or enolet. The steroids can e.g. be derived from estran-, androstane-, testane-, etiocholan-, pregnan-, spirostane-, furostane-, bufostane-, cholan-, cholestane-, nor. and the bisnor cholestane or ergostane series, respectively their stereoisomers, and besides the two neighboring oxo groups contain further substituents in the usual positions.

Følgende delformel av steroidkjernen The following partial formula of the steroid nucleus

er felles for disse utgangsstoffer are common to these starting materials

Omsetningen ifølge framgangsmåten foregår med hydrazin eller dets derivater slik som hydrazinhydrat eller semikarbazid henholdsvis deres salter, f. eks. acetater, klorider eller sulfater, sammen med basiske alkalimetallforbindelser, fremfor alt alkali. metallhydroksyder eller -alkoholater, slik som natrium, eller kaliumhydroksyd, -me-tylat eller -etylat. Reaksjonen utføres for-trinsvis i organiske oppløsningsmidler, sær. lig i mono- eller polyoksyforbindelser, f. eks. glykol-, di- eller polyetylenglykol, pro-pylenglykol, butanol eller benzylalkohol, videre også i kullvannstoffer, slik som xylol eller tetralin. Hensiktsmessig oppheter man ved en temperatur ved hvilken allerede kvelstoff utvikles sterkt, som ved 120 —150°, og så lenge inntil det har dannet seg den beregnede mengde kvelstoff for fjernelse av en oksogruppe. The reaction according to the method takes place with hydrazine or its derivatives such as hydrazine hydrate or semicarbazide or their salts, e.g. acetates, chlorides or sulfates, together with basic alkali metal compounds, above all alkali. metal hydroxides or alcoholates, such as sodium or potassium hydroxide, methylate or ethylate. The reaction is preferably carried out in organic solvents, esp. lig in mono- or polyoxy compounds, e.g. glycol, di- or polyethylene glycol, propylene glycol, butanol or benzyl alcohol, further also in hydrocarbons, such as xylol or tetralin. It is expedient to heat at a temperature at which nitrogen is already strongly developed, such as at 120-150°, and for as long as the calculated amount of nitrogen has formed for the removal of an oxo group.

Oppfinnelsen beskrives i de følgende eksempler. Mellom vektdel og volumdel består det samme forhold som mellom gram og ems. Temperaturene er angitt i Celsiusgrader. The invention is described in the following examples. Between weight part and volume part there is the same relationship as between grams and ems. The temperatures are indicated in degrees Celsius.

Eksempel 1: Example 1:

40,4 vektdeler 3 a-oksy-ll,12-diketo-cholansyre, som delvis foreligger i enolform, tilsettes 20 volumdeler 10-n. natronlut, 200 volumdeler etylenglykol og 20 volumdeler hydrazinhydrat. Man oppvarmer 2 timer under omrøring til 135—145°, idet det avspaltes 2200 volumdeler kvelstoff. Etter avkjøling innføres den med 250 volumdeler vann f or tynnede reaksjonsoppløs. ning i 300 volumdeler 2-n. saltsyre. Det utfelte og fra moderluten adskilte reaksjonsprodukt oppløser man i 500 volumdeler 5-n. natronlut, rører oppløsningen ut med ki-selgur eller filterasbest, filtrerer den og lar den strømme inn i 200 volumdeler eddik-syre i 300 volumdeler vann. Man får 37,2 vektdeler 3 a-oksy-ll-keto-cholansyre med sm.p. = 215—218°. 40.4 parts by weight of 3α-oxy-11,12-diketocholanic acid, which is partly present in enol form, are added to 20 parts by volume of 10-n. caustic soda, 200 parts by volume ethylene glycol and 20 parts by volume hydrazine hydrate. It is heated for 2 hours with stirring to 135-145°, as 2,200 parts by volume of nitrogen are split off. After cooling, it is introduced with 250 parts by volume of water for the diluted reaction solution. ning in 300 volume parts 2-n. hydrochloric acid. The precipitated and separated reaction product from the mother liquor is dissolved in 500 parts by volume of 5-n. caustic soda, stirs the solution with diatomaceous earth or filter asbestos, filters it and allows it to flow into 200 parts by volume of acetic acid in 300 parts by volume of water. 37.2 parts by weight of 3α-oxy-ll-keto-cholanic acid with m.p. = 215-218°.

Eksempel 2: Example 2:

44,6 vektdeler A9'13-3 a, ll-dioksy-12-keto-cholensyre-3-acetat oppvarmes sammen med 30 volumdeler 10-n. natronlut, 200 volumdeler etylenglykol og 20 volumdeler hydrazinhydrat under omrøring i 2—3 timer til 130°, idet det avspaltes 2200 volumdeler kvelstoff. Man fortynner den av-kjølte reaksjonsoppløsning med 250 volumdeler vann og lar denne strømme inn i 300 volumdeler 2-n. saltsyre. Det utfelte reaksjonsprodukt suges fra, vaskes og tørkes. Man får 39 vektdeler 3 a-oksy-ll-keto-cholansyre med sm.p. = 212—215°. 44.6 parts by weight of A9'13-3 a, 11-dioxy-12-keto-cholenic acid-3-acetate are heated together with 30 parts by volume of 10-n. caustic soda, 200 parts by volume of ethylene glycol and 20 parts by volume of hydrazine hydrate with stirring for 2-3 hours at 130°, as 2200 parts by volume of nitrogen are split off. The cooled reaction solution is diluted with 250 parts by volume of water and allowed to flow into 300 parts by volume of 2-n. hydrochloric acid. The precipitated reaction product is sucked off, washed and dried. 39 parts by weight of 3α-oxy-ll-keto-cholanic acid with m.p. = 212-215°.

Utgangsstoffet fåes ved oppløsning av The starting material is obtained by dissolving

3 a-oksy-ll,12-diketo-cholansyre i den 3-5 ganger så store mengde iseddik på kokende vannbad og avkjøling, sm.p. = 156—158° 3 a-oxy-11,12-diketo-cholanic acid in the 3-5 times larger amount of glacial acetic acid on a boiling water bath and cooling, m.p. = 156-158°

[a]D + 85° (i dioksan). [a]D + 85° (in dioxane).

Eksempel 3: Example 3:

50,2 vektdeler A9-ii-3 a,ll-diacetoksy-12-keto-cholensyremetylester oppvarmes sammen med 50 volumdeler 10-n. natronlut, 20 volumdeler hydrazinhydrat og 200 volumdeler etylenglykol under omrøring til 125—130° inntil det avspaltes 2200 volumdeler kvelstoff. Deretter avkjøler man, fortynner med 200 volumdeler vann og lar strømme inn i 300 volumdeler 2-n. saltsyre. Det utfelte reaksjonsprodukt suges fra, vaskes med vann og tørkes. Man får 38 vektdeler 3 a-oksy-ll-keto-cholansyre med sm.p. = 214—218°. 50.2 parts by weight of A9-ii-3 a,ll-diacetoxy-12-keto-cholenic acid methyl ester are heated together with 50 parts by volume of 10-n. caustic soda, 20 parts by volume of hydrazine hydrate and 200 parts by volume of ethylene glycol with stirring at 125-130° until 2200 parts by volume of nitrogen are split off. It is then cooled, diluted with 200 parts by volume of water and allowed to flow into 300 parts by volume of 2-n. hydrochloric acid. The precipitated reaction product is sucked off, washed with water and dried. 38 parts by weight of 3α-oxy-ll-keto-cholanic acid with m.p. = 214-218°.

Eksempel 4: Example 4:

56,7 vektdeler A23-3 a-acetoksy-11,12-diketo-24,24-difenylcholen, som delvis foreligger i enolform, oppvarmer man sammen med 50 volumdeler 10-n. natronlut, 200 volumdeler dietylenglykol og 20 volumdeler hydrazinhydrat under omrøring til 124— 125° inntil det avspaltes 2200 volumdeler kvelstoff. Deretter deles reaksjonsblandingen i vann, og det utfelte reaksjonsprodukt ekstraheres med eter, eteroppløsningen vaskes med vann, tørkes og inndampes. Man oppløser resten (51 vektdeler) i 100 volumdeler pyridin og tilsetter 50 volumdeler acetanhydrid. Etter henstand natten over konsentreres oppløsningen i vakuum, acetyleringsproduktet opptas i eter, vaskes etter hverandre med fortylnnet saltsyre, natriumbikarbonat og vann. Etter tørkning konsentrerer man til et lite volum, tilsetter 250 volumdeler etanol, avdamper 70 volumdeler etanol og lar avkjøle. Det krystalliserer 48,2 vektdeler A 23-3 a-acetoksy-11-keto-24,24-difenyl-cholen, sm.p. = 168 — 169°, [a]D + 77° (i dioksan). 56.7 parts by weight of A23-3 α-acetoxy-11,12-diketo-24,24-diphenylcholine, which is partly present in enol form, is heated together with 50 parts by volume of 10-n. caustic soda, 200 parts by volume of diethylene glycol and 20 parts by volume of hydrazine hydrate with stirring to 124-125° until 2200 parts by volume of nitrogen are split off. The reaction mixture is then divided into water, and the precipitated reaction product is extracted with ether, the ether solution is washed with water, dried and evaporated. The residue (51 parts by weight) is dissolved in 100 parts by volume of pyridine and 50 parts by volume of acetic anhydride are added. After standing overnight, the solution is concentrated in vacuo, the acetylation product is taken up in ether, washed successively with dilute hydrochloric acid, sodium bicarbonate and water. After drying, concentrate to a small volume, add 250 parts by volume of ethanol, evaporate 70 parts by volume of ethanol and allow to cool. It crystallizes 48.2 parts by weight of A 23-3 α-acetoxy-11-keto-24,24-diphenyl-choline, m.p. = 168 — 169°, [a]D + 77° (in dioxane).

Det som utgangsmateriale anvendte A23-3a-acetoksy-ll,12-diketo-24,24-di-fenyl-cholen kan fremstilles som følger: 160 vektdeler wismuth-trioksyd, 160 volumdeler iseddik og 1500 volumdeler klorbensol opphetes under omrøring til kok-ning, og innen 1 time avdestilleres 300 volumdeler væske inntil destillasjonstempe-raturen overstiger 120°. Deretter tilsettes 71,6 vektdeler A'23-3a-acetoksy-12flj-oksy-ll-keto-24,24-difenyl-cholen oppløst i 50 volumdeler klorbensol og 300 volumdeler iseddik. Under omrøring avdestilleres nok en gang 300 volumdeler oppløsningsmiddel i løpet av 1—1 y. 2 time, inntil destillasjons-temperaturen overstiger 120°, hvorved far-gen på reaksjonsblandingen slår om fra hvit til grå. Deretter avkjøler man, filtrerer ,inndamper det klare filtrat og krystalliserer resten av isopropyleter. Man får 48,5 vektdeler A23-3ct-acetoksy-ll,12-diketo-24,24-difenyl-cholen med sm.p. = 142—144° The A23-3a-acetoxy-11,12-diketo-24,24-di-phenyl-choline used as starting material can be prepared as follows: 160 parts by weight of bismuth trioxide, 160 parts by volume of glacial acetic acid and 1500 parts by volume of chlorobenzene are heated while stirring to boiling , and within 1 hour 300 parts by volume of liquid are distilled off until the distillation temperature exceeds 120°. 71.6 parts by weight of A'23-3a-acetoxy-12flj-oxy-11-keto-24,24-diphenyl-choline dissolved in 50 parts by volume of chlorobenzene and 300 parts by volume of glacial acetic acid are then added. While stirring, 300 parts by volume of solvent are once again distilled off over the course of 1-1 y. 2 hours, until the distillation temperature exceeds 120°, whereby the color of the reaction mixture changes from white to grey. The clear filtrate is then cooled, filtered, evaporated and the remainder crystallized from isopropyl ether. 48.5 parts by weight of A23-3ct-acetoxy-11,12-diketo-24,24-diphenyl-choline with m.p. = 142-144°

[a?<j>f = + 100° (c = 1 i dioksan). [a?<j>f = + 100° (c = 1 in dioxane).

Moderlutene gir etter inndampning og acetylering av resten med kokende acetanhydrid 19,4 vektdeler A23-3a-acetoksy-ll,12-diketo-24,24-difenyl-cholen-ll-enol-acetat med sm.p. = 165—167°, [a] f = + 125° (c = 1 i dioksan). After evaporation and acetylation of the residue with boiling acetic anhydride, the mother liquors give 19.4 parts by weight of A23-3a-acetoxy-11,12-diketo-24,24-diphenyl-cholen-11-enol-acetate with m.p. = 165—167°, [a] f = + 125° (c = 1 in dioxane).

Eksempel 5: 44,4 vektdeler 3[3-oksy-ll,12-diketo-iso-allospirostan, som delvis foreligger som enol, oppvarmes sammen med 20 volumdeler 10-n. natronlut, 200 volumdeler etylenglykol og 20 volumdeler hydrazinhydrat under omrøring til 130—135° inntil det er avspaltet 2200 volumdeler kvelstoff. Den avkjølte oppløsning fortynner man med vann og ekstraherer det utfelte reaksjonsprodukt med en eter-kloroform-blanding Example 5: 44.4 parts by weight of 3[3-oxy-11,12-diketo-iso-allospirostane, which is partly present as enol, is heated together with 20 parts by volume of 10-n. caustic soda, 200 parts by volume of ethylene glycol and 20 parts by volume of hydrazine hydrate while stirring to 130-135° until 2200 parts by volume of nitrogen have been split off. The cooled solution is diluted with water and the precipitated reaction product is extracted with an ether-chloroform mixture

(4 : 1). Ekstraktet vaskes deretter med vann, deretter tørkes og inndampes. Fra eter- eller eter-pentan-oppløsningen av resten krystalliserer 29,7 vektdeler av 3(3-oksy-ll-keto-iso-allo-spirostan med sm.p. = 216—227°. Ved omkrystallisering stiger smeltepunktet til 229—232°, [a]n —29° (i kloroform). (4 : 1). The extract is then washed with water, then dried and evaporated. From the ether or ether-pentane solution of the residue crystallizes 29.7 parts by weight of 3(3-oxy-11-keto-iso-allo-spirostane with m.p. = 216—227°. On recrystallization the melting point rises to 229— 232°, [a]n —29° (in chloroform).

Claims (2)

1. Framgangsmåte til partiell fjernelse av oksogrupper fra 11,12-dioksoforbindelser fra steroidrekken, karakterisert ved at man oppheter disse, deres enoler eller enolater med hydrazin eller dets derivater i nærvær av en basisk alkaliforbindelse til en temperatur ved hvilken det inntrer kvel-stoffutvikling, inntil høyst 160°.1. Process for the partial removal of oxo groups from 11,12-dioxo compounds from the steroid series, characterized by heating these, their enols or enolates with hydrazine or its derivatives in the presence of a basic alkali compound to a temperature at which nitrogen evolution occurs, up to a maximum of 160°. 2. Framgangsmåte ifølge påstand 1— 2, karakterisert ved at man arbeider ved en temperatur på 120—150°.2. Method according to claims 1-2, characterized by working at a temperature of 120-150°.
NO167398A 1966-04-13 1967-03-21 NO115262B (en)

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ES (1) ES338704A1 (en)
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US3646991A (en) * 1970-06-22 1972-03-07 Armsted Ind Inc Top block shift
FR2534505A1 (en) * 1982-10-14 1984-04-20 Vinogradov Viktor Upset-forming machine
FR2642682B1 (en) * 1989-01-16 1991-05-17 Creusot Loire DEVICE FOR SUPPORTING AND ADJUSTING THE POSITION OF AN UPPER SPACER OF A DIE MOLD UNDER PRESSURE OF FLAT METAL PRODUCTS SUCH AS SLABS
FR2642685B1 (en) * 1989-01-16 1991-05-17 Creusot Loire PRESSURE CASTING PROCESS FOR FLAT METAL PRODUCTS SUCH AS SLABS AND DEVICE FOR CARRYING OUT SAID METHOD
FR2642683B1 (en) * 1989-01-16 1991-05-17 Creusot Loire REAR SPACER OF A PRESSURE CAST MOLD OF FLAT METAL PRODUCTS SUCH AS SLABS

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US2289928A (en) * 1940-12-14 1942-07-14 Parker White Metal & Machine C Die casting machine
FR899292A (en) * 1942-10-29 1945-05-25 Ig Farbenindustrie Ag Device for controlling the recoil movement of the movable mold carrier in hydraulic die-casting machines
US3263277A (en) * 1963-06-04 1966-08-02 Mannesmann Meer Ag Hold-shut device for injection molding
US3340926A (en) * 1964-07-14 1967-09-12 Sylvester Entpr Casting apparatus
US3340798A (en) * 1965-01-28 1967-09-12 Cincinnati Butchers Supply Co Mold for food products

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