SI9200291A - New method for the production of aminoalkanphosphonic acids, their salts and/or esters - Google Patents

New method for the production of aminoalkanphosphonic acids, their salts and/or esters Download PDF

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SI9200291A
SI9200291A SI19929200291A SI9200291A SI9200291A SI 9200291 A SI9200291 A SI 9200291A SI 19929200291 A SI19929200291 A SI 19929200291A SI 9200291 A SI9200291 A SI 9200291A SI 9200291 A SI9200291 A SI 9200291A
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acid
hydrogen atom
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Georges Axiotis
Helene Deweerdt
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Rhone-Poulenc Agrochimie
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/38Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
    • C07F9/3804Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)] not used, see subgroups
    • C07F9/3808Acyclic saturated acids which can have further substituents on alkyl
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/38Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/38Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
    • C07F9/40Esters thereof
    • C07F9/4003Esters thereof the acid moiety containing a substituent or a structure which is considered as characteristic
    • C07F9/4006Esters of acyclic acids which can have further substituents on alkyl

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Abstract

The present invention relates to a new process for obtaining alpha -aminoalkanephosphonic acids and/or salts or esters of general formula (I): <IMAGE> with R1, R2, which are identical or different, chosen from a hydrogen atom, a linear or branched alkyl group with one to six carbon atoms, or an alkali metal or alkaline-earth metal atom. R3 = a hydrogen atom or an alkyl, cycloalkyl, aryl or aralkyl group, it being possible for these groups to be optionally substituted by one or a number of heteroatoms, preferably halogen. R4 = a hydrogen atom or a linear or branched alkyl group with 1 to 4 carbon atoms.

Description

NOV POSTOPEK ZA PRIDOBIVANJE AHINOALKANFOSFONSKIH KISLIN,A NEW PROCEDURE FOR THE ACHIEVEMENT OF AHINOALKANPHOSPHONIC ACIDS,

NJIHOVIH SOLI IN/ALI ESTROVTHEIR SALTS AND / OR ESTERS

NOV POSTOPEK ZA PRIDOBIVANJE AMINOALKANFOSFONSKIH KISLIN,A NEW PROCEDURE FOR THE PREPARATION OF AMINO-ALKANPHOSPHONIC ACIDS,

NJIHOVIH SOLI IN/ALI ESTROVTHEIR SALTS AND / OR ESTERS

Ta izum se nanaša na nov postopek za pridobivanje cCaminoalkanfosfonskih kislin in/ali soli ali estrov splošne formule(I) :The present invention relates to a novel process for the preparation of cCaminoalkanephosphonic acids and / or salts or esters of general formula (I):

RjO NHR4 \ i 4 RjO NHR 4 \ and 4

P -CH — Ro / II 5 P -CH - Ro / II 5

R2CT 0 (I) z R*, R2, identičnima ali različnima, ki smo jih izbrali med vodikovim atomom, nerazvejeno ali razvejeno alkilno skupino z enim do šestimi atomi ogljika, in enim atomom alkalijskih ali zamljoalkalijskih kovin.R 2 CT 0 (I) with R *, R 2 identical or different, selected from a hydrogen atom, a straight or branched alkyl group of one to six carbon atoms, and one atom of alkali or alkaline earth metals.

Ra = atom vodika, ali alkilna, cikloalkilna, arilna ali aralkilna skupina, pri tem te skupine lahko vsebujejo en heteroatom in so eventuelno lahko substituirane z enim ali več atomi, predvsem s halogenom.Ra = a hydrogen atom, or an alkyl, cycloalkyl, aryl or aralkyl group, these groups may contain one heteroatom and may be optionally substituted by one or more atoms, in particular halogen.

R^ = atom vodika, nerazvejena ali razvejena alkilna skupina, z 1 do 4 atomi ogljika.R ^ = hydrogen atom, unbranched or branched alkyl group, having 1 to 4 carbon atoms.

Produkti formule (I) so znani in se uporabljajo kot fungicidi (evropski patent 0153284 in USP 4994447 inThe products of formula (I) are known and used as fungicides (European patent 0153284 and USP 4994447 and

4888330). Produkt, v katerem so R*, Rz in R^ atom vodika in4888330). A product in which R *, R z and R ^ are a hydrogen atom and

R» etil, je ampropilfos, komerci aliziran, ki se lahko uporablja za zdravljenje listov ali semena.R »ethyl is ampropylphos, commercialized, which can be used to treat leaves or seeds.

Dokazano je, da načini za pridobivanje produktov opisani v zgoraj omenjenih patentih ne omogočajo industrijsko proizvodnjo teh produktov, posebej zaradi katalitičkih procesov s hidrogenizacijo, pogojev zvišane temperature in pritiska, in preveč dolgih časov reakcije.It has been demonstrated that the methods of obtaining the products described in the aforementioned patents do not allow the industrial production of these products, especially due to catalytic processes by hydrogenation, high temperature and pressure conditions, and too long reaction times.

Eden cilj tega izuma je, torej, priti do teh spojin na bolj ekonomičen način, kot so prej opisani načini pridobivanja.One object of the present invention, therefore, is to obtain these compounds in a more economical manner than the preparation methods described above.

Drugi cilj izuma je pridobivanje spojin formule (I) pod veliko milejšimi pogoji hidrolize kot so že znani in predvsem z veliko krajšim časom reakcije.Another object of the invention is to provide compounds of formula (I) under much milder hydrolysis conditions than already known and, in particular, with a much shorter reaction time.

Se več, tretji cilj tega izuma je uporaba postopka, ki omogoča boljšo kontrolo vodnih i plinskih -fluidov.Moreover, a third object of the present invention is to use a process that allows for better control of aqueous and gas fluids.

Končno, še en cilj izuma je pridobivanje spojine formule (I) z optimaliziranim dobitkom in čistoto.Finally, another object of the invention is to provide a compound of formula (I) in optimized yield and purity.

Postopek za pripravo (R,S) 1 aminol kan-fos-fonskih kislin ali estrov in soli poteka v treh (kisline) ali štirih (estri, soli) stopnjah, ki jih lahko shematiziramo na sledeči način:The process for the preparation of (R, S) 1 aminol can-phosphonic acids or esters and salts is carried out in three (acids) or four (esters, salts) stages, which can be schematized as follows:

a)a)

FUFU

H + R4NH2 H + R 4 NH 2

R3 _CH —NR4 + H2OR 3 _CH —NR 4 + H 2 O

b)b)

R3-CH = NR4 +R 3 -CH = NR 4 +

R,0 1 \R, 0 1 \

P/ r2o oP / r 2 oo

RlO^RlO ^

P /H r2o o chnhr4 lP / H r 2 oo chnhr 4 l

*3* 3

c) R.Oc) R.O

PP

chnhr4 + H2SO4->chnhr 4 + H 2 SO 4 ->

HO r2o oHO r 2 oo

p — chnh2 p - chnh 2

d)d)

CHNH2 + nR5OH -P r5o o chnh2 CHNH 2 + nR 5 OH -P r 5 oo chnh 2

z R= = RT in/ali Rz, ali atom alkalijske kovine, predvsem Na ali K, in n = 1 ali 2.with R = = R T and / or R z , or an alkali metal atom, in particular Na or K, and n = 1 or 2.

Reakcijo a) med enim primarnim aminom in enim karboni1ni m derivatom (ali zaščiteno obliko karbonilnega derivata, se pravi acetalom, hemiacetalom ali dioksolanom in je, torej, treba izpeljati reakcijo v kisli sredini, da bi pripravili karboni1) lahko napišemo po shemi:The reaction a) between one primary amine and one carbonyl derivative (or a protected form of a carbonyl derivative, i.e. acetal, hemiacetal, or dioxolane and, therefore, an acidic reaction must be carried out in order to prepare the carbonyls) can be written as follows:

Ri_C _H J HRi_C _H J H

II + R4NH2 _R3 — CH— NR4 + H20II + R 4 NH 2 _R 3 - CH— NR 4 + H 2 0

Reakcijo med aldehidom, na primer propanalom, in primarnim aminom, na primer terc—buti1 aminom, izpeljemo v cikloheksanu na sobni temperaturi (20°C). Tako dobimo odgovarjajoči imin, na primer terc-buti1propanimin, ki je samo vmesna spojina. Njo lahko, torej, uporabimo ne, da bi je dodatno tretirali, v naslednji stopnji reakcije (etapa b), toda ta vodi povišanemu procentu onesnaženosti. Destiliran imin omogoča boljšo selektivnost, toda v tem primeru se zaradi destilacije izgubi dober del (30%) sintetiziranega imina.The reaction between an aldehyde, for example propanal, and a primary amine, such as tert-butyl amine, is carried out in cyclohexane at room temperature (20 ° C). This gives the corresponding imine, for example tert-butylpropanamine, which is an intermediate only. It can therefore be used not to treat it further in the next stage of reaction (step b), but this leads to an increased percentage of contamination. Distilled imine provides better selectivity, but in this case, a good portion (30%) of the synthesized imine is lost due to distillation.

Vodo, ki se tvori in ki je odgovorna za povišan procent onesnaženosti, lahko enostavno odlijemo če stopnjo a) izpeljemo v organskem topil.u.The water that is responsible for the increased percentage of contamination can be easily drained if step a) is carried out in an organic solvent.u.

S topilom kot je cikloheksan odstranimo 95% te vode, ki se tvori, medtem ko s uporabo diklorometana lahko odstranimo samo 61% od količine vode, ki je nastala, s toluenom 83% in s zmesjo toluen-natrijev karbonat 92%.A solvent such as cyclohexane removes 95% of this water, while using dichloromethane, only 61% of the amount of water produced is removed with toluene 83% and with a mixture of toluene sodium carbonate 92%.

Preostalo vodo lahko odstranimo z azeotropično destilacijo, toda za to je treba izbrati tako temperaturo (80°C s cikloheksanom), da se pri tem imin degradira. Zaradi tega torej rajši delamo s cik 1oheksanom kot topilom in vodo, ki se tvori, enostavno odlijemo.The remaining water can be removed by azeotropic distillation, but to do so, a temperature (80 ° C with cyclohexane) must be selected so that the imine is degraded. Therefore, we prefer to work with cyclohexane as a solvent, and the water that is formed is easily cast.

Stopnjo b) kondenzacije imina, ki smo ga pridobili v a), z d i al ki Ι-fosfatom, izpeljemo po reakciji:The degree of b) condensation of the imine obtained in a) with d and al k which is Ι-phosphate is carried out after the reaction:

RiO R,0 1 \ 1 \RiO R, 0 1 \ 1 \

R3— CH=:NR4 + P---H -> P -CHNHR,R 3 - CH =: NR 4 + P --- H -> P -CHNHR,

Z 11 Z n t 4 r2o o r2o o r3 Z 11 Z nt 4 r 2 oor 2 oor 3

Stopnje a) in b) smo realizirali v organskem topilu, takem kot je cikloheksan, diklorometan ali toluen. Organsko raztopino imina, ki smo ga pripravili v stopnji a) smo prilili na dialki 1fosfit, ki je bil čist ali pa v organski raztopini.Steps a) and b) were realized in an organic solvent such as cyclohexane, dichloromethane or toluene. The organic solution of imine prepared in step a) was poured into dialka 1 phosphite, which was pure or in organic solution.

Stopnjo c) hidrolize diestra, ki smo ga pridobili in precipitaci jo nastale dikisline smo izpeljali po shemi:Stage c) hydrolysis of the diester obtained and the precipitations of the resulting diacids were carried out according to the scheme:

RiO Z IIRiO Z II

P — CHNHR4 + HoSOa II I * z P - CHNHR 4 + HoSOa II I * z

R2O O RjR2O O Rj

HOHO

Diestersko spojino, ki smo je pridobili po stopnji b) smo izolirali in uporabili kot tako. Toda, spojine za katere se je pokazalo, da so bolj prikladne kot fungicidi, so kisline in soli, se pravi spojine za katere sta Ri in/ali R3 izbrana izmed alkalijskih ali zemljoalkalijskih kovin. Ker je kislina, torej, prikladna ali kot taka, ali kot vmesni produkt v pridobivanju soli, praktično vedno realiziramo to stopnjo hidrolize, ki ji sledi precipitacija nastale fosfonske kisline.The diester compound obtained after step b) was isolated and used as such. However, a compound which has been shown to be more suitable as fungicides, the acids and salts, that is a compound for which Ri and / or R 3 is selected from alkali or alkaline earth metal. Since acid, therefore, is suitable either as such or as an intermediate in salt production, it is practically always possible to realize this degree of hydrolysis followed by the precipitation of the phosphonic acid formed.

Pogoji hidrolize c) so bolj blagi kot tisti prej opisani.The hydrolysis conditions c) are milder than those described previously.

Pravzaprav smo to stopnjo že poznali, kot elementarno reakcijo kisle hidrolize 1-aminoalkantosfonskega estra, toda s uporabo bromovodikove kisline, pod pritiskom in pri temperaturi od 175-180°C, v trajanju 48 ur.In fact, this step was already known as the elemental reaction of acid hydrolysis of 1-aminoalkanthosphonic ester, but using hydrobromic acid, under pressure and at a temperature of 175-180 ° C, for 48 hours.

Uporaba po izumu 2 do 5 ekvivalentov žveplove (VI) kisline po molu diestra omogoča realizacijo hidrolize v nekaj urah (4 do 6) pri atmosferskem pritisku in temperaturi reda 120The use according to the invention of 2 to 5 equivalents of sulfuric (VI) acid per mole of diester enables the hydrolysis to be carried out in a few hours (4 to 6) at atmospheric pressure and temperature of the order of 120

140°C.140 ° C.

V teh pogojih se sprostita dve kislinski funkciji, kakor tudi sekundarni amin, ki zopet daje NH3. Pridobivanje spojin v katerih je R^ različno od atoma vodika je možno če reakcijo izpeljemo pri nižjih temperaturah, na primer pri približno 80°C. V tem primeru se tvorita samo dve kislinski funkci ji.Under these conditions, two acidic functions are released as well as a secondary amine which again gives NH 3 . The preparation of compounds in which R 2 is other than a hydrogen atom is possible if the reaction is carried out at lower temperatures, for example at about 80 ° C. In this case, only two acid functions are formed.

Eventuelno stopnjo d) pretvarjanja v sol — esterifikači je dikisline pripravljene v c) prikaže sledeča reakcija:Eventual stage d) of conversion to salt - esterifiers is the diacids prepared in c) the following reaction is displayed:

HOHO

HOHO

PP

IIII

CHNH? + nRcOH->CHNH ? + nRcOH->

i K3and K 3

R5o^R 5 o ^

P — CHNH? /ii i z r5o o r3 kjer je R= = Rx in/ali R2, predvsem Na ali K, in π = 1 aliP - CHNH ? / ii i with r 5 oor 3 where R = = R x and / or R 2 , in particular Na or K, and π = 1 or

2. Kadar je n = 1, je eden od dveh R= atom vodika.2. When n = 1, one of the two R = is a hydrogen atom.

Sledeči primeri ilustrirajo ta izum na način, ki ni omejevalen.The following examples illustrate the invention in a non-limiting manner.

PRIMER 1: Sinteza aminopropanfosfonske kisline (postopek z dietilfosfitom 1).EXAMPLE 1 Synthesis of Aminopropanophosphonic Acid (Diethylphosphite 1 Procedure).

a) Prilijemo 3 mola (174 g) propanala, v eni uri, na 3 mola (217 g) terc-buti1amina, ki se nahaja v bučki pri sobni temperaturi (20°C). Po koncu prilivanja dodamo 373 g cik 1oheksana, da bi odlili vodo, ki se tvori. Tako pridobimoa) Add 3 moles (174 g) of propane, in one hour, to 3 moles (217 g) of tert-butylamine located in a flask at room temperature (20 ° C). At the end of the infusion, 373 g of cyclohexane was added to drain the resulting water. This is how we gain

51,5 g vodne -faze in 734,5 g organske faze (d = 0,786).51.5 g of aqueous phase and 734.5 g of organic phase (d = 0.786).

b) Nato vzamemo 183 g predhodne reakcijske zmesi (organska faza) tako, da imamo 0,75 mola (84,75 g) nastalega imina, ki ga v eni uri prilijemo na 0,75 molov (103,5 g) dieti1fosfita segretega pri 60°C.b) Then take 183 g of the preceding reaction mixture (organic phase) so as to have 0.75 mol (84.75 g) of the resulting imine, which is added to 0.75 mol (103.5 g) of diethyl phosphite heated at one hour 60 ° C.

Celotno reakcijsko zmes (286,5 g s 34% cik 1oheksana) pustimo pri 60°C potem pa v eni uri povišamo temperaturo do 80°C in jo tako vzdržujemo še eno uro, preden vstavimo gretje in mešanje.The whole reaction mixture (286.5 g with 34% cyclohexane) was left at 60 ° C and then raised to 80 ° C for one hour and maintained for one hour before heating and stirring was inserted.

Tako dosežemo 97, oziroma 96% stopnjo transformacije (ST) imina in fosfita in dobitek reakcije (DR) z ozirom na pričakovani diester 89% in na nečistočo hidroksi (EtO) 2F‘OCH (OH) Et) 6%.Thus, 97% and 96%, respectively, of the transformation (ST) of imine and phosphite and the yield of reaction (DR) are obtained with respect to the expected diester of 89% and to the impurity hydroxy (EtO) 2 F'OCH (OH) Et) 6%.

c) Hidrolizo diestra dosežemo s 3 ekvivalenti žveplove (VI) kisline (96%) po molu diestra pri temperaturic) Hydrolysis of the diester is achieved with 3 equivalents of sulfuric acid (96%) per mole of diester at temperature

140°C. Diester izlijemo v toplo kislo raztopino. Po petih urah reakcije tretiramo nastalo dikislino v vodni fazi z metanolom potem pa s trieti1aminom (NEt3).140 ° C. Pour the diester into warm acidic solution. After five hours of the reaction, the resulting aqueous dioxide was treated with methanol followed by triethylamine (NEt 3 ).

Tako dobimo naslednje rezultate:This gives the following results:

DR - aminoalkanfosfonska kislina/diester = 81%DR - aminoalkanephosphonic acid / diester = 81%

Čistoča aminoalkanfosfonske kisline = 99%.Purity of aminoalkanephosphonic acid = 99%.

PRIMER 2: Sinteza aminopropanfosfonske kisline (postopek z dietilfosfitom 2).EXAMPLE 2 Synthesis of Aminopropanephosphonic Acid (Diethylphosphite 2 Process).

a) V bučko damo 2 mola (146 g) terc-butilamina pri 20°C in nato na amin zlijemo 2 mola (116 g) propanala pri 20θ0.a) Put 2 moles (146 g) of tert-butylamine at 20 ° C into the flask and then pour 2 moles (116 g) of propane at 20 θ 0 onto the amine.

Na koncu dodajanja propanala dodamo 250 g cikloheksana, da bi omogočili odlivanje. Tako dobimo 35 g vodne faze in 477 g organske faze (d = 0,78), katero razdelimo na dva dela po250 g of cyclohexane were added at the end of the propanal addition to allow for leaching. This gives 35 g of the aqueous phase and 477 g of the organic phase (d = 0.78), which is divided into two parts

238,5 g.238,5 g.

b) Od enega od teh delov vzamemo 179 g na tak način, da imamo 0,75 molov (84,75 g) imina, ki ga zlijemo na 0,75 molov (103,5 g) dieti1fosfita, pri 50°C in v času 40 minut ob mešanju. Potem temperaturo zvišamo do 60°C in tako pustimo 6 ur. Po uparevanju 278 g nastale zmesi v laboratorijskem vakuumu pri 70°C dobimo 184 g produkta čigar analizo izpeljemo s plinsko kromatografijo in NMR.b) Take 179 g from one of these portions in such a way that 0.75 moles (84.75 g) of imine are poured into 0.75 moles (103.5 g) of diethyl phosphite at 50 ° C and in 40 minutes stirring time. Then the temperature was raised to 60 ° C, leaving for 6 hours. Evaporation of 278 g of the resulting mixture in a laboratory vacuum at 70 ° C yields 184 g of the product whose analysis is performed by gas chromatography and NMR.

ss

Tako je rezultat sledeči:Thus the result is as follows:

ST terc-buti1propanimi na = 96%ST tert-butylpropane at = 96%

ST dieti 1-fos-fita = 97%ST Diet for 1-Phos-Fit = 97%

DR računajoč diester = 90%DR counting diester = 90%

DR računajoč hidroksi nečistočo = 7,2%DR calculated hydroxy impurity = 7.2%

Diester potem prečistimo z ispi ranjem z bazami (NaOH 20% potem voda) da bi eliminirali nečistočo hidroksi (EtO)sPOCH(OH)Et). Potrebna so večkratna izpiranja, da bi količino zaostale hidroksi nečistoče omejili do 0,5 molarnihThe diester was then purified by washing with bases (NaOH 20% then water) to eliminate impurity hydroxy (EtO) withPOCH (OH) Et). Multiple rinses are needed to limit the amount of residual hydroxy impurity to 0.5 molar

%. Po enem samem izpiranju z vodo pri 60°C, v času 1 ure 40 minut, ostane v končni zmesi 6% te nečistoče.%. After a single rinse with water at 60 ° C for 1 hour 40 minutes, 6% of this impurity remains in the final mixture.

c) Z enim delom pri dobijenega diestra, prečistili do 95%, izpeljemo hidrolizo s 3 žveplove (VI) kisline (96%) po molu diestra pric) One part of the obtained diester, purified to 95%, hydrolysis with 3 sulfuric acid (96%) per mole of diester at

140°C. Diester prilijemo topli kisli raztopini urah reakcije tretiramo pridobljeno dikislino v metanolom potem pa s trieti1aminom (NEt3).140 ° C. The diester was added to the warm acidic solution for hours of the reaction, the resulting dichloromethane was treated with methanol then triethylamine (NEt 3 ).

ki smo ga ekvi valenti temperaturi . Po petih vodni fazi zwhich we have equated to temperature. After five water phase with

Tako dobimo sledeče rezultate:Thus we obtain the following results:

DR računajoč aminoalkantosfonsko k i sl i ησ/di ester = 88%DR calculated aminoalkanthosphonic k and sl and ησ / di ester = 88%

Čistota aminoalkantosfonske kisline = > 99%.Purity of aminoalkanthosphonic acid => 99%.

PRIMER 3: Sinteza aminopropanfostonske kisline (postopek z dimeti 1fostitom 1)EXAMPLE 3 Synthesis of Aminopropanopostonic Acid (Smoke 1 Process 1)

a) V bučko pri 200°C vlijemo 2 mola (146 g) tercbutilamina in nato na amin prilijemo 2 mola (116 g) propanala pri 2Q°C. Na koncu uvajanja propanala dodamo 250 g ci k 1oheksana da bi omogočili odlivanje. Tako dobimo 35 g vodne -faze in 477 g organske -faze (d = 0,78) , ki jo razdelimo v dva dela po 238,5 g.a) Pour 2 moles (146 g) of tertbutylamine into a flask at 200 ° C and then pour 2 moles (116 g) of propane at 2Q ° C onto the amine. At the end of the propanal introduction, 250 g of ci k 1ohexane was added to allow for leaching. This gives 35 g of the aqueous phase and 477 g of the organic phase (d = 0.78), which is divided into two parts of 238.5 g each.

b) Od enega od teh delov vzamemo 179 g tako, da imamob) From one of these portions we take 179 g so that we have

0,75 mola (84,75 g) imina, ki ga zlijemo v 40 minutah, med mešanjem pri 50°C, na 0,75 mola (82,5 g) dimetiIfosfita.0.75 mol (84.75 g) of imine, which is poured over 40 minutes, while stirring at 50 ° C, to 0.75 mol (82.5 g) of dimethylphosphite.

Potem povišamo temperaturo do 6O°C in tako pustimo 6 ur. Po uparevanju 257 g pridobljene zmesi v 1aboratorijskem vakuumu na 70°C, dobimo 164 g produkta, ki ga analiziramo s plinsko kromatografijo in NMR.The temperature was then raised to 6 ° C, leaving it for 6 hours. Evaporation of 257 g of the resulting mixture in a laboratory vacuum at 70 ° C yields 164 g of the product which is analyzed by gas chromatography and NMR.

Tedaj so rezultati sledeči:Then the results are as follows:

Stopnja transformacije (ST) imina = 1007Transformation rate (ST) of imine = 1007

ST dimeti1fosfita (DMP) = 1007ST dimethyl phosphite (DMP) = 1007

Dobitek reakcije (DR): diester/DMP = 907Reaction Yield (DR): Diester / DMP = 907

DR: hidroksi (MeO)^POCH(OH)Et)/DMP = 4,87DR: hydroxy (MeO) ^ POCH (OH) Et) / DMP = 4.87

Ostale nečistoče = 4,37Other impurities = 4.37

c) S 3 ekvivalenti žveplove (VI) kisline izpeljemo hidrolizo pripravijenega diestra pri 130°C v času štirih ur.c) With 3 equivalents of sulfuric (VI) acid, hydrolysis of the prepared diester is carried out at 130 ° C for four hours.

Nato oborimo nastalo kislino z metanolom in trieti1aminam.The resulting acid is then precipitated with methanol and triethylamine.

Tako imamo:Thus we have:

DR: aminopropanfosfonska kisiina/diester = 857DR: Aminopropane phosphonic acid / diester = 857

DR: aminopropanfosfonska kislina/dimeti 1fosfit = 777DR: Aminopropanophosphonic acid / dimethyl 1phosphite = 777

Čistoča aminopropanfosfonske kisline = 997..Purity of Aminopropanophosphonic Acid = 997..

PRIMER 4: Sinteza aminopropanfosfonske kisline (postopek z dimetilfosfitom 2).EXAMPLE 4 Synthesis of Aminopropanophosphonic Acid (Dimethyl Phosphite 2 Process).

a) V bučko damo 3,5 mola (258 g) terc-butilamina (d =a) Put 3.5 mol (258 g) of tert-butylamine (d =

0,7). V času 1 ure zlijemo pri 20°C 3,5 mole (203 g) propanala (d = 0,8) na amin. Potem dodamo 461 g cikloheksana, da dosežemo odlivanje, ki pripelje do 60,5 g vodne faze (na ta način odstranimo 967 vode, ki se tvori) in 860 g organske faze (d = 0,76).0.7). Pour 3.5 moles (203 g) of propanal (d = 0.8) per amine over 1 hour at 20 ° C. Then 461 g of cyclohexane is added to give an outflow that results in 60.5 g of the aqueous phase (thus removing 967 of the resulting water) and 860 g of the organic phase (d = 0.76).

b) V drugi bučki pomešamo 2,5 mola (275 g) dimeti1fosfita in 275 g cik1oheksana. To zmes segrevamo tako, da je temperatura 80°C. Pri tej temperaturi uvajamo 614,3 g organske faze, kar ustreza 2,5 molom imina. Prilivanje izvajamo eno uro in v tem času destiliramo cikloheksan, ki vsebuje en del propanala, ki se tvori pri degradaciji imina.b) In the second flask, 2.5 mol (275 g) of dimethyl phosphite and 275 g of cyclohexane are mixed. This mixture is heated to a temperature of 80 ° C. At this temperature, 614.3 g of the organic phase is introduced, which corresponds to 2.5 moles of imine. The inflow is carried out for one hour, during which time the cyclohexane containing one part of the propane formed during the degradation of imine is distilled.

Nato vzdržujemo temperaturo pri 88°C 4 ure. Destilacija pripelje do 178 g ciklobeksanske raztopine.The temperature was then maintained at 88 ° C for 4 hours. Distillation results in 178 g of cyclobeksan solution.

Potem vzamemo 955 g reakcijske zmesi. Bilanca substance pokaže izgubo 28 g. Ta reakcijska zmes (932 g, po odvzemanju vzorcev za analizo) pripelje do 517 g suhega ekstrakta, ki ga analiziramo s plinsko kromatografijo in NMR.Then 955 g of the reaction mixture are taken. The substance balance shows a loss of 28 g. This reaction mixture (932 g, after sampling for analysis) yielded 517 g of the dry extract, which was analyzed by gas chromatography and NMR.

Tako dobimo:So we get:

ST dimeti 1fosfita = 1007ST dimethyl 1phosphite = 1007

DR: diester/dimeti1fosfit = 947DR: diester / dimethyl1phosphite = 947

DR: hidroksi/dimetilfosfit = 27.DR: hydroxy / dimethyl phosphite = 27.

Destilacija je torej omogočila znatno zmanjšanje tvorbe nečistoče hidroksi (MeO)2P0CH(OH)Et.Distillation thus allowed a significant reduction in the formation of hydroxy (MeO) 2 P0CH (OH) Et impurity.

c) Diester (470 g, 2,03 mola) ki smo ga pripravili zlijemo pri 20°C v 30 minutah na raztopino 967 žveplove (VI) kisline (643 g, torej 6,3 mola ali 3,1 ekv. kislina/mol diestra). Potem dvignemo temperaturo do 130°C in jo vzdržujemo pet ur. Po precipitaci ji z metanolom (1,6 ml/g raztopine) in s trieti1aminom (340 g/mol diestra) pri 20°C in pH 5 dobimo:c) The diester (470 g, 2.03 mol) prepared at 20 [deg.] C. in 30 minutes to a solution of 967 sulfuric (VI) acid (643 g, thus 6.3 mol or 3.1 eq. acid / mol) diestra). Then raise the temperature to 130 ° C and maintain it for five hours. After precipitation with methanol (1.6 ml / g solution) and triethylamine (340 g / mol diester) at 20 ° C and pH 5, the following is obtained:

DR: aminopropanfosfonska kislina /diester = 84%DR: Aminopropanophosphonic acid / diester = 84%

DR: ami nopropanf osf onska k i sl i na/di meti 1 -f osf i t = 79%DR: ami nopropanf osf onic k i sl i na / di meti 1 -f osf i t = 79%

Čistoča aminopropanfosfonske kisline = 99,1%Aminopropanophosphonic acid purity = 99.1%

PRIMER 5: Stopnje a) in b) z dietilfosfitom ( drugo topilo).EXAMPLE 5 Stages a) and b) with diethylphosphite (second solvent).

a) V bučko damo 1 mol (73 g) terc-buti1amina pri sobni temperaturi. Nato prilijemo 1 mol (58 g) propanala v 15 minutah. Po 45 minutah dodamo 130 g dik1orometana in 2 ga) Put 1 mole (73 g) of tert-butylamine at room temperature into the flask. Then add 1 mole (58 g) of propane in 15 minutes. After 45 minutes, 130 g of dichloromethane and 2 g were added

NaCl, da bi izvedli odlivanje. Tako dobimo 13 g vodneNaCl to perform the casting. This gives 13 g of aqueous

-faze (61% vode, ki se je tvorila je, torej, odstranjeno) in-phase (61% of the water that was formed was removed) and

247 g organske faze, ki jo po odvzemanju 4 g destiliramo pri247 g of the organic phase distilled at 4 g after removal

50°C 20 minut. F‘o končani destilaciji dobimo 236 g reakcijske zmesi.50 ° C for 20 minutes. Finished distillation gave 236 g of the reaction mixture.

b) Vzamemo 118 g te zmesi in jo zlijemo na 0,4 mola (55b) Take 118 g of this mixture and pour it on 0,4 mol (55 ml)

g) dietilfasfita pri 25°C. Potem zvičarno temperaturo v 15 minutah do 57°C, tako da dosečemo blago povratno destilacijo. To temperaturo vzdržujemo 3 ure.g) diethylphosphite at 25 ° C. Then the sonic temperature in 15 minutes to 57 ° C to achieve gentle reverse distillation. This temperature was maintained for 3 hours.

Pod temi pogoji dosežemo naslednje rezultate:Under these conditions, the following results are obtained:

ST terc-butiIpropanimina =91%ST tert-butylpropane = 91%

ST dietilfosfita = 9S%ST of diethylphosphite = 9S%

DR: diester = 76%DR: diester = 76%

DR: hidroksi nečistoče = 15%DR: hydroxy impurities = 15%

Claims (16)

PATENTNI ZAHTEVKIPATENT APPLICATIONS 1. Postopek za pripravo ot-aminoalkan-fostonske kisline, njene soli ali estra splošne -formule (I):1. A process for the preparation of ot-aminoalkane-fostonic acid, its salt or an ester of the general formula (I): / H r2o o v kateri so Rx, R3, identični ali različni, ki smo jih izbrali med vodikovim atomom, nerazvejeno ali razvejeno alkilno skupino z enim do šestimi atomi ogljika, in enim atomom alkalijskih ali zamljoalkalijskih kovin,/ H r 2 o which R x , R 3 , identical or different, are selected from a hydrogen atom, a straight or branched alkyl group of one to six carbon atoms, and one atom of alkali or alkaline earth metals, R3 = atom vodika, ali alkilna, cik 1oalki1 na, arilna ali aralkilna skupina, pri tem te skupine lahko vsebujejo en heteroatom in so eventuelno lahko substituirane z enim ali več atomi, predvsem s halogenom,R 3 = a hydrogen atom, or an alkyl, cycloalkyl, aryl or aralkyl group, these groups may contain one heteroatom and may be optionally substituted by one or more atoms, in particular halogen, R* — atom vodika, nerazvejena ali razvejena alkilna skupina, z 1 do 4 atomi ogljika, označen s tem, da vsebuje tri (kisline) ali štiri (soli ali estri) stopnje, celino teh štiri stopenj opiše sledeča skupna shema:R * is a hydrogen atom, a branched or branched alkyl group of 1 to 4 carbon atoms, characterized in that it contains three (acids) or four (salts or esters) stages, the whole of these four stages is described by the following common scheme: a)a) R3 — C — HR 3 - C - H II (III)II (III) R3 _ CH= NR4+H2O (IV)R 3 _ CH = NR 4 + H 2 O (IV) b) r3~b) r 3 ~ - CH= NR4 +- CH = NR 4 + RiO RiO R,0 1 \R, 0 1 \ Z? Z? - H —Z P— CHNHR4 / 11 1 4 - H -ZP- CHNHR 4/11 1 4 R20 0R 2 0 0 r2o 0 r3 r 2 o 0 r 3 (IV) (IV) (V) (V) (VI) (VI) c) c) R,0 \ R, 0 \ HO HO P__ Zil r2o 0P__ Zil r 2 o 0 chnhr4 1 *3chnhr 4 1 * 3 + H2SO4-P / u H0x 0+ H 2 SO 4 -P / u H0 x 0 CHNH- 1 r3 CHNH- 1 r 3
(VI) (la)(VI) d) eventuelnod) possibly H0. H0 . Rs0 a \R s 0 a \ P— CHNHo + nRcOH P— CHNHo + nRcOH Z Z P P CHNH- CHNH- z II l Δ J HO 7 0 R3 z II l Δ J HO 7 0 R 3 r5oz 0r 5 o z 0 1 r3 1 r 3 (la) (la) (Ib) (Ib)
pri tem je R= enako Rx in/ali R21 ali atom alkalijske kovine, predvsem Na ali K, in n je 1 ali 2, pod pogojem, da je, kadar je n = 1, eden od dveh R=, atom vodika.wherein R = is equal to R x and / or R21 or an alkali metal atom, in particular Na or K, and n is 1 or 2, provided that when n = 1, one of the two R = is a hydrogen atom.
2. Postopek po zahtevku 1, označen s tem, da je v stopnji d) R-s atom natrija ali kalija.Process according to claim 1, characterized in that in step d), R is a sodium or potassium atom. 3. Postopek po zahtevku 1, označen s tem, da se stopnje a) in b) izpeljejo v organskem topilu, ki se ne meša, ali pa malo, z vodo.Process according to claim 1, characterized in that steps a) and b) are carried out in a water-immiscible or slightly miscible organic solvent. 4. Postopek po zahtevku 3, označen s tem, da je organsko topilo izbrano iz skupine, ki vsebuje cikloheksan, diki or ometan ali toluen.Process according to claim 3, characterized in that the organic solvent is selected from the group consisting of cyclohexane, dicyclohexane or toluene. 5. Postopek po zahtevku 4, označen s tem, da je organsko topilo cikloheksan.5. The process according to claim 4, wherein the organic solvent is cyclohexane. 6. Postopek po zahtevku 1, označen s tem, da je karbonilna spojina v nezaščiteni obliki, keton ali aldehid, ali v zaščiteni obliki, acetal, hemiacetal ali dioksolan.Process according to claim 1, characterized in that the carbonyl compound is in unprotected form, ketone or aldehyde, or in protected form, acetal, hemiacetal or dioxolane. 7. Postopek po zahtevku 6, označen s tem, da je karbonilna spojina (II) propanal.Process according to claim 6, characterized in that the carbonyl compound (II) is propanal. 8. Postopek po zahtevku 1, označen s tem, da je amin (III) izbran med metil-, etil-, propil- ali izpopropil-, ali n-butil- ali terc-buti1aminam.Process according to claim 1, characterized in that the amine (III) is selected from methyl, ethyl, propyl or isopropyl- or n-butyl or tert-butylamine. 9. Postopek po zahtevku 8, označen s tem, da je amin (III) terc—butilamin.Process according to claim 8, characterized in that the amine (III) is tert-butylamine. 10. Postopek po zahtevku 1, označen s tem, da se stopnja a) izpelje z molskim presežkom amina (III) s ozirom na karbonilni derivat (II), ob odstranitvi vode.Process according to claim 1, characterized in that step a) is carried out with a molar excess of amine (III) with respect to the carbonyl derivative (II) upon removal of water. 11. Postopek po zahtevku 1, označen s tem, da je v stopnji b) dialki 1fostitna spojina (V) dimetil- ali dieti l-fos-f it.A process according to claim 1, characterized in that in step b) the dialky is a 1-phostite compound (V) of dimethyl or diethyl l-phosph-f it. 12. Postopek po zahtevku 1, označen s tem, da se v stopnji c) uporablja žveplova (VI) kislina, po 2 do 5 ekvivalentov kisline po molu diestra (VI) pri temperaturi med 80 in 150°C.Process according to claim 1, characterized in that in step c) sulfuric acid (2 to 5 equivalents of acid per mole of diester (VI) is used at a temperature between 80 and 150 ° C. 13. Postopek po zahtevku 12, označen s tem, da se reakcija izpelje s približno 3 ekvivalenti žveplove (VI) kisline pri 130—14Q°C.Process according to claim 12, characterized in that the reaction is carried out with about 3 equivalents of sulfuric acid at 130-14Q ° C. 14. Postopek po zahtevku 1, označen s tem, da se pri pH = 5 na koncu stopnje c) aminoalkanfosfonska kislina (la), ki se tvori, prečisti s prečipitaci jo v močni organski ali anorganski bazi.A process according to claim 1, characterized in that at pH = 5 at the end of step c) the aminoalkanophosphonic acid (Ia) formed is purified by precipitation in a strong organic or inorganic base. 15. Postopek po zahtevku 14, označen s tem, da je baza trietilamin.The process of claim 14, wherein the base is triethylamine. 16. Postopek po zahtevku 1 za pridobivanje spojine formule (I) v kateri Rt in R3 skupaj nista atom vodika, označen s tem, da se pusti reagirati en mol aminoalkanfosfonske kisline (la), nastale v stopnji c) s približno 1 ali 2 moli spojine R=0H, kjer ima R= isti pomen kot Ri ali R3.A process according to claim 1 for the preparation of a compound of formula (I) in which R t and R 3 together are not a hydrogen atom, characterized in that one mole of aminoalkanphosphonic acid (Ia) formed in step c) of about 1 is reacted or 2 moles of the compound R = 0H, where R = has the same meaning as Ri or R 3 .
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