AU663259B2 - A process for the preparation of alkylphosphocholines and the production thereof in pure form - Google Patents

A process for the preparation of alkylphosphocholines and the production thereof in pure form Download PDF

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Publication number
AU663259B2
AU663259B2 AU66059/94A AU6605994A AU663259B2 AU 663259 B2 AU663259 B2 AU 663259B2 AU 66059/94 A AU66059/94 A AU 66059/94A AU 6605994 A AU6605994 A AU 6605994A AU 663259 B2 AU663259 B2 AU 663259B2
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ion exchanger
alkylphosphocholines
prepared
mixed
purification process
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AU6605994A (en
Inventor
Jurgen Engel
Bernd Kutscher
Ulf Niemeyer
Gerhard Nossner
Alfred Olbrich
Wolfgang Schumacher
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Baxter Healthcare SA
Baxter International Inc
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Asta Medica GmbH
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Assigned to BAXTER HEALTHCARE S.A., BAXTER INTERNATIONAL INC. reassignment BAXTER HEALTHCARE S.A. Alteration of Name(s) in Register under S187 Assignors: ASTA MEDICA AKTIENGESELLSCHAFT
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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
    • C07F9/06Phosphorus compounds without P—C bonds
    • C07F9/08Esters of oxyacids of phosphorus
    • C07F9/09Esters of phosphoric acids
    • C07F9/091Esters of phosphoric acids with hydroxyalkyl compounds with further substituents on alkyl

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Steroid Compounds (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Cephalosporin Compounds (AREA)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)

Abstract

Process for the preparation of C14-C18-alkylphosphocholines in a one-pot process by reaction of an n-alkanol having a chain length of C14-C18 with phosphorus oxychloride in an inert solvent or else without solvent in the presence or absence of a basic substance, and further reaction of the reaction product in an inert solvent with a choline salt in the presence of a basic substance to give the phosphoric acid diester chloride, followed by hydrolysis and isolation of alkylphosphocholine, and, if appropriate, purification by means of a mixed-bed ion exchanger or in succession with an acidic ion exchanger and a basic ion exchanger.

Description

I
A Process For The Production Of Alkylphosphocholines In Pure Form Eibl et al. (EP 225,608) describe the preparation and use of alkylphosphocholines for the treatment of tumours. The starting substances are in the Eibl process of preparation are the n-alcohol and phosphorus oxychloride. They are reacted to phosphoric acid ester dichloride in tetrahydrofuran. In a second step 2-aminoethanol is reacted with the phosphoric acid ester dichloride to 2-hexadecyl-1,3,2-oxaphospholan-2oxide in dioxan. Hydrolysis with 2N hydrochloric acid yields the open-chain amine which is exhaustively methylated to alkylphosphocholine with dimethyl sulphate in 2propanol.
This process has the following disadvantages: it is necessary to isolate and purify the intermediate products. In addition, alkylating reagents are used. The use of potassium carbonate as an auxiliary base in this step of the process leads to the product having a potassium content that is undesirably high for pharmaceutical purposes.
Long-chain alkylphosphocholines having an antimicrobial effect are described by Kanetani et al., Nippon Kayaku Kaushi, 2, 1452 (1984).
i. They are prepared using the following process: ethylene glycol and phosphorus trichloridc are reacted to form 2-ch!oro-l,3,2dioxaphospholane, the product purified by distillation is oxidized with oxygen to 2-chloro- 20 1,3,2-dioxaphospholane-2oxide and then distilled again. The 2-chloro-1,3,2dioxaphospholane-2-oxide is then reacted with 1-hexadecanol to 2-hexadecyl-1,3,2dioxaphospholane-2-oxide. The 2-hexadecyl-1,3,2-dioxaphospholane-2-oxide is re'ctd with trimethylamine in the autoclave to hexadecylphosphocholine, the raw product is purified both with alkaline and with acid ion exchangers and recrystallized from acetone/chloroform. The analogous process is also used to prepare the octyl-, decyl-, dodecyl, tetradecyl and octadecyl derivatives.
The disadvantage of this process is that it is necessary to work with increased pressure in the last step ol the process and that the use of trimethylamine constitutes an industrial hygiene problem in the technical plpara:o 'i of the substance. It is also a 30 disadvantage that the hydrolysis-sensitive intermediate products 2-chloro-1,3,2dioxaphrspholane, 2-chloro-1,3 ,2-dioxaphospholane-2-oxide and 2-hexadecyl-2-oxa- 1,3,2-dioxaphospholane need to be isolated and purified. In addition, environmentallyunfriendly solvents such as benzene are used, the solvents being changed from step to step.
All known processes use chromatographic methods for working up and purifying the raw products.
However, chromatographic working up processes of this kind have the following disadvantages: their conversion to a technical scale causes difficulties since the dimensions of the stationary phase cannot be increased at will, IG:\WPUSER\LIUBVV0270:CE ;hromatographic processes are time-consuming.
The invention relates to a new, advantageous method of purifying alkylphosphocholines.
The process of preparing alkylphosphocholines is the subject of Australian Patent Application No. 19441/92.
The process of the invention avoids the time-consuming chromatographic step during working up.
The product purity achieved in the process claimed is greater than in the known processes.
According to a broad form of the invention there is provided a purification process for alkylphosphocholines characterized in that a solution of alkylphosphocholines, prepared using conventional processes is prepared and treated in an organic agent with a mixed-bed ion exchanger or successively with an acid ion exchanger and a basic ion exchanger.
The product prepurified in the manner described in Australian Patent Application No. 19441/92 may be taken up in anhydrous alcohols (C 1 to C4) or in alcohols which contain no mo,'e than up to 5 percent by weight of water at 20 0 C to 60 0 C, preferably 40 0 C and insoluble constituents filtered off. Alcohols that may for example be used are methanol, ethanol, isopropanol, butanol, isobutanol.
20 The prepurified product may also be dissolved in water. The filtrate obtained is then stirred with a mixed-bed ion exchanger, for example AmberliteR MB3, for example for 1 to 5 hours, preferably 2 hours at 10 0 C to 50 0 C, preferably 20°C. Instead of a mixed-bed ion exchanger the purification may also be effected simultaneously or successively with an acid ion exchanger and a basic ion exchanger.
Ion exchangers which may also be used are all insoluble solids which contain ion exchanging groups.
Acid ion exchangers are those which contain for example acid groups such as sulphonic a -d groups, carboxyl groups. Examples are ion exchangers with sulphonic acid groups in a polystyrene matrix such as Amberlite R IR 120, DowexR HCR, DuoliteR 30 C 20 or LewatitR S 100.
Weakly acid ion exchangers are for example those which carry carboxylic acid groups on the basis of a polyacrylic acid matrix, such as AmberliteR IRC 76, DuoliteR C 433 or ReliteR CC.
Basic ion exchangers that may for example be considered are those carrying on a polymer matrix polystyrene matrix) primary, secondary, tertiary or quaternary amino groups such as DuoliteR A 101, DuoliteR A 102, DuoliteR15 A 348, DuoliteR A 365, DuoliteR A 375, AmberliteR IRA 67, DuoliteR A 375, AmberliteR IRA 458 and DuoliteR A 132.
Mixed-bed ion exchangers are mixtures of acid and alkaline ion exchanger resins, such as AmberliteR MBI, AmberliteR MB2, AmberliteR MB3 and AmberliteR MB6.
G:\WPUSER\LUBVV00270:CE _L It is also possible to use all conventional ion exchangers in the process.
Reference is also made to Ullmann's Encyclopedia of Industrial Chemistry, Edition (1989), Volume A14, p. 450.
Following vacuum suctioning of the ion exchanger resin the mixture is evaporated under reduced pressure (for example 20 Torr to 200 Torr) at 40°C to 70 0 C and the mixture is then recrystallized from halogenated hydrocarbons or from alcohol/ketone mixtures.
Halogenated hydrocarbons that may for example be considered for the recrystallization are hydrocarbons containing 1 to 6 carbon atoms where one or several or all carbon atoms are replaced by chlorine atoms.
It is for example possible to use methylene chloride, chloroform, ethylene chloride, chlorobenzene.
Alcohols that may be considered are saturated aliphatic alcohols with 1 to 6 carbon atoms and 1 to 2 hydroxyl groups. Ketones that may be considered are saturated, aliphatic ketones with 3 to 8 carbon atoms, The mixing ratio alcohol:ketone is 1 to 1-5 (volume/volume). An ethanol/acetone mixture in the ratio of 1:1 is particularly preferred.
The crystals of alkylphosphocholine obtained are suction filtered and if necessary washed for example with saturated hydrocarbons containing 1 to 6 carbon atoms.
20 (Temperature of the washing liquid for example 15 to 30 0
C),
Drying is effected for example in a vacuum at 40 0 C to 80 0 C over conventional drying agents, for example phosphorus pentoxide or silica gel.
Example 1 Preparation of hexadecyl phosphocholine 25 1.0 Mol (92ml) POC13 in 1.5L chloroform are added to a 6 litre stirring apparatus under nitrogen and cooled in an ice bath to 5°C. 0.90Mol (218g) hexadecanol are dissolved in 700ml chloroform and added dropwise together with 4.00Mol (320ml) pyridine at a temperature of 5-12 0 C. Dropping time: 1.25 hours. The dropping funnel is then flushed with the remaining 300ml chloroform. After one and a half hours poststirring at 0-5 0 C, 1.35Mol (372g) Folid choline tosylate are added and then 400ml pyridine added dropwise over 15 minutes. This causes the temperature to rise to 20 0
C.
The ice bath is removed and the reaction mixture is stirred at room temperature for 3 hours. For purposes of hydrolysis 150ml water are added dropwise over 20 minutes, the temperature rising from 25°C to 36°C. After stirring for half an hour, the reaction solution is washed in each case once with 1,50 litres water/methanol 1.50 litres 3% sodium carbonate/methanol and 1.50 litres water/methanol The chloroform phase washed in this manner is dried over sodium sulphate and evaporated in a rotary evaporator in a vacuum after addition of 50ml iso-propanol. n-butanol is added for drying and the mixture is evaporated in a rotary evaporator again.
IG:\WPUSER\LIBVV00270:CE
L
Purification is carried out as follows: The residue is suspended in 2.0 litres acetone, stirred for approx. 2 hours, suction filtered and dried at 30 0 C in a vacuum. Raw yield: 325g The raw product is taken up in 3.0 litres absolute ethanol and insoluble portions filtered off. The filtrate is a stirred for two hours with 1.0 litre mixed-bed ion exchanger Amberlite MB 3R(FLTUKA).
After suction filtration of the ion exchanger resin the mixture is evaporated in a rotary evaporator in a vacuum and then recrystallized once from 0.70 litres methylene chloride.
Complete crystallization is achieved in the refrigerator. The crystals are suction filtered and washed with pentane. The mixture is then dried in a vacuum at 30 0 C over phosphorus pentoxide.
Yield 193g (0.47Mol, 53%) The reaction product has a mclting point of 241-245 C.
Examples 2-5 are prepared according to the same procedure.
Example 2:
.O
.II D-19390: H 3
C-(CH
2 13
-O-P-O-(CH
2 2 -N(CH3)3 0© Mp: 260 0 C (disintegration)
C
19
H
42
NO
4 P (379.52) TL: 89 a (chloroform/methanol/ammonia 25% 70:20:10) Rf: 0.27 EA: calc. C 60.13% H 11.16% N 3.69% H20 57.41% 11.16% 3.52% found C 57.40% H 11.42% N 3.61% 57.43% 11.47% 3.65% 20 'H-NMR: (250 MHz, CDC1 3 5 0.90 ppm 3H) 3.80 2H) 1.25 22H) 3.85 2H) 1.55 2H) 4.25 2H) 3.40 9H) Example 3:
O
II
G
D-20403: H 3
C-(CH
2
(CH
2 2 -N(CH3)3 6o IG:\WPUSER\LIBVVI00270;CE Mp: 244'C (disintegration)
C
20 11 44 N0C 4 P (393.555) -TL: 89 a (chloroform/methanol/amimonia 25
EA:
Rf: 0.49 cal'z.
*21120 found C 61 .04% 55.92% C 56. 14% 55.74% -70:40:10) 11.27% 11.26% 10.99% 10.85% N 3.56% 3.26% N 3.67% 3.59% TT.-NMR: (250 MHz, CDCl 3 8 0.90 ppm 3H1) 3.80 211) 1.30 (in, 24H1) 3.85 (in, 211) 1.55 2H1) 4.25 (in, 211) 3.40 9H1) 0 0.
Example 4: 0 D-19767: H 3 0-(0H 2 16 0--(H 2 2
-N(CH
3 3 Mp: 254-256'C
C
22 11 48 N0 4 P (421.61) ITL: 127 c (I-butanol/glacial acetic acid/water Rf: 0.34 caic.
*1120 found C 62.68% 60.11 C 60.2% 60.5'% -60:20:20) 11 11.48% 11.46% 1111.7% 11.7% N 3.32% 3.19% N 3.1% 'H-NMR: (250 MHz, CDC1 3 5 0.90 ppm 311) 3.80 211) 1.25 (in, 2811) 3.85 (in, 211) 1.60 211) 4.25 (in, 211) 3.40 911) Example 0 D-19391: H 3
C-(CH
2 )17r-O-P H 2 2 -N(CH)3 Mp: 258 0 C (disintegration) jG:%WPUSER\UBVVOO270:CE
C
2 3
H
50 N0 4 P (435.62) TL: 126 (1-butanol/glacial acetic acid/water =40: 10: Rf: 0, 3 EA: caic. C 63.41 H111.57% N 3.22 *1120 60.90% 11.55% 3.09% found C 60.80% H 11.93% N 3.15 60.83% 12.02% 3.15% 'H-NMR: (250 MHz, CDC1 3 8= 0.90 ppm 3H) 3.80 211) 1.25 (in, 3011) 3.85 (mn, 2H) 1.60 211) 4.30 (in, 211) 3.40 911) too.* IGAWPUSEVAWIDVVIO027O:CE

Claims (4)

1. A purification process for alkylphosphocholines characterized in that a solution of alkylphosphocholines, prepared using conventional processes is prepared and treated in an organic agent with a mixed-bed ion exchanger or successively with an acid ion exchanger and a basic ion exchanger.
2. A purification process for alkylphosphocholines substantially as hereinbefore described with reference to any one of the Examples.
3. A C 14 -C 18 -alkylphosphocholine derivative whenever purified by a process according to claim 1 or 2.
4. A method of treating a tumour in a patient requiring such treatment comprising administering to said patient an effective amount of a derivative as defined in claim 3. Dated 28 June, 1994 ASTA Medica Aktiengsellschaft 15 Patent Attorneys for the Applicant/Nominated Person SPRUSON FERGUSON *o o*o* IG:\WPU' ER\LIBW100270;CE I a A Process For The Production Of Alkyiphosphocholines In Pure Form Abstract A purification process for alkylphosphor-hnlines charL. .,ised in that a solution of alkyiphosphocholines, prepared using conventional pik sses, is prepared and treated in an organic agent with a mixed-bed ion exchanger or successively wvith an acid ion exchanger and a basic ion exchanger. *a sees a. a a a. a. a. a a. INMABTIMM.CE I of I
AU66059/94A 1991-07-04 1994-06-29 A process for the preparation of alkylphosphocholines and the production thereof in pure form Expired AU663259B2 (en)

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DE4122127 1991-07-04

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DK0521353T3 (en) * 1991-07-04 1996-05-13 Asta Medica Ag Antineoplastic drug containing octadecyl (2- (N-methylpiperidino) ethyl) phosphate as an active ingredient and process for its preparation

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU3239489A (en) * 1988-04-04 1989-10-05 American Cyanamid Company Novel antagonists of platelet activating factor
WO1990013552A1 (en) * 1989-05-08 1990-11-15 Istituto Chemioterapico Italiano Fine Chemicals S.P.A. PROCESS FOR THE PREPARATION OF L-α-GLYCERYLPHOSPHORYLCHOLINE AND OF L-α-GLYCERYLPHOSPHORYLETHANOLAMINE

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* Cited by examiner, † Cited by third party
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DE3164332D1 (en) * 1980-10-21 1984-07-26 Boehringer Mannheim Gmbh Phospholipids that contain sulphur, process for their preparation and medicines containing these compounds
JPS60184092A (en) * 1984-03-01 1985-09-19 Kao Corp Phosphoric ester and its preparation
IE59778B1 (en) * 1985-12-04 1994-04-06 Max Planck Gesellschaft Medicament with anti-tumour action containing hexadecylphosphocholine

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU3239489A (en) * 1988-04-04 1989-10-05 American Cyanamid Company Novel antagonists of platelet activating factor
EP0336142A2 (en) * 1988-04-04 1989-10-11 American Cyanamid Company Novel antagonists of platelet activating factor
WO1990013552A1 (en) * 1989-05-08 1990-11-15 Istituto Chemioterapico Italiano Fine Chemicals S.P.A. PROCESS FOR THE PREPARATION OF L-α-GLYCERYLPHOSPHORYLCHOLINE AND OF L-α-GLYCERYLPHOSPHORYLETHANOLAMINE

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ES2108715T3 (en) 1998-01-01
NO922612L (en) 1993-01-05
IL102379A0 (en) 1993-01-14
DE4220852A1 (en) 1993-01-14
NO981742D0 (en) 1998-04-17
IL102379A (en) 1996-10-31
GR3025490T3 (en) 1998-02-27
SG47844A1 (en) 1998-04-17
FI923087A (en) 1993-01-05
JP3171279B2 (en) 2001-05-28
ZA924980B (en) 1993-04-28
CN1034941C (en) 1997-05-21
FI923087A0 (en) 1992-07-03
PL169571B1 (en) 1996-08-30
EP0521297B1 (en) 1997-09-17
CN1068331A (en) 1993-01-27
IE80555B1 (en) 1998-09-23
CA2073126C (en) 2001-09-04
AU652646B2 (en) 1994-09-01
CA2073126A1 (en) 1993-01-05
AU6605994A (en) 1994-09-22
NO304316B1 (en) 1998-11-30
DE4220852C2 (en) 2000-10-19
EG20551A (en) 1999-07-31
HUT61560A (en) 1993-01-28
DK0521297T3 (en) 1998-05-04
AU1944192A (en) 1993-01-07
HU9202233D0 (en) 1992-10-28
NO981742L (en) 1993-01-05
HU219243B (en) 2001-03-28
PL295129A1 (en) 1993-06-28
IE922182A1 (en) 1993-01-13
JPH05186483A (en) 1993-07-27
NO304232B1 (en) 1998-11-16
ATE158295T1 (en) 1997-10-15
NO922612D0 (en) 1992-07-02

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