WO2013180730A1 - Procédé de fabrication à rendement élevé et à grande échelle pour des esters pentaalkyliques de dtpa à pureté élevée - Google Patents

Procédé de fabrication à rendement élevé et à grande échelle pour des esters pentaalkyliques de dtpa à pureté élevée Download PDF

Info

Publication number
WO2013180730A1
WO2013180730A1 PCT/US2012/040347 US2012040347W WO2013180730A1 WO 2013180730 A1 WO2013180730 A1 WO 2013180730A1 US 2012040347 W US2012040347 W US 2012040347W WO 2013180730 A1 WO2013180730 A1 WO 2013180730A1
Authority
WO
WIPO (PCT)
Prior art keywords
dtpa
diethylenetriaminepentaacetic acid
formula
pentaalkyl
ester
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US2012/040347
Other languages
English (en)
Inventor
Lowell Jeffry LAWRENCE
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to PCT/US2012/040347 priority Critical patent/WO2013180730A1/fr
Publication of WO2013180730A1 publication Critical patent/WO2013180730A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/14Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof
    • C07C227/18Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof by reactions involving amino or carboxyl groups, e.g. hydrolysis of esters or amides, by formation of halides, salts or esters

Definitions

  • the present invention relates to the development of a large-scale manufacturing process applicable to the preparation of pentaalkyl esters of diethylenetriaminepentaacetic acid (hereinafter referred to as DTPA) of formula (I), and more particularly the pentaethyl ester of diethylenetriaminepentaacetic acid (hereinafter referred to as C2E5) of formula (II).
  • DTPA pentaalkyl esters of diethylenetriaminepentaacetic acid
  • C2E5 pentaethyl ester of diethylenetriaminepentaacetic acid
  • DTPA of formula (III) is a ligand widely used for the clathration of metal ions
  • DTPA transuranic radionuclides
  • the calcium and zinc salts of DTPA are both approved by the Food and Drug Administration for the removal (decorporation) of transuranic radionuclides such as Plutonium, Americium and Curium from the body of humans following contamination by these highly toxic elements.
  • DTPA is a highly polar compound and therefore must be administered intravenously in order to enter the bloodstream and remove the contaminating radionuclides, which are eliminated in the urine and feces following chelation by DTPA.
  • the document describes a new commercially viable, safe and industrially suitable process for the preparation of pentaalkyl esters of diethylenetriaminepentaacetic acid of formula (I), and the pentaethyl ester of diethylenetriaminepentaacetic acid of formula (II) by using concentrated hydrochloric acid (Cone. HCl) instead of concentrated sulfuric acid (Cone. H 2 SO 4 ) as an acid for the esterifaction of DTPA of the formula (III).
  • the pentaalkyl or pentaethyl ester product is extracted with ethyl acetate (EtOAc) instead of dichloromethane (DCM), and then washed with aq.
  • an acid used for the esterification of DTPA is selected from both Bronstead acids, but more particularly, Concentrated Hydrochloric acid (Cone. HC1).
  • concentrated hydrochloric acid has a molar concentration of greater than about 12M.
  • the alcohol used is not particularly restricted. A lower molecular weight alcohol is preferably used, more particularly methanol, ethanol, propanol, iso-propanol and the like, and most preferably ethanol. The alcohol must be used in excess and there is no need to use other solvents in the esterification reaction.
  • the esterification reaction temperature may preferably be at reflux temperature of the alcohol employed.
  • a preferred reaction time may be from 1 to 48 hours depending on the volume of the reaction being performed.
  • the crude product is extracted with a suitable solvent selected from methylacetate, ethyl acetate, propylacetate, benzene, toluene, xylene, diethyl ether, diisopropyl ether, t-butyl methyl ether and other non-halogenated organic solvents, and the like mixtures thereof, but more particularly ethyl acetate (EtOAc).
  • EtOAc ethyl acetate
  • the resulting organic layer is washed with aq. Alkaline solution selected from aq. Potassium bicarbonate (aq.
  • KHCO 3 aq. Potassium carbonate
  • aq. K 2 CO 3 aq. Sodium bicarbonate
  • aq. Na 2 C0 3 aq. Sodium Carbonate
  • other mild inorganic bases but more particularly aq. Potassium bicarbonate (aq. KHCO 3 ) solution.
  • DTPA 20 kg was added to a mixture of alcohol (500 L) and concentrated hydrochloric acid (32% w/v, 6.8 kg) at 20-25°C.
  • the reaction mixture was slowly heated to reflux temperature of the alcohol and maintained for 48 hours at reflux temperature.
  • the progress of the reaction was monitored on thin layer chromatography (TLC).
  • TLC thin layer chromatography
  • the reaction mixture is concentrated under vacuum distillation at 60-65 °C to remove ethanol, water, hydrochloric acid, and other volatiles to give a thick glassy oil.
  • the obtained residue was dissolved in ethyl acetate (80 L).
  • the resultant solution was washed 4 times with saturated aq. Potassium bicarbonate solution (saturated aq.
  • DTPA 20 Kg was added to a mixture of ethanol (500 L) and concentrated hydrochloric acid (32% w/v, 6.8 kg) at 20-25°C.
  • the reaction mixture was slowly heated to 76°C and maintained for 48 hours at 76-78°C.
  • the progress of the reaction was monitored using thin layer chromatography (TLC).
  • TLC thin layer chromatography
  • the reaction mixture was concentrated under vacuum distillation at 60-65°C to remove ethanol, water, hydrochloric acid, and other volatile components to give a thick glassy oil.
  • the residue was dissolved in ethyl acetate (80 L). The resulting solution was washed 4 times with saturated aq. Potassium bicarbonate solution (saturated aq.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
PCT/US2012/040347 2012-06-01 2012-06-01 Procédé de fabrication à rendement élevé et à grande échelle pour des esters pentaalkyliques de dtpa à pureté élevée Ceased WO2013180730A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/US2012/040347 WO2013180730A1 (fr) 2012-06-01 2012-06-01 Procédé de fabrication à rendement élevé et à grande échelle pour des esters pentaalkyliques de dtpa à pureté élevée

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2012/040347 WO2013180730A1 (fr) 2012-06-01 2012-06-01 Procédé de fabrication à rendement élevé et à grande échelle pour des esters pentaalkyliques de dtpa à pureté élevée

Publications (1)

Publication Number Publication Date
WO2013180730A1 true WO2013180730A1 (fr) 2013-12-05

Family

ID=49673775

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2012/040347 Ceased WO2013180730A1 (fr) 2012-06-01 2012-06-01 Procédé de fabrication à rendement élevé et à grande échelle pour des esters pentaalkyliques de dtpa à pureté élevée

Country Status (1)

Country Link
WO (1) WO2013180730A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12577503B2 (en) 2021-07-16 2026-03-17 Dow Global Technologies Llc Cleaning booster additive
US12577504B2 (en) 2021-07-16 2026-03-17 Dow Global Technologies Llc Liquid laundry detergent

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4831175A (en) * 1986-09-05 1989-05-16 The United States Of America As Represented By The Secretary Of The Department Of Health And Human Services Backbone polysubstituted chelates for forming a metal chelate-protein conjugate
US5780670A (en) * 1995-07-21 1998-07-14 Tohoku University DTPA derivatives modified with non-ester bond and a process for synthesizing them
US7279149B2 (en) * 2003-10-29 2007-10-09 Mayo Foundation For Medical Education And Research Amino acid composition with increased blood brain barrier permeability
US8030358B2 (en) * 2007-10-29 2011-10-04 University Of Kentucky Research Foundation Methods and pharmaceutical compositions for decorporation of radioactive compounds

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4831175A (en) * 1986-09-05 1989-05-16 The United States Of America As Represented By The Secretary Of The Department Of Health And Human Services Backbone polysubstituted chelates for forming a metal chelate-protein conjugate
US5780670A (en) * 1995-07-21 1998-07-14 Tohoku University DTPA derivatives modified with non-ester bond and a process for synthesizing them
US7279149B2 (en) * 2003-10-29 2007-10-09 Mayo Foundation For Medical Education And Research Amino acid composition with increased blood brain barrier permeability
US8030358B2 (en) * 2007-10-29 2011-10-04 University Of Kentucky Research Foundation Methods and pharmaceutical compositions for decorporation of radioactive compounds

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US12577503B2 (en) 2021-07-16 2026-03-17 Dow Global Technologies Llc Cleaning booster additive
US12577504B2 (en) 2021-07-16 2026-03-17 Dow Global Technologies Llc Liquid laundry detergent

Similar Documents

Publication Publication Date Title
DK2435439T3 (en) PREPARATION OF nalmefene HYDROCHLORIDE FROM naltrexone
JP6055183B2 (ja) ナルメフェン塩酸塩二水和物
JP5988272B2 (ja) オキシコドンの合成及び精製プロセス
CN102503805A (zh) 利用重排反应制备4-联苯乙酸的方法
PL168847B1 (pl) Sposób otrzymywania diacetyloreiny PL PL PL
RU2260582C2 (ru) Способ очистки правастатина
WO2013180730A1 (fr) Procédé de fabrication à rendement élevé et à grande échelle pour des esters pentaalkyliques de dtpa à pureté élevée
EA024688B1 (ru) Способ получения ситаглиптина и его фармацевтически приемлемых солей
US10538507B2 (en) Preparation process for high-purity dabigatran etexilate
DK2788357T3 (en) METHOD FOR RECOVERING NALMEPHEN HYDROCHLORIDE
CN105646446B (zh) 一种纯化阿格列汀的方法
TW200846354A (en) Trityl chloride recovery
HRP20030438A2 (en) A process for the preparation of 1-(aminomethyl) cyclohexaneacetic acid
RU2712232C1 (ru) Улучшенный способ получения налмефена из налтрексона
WO2006099635A1 (fr) Isolation de la galanthamine a partir d’un materiau biologique
CN102633796B (zh) 一种苦参酸类衍生物的制备方法
KR100881890B1 (ko) 사포그렐레이트 염산염의 제조방법
NO312831B1 (no) Fremgangsmåte ved fremstilling av 3-amin-1,2-propandiol
CN102030674A (zh) 西司他丁中间体的制备方法
WO2011004281A1 (fr) Procédé pour la préparation d’une forme amorphe de rabéprazole sodium
US20250026708A1 (en) Process for preparation of triheptanoin
Clowes VARIETIES.
CN1966485A (zh) 一种莽草酸衍生物的合成方法
JP2004002447A (ja) 工業的に生産されたプラバスタチンナトリウム含有組成物
JPH03294273A (ja) トリスチルベン化合物

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12877944

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 12877944

Country of ref document: EP

Kind code of ref document: A1