WO1991012256A1 - Process for preparing l-alpha-glycerylphosphoryl-d-myoinositol and its salts - Google Patents

Process for preparing l-alpha-glycerylphosphoryl-d-myoinositol and its salts Download PDF

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WO1991012256A1
WO1991012256A1 PCT/EP1991/000216 EP9100216W WO9112256A1 WO 1991012256 A1 WO1991012256 A1 WO 1991012256A1 EP 9100216 W EP9100216 W EP 9100216W WO 9112256 A1 WO9112256 A1 WO 9112256A1
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gpi
crude
acid
salts
methanol
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PCT/EP1991/000216
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French (fr)
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Giovanni Tronconi
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Istituto Chemioterapico Italiano Fine Chemicals S.P.A.
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Priority to AT91903313T priority Critical patent/ATE100455T1/en
Priority to DE69101056T priority patent/DE69101056T2/en
Priority to CA002075504A priority patent/CA2075504C/en
Priority to US07/916,978 priority patent/US5306840A/en
Publication of WO1991012256A1 publication Critical patent/WO1991012256A1/en

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/06—Phosphorus compounds without P—C bonds
    • C07F9/08—Esters of oxyacids of phosphorus
    • C07F9/09—Esters of phosphoric acids
    • C07F9/117—Esters of phosphoric acids with cycloaliphatic alcohols

Definitions

  • the present invention relates to a process for the preparation of L- ⁇ -glycerylphosphoryl-D-myoinositol and the salts thereof from crude or partially purified phosphatides.
  • GPI as the cyclohexylammonium salt by acylating pure phosphatidylinositol (PI), a substance which is not commercially available and is obtained by means of a laborious process which cannot be carried out industrially.
  • the present invention provides a simple and economic process for the preparation of free acid GPI as well as the salts thereof, of general formula (I)
  • GPI is the glycerylphosphorylmyoinositol anion
  • X is Na, Ca, Mg, Al, Zn, NH 4 ;
  • n is an integer from 1 to 3.
  • the process essentially consists in purificating crude GPI by means of weak basic resins, using diluted aqueous solutions of an organic acid, such as formic acid or acetic acid.
  • an organic acid such as formic acid or acetic acid.
  • impurities less acid than GPI L- -glycerylphosphorylethanolamine (GPE), N-acyl GPE etc.
  • GPE L- -glycerylphosphorylethanolamine
  • N-acyl GPE etc. pure GPI i-s recovered washing the resin with a more concentrated aqueous solution of the organic acid, without eluting the impurities more acid than GPI
  • GPS L- -glycerylphosphorylserine
  • glycerophosphoric acid etc.
  • An alcoholic suspension (preferably in methanol or ethanol) of the mixtures of the crude or partially purified phospholipids is treated with alkali metal alkoxides (preferably sodium or potassium methoxide, ethoxide or tert-butoxide).
  • alkali metal alkoxides preferably sodium or potassium methoxide, ethoxide or tert-butoxide.
  • the insoluble residue is filtered and suspended again in the reaction solvent, the suspension is adjusted to neutral or slightly acid pH (preferably from 4 to 7) with a mineral acid (hydrochloric, sulfuric, phosphoric acids) or with an organic acid (preferably formic, acetic, propionic acids), then it is filtered again.
  • the solid containing crude GPI Na or GPI K (depending on the used alkoxide) is suspended in water (in a water/solid v/w ratio preferably from 1 to 2) and the suspension is added with an alcohol (preferably methanol, ethanol or isopropanol in a v/v ratio, with respect to the used water, preferably from 1.5 to 3).
  • alcohol preferably methanol, ethanol or isopropanol in a v/v ratio, with respect to the used water, preferably from 1.5 to 3
  • the residue is filtered and washed with the same hydroalcoholic mixture as the one used in the suspension. Alcohol is distilled off from the obtained hydroalcoholic extract, then the aqueous solution is eluted first through a cationic resin in the acidic form, then through a weak acid resin (preferably in form of hydroxide, acetate, formate).
  • the resin is washed first with water, then with a diluted aqueous solution of an organic acid (preferably formic, acetic, propionic acids) in a concentration from 1 to 3% w/v, thereafter pure GPI is recovered washing the resin with a solution of the above cited organic acid in a concentration from 5 to 10% w/v.
  • the resulting solution is concentrated to small volume under reduced pressure, preferably so as to obtain a GPI concentration not above 10% w/v, then it is poured into acetone to obtain GPI in semi-solid form.
  • the supernatant waters are decanted, the residue is taken up into alcohol (preferably methanol, ethanol or isopropanol) and the solid acid GPI is isolated.
  • alcohol preferably methanol, ethanol or isopropanol
  • the salts of general formula (I) are obtained treating an aqueous solution of the obtained acid GPI with a carbonate, hydrogen carbonate, oxide, hydroxide of the metal corresponding to the desired salt, subsequently concentrating the solution to small volume and finally precipitating with an alcohol (preferably methanol, ethanol or isopropanol).
  • an alcohol preferably methanol, ethanol or isopropanol
  • the residue is suspended in water (800 ml), 1.6 1 of methanol are slowly added to the mixture, which is then stirred for about 30 minutes, then filtered, washing the residue on the filter with 2 x 300 ml of a 2:1 methanol/water mixture.
  • the hydroalcoholic solutions are combined, methanol is distilled off under vacuum, the aqueous solution is treated twice with a mixture of decolourizing charcoal (10 g) and diatomaceous earth (10 g).
  • the solution is filtered and eluted through 300 ml of a IR-120 H resin, washing the resin with 600 ml of water.
  • the resulting solution is eluted on 200 ml of a IR-93 OH resin, washing the resin first with water, then with a 3% w/v aqueous solution of acetic acid until impurities are completely removed (checking by T.L.C.).
  • the resin is washed with a 8% w/v aqueous solution of acetic acid until complete recovery of GPI, the solution is concentrated under vacuum to small volume (about 300 ml), then poured into acetone (4 1) under stirring. The mixture is stirred at room temperature for 6 hours, then decanted and the supernatant waters are discarded.
  • a solution of 15 g of pure acid GPI (obtained according to the process of example 1) in 150 ml of water is adjusted to pH 8 by addition of cyclohexylamine, then concentrated to small volume (about 30 ml) and diluted with ethanol (about 200 ml).
  • the obtained precipitate, after filtration, is crystallized from ethanol and dried under vacuum at 40oC over phosphoric anhydride. 14.5 g of GPI cyclohexylammonium salt are obtained.
  • a solution of 15 g of acid GPI (obtained according to the process of example 1) in 150 ml of water is adjusted to pH 5.5 by addition of calcium carbonate.
  • the mixture is filtered, concentrated under vacuum to small volume (about 30 ml), then poured into 150 ml of methanol under stirring. Stirring is continued at room temperature for 1 hour, then the product is filtered, washing with methanol, and dried under vacuum at 40°C, to obtain 15 g of pure (GPI) 2 Ca (a nearly non hygroscopic solid).
  • GPI K and GPI NH 4 are respectively obtained.
  • a suspension of deoleated soy lecithin (1 kg) in methanol (2 1) is stirred at room temperature for 2 hours, then filtered.
  • the residue is washed with methanol (800 ml), then suspended again in methanol and stirring at room temperature for one hour.
  • the residue is filtered, washing with methanol (500 ml), then suspended in methanol (2.5 1) containing 40 g of sodium methoxide and treated as described in examples 1 and 3. 25 g of (GPI) 2 Mg are obtained.
  • a suspension of 500 g of phosphatides (containing about 10% PI, 10% PS, 30% PC, 30% PE) in methanol (3 1) containing 30 g of sodium methoxide is treated according to the process of examples 1 and 3. 9.6 g of (GPI) 2 Ba are obtained.
  • the process yields show significant changes as the PI content in crude phosphatides generally can vary markedly.

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Abstract

A process for the preparation of L-α-glycerylphosphoryl-D-myoinositol and the salts thereof by extracting a crude deacylated mixture of phospholipids with a hydroalcoholic solution, then eluting on weak basic resins under controlled conditions.

Description

Process for preparing L-alpha-Glycerylphosphoryl-D- Myoinositol and its salts.
The present invention relates to a process for the preparation of L-α-glycerylphosphoryl-D-myoinositol and the salts thereof from crude or partially purified phosphatides.
The preparation of L-α-glycerylphosphoryl-D- myoinositol (GPI) and the pharmaceutically acceptable salts thereof has not been described up to now.
Brown (J. Chem. Soc., 3774, 1959) and Brokeroff (J. Am. Chem. Soc, 2591, 1959) obtained GPI as the cyclohexylammonium salt by acylating pure phosphatidylinositol (PI), a substance which is not commercially available and is obtained by means of a laborious process which cannot be carried out industrially.
Lapage (J. Am. Chem. Soc, 3713, 1960) obtained GPI as the cyclohexylammonium salt by acylating maize crude phosphatides but, even though the purification is carried out on strong basic ion exchange resins with gradient elutions, the resulting cyclohexylammoniu salt is not pure and repeated crystallizations must be performed in order to purify it.
The difficulty in obtaining pure GPI starting from not highly pure PI was confirmed by Hawthorne (Biochem. J., 195, 1959), who isolated GPI as the barium salt and obtained interesting results only by means of chromatography on strong basic ion exchange resins, with a gradient of a mixture of ammonium formate and sodium tetraborate and using pure PI.
The present invention provides a simple and economic process for the preparation of free acid GPI as well as the salts thereof, of general formula (I)
(GPl-)n Xn+ (I) wherein :
GPI is the glycerylphosphorylmyoinositol anion;
X is Na, Ca, Mg, Al, Zn, NH4 ;
n is an integer from 1 to 3.
starting from crude or partially purified phosphatides. The process essentially consists in purificating crude GPI by means of weak basic resins, using diluted aqueous solutions of an organic acid, such as formic acid or acetic acid. Thereby first the impurities less acid than GPI (L- -glycerylphosphorylethanolamine (GPE), N-acyl GPE etc.) are removed washing the resin with a diluted aqueous solution of the organic acid, without eluting GPI, then pure GPI i-s recovered washing the resin with a more concentrated aqueous solution of the organic acid, without eluting the impurities more acid than GPI (L- -glycerylphosphorylserine (GPS), glycerophosphoric acid, etc.), which can be eluted only when using saline aqueous solutions, but not with aqueous solutions of organic acids.
This simple purification cannot be achieved when using strong basic resins, since the complete elimination of GPE is very laborious and above all since GPI cannot be recovered washing the resin with an aqueous solution of an organic acid: in fact, in this instance, saline aqueous solutions must be used, which involve the use of awkward chromatographic techniques to separate GPI from acidic impurities.
The process according to the invention can be summarized as follows :
An alcoholic suspension (preferably in methanol or ethanol) of the mixtures of the crude or partially purified phospholipids is treated with alkali metal alkoxides (preferably sodium or potassium methoxide, ethoxide or tert-butoxide). When the reaction is over, the insoluble residue is filtered and suspended again in the reaction solvent, the suspension is adjusted to neutral or slightly acid pH (preferably from 4 to 7) with a mineral acid (hydrochloric, sulfuric, phosphoric acids) or with an organic acid (preferably formic, acetic, propionic acids), then it is filtered again. The solid containing crude GPI Na or GPI K (depending on the used alkoxide) is suspended in water (in a water/solid v/w ratio preferably from 1 to 2) and the suspension is added with an alcohol (preferably methanol, ethanol or isopropanol in a v/v ratio, with respect to the used water, preferably from 1.5 to 3). The residue is filtered and washed with the same hydroalcoholic mixture as the one used in the suspension. Alcohol is distilled off from the obtained hydroalcoholic extract, then the aqueous solution is eluted first through a cationic resin in the acidic form, then through a weak acid resin (preferably in form of hydroxide, acetate, formate). The resin is washed first with water, then with a diluted aqueous solution of an organic acid (preferably formic, acetic, propionic acids) in a concentration from 1 to 3% w/v, thereafter pure GPI is recovered washing the resin with a solution of the above cited organic acid in a concentration from 5 to 10% w/v. The resulting solution is concentrated to small volume under reduced pressure, preferably so as to obtain a GPI concentration not above 10% w/v, then it is poured into acetone to obtain GPI in semi-solid form. The supernatant waters are decanted, the residue is taken up into alcohol (preferably methanol, ethanol or isopropanol) and the solid acid GPI is isolated.
The salts of general formula (I) are obtained treating an aqueous solution of the obtained acid GPI with a carbonate, hydrogen carbonate, oxide, hydroxide of the metal corresponding to the desired salt, subsequently concentrating the solution to small volume and finally precipitating with an alcohol (preferably methanol, ethanol or isopropanol).
EXAMPLE 1 : PREPARATION OF GPI
A suspension of deoleated soy lecithin (1.22 kg) in methanol (4.5 1) containing sodium methoxide (60 g) is stirred at room temperature for 4 hours. The residue
(equivalent to 600 g of dry residue) is filtered, washed with methanol (2 x 0.5 1), then suspended again in methanol (1.3 1) and added with glacial acetic acid to adjust pH to about 4.5 (about 54 ml). The residue is filtered again, washed on filter with methanol (2 x 300 ml), then dried at 40°C under vacuum to obtain 400 g of dry product, containing about 10% GPI Na.
The residue is suspended in water (800 ml), 1.6 1 of methanol are slowly added to the mixture, which is then stirred for about 30 minutes, then filtered, washing the residue on the filter with 2 x 300 ml of a 2:1 methanol/water mixture. The hydroalcoholic solutions are combined, methanol is distilled off under vacuum, the aqueous solution is treated twice with a mixture of decolourizing charcoal (10 g) and diatomaceous earth (10 g). The solution is filtered and eluted through 300 ml of a IR-120 H resin, washing the resin with 600 ml of water. The resulting solution is eluted on 200 ml of a IR-93 OH resin, washing the resin first with water, then with a 3% w/v aqueous solution of acetic acid until impurities are completely removed (checking by T.L.C.). The resin is washed with a 8% w/v aqueous solution of acetic acid until complete recovery of GPI, the solution is concentrated under vacuum to small volume (about 300 ml), then poured into acetone (4 1) under stirring. The mixture is stirred at room temperature for 6 hours, then decanted and the supernatant waters are discarded. 600 ml of ethanol are added, the mixture is stirred for 5 hours at room temperature, then decanted and the supernatant waters are discarded. 300 ml of ethanol are further added, the mixture is stirred for 18 hours at room temperature, and the product is filtered, washed with ethanol and dried under vacuum at 30°C on phosphoric anhydride, to obtain 31 g of GPI.
C9H19 O11P (M.W. = 334.23)
Calculated: C = 32.34%; H = 5.73%
Found: C = 32.19%; H = 5.83%
1H-NMR (D2O): δ ppm: 3.20-3.75 (6 H, m); 3.75-4.10 (4 H, m); 4.20 (1 H, m); Mass :
333= [M-1 ] ; 259= [ (M-1 )-C3H6O2 ] ; 241= [ (M-1 )-C3H6O2-H2O] ;
163= [C6H1 1O5 ]
αD = -17.36 (c= 2 in water )
m.p. 145÷150°C (dec.)
EXAMPLE 2 : PREPARATION OF GPI CYCLOHEXYLAMMONIUM SALT
A solution of 15 g of pure acid GPI (obtained according to the process of example 1) in 150 ml of water is adjusted to pH 8 by addition of cyclohexylamine, then concentrated to small volume (about 30 ml) and diluted with ethanol (about 200 ml). The obtained precipitate, after filtration, is crystallized from ethanol and dried under vacuum at 40ºC over phosphoric anhydride. 14.5 g of GPI cyclohexylammonium salt are obtained.
C15H32N O11P (M.w. = 433.4)
Figure imgf000008_0001
Calculated: C = 41.57%; H = 7.44%; N = 3.23% Found: C = 41.67%; H = 7.42%; N = 3.20%
1H-NMR (D2O) δ ppm: 1.00-1.20 (m; 4H; cyclohexyl);
1.33-1.48 (m; 2H; cyclohexyl); 1.48-1.60 (m; 2H; cyclohexyl); 1.67-1.80 (m; 2H; cyclohexyl); 2.80-3.00 (m; CH-10); 3.08 (dd; CH-5; J5-4=J5-6=9.3 Hz); 3.29 (dd; CH-3; J3-2=2.70 Hz; J3-4=9.30 Hz); 3.34-3.44 (m; CH-4 + CH2-9); 3.50 (dd; CH-6; J6-5=J6-1=9.30 Hz); 3.60-3.78 (m; CH-1 + CH-8 + CH2-7); 4.00 (dd; CH-2 ; J2- 3=J2-1=2.70); 4.60 (s; DHO);
13C-NMR (D2O) (fully decoupled): δ ppm: 26.19 (s; C- 12+C-14); 26.68 (s; C-13); 32.72 (s; C-11+C-15); 52.74 (s; C-10); 64.43 (s; C-9); 68.70 (d; C-7; JC-O-P=5.72 Hz); 73.02 (d; C-8); 73.10 (s; C-3); 73.65 (m; C-2+C- 6); 74.58 (s; C-4); ppm 76.32 (s, C-5); 78.60 (d, C-1; JC-O-P=5.9 Hz);
αC = -13.2 (c = 2.09 in water)
EXAMPLE 3 : PREPARATION OF (GPI)2Ca
A solution of 15 g of acid GPI (obtained according to the process of example 1) in 150 ml of water is adjusted to pH 5.5 by addition of calcium carbonate. The mixture is filtered, concentrated under vacuum to small volume (about 30 ml), then poured into 150 ml of methanol under stirring. Stirring is continued at room temperature for 1 hour, then the product is filtered, washing with methanol, and dried under vacuum at 40°C, to obtain 15 g of pure (GPI)2Ca (a nearly non hygroscopic solid).
C18H36O22P2Ca (M.W. = 706.5)
Ca++
Figure imgf000009_0001
Calculated: C = 30.60%; H = 5.13%; Ca= 5.67% Found: C = 30.56%; H = 5.12%; Ca= 5.58%
1H-NMR (D2O) δ ppm: 3.37 (dd, CH-5; J5-6=J5-4=9.27 Hz); 3.58 (dd, CH-3; J3-2=2.78 Hz; J3-4=9.27 Hz); 3.65-3.75 (m; CH-4 + CH2-9); 3.79 (dd, CH-6; J6-5=J6-1=9.27 Hz); 3.90-4.10 (m; CH-1 + CH-8 + CH2-7); 4.31 (dd, CH-2; J2- 3=J2-1=2.78z); 4.80 (s; DHO)
13C-NMR (D2O) (fully decoupled) δ ppm: 69.03 (s; C-9); 73.34 (d; C-7 ; JC-O-P=5.6 Hz); 77.60 (d; C-8); 77.71 (s; C-3); 78.25 (m; C-2+C-6); 79.16 (s; C-4 ); 80.88 (s; C-5); 83.13 (d; C-1; JC-O-P=5.90 Hz)
αD = -15.46 (c = 2.07 in water)
Following the same process as described in example 3, but using magnesium or barium carbonates, (GPI)2Mg and (GPI)2Ba are respectively obtained.
C18H36 O22P2Mg (M.W. = 690.74)
Calculated: C = 31.30%; H = 5.25%; Mg= 3.52%
Found: C = 31.35%; H = 5.21%; Ca= 3.50%
αD = -15.68 (c = 3.1 in water)
C18H36O 22P2Ba (M.W. = 803.78) Calculated: C = 26.89%; H = 4.51%
Found: C = 26.74%; H = 4.69%
αD = -14.8 (c = 3.79 in water)
Following the same process as described in example 3, but using sodium, potassium or ammonium hydroxides, hydrogen carbonates or carbonates in such amounts as to adjust the pH of the solution from 4.5 to 5, GPI Na,
GPI K and GPI NH4 are respectively obtained.
C9H18O 11PNa (M.W. 356.21)
Calculated: C = 30.35%; H = 5.09%
Found: C = 30.28%; H = 5.18% αD = -14.9 (c = 3.3 in water)
C9H18O11PKa (M.W. 363.32)
Calculated: C = 29.75%; H = 4.99%
Found: C = 29.84%; H = 5.05%
αD = -15.1 (c = 2.3 in water)
C9H18O11PNH4 (M.W. 351.25)
Calculated: C = 30.77%; H = 6.31%; N = 3.98%
Found: C = 30.84%; H = 6.45%; N = 3.85%
αD = -16.1 (c = 1.4 in water)
The above described salts can be obtained treating directly the aqueous solution of acid GPI of example 1, as described in example 3.
EXAMPLE 4 : PREPARATION OF (GPI)2Mg from partially purified phosphatidylinositol
A suspension of deoleated soy lecithin (1 kg) in methanol (2 1) is stirred at room temperature for 2 hours, then filtered. The residue is washed with methanol (800 ml), then suspended again in methanol and stirring at room temperature for one hour. The residue is filtered, washing with methanol (500 ml), then suspended in methanol (2.5 1) containing 40 g of sodium methoxide and treated as described in examples 1 and 3. 25 g of (GPI)2Mg are obtained.
EXAMPLE 5 : PREPARATION OF (GPI)2Ba FROM ORGAN CRUDE PHOSPHATIDES
A suspension of 500 g of phosphatides (containing about 10% PI, 10% PS, 30% PC, 30% PE) in methanol (3 1) containing 30 g of sodium methoxide is treated according to the process of examples 1 and 3. 9.6 g of (GPI)2Ba are obtained. The process yields show significant changes as the PI content in crude phosphatides generally can vary markedly.

Claims

1. A process for the preparation of acid L-α- glycerylphosphoryl-D-myoinositol and the salts thereof, of general formula (I)
(GPI-)n Xn+ (I) wherein :
GPI is the glycerylphosphorylmyoinositol anion;
X is Na, Ca, Mg, Al, Zn, NH4;
n is an integer from 1 to 3 ;
by deacylation of crude or partially purified
phosphatides, which process comprises :
a) extracting GPI Na or GPI K from the insoluble residue of the crude deacylated mixture by means of an hydroalcoholic mixture;
b) subjecting the resulting crude GPI, after elimination of the metal ion, to purification on weak basic resins, first removing neutral or acid impurities weaker than GPI, by washing the resin with an aqueous solution of an organic acid, then recovering pure GPI by washing the resin with a more concentrated solution of an organic acid.
2. A process as claimed in claim 1, in which process methanol, ethanol, isopropanol in an alcohol/water v/v ratio from 1.5 to 3 are used in step a).
3. A process as claimed in claim 1, in which process formic, acetic or propionic acids in concentrations from 1 to 3% w/v are used in step b ) to remove impurities , and an aqueous solution of formic, acetic or propionic acids in concentrations from 5 to 10% w/v are used to recover GPI.
4. A process as claimed in any one of the previous claims, in which process crude or partially purified phospholipids are used as starting materials.
5. Glycerylphosphorylmyoinositol and the salts thereof in solid form.
PCT/EP1991/000216 1990-02-09 1991-02-05 Process for preparing l-alpha-glycerylphosphoryl-d-myoinositol and its salts WO1991012256A1 (en)

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AT91903313T ATE100455T1 (en) 1990-02-09 1991-02-05 PROCESS FOR THE PREPARATION OF L-ALPHAGLYZERYLPHOSPHORYL-D-MYOINOSITOL AND ITS SALTS.
DE69101056T DE69101056T2 (en) 1990-02-09 1991-02-05 METHOD FOR PRODUCING L-ALPHA-GLYZERYLPHOSPHORYL-D-MYOINOSITOL AND ITS SALTS.
CA002075504A CA2075504C (en) 1990-02-09 1991-02-05 Process for preparing l-alpha-glycerylphosphoryl-d-myoinositol and its salts
US07/916,978 US5306840A (en) 1990-02-09 1991-02-05 Process for preparing pure L-α-glycerylphosphoryl-D-myoinositol and its salts

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Publication number Priority date Publication date Assignee Title
WO1995020596A1 (en) * 1994-01-28 1995-08-03 Boehringer Mannheim Gmbh Method of preparing unsymmetrical phosphoric acid diesters
JPH09508135A (en) * 1994-01-28 1997-08-19 ベーリンガー マンハイム ゲゼルシャフト ミット ベシュレンクテル ハフツング Process for producing asymmetric phosphoric acid diester and salt thereof
WO2002038575A1 (en) * 2000-11-07 2002-05-16 I.R.B. Istituto Di Ricerche Biotecnologiche S.R.L. Glycerophosphoinositol derivatives as modulators of cytosolic a2 phospholipase
US7625883B1 (en) 2000-11-07 2009-12-01 I.R.B. Istituto di Ricerche Biotechnologiche S.R.L. Glycerophosphoinositol derivatives as modulators of cytosolic A2 phospholipase
CN104447856A (en) * 2014-12-11 2015-03-25 河南省农科院农副产品加工研究所 Preparation method of glycerol phosphatidylinositol

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ES2062765T3 (en) 1994-12-16
EP0514418B1 (en) 1994-01-19
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IT9019323A1 (en) 1991-08-09
IT1238683B (en) 1993-09-01
ATE100455T1 (en) 1994-02-15
DK0514418T3 (en) 1994-05-30
JPH05504351A (en) 1993-07-08
AU7210291A (en) 1991-09-03
EP0514418A1 (en) 1992-11-25
HUT62304A (en) 1993-04-28
IT9019323A0 (en) 1990-02-09
HU9202560D0 (en) 1992-10-28
DE69101056D1 (en) 1994-03-03
JP2964458B2 (en) 1999-10-18
HU210285B (en) 1995-03-28
CA2075504C (en) 2001-09-11
DE69101056T2 (en) 1994-06-01
US5306840A (en) 1994-04-26

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