Methods of synthesizing 2-[4-[(2,3,4-trimethoxyphenyl)methyl]piperazin-1-yl]ethyl pyridine-3-carboxylate

Information

  • Patent Grant
  • 11780811
  • Patent Number
    11,780,811
  • Date Filed
    Monday, June 28, 2021
    3 years ago
  • Date Issued
    Tuesday, October 10, 2023
    a year ago
  • Inventors
  • Original Assignees
    • IMBRIA PHARMACEUTICALS, INC. (Boston, MA, US)
  • Examiners
    • Solola; Taofiq A
    Agents
    • Brown Rudnick LLP
    • Schoen; Adam M.
Abstract
The invention provides methods of chemical synthesis of the pharmacological agent 2-[4-[(2,3,4-trimethoxyphenyl)methyl]piperazin-1-yl]ethyl pyridine-3-carboxylate, also called CV-8972. The methods entail formation of a free base form of 2-[4-[(2,3,4-trimethoxyphenyl)methyl]piperazin-1-yl]ethanol, also called CV-8814, as intermediate without producing a salt form of CV-8814.
Description
FIELD OF THE INVENTION

The invention relates to methods of chemical synthesis of the pharmacological agent 2-[4-[(2,3,4-trimethoxyphenyl)methyl]piperazin-1-yl]ethyl pyridine-3-carboxylate.


BACKGROUND

Heart disease is the leading cause of death worldwide, accounting for 15 million deaths across the globe in 2015. In many forms of heart disease, decreased cardiac efficiency stems from changes in mitochondrial energy metabolism. Mitochondria are sub-cellular compartments in which metabolites derived from glucose and fatty acids are oxidized to produce high-energy molecules. Increasing fatty acid oxidation in the heart decreases glucose oxidation, and vice versa. Glucose oxidation is a more efficient source of energy, but in certain types of heart disease, such as angina, heart failure, ischemic heart disease, and diabetic cardiomyopathies, fatty acid oxidation predominates in cardiac mitochondria. As a result, the pumping capacity of the heart is reduced.


SUMMARY

CV-8972, which has the IUPAC name 2-[4-[(2,3,4-trimethoxyphenyl)methyl]piperazin-1-yl]ethyl pyridine-3-carboxylate and the following structure:




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was recently identified as a promising therapeutic candidate for cardiovascular conditions. Prior schemes for synthesis of CV-8972 require formation of a free base form of 2-[4-[(2,3,4-trimethoxyphenyl)methyl]piperazin-1-yl]ethanol, also called CV-8814, and conversion of the free base form of CV-8814 to a hydrochloride salt. In such schemes, CV-8814 must then be converted back to its free base form for coupling to nicotinic acid to form the free base form of CV-8972.


The invention provides a CV-8972 synthesis scheme that bypasses the reversible conversion of CV-8814 between the free base and HCl salt forms. In the schemes provided herein, the free base form of CV-8814 is formed in a reductive amination reaction, and the free base product is used directly as a substrate for coupling to nicotinic acid to form CV-8972. Because fewer steps are required, the synthesis schemes of the invention are simpler, faster, and provide better yields than prior methods of making CV-8972.


In an aspect, the invention provides methods for preparing a compound of Formula (X):




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by performing the steps of:


reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol to produce a free base form of a compound of Formula (IX):




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and


reacting the free base form of the compound of Formula (IX) with nicotinic acid to produce the compound of Formula (X), wherein the method does not comprise producing a salt form of the compound of Formula (IX).


The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may include one or more solvents, catalysts, or other chemicals. The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may include one or more of sodium triacetoxyborohydride, acetic acid, and 2-methyltetrahydrofuran.


The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may be performed at a defined temperature. The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may be performed at from about 10° C. to about 30° C., from about 15° C. to about 30° C., from about 20° C. to about 30° C., from about 25° C. to about 30° C., from about 10° C. to about 25° C., from about 15° C. to about 25° C., from about 20° C. to about 25° C., from about 10° C. to about 20° C., or from about 15° C. to about 20° C.


The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may not include a specific solvent, catalyst, or other chemical. The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may not include dichloromethane.


The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may produce a free base form of the compound of Formula (X).


The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may include one or more solvents, catalysts, or other chemicals. The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may include one or more of 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide, 4-(dimethylamino)pyridine, and dichloromethane.


The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may be performed at a defined temperature. The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may be performed at from about 15° C. to about 30° C., from about 20° C. to about 30° C., from about 25° C. to about 30° C., from about 15° C. to about 25° C., from about 20° C. to about 25° C., or from about 15° C. to about 20° C.


The method may include converting the free base form of the compound of Formula (X) to a salt form of the compound of Formula (X). The salt form of the compound of Formula (X) may be a HCl salt. The salt form of the compound of Formula (X) may be monohydrate.


The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may include one or more solvents, catalysts, or other chemicals. The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may include one or more of HCl and methyl ethyl ketone.


The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may be performed at a defined temperature. The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may be performed at from about 40° C. to about 60° C., from about 45° C. to about 60° C., from about 50° C. to about 60° C., from about 55° C. to about 60° C., from about 40° C. to about 55° C., from about 45° C. to about 55° C., from about 50° C. to about 55° C., from about 40° C. to about 50° C., from about 45° C. to about 50° C., from about 40° C. to about 50° C., about 40° C., about 45° C., about 50° C., about 55° C., or about 60° C.


The method may include converting the salt form of the compound of Formula (X) from a first crystal form to a second crystal form. Each of the first and second crystal forms may independently be Form A, Form B, Form C, Form D, or Form E.


The step of converting the salt form of the compound of Formula (X) from a first crystal form to a second crystal form may include one or more of changing the solvent of the salt form of the compound of Formula (X) and incubating the salt form of the compound of Formula (X), at about 60° C.


The method may be performed without the use of one or more solvents, catalysts, or other chemicals. The method may be performed without the use of one or more of dioxane, ethylacetate, or potassium carbonate.


The method may include purifying the free base form of the compound of Formula (IX). The method may include crystallizing the free base form of the compound of Formula (IX).


In another aspect, the invention provides methods of preparing a compound of Formula (X) by performing the steps of:


reacting a compound of Formula (1):




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with a compound of Formula (2):




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to produce a free base form of a compound of Formula (IX):




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reacting the free base form of a compound of Formula (IX) with a compound of Formula (3):




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to produce a free base form of the compound of Formula (X); and


converting the free base form of the compound of Formula (X) to a HCl salt of the compound of Formula (X),


wherein the method does not comprise producing a salt form of the compound of Formula (IX).


The method may include purifying the free base form of the compound of Formula (IX). The method may include crystallizing the free base form of the compound of Formula (IX).







DETAILED DESCRIPTION

The recently-identified compound CV-8972 holds promise as a therapeutic agent for treating a variety of conditions, including cardiovascular conditions, rheumatic diseases, fibrosis, and cancer. CV-8972, which has the IUPAC name 2-[4-[(2,3,4-trimethoxyphenyl)methyl]piperazin-1-yl]ethyl pyridine-3-carboxylate and the following structure:




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is metabolized in the body into two sets of products that increase mitochondrial energy production in different ways. In an initial reaction, the molecule is split into CV-8814, which has the following structure:




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and nicotinic acid. Over time, CV-8814 converted in the body to trimetazidine. Both CV-8814 and trimetazidine inhibit beta-oxidation of fatty acids and therefore shift mitochondrial metabolism toward oxidation of glucose, a more oxygen-efficient source of energy. Nicotinic acid serves as precursor for synthesis of nicotinamide adenine dinucleotide (NAD+). NAD+ promotes mitochondrial respiration to drive ATP synthesis, regardless of whether glucose or fatty acids are used as the carbon source. Thus, the two sets of products that result from breakdown of CV-8972 in vivo act synergistically to stimulate energy production in mitochondria in cardiac tissue and other cell types. CV-8972 and its mechanism of action are described in U.S. Pat. No. 10,556,013, the contents of which are incorporated herein by reference.


U.S. Pat. No. 10,556,013 also provides a scheme for synthesis of CV-8972. The scheme entails formation of a free base form of CV-8814 by reductive amination of 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol. Due to the difficulty of isolating CV-8814 in a solid form in this prior method, the product of this reaction is then converted to a hydrochloride salt of CV-8814. However, CV-8814 must be converted back to its free base form for use in the esterification reaction with nicotinic acid that produces CV-8972.


The invention provides CV-8972 synthesis schemes in which the free base form of CV-8814 formed as a product in the reductive amination reaction can be used directly as a substrate in the esterification reaction. The invention is based in part on the identification of conditions that improve the stability of CV-8814 free base and allow the free base form to be crystallized. Thus, the schemes provided herein obviate the need to convert CV-8814 from its free base form to a HCl salt and then back to the free base form. Consequently, the invention provides simpler, quicker, and higher-yield methods for making CV-8972.


The invention provides methods for preparing a compound of Formula (X):




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by performing the steps of:


reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol to produce a free base form of a compound of Formula (IX):




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and


reacting the free base form of the compound of Formula (IX) with nicotinic acid to produce the compound of Formula (X),


wherein the method does not comprise producing a salt form of the compound of Formula (IX).


2,3,4-trimethoxybenzaldehyde has the following structure:




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2-(piperazin-1-yl)ethan-1-ol has the following structure:




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Nicotinic acid has the following structure:




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The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may include one or more solvents, catalysts, or other chemicals. The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may include one or more of sodium triacetoxyborohydride, acetic acid, and 2-methyltetrahydrofuran.


The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may be performed at a defined temperature. The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may be performed at from about 10° C. to about 30° C., from about 15° C. to about 30° C., from about 20° C. to about 30° C., from about 25° C. to about 30° C., from about 10° C. to about 25° C., from about 15° C. to about 25° C., from about 20° C. to about 25° C., from about 10° C. to about 20° C., or from about 15° C. to about 20° C.


The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may not include a specific solvent, catalyst, or other chemical. The step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol may not include dichloromethane.


The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may produce a free base form of the compound of Formula (X).


The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may include one or more solvents, catalysts, or other chemicals. The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may include one or more of 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide, 4-(dimethylamino)pyridine, and dichloromethane.


The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may be performed at a defined temperature. The step of reacting the free base form of the compound of Formula (IX) with nicotinic acid may be performed at from about 15° C. to about 30° C., from about 20° C. to about 30° C., from about 25° C. to about 30° C., from about 15° C. to about 25° C., from about 20° C. to about 25° C., or from about 15° C. to about 20° C.


The method may include converting the free base form of the compound of Formula (X) to a salt form of the compound of Formula (X). The salt form of the compound of Formula (X) may be a HCl salt. The salt form of the compound of Formula (X) may be monohydrate.


The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may include one or more solvents, catalysts, or other chemicals. The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may include one or more of HCl and methyl ethyl ketone.


The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may be performed at a defined temperature. The step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) may be performed at from about 40° C. to about 60° C., from about 45° C. to about 60° C., from about 50° C. to about 60° C., from about 55° C. to about 60° C., from about 40° C. to about 55° C., from about 45° C. to about 55° C., from about 50° C. to about 55° C., from about 40° C. to about 50° C., from about 45° C. to about 50° C., from about 40° C. to about 50° C., about 40° C., about 45° C., about 50° C., about 55° C., or about 60° C.


The compound of Formula (X) may exist in at least five crystal forms: Form A, Form B, Form C, Form D, and Form E. Form A is monohydrate, and Forms B, D, and E are anhydrous. The method may include converting the compound of Formula (X) from a first crystal form to a second crystal form. Each of the first and second crystal forms may independently be Form A, Form B, Form C, Form D, or Form E. The method may include one or more of the following conversions of the compound of Formula (X): from an anhydrous form to a hydrated form; from a hydrated form to an anhydrous form; from one anhydrous form to another; and from one hydrated form to another.


The step of converting the salt form of the compound of Formula (X) from a first crystal form to a second crystal form may include one or more of changing the solvent of the salt form of the compound of Formula (X) and incubating the salt form of the compound of Formula (X), at about 60° C.


The method may be performed without the use of one or more solvents, catalysts, or other chemicals. The method may be performed without the use of one or more of dioxane, ethylacetate, or potassium carbonate.


The method may include purifying the free base form of the compound of Formula (IX). The method may include crystallizing the free base form of the compound of Formula (IX).


EXAMPLES
Example 1

Introduction


CV-8972 was synthesized according to Scheme 1.




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Step 1 is a reductive amination using 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol starting materials, with sodium triacetoxyborohydride (STAB) as the reductant, in the presence of catalytic acetic acid (AcOH), and 2-methyltetrahydrofuran (2-MeTHF) as solvent. After the reaction is completed, an aqueous workup, solvent exchange to MTBE, and recrystallization from MTBE/n-heptane forms the intermediate CV-8814 Free Base (CV8814 Free Base).


In step 2, CV-8814 Free Base (CV8814 Free Base) undergoes acid coupling with nicotinic acid in the presence of 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide (EDC) and catalytic 4-(dimethylamino)pyridine (DMAP) in dichloromethane (DCM) solvent. After aqueous workup, CV8972 Free Base is formed. Solvent exchange to 2-butanone (MEK) followed by addition into concentrated HCl in MEK forms CV8972 Monohydrate intermediate.


The final step 3 is a form conversion in a mixture of water, methanol, and MEK at 60° C.±5° C. followed by a precipitation by the addition of MEK to obtain the desired form A of final product CV-8972 by XRPD analysis.


Manufacturing Details


Manufacturing details are provided in Table 1.














TABLE 1







Amount
Amount






Started
Produced
Yield
HPLC


Step#
BOP#
(Kg)
(Kg)
(%)
Purity (%)







1
2493-1903-00484
27.5 kg
34.0 kg
76.0%
100.0%


2
2479-1903-00489
28.8 kg
48.6 kg
96.4%
 99.1%


3
2479-1904-00494
48.5 kg
41.7 kg
86.0%
 99.9%









Production Details


Step 1, formation of CV8814 Free Base (2493-1903-00487), was performed according to Scheme 2.




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Production details for step 1 are provided in Table 2.















TABLE 2











Actual





Equiv.

Expected
Quantity


Identity
Vendor/Grade/
MW
Moles/
Moles
Quantity
Used


Name
Catalog #
g/mol
mol-LR
moles
Units
Units







2,3,4-Trimethoxy-
Oakwood/98%/
196.20
1.00
140.16
 27.5 kg
 27.5 kg


benzaldehyde
078721; Chem-Impex/








NA/26868; Chem-








Impex/NA/26868







1-(2-hydroxyethyl)piperazine
Aldrich/98%/
130.19
1.1 
154.18
 20.1 kg
 20.0 kg



H28807







2-Methyltetrahydrofuran (2-
Aldrich/≥99.5%/
N/A
N/A
N/A
309.5 kg
 338.3 kg


MeTHF)
155810



Plus As








Needed



Acetic Acid (AcOH)
Aldrich/≥99%/
N/A
N/A
N/A
 1.40 kg
1.4101 kg



A6283







Sodium Triacetoxy
Oakwood/95%/
211.94
2.00
280.32
 59.4 kg Plus
 60.3 kg


Borohydride (STAB)
044864



As Needed



Sodium Hydroxide solution,
Aldrich/50% in H2O/
40
6.09
853.57
 68.3 kg
 68.3 kg


50% in H2O (50% NaOH in
415413







H2O)








Sodium Chloride
Aldrich/ACS/
N/A
N/A
N/A
 19.0 kg
 19.0 kg


(NaCl)
S9888







Methyl tert-Butyl Ether
Aldrich/ACS/
N/A
N/A
N/A
417.3 Plus
 552.1 kg


(MTBE)
443808; Oakwood/



As Needed




ACS/099538







Water
Mediatech/WFI/25-
N/A
N/A
N/A
323.4 kg
 323.4 kg



055-X1; RMBI/USP/








WPW-USN-2XL







Heptane
Aldrich/99%/
N/A
N/A
N/A
159.8 kg
 162.1 kg



H2198; Oakwood/








ACS/044743; BDH/








ACS/BDH1127







Nitrogen Gas
Airgas ≥
N/A
N/A
N/A
Quantity
Quantity


(house system)
99%



Sufficient
Sufficient







(QS)









  • 1) Sodium Triacetoxy Borohydride (STAB; 60.3 kg; CHP Lot #: 181-190220) and 2-MeTHF (189.2 kg; CHP Lot #: 234-190227) was charged to reactor R-401.

  • 2) The contents of R-401 were agitated and the temperature was adjusted to 15° C.±5° C.

  • 3) 2,3,4-trimethoxybenzaldehyde (27.5 kg; CHP Lot #: 275-190311, 142-190212) and 2-MeTHF (71.1 kg: CHP Lot #: 234-190227) was charged to reactor R-402.

  • 4) Agitation of reactor R-402 was started.

  • 5) 2-(piperazin-1-yl)ethan-1-ol (20.0 kg; CHP Lot #: 173-190220) and 2-MeTHF (47.3 kg; CHP Lot #: 234-190227) was charged to reactor R-402.

  • 6) The contents of reactor R-402 were agitated for at least 5 minutes.

  • 7) Acetic Acid (1.41 kg: CHP Lot #: 151-190214) was charged to reactor R-401 while keeping the temperature of the mixture below 25° C.

  • 8) Tmax=14.4° C.

  • 9) The contents of reactor R-402 were transferred over 1 h 19 min while keeping the temperature of the mixture below 25° C.

  • 10) Tmax=29.2° C. (the temperature went out of range during the addition)

  • 11) The reaction was approved to proceed forward

  • 12) The temperature of the contents of R-401 were adjusted to 20° C.±5° C. and agitated for at least 6 hours at 20° C.±5° C.

  • 13) The contents of R-401 were sampled after approximately 19 hours.

  • 14) Analysis of the sample by QC indicated no peak of 2,3,4-trimethoxybenzaldehyde was detected. (specification ≤1.5 area %)

  • 15) The temperature of the contents of R-401 were adjusted to 15° C.±5° C.

  • 16) Water (247.5 kg; CHP Lot #: 232-190227) was charged to R-401 while keeping the temperature below 25° C.

  • 17) Tmax=14.6° C.

  • 18) The temperature of the contents of R-401 was adjusted to 20° C.±5° C. and the contents were agitated for 30 minutes.

  • 19) The contents of R-401 were allowed to settle for 30 minutes.

  • 20) Phase cut was performed with the aqueous layer being transferred to R-402.

  • 21) MTBE (203.8 kg; CHP Lot #: 207-190222) was charged to R-402.

  • 22) The temperature of the contents of R-402 was adjusted to 0° C.±5° C.

  • 23) 50% NaOH (68.3 kg; CHP Lot #: 145-190213, 150-190214) was charged to R-402 while maintaining a temperature below 25° C.

  • 24) Tmax=11.5° C.

  • 25) After complete addition, the temperature of the contents of R-402 was adjusted to 20° C.±5° C.

  • 26) The contents in R-402 were agitated for at least 30 min, followed by allowing the contents to settle for at least 30 min.

  • 27) A phase cut was performed with the aqueous layer being transferred to reactor R-401 and the organic layer remaining in reactor R-402.

  • 28) MTBE (61.0 kg; CHP Lot #: 207-190222) was charged to R-401.

  • 29) The temperature of the contents of R-401 was adjusted to 20° C.±5° C.

  • 30) The contents in R-401 were agitated for at least 15 min, followed by allowing the contents to settle for at least 15 min.

  • 31) A phase cut was performed with the aqueous layer being transferred to a drum and the organic later remaining in reactor R-401.

  • 32) FIO pH check of drummed aqueous layer pH=13.20

  • 33) The contents in R-402 were transferred to R-401.

  • 34) 20% NaCl solution (94.4 kg; NaCl: 19.0 kg, CHP Lot #: 156-190214; Water (75.9 kg; CHP Lot #: 232-190227) was charged to R-401, agitated for at least 15 minutes and allowed to settle for at least 30 minutes.

  • 35) A phase cut was performed with the aqueous layer being transferred to a drum.

  • 36) The solution in R-401 was distilled under reduced pressure while maintaining a temperature <45° C. to approximately ˜55 L total volume.

  • 37) MTBE (61.1 kg; CHP Lot #: 207-190222) was charged to R-401.

  • 38) The contents in R-401 were distilled under reduced pressure while maintaining a temperature <45° C. to approximately ˜82 L total volume.

  • 39) MTBE (61.1 kg; CHP Lot #: 207-190222) was charged to R-401.

  • 40) The contents in R-101 were distilled under reduced pressure while maintaining a temperature <45° C. to approximately ˜82 L total volume.

  • 41) The contents of R-401 were sampled (IPC sample: 2493-1903-00484-85-01) to check the water content of the solution by KF analysis.

  • 42) KF=1.6% (specification ≤0.5%)

  • 43) MTBE (61.1 kg; CHP Lot #: 207-190222) was charged to R-401.

  • 44) The contents in R-101 were distilled under reduced pressure while maintaining a temperature <45° C. to approximately ˜82 L total volume.

  • 45) The contents of R-401 were sampled (IPC sample: 2493-1903-00484-88-01) to check the water content of the solution by KF analysis.

  • 46) KF=0.8% (specification ≤0.5%)

  • 47) MTBE (61.1 kg; CHP Lot #: 207-190222) was charged to R-401.

  • 48) The contents in R-101 were distilled under reduced pressure while maintaining a temperature <45° C. to approximately ˜82 L total volume.

  • 49) The contents of R-401 were sampled (IPC sample: 2493-1903-00484-91-01) to check the water content of the solution by KF analysis.

  • 50) KF=0.4% (specification ≤0.5%)

  • 51) MTBE (30.9 kg; CHP Lot #: 207-190222) was charged to R-401.

  • 52) The temperature of the contents of R-401 was adjusted to 40° C.±5° C.

  • 53) Heptane (56.3 kg; CHP Lot #: 233-190227) was charged over 8 min to R-401 while maintaining the temperature at 40° C.±5° C.

  • 54) Tmin=38.1° C.

  • 55) A FIO sample (FIO sample: 2493-1903-00484-100-01) was taken to observe the ratio of MTBE:Heptane of the contents in R-401. The ratio was 1.5:6.0.

  • 56) The temperature of the contents of R-401 were adjusted to 28° C.±5° C. (Target 26° C. to 29° C.). over at least 30 min and agitated at that temperature for at least 30 min.

  • 57) Solid formation was observed.

  • 58) The temperature of the contents of R-401 were adjusted to 30° C.±3° C. and agitated for at least 30 min.

  • 59) Heptane (56.4 kg; CHP Lot #: 233-190227) was charged over 24 min to R-401 while maintaining the temperature at 30° C.±5° C.

  • 60) Tmin=30.2° C.

  • 61) The temperature of the contents of R-401 were adjusted to 30° C.±3° C. and agitated for at least 20 min.

  • 62) The temperature of the contents of R-401 were adjusted to 20° C.±5° C. over at least 30 min and agitated for at least 20 min.

  • 63) The temperature of the contents of R-401 were adjusted to 5° C.±5° C. over at least 30 min and agitated for at least 30 min.

  • 64) The solid was collected on Filter-FD-400.

  • 65) The contents of Filter-FD-400 were washed with cold heptane (49.4 kg; CHP Lot #: 233-190227).

  • 66) The contents of Filter-FD-400 were dried under vacuum at ≤25° C. with a stream of N2 for at least 16 hours.

  • 67) An IPC sample (IPC sample: 2493-1903-00484-122-01) was submitted to QC for LOD.
    • LOD=0.20% (specification ≤0.5%)

  • 68) The product CV-8814 Free Base (CV8814 Free Base) was double bagged, goose necked, and weighed.

  • 69) Analysis of dried material (IPC sample: 2493-1903-00484-122-01):
    • Appearance: White to off white solid
    • Weight: 34.0 kg (78.0% yield)
    • HPLC Purity=100.0%
    • 1H NMR: conforms to structure

  • 70) A 5 kg portion of CV-8814 Free Base (CV8814 Free Base) was removed from the bulk material double bagged, goose necked, and set aside for release under the Lot #2493-1903-00484.



Step 2, formation of CV8972 Monohydrate (2479-1903-00489), was performed according to Scheme 3.




embedded image


Production details for steps 2a and 2b are provided in Table 3.















TABLE 3











Actual





Equiv.

Expected
Quantity


Identity
Vendor/Grade/
MW
Moles/
Moles
Quantity
Used


Name
Catalog #
g/mol
mol-LR
moles
Units
Units





















CV8814 Free Base (IMB-
CHP/NA/CHP Lot
310.39
1.00
92.79
 28.8 kg
 28.8 kg


1028814)
#








2493-1903-00484







Nicotinic Acid
Aldrich/≥98%/
123.11
1.5
139.19
 17.1 kg
 17.1 kg



N4126; Alfa Aesar/








99%/A12683







CV8814 Free Base (IMB-
CHP/NA/CHP Lot
310.39
1.00
92.79
 28.8 kg
 28.8 kg


1028814)
#








2493-1903-00484







Nicotinic Acid
Aldrich/≥98%/
123.11
1.5
139.19
 17.1 kg
 17.1 kg



N4126; Alfa Aesar/








99%/A12683







Dichloromethane (DCM)
Aldrich/ACS/
N/A
N/A
N/A
536.2 kg
533.4 kg



D65100







EDC
Oakwood/99%/
191.71
1.5
139.19
 26.7 kg
 26.7 kg



024810;








Chem-Impex/








≥99%/00050







4-(Dimethylamino)pyridine
Aldrich/≥99%/
122.17
0.15
13.92
 1.70 kg
 1.70 kg


(DMAP)
107700







Hydrochloric Acid (Conc
Avantor/ACS/
36.46
3.3
306.21
 30.2 kg
 30.2 kg


HCl)
2612-X1







Sodium Bicarbonate
Aldrich/ACS/
N/A
N/A
N/A
  4.0 kg
 4.00 kg


(NaHCO3)
S6014







Water
Mediatech/WFI/
N/A
N/A
N/A
140.9 kg
140.4 kg



25-055-X1; RMBI/








USP/








WPW-USN-2XL







Methyl Ethyl Ketone
Oakwood/99.9%/
N/A
N/A
N/A
858.0 kg
857.8 kg


(MEK)
075238







Nitrogen Gas
Airgas ≥
N/A
N/A
N/A
Quantity
Quantity


(house system)
99%



Sufficient
Sufficient







(QS)









  • 1) Nicotinic Acid (17.1 kg, CHP Lot #201-190222) and DCM (153.0 kg, CHP Lot #328-190326) were charged to reactor R-401.

  • 2) The contents of R-401 was agitated and the temperature was adjusted to 15±5° C.

  • 3) CV8814 Free Base (28.8 kg, CHP Lot #2493-1903-00484), EDC (26.7 kg, CHP Lot #147-190213), DMAP (1.70 kg, CHP Lot #152-190214), and DCM (306.6 kg, CHP Lot #328-190326) were charged to reactor R-402.

  • 4) The contents of the R-402 were agitated for at least 20 minutes.

  • 5) The contents of R-402 were transferred to R-401 over at least 30 minutes while keeping the temperature below 25° C.

  • 6) Tmax=20.0° C.

  • 7) The temperature of the contents of R-401 were adjusted to 20±5° C. and was agitated for at least 16 hours.

  • 8) The contents of R-401 were sampled after approximately 16 hours.

  • 9) Analysis of the sample by QC indicated 0% (0.05%) of CV-8814 Free Base (CV8814 Free Base) with respect to CV8972 was detected (Specification: ≤1% CV8814 Free Base).

  • 10) The contents of the R-401 were adjusted to 10±5° C.

  • 11) Water (29.2 kg, CHP Lot #329-190326) was slowly added while keeping the temperature below 25° C.

  • 12) Tmax=12.3° C.

  • 13) The temperature of the contents of R-401 was adjusted to 20±5° C., agitated for at least 15 min and allowed to settle for at least 15 min.

  • 14) Phases were separated.

  • 15) The lower organic layer containing product was transferred to reactor R-402. The aqueous layer was sent to a drum.

  • 16) Water (29.0 kg, CHP Lot #329-190326) was charged to the reactor.

  • 17) The biphasic mixture was agitated for 15 min and allowed to settle for 15 min.

  • 18) Phases were separated.

  • 19) The organic layer containing product was transferred to reactor R-401. The aqueous layer was sent to a drum.

  • 20) 8% NaHCO3 aqueous solution (Sodium Bicarbonate, 4.0 kg, CHP Lot #192-190221; Water, 53.2 kg, CHP Lot #329-190326) was added to the reactor.

  • 21) The mixture was agitated for at least 15 min and allowed to settle for at least 15 min.

  • 22) Phases were separated.

  • 23) The lower organic layer containing product was transferred to reactor R-402. The aqueous layer was sent to a drum.

  • 24) Water (29.0 kg, CHP Lot #329-190326) was added to the reactor.

  • 25) The mixture was agitated for at least 15 min and allowed to settle for at least 15 min.

  • 26) R-401 was cleaned with Water (17.6 kg, CHP Lot #329-190326) and MEK (5.9 kg, CHP Lot #330-190326) and dried with a stream of N2.

  • 27) Phases were separated.

  • 28) The lower organic layer containing product was transferred to reactor R-401. The aqueous layer was sent to a drum.

  • 29) The contents of R-401 were concentrated under reduced pressure to approx. 72 L keeping the temperature below 45° C.

  • 30) Tmax=32.0° C.

  • 31) MEK (139.0 kg, CHP Lot #330-190326) was charged to R-401.

  • 32) The contents of R-401 were concentrated under reduced pressure to approx. 72 L keeping the temperature below 45° C.

  • 33) Tmax=32.0° C.

  • 34) MEK (139.1 kg, CHP Lot #330-190326) was charged to R-401.

  • 35) The contents of R-401 were concentrated under reduced pressure to approx. 72 L keeping the temperature below 45° C.

  • 36) Tmax=29.2° C.

  • 37) FIO 1H NMR to determine the DCM:MEK ratio was taken. DCM:MEK=1:214.9

  • 38) MEK (185.5 kg, CHP Lot #330-190326) was charged to R-401.

  • 39) MEK (208.7 kg, CHP Lot #330-190326) and conc. HCl (30.2 kg, CHP Lot #274-190311) were charged to a cleaned R-402.

  • 40) The temperature of the contents of reactor was adjusted to 25±5° C.

  • 41) The contents of R-401 were transferred to R-402 over approx. 1 hour while maintaining a temperature below 35° C.

  • 42) Tmax=27.2° C.

  • 43) The temperature of the contents of R-402 was heated to 50±5° C. and was agitated for at least 1 hour.

  • 44) The temperature of the contents of the reactor was cooled to 20±5° C. over 2 hours.

  • 45) The contents of the reactor were agitated at 20±5° C. for 15 hours.

  • 46) The solid was filtered.

  • 47) The filter cake was rinsed with MEK (58.0 kg, CHP Lot #330-190326).

  • 48) The filter cake was rinsed with MEK (58.0 kg, CHP Lot #330-190326).

  • 49) The wet cake was dried in tray dryer 20-25° C. without nitrogen bleed for at least 16 hours.

  • 50) An IPC sample (IPC sample: 2479-1903-00489-87-01) was submitted to QC for KF.
    • Water content (Specification: ≤4% by cKF): 3.3%

  • 51) The product CV8972 Monohydrate was doubled bagged, goose necked, and weighed.

  • 52) Analysis of the dried material (IPC sample: 2479-1903-00489-87-01): Appearance: White to off-white solid
    • Weight: 48.6 kg (96.4% yield)
    • 1H NMR: conforms to structure
    • HPLC purity (area %): 99.1%
    • FIO Residual Solvents GC Analysis:
      • 2-MeTHF: No Peak
      • DCM: No Peak
      • MTBE: No Peak
      • Heptane: No Peak
      • MEK: 343 ppm
      • Acetic Acid: 874 ppm



Step 3, formation of CV-8972 (2479-1904-00494), was performed according to Scheme 4.




embedded image


Production details for step 3 are provided in Table 4.















TABLE 4











Actual





Equiv.

Expected
Quantity


Identity
Vendor/Grade/
MW
Moles/
Moles
Quantity
Used


Name
Catalog #
g/mol
mol-LR
moles
Units
Units







CV8972
CHP/NA/CHP Lot #2479-
542.88
1
89.34
  48.5 kg
  48.5 kg


monohydrate
1903-00489







Methanol
Aldrich/ACS/179337;
N/A
N/A
N/A
 230.5 kg
 230.5 kg



Pharmco/WORLD/








339WORLD-X1; BDH/ACS/








BDH1135







Methyl Ethyl
Oakwood/99.9%/075238
N/A
N/A
N/A
1147.8 kg
1149.4 kg


Ketone (MEK)








Water
Mediatech/WFI/25-055-X1;
N/A
N/A
N/A
  72.8 kg
  72.5 kg



RMBI/USP/WPW-USN-2XL







Nitrogen Gas
Airgas ≥
N/A
N/A
N/A
Quantity
Quantity


(house system)
99%



Sufficient
Sufficient







(QS)









  • 1) CV8972 monohydrate (48.5 kg, CHP Lot #2479-1903-00489), Water (48.5 kg, CHP Lot #329-190326), Methanol (19.2 kg, CHP Lot #379-190404), and MEK (39.0 kg, CHP Lot #330-190326) were charged respectively to a reactor R-402.

  • 2) The contents of the R-402 was adjusted to 20° C.±5° C. and agitated until a solution was obtained.

  • 3) The contents of R-402 were transferred to R-401 through a 0.45 micron in-line filter.

  • 4) Water (24.0 kg, CHP Lot #329-190326) and Methanol (19.2 kg, CHP Lot #379-190404) were charged to R-402 and transferred to R-401 through a 0.45 micron in-line filter.

  • 5) Methanol (192.1 kg, CHP Lot #379-190404) was charged to R-401 through a 0.45 micron in-line filter.

  • 6) The temperature of the contents of R-401 was adjusted to 60±5° C.

  • 7) MEK (899.6 kg, CHP Lot #330-190326; 380-190404) was charged to R-401 through a 0.45 micron in-line filter over approx. 2 hours while maintaining a temperature of 60±5° C.

  • 8) The contents of R-401 were agitated at 60±5° C. for at least 4 hours.

  • 9) The temperature of R-401 was adjusted to 20±5° C. over at least 3 hours.

  • 10) The contents of R-401 were agitated at 20±5° C. for approx. 9 hours.

  • 11) The contents of R-401 were sent to a filter.

  • 12) The filter cake was rinsed with MEK (105.4 kg, CHP Lot #380-190404).

  • 13) The filter cake was rinsed with MEK (105.4 kg, CHP Lot #380-190404).

  • 14) The wet cake were dried on filter with vacuum for at least 30 minutes.

  • 15) The wet cake was packaged into a filer dryer and dried under reduced pressure at ≤30° C. for at least 12 hours.

  • 16) An IPC sample (IPC sample: 2479-1904-00494-32-01) was submitted to QC for KF and Residual Solvent GC.
    • Water content (Specification: 2.8-3.8% by cKF)=3.5%
    • Residual Solvent GC Analysis (Specification: MeOH≤3000 ppm; MEK ≤5000 ppm) MeOH=215 ppm; MEK=185 ppm

  • 17) The product CV-8972 was double bagged, goose necked, and weighed.

  • 18) Analysis of the dried material (IPC sample: 2479-1904-00494-32-01)
    • Appearance: White to off-white solid
    • Weight=41.7 kg (86.0% yield)
    • HPLC purity (area %)=99.9%
      • Known Impurities:
        • Nicotinic Acid: No Peak
        • DMAP: No Peak
        • CV8814: 0.1%
        • 2,3,4-Trimethoxy Benzaldehyde: No Peak
        • Trimetazidine: No Peak
        • CV-10099: No Peak
        • CV-10046: No Peak
        • XRPD: Conforms to Form A
        • Chloride Ion content: 19.4%
        • 1H NMR: conforms to structure



Conclusion


The results provided above show that CV-8972 can be synthesized using Scheme 1. The reductive amination in step 1 using 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol starting materials, sodium triacetoxyborohydride (STAB) as the reductant, catalytic acetic acid (AcOH), and 2-methyltetrahydrofuran (2-MeTHF) gave a 78.0% yield of CV-8814 Free Base (CV8814 Free Base) with 100.0% purity by HPLC after aqueous workup, solvent exchange, and crystallization. A 5 kg portion of CV-8814 Free Base (CV8814 Free Base) was diverted from the synthesis for release. The step 2 coupling of CV8814 Free Base with nicotinic acid in the presence of EDC and catalytic DMAP in DCM went to complete conversion to CV8972 Free Base by HPLC IPC. Solvent exchange to MEK and addition into concentrated HCl in MEK afforded CV8972 Monohydrate in a 96.4% yield with 99.1% purity by HPLC. The final form conversion in step 3 was completed by heating CV8972 Monohydrate to 60° C.±5° C. in a mixture of water, methanol, and MEK and precipitating out with the addition of MEK. The white solid CV-8972 was obtained as form A confirmed by XRPD analysis, in an 86.0% yield with 99.9% purity by HPLC. The overall yield of the GMP synthesis of CV-8972 was 64.7%. The final amount of CV-8972 produced was 41.7 kg.


INCORPORATION BY REFERENCE

References and citations to other documents, such as patents, patent applications, patent publications, journals, books, papers, web contents, have been made throughout this disclosure. All such documents are hereby incorporated herein by reference in their entirety for all purposes.


EQUIVALENTS

Various modifications of the invention and many further embodiments thereof, in addition to those shown and described herein, will become apparent to those skilled in the art from the full contents of this document, including references to the scientific and patent literature cited herein. The subject matter herein contains important information, exemplification, and guidance that can be adapted to the practice of this invention in its various embodiments and equivalents thereof.

Claims
  • 1. A method for preparing a compound of Formula (X):
  • 2. The method of claim 1, wherein the step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol comprises sodium triacetoxyborohydride.
  • 3. The method of claim 1, wherein the step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol comprises acetic acid.
  • 4. The method of claim 1, wherein the step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol comprises 2-methyltetrahydrofuran.
  • 5. The method of claim 1, wherein the step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol is performed at from about 15° C. to about 25° C.
  • 6. The method of claim 1, wherein the step of reacting 2,3,4-trimethoxybenzaldehyde and 2-(piperazin-1-yl)ethan-1-ol does not comprise dichloromethane.
  • 7. The method of claim 1, wherein the step of reacting the free base form of the compound of Formula (IX) with nicotinic acid produces a free base form of the compound of Formula (X).
  • 8. The method of claim 7, wherein the step of reacting the free base form of the compound of Formula (IX) with nicotinic acid comprises 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide.
  • 9. The method of claim 7, wherein the step of reacting the free base form of the compound of Formula (IX) with nicotinic acid comprises 4-(dimethylamino)pyridine.
  • 10. The method of claim 7, wherein the step of reacting the free base form of the compound of Formula (IX) with nicotinic acid comprises dichloromethane.
  • 11. The method of claim 7, wherein the step of reacting the free base form of the compound of Formula (IX) with nicotinic acid is performed at from about 20° C. to about 25° C.
  • 12. The method of claim 7, wherein the method further comprises converting the free base form of the compound of Formula (X) to a salt form of the compound of Formula (X).
  • 13. The method of claim 12, wherein the salt form of the compound of Formula (X) is a HCl salt.
  • 14. The method of claim 12, wherein the salt form of the compound of Formula (X) is monohydrate.
  • 15. The method of claim 12, wherein the step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) comprises HCl.
  • 16. The method of claim 12, wherein the step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) comprises methyl ethyl ketone.
  • 17. The method of claim 12, wherein the step of converting the free base form of the compound of Formula (X) to the salt form of the compound of Formula (X) is performed at about 50° C.
  • 18. The method of claim 12, wherein the method further comprises converting the salt form of the compound of Formula (X) from a first crystal form to a second crystal form.
  • 19. The method of claim 18, wherein the step of converting the salt form of the compound of Formula (X) from the first crystal form to the second crystal form comprises one selected from the group consisting of precipitating the salt form of the compound of Formula (X), changing the solvent of the salt form of the compound of Formula (X), and incubating the salt form of the compound of Formula (X), at about 60° C.
  • 20. The method of claim 1, wherein the method does not comprise use of dioxane, ethylacetate, or potassium carbonate.
  • 21. A method for preparing a compound of Formula (X):
CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims the benefit of, and priority to, U.S. Provisional Patent Application No. 63/046,123, filed Jun. 30, 2020, the contents of which are incorporated by reference.

US Referenced Citations (72)
Number Name Date Kind
4100285 Murai et al. Jul 1978 A
4166452 Generales, Jr. Sep 1979 A
4256108 Theeuwes Mar 1981 A
4265874 Bonsen et al. May 1981 A
4574156 Morita et al. Mar 1986 A
4845099 Ruger et al. Jul 1989 A
4876257 Hajos et al. Oct 1989 A
4885300 Press et al. Dec 1989 A
5077288 Lavielle et al. Dec 1991 A
5286728 Ferrini Feb 1994 A
5340809 Gaudry et al. Aug 1994 A
5380726 Ferrini Jan 1995 A
5384319 Ferrini Jan 1995 A
5397780 Mizuno et al. Mar 1995 A
5399557 Mizuno et al. Mar 1995 A
5401743 Rendenbach-Mueller et al. Mar 1995 A
5428038 Chatterjee et al. Jun 1995 A
5527800 Goto et al. Jun 1996 A
5591849 Kato et al. Jan 1997 A
5641779 Halazy et al. Jun 1997 A
5770735 Emonds-Alt et al. Jun 1998 A
5776937 Gante et al. Jul 1998 A
5849745 Wierzbicki et al. Dec 1998 A
5856326 Anthony et al. Jan 1999 A
5962448 Mizuno et al. Oct 1999 A
5977111 Mizuno et al. Nov 1999 A
6087346 Glennon et al. Jul 2000 A
6121267 Glase et al. Sep 2000 A
6200989 Gillis et al. Mar 2001 B1
6214841 Jackson et al. Apr 2001 B1
6271223 Mizuno et al. Aug 2001 B1
6331623 Mizuno et al. Dec 2001 B1
6528529 Brann et al. Mar 2003 B1
6562978 Imamura et al. May 2003 B1
6693099 Degenhardt et al. Feb 2004 B2
7638531 Mutahi et al. Dec 2009 B2
7666866 Franciskovich et al. Feb 2010 B2
7772251 Sturzebecher et al. Aug 2010 B2
7968538 Becker et al. Jun 2011 B2
8016783 Pastore et al. Sep 2011 B2
8202901 Lopaschuk et al. Jun 2012 B2
8461117 Sufi et al. Jun 2013 B2
8569495 Chassaing et al. Oct 2013 B2
8697661 Kritikou Apr 2014 B2
9096538 Nakamura et al. Aug 2015 B2
9120801 Alisi et al. Sep 2015 B2
10167258 Chuang et al. Jan 2019 B2
10556013 Levin Feb 2020 B2
10918728 Levin Feb 2021 B2
20030191182 Lopaschuk et al. Oct 2003 A1
20030232877 Sikorski et al. Dec 2003 A1
20040082564 Arrhenius et al. Apr 2004 A1
20050004121 Palani et al. Jan 2005 A1
20070004750 Lorsbach et al. Jan 2007 A1
20080108618 Brann et al. May 2008 A1
20080161400 Virsik et al. Jul 2008 A1
20090197891 Lecanu et al. Aug 2009 A1
20090258064 Newell et al. Oct 2009 A1
20100022530 Schiemann et al. Jan 2010 A1
20110046370 Sim et al. Feb 2011 A1
20110137362 Foreman et al. Jun 2011 A1
20110212072 Henkel et al. Sep 2011 A1
20120214818 Dudley Aug 2012 A1
20160060530 Archetti et al. Mar 2016 A1
20160346397 Milne et al. Dec 2016 A1
20170008950 Capon Jan 2017 A1
20170105414 Nakano et al. Apr 2017 A1
20180360975 Levin Dec 2018 A1
20190084917 Savourey et al. Mar 2019 A1
20190216936 Levin Jul 2019 A1
20200138963 Levin May 2020 A1
20210353617 Levin et al. Nov 2021 A1
Foreign Referenced Citations (47)
Number Date Country
2170615 Mar 1995 CA
2186010 Sep 1995 CA
101747292 Jul 2011 CN
2714996 Oct 1977 DE
0144991 Jun 1985 EP
0251141 Jan 1988 EP
615855 Sep 1994 EP
661266 Jul 1995 EP
749967 Dec 1996 EP
1634598 Mar 2006 EP
1886994 Feb 2008 EP
2727916 May 2014 EP
S57131777 Aug 1982 JP
2000147773 May 2000 JP
2006113343 Apr 2006 JP
2015017236 Jan 2015 JP
1995000165 Jan 1995 WO
9626196 Aug 1996 WO
9630054 Oct 1996 WO
9630343 Oct 1996 WO
9728141 Aug 1997 WO
9746549 Dec 1997 WO
9858638 Dec 1998 WO
9950247 Oct 1999 WO
2001005763 Jan 2001 WO
2002058698 Aug 2002 WO
2002064576 Aug 2002 WO
2003006628 Jan 2003 WO
2006027223 Mar 2006 WO
2006117686 Nov 2006 WO
2006133784 Dec 2006 WO
2007075629 Jul 2007 WO
2007096251 Aug 2007 WO
2007116074 Oct 2007 WO
2007116243 Oct 2007 WO
2008109991 Sep 2008 WO
2009015485 Feb 2009 WO
2009058818 May 2009 WO
2009066315 May 2009 WO
2009156479 Dec 2009 WO
2011032099 Mar 2011 WO
2012049101 Apr 2012 WO
2015018660 Feb 2015 WO
2016005576 Jan 2016 WO
2016107603 Jul 2016 WO
2018236745 Dec 2018 WO
2020081361 Apr 2020 WO
Non-Patent Literature Citations (36)
Entry
Bhosle, 2006, Mutual Prodrug Concept: Fundamentals and Applications, Indian Journal of Pharmaceutical Sciences, May-June, pp. 286-294.
Cheng, 2006, Discovery of Potent and Orally Available Malonyl-CoA Decarboxylase Inhibitors as Cardioprotective Agents, J. Med. Chem. 49:4055-4058.
Cheng, 2006, Synthesis and structure-activity relationship of small-molecule malonyl coenzyme A decarboxylase nhibitors, J. Med. Chem. 49:1517-1525.
DAS, 1995, Essential Fatty Acid Metabolism in Patients with Essential Hypertension, Diabetes Mellitus and Coronary Heart Disease, Prostaglandins Leukotrienes and Essential Fatty Acids, 52, 387-391.
Extended European Search Report issued in European Application No. 18821590.9, dated Oct. 5, 2020, 33 pages.
Fillmore, 2014, Malonyl CoA: A Promising Target for the Treatment of Cardiac Disease, Int. Union of Biochem. and Mol. Biol., 66(3):139-146.
Fillmore, 2014, Mitochondrial fatty acid oxidation alterations in heart failure, ischemic heart disease and diabetic cardiomyopathy, Brit. J. Pharmacol. 171:2080-2090.
Folmes, 2005, Fatty Acid Oxidation Inhibitors in the Management of Chronic Complications of Atherosclerosis, Current Atherosclerosis Reports 2005, 7, 63-70.
GAO, 2011, Echocardiography in Mice. Curr Protoc Mouse Biol, 1:71-83.
GIBBS, 1995, Cardiac efficiency, Cardiovasc. Res. 30:627-634.
International Search Report and Written Opinion issued in International Application No. PCT/US2020/034611, dated Oct. 14, 2020, 45 pages.
International Search Report and Written Opinion issued in International Application No. PCT/US2020/34608, dated Oct. 14, 2020, 28 pages.
International Search Report and Written Opinion issued in International Application No. PCT/US2020/34609, dated Oct. 14, 2020, 22 pages.
International Search Report and Written Opinion issued in International Application No. PCT/US2021/039303, dated Nov. 26, 2021, 19 pages.
International Search Report and Written Opinion dated Nov. 5, 2018, for International Patent Application PCT/US2018/038067 with International filing date Jun. 18, 2018 (11 pages).
International Search Report issued in an International Application No. PCT/US2021/030450, dated Sep. 27, 2021, 9 pages.
Kantor, 2000, The Antianginal Drug Trimetazidine Shifts Cardiac Energy Metabolism From Fatty Acid Oxidation to Glucose Oxidation by Inhibiting Mitochondrial Long-Chain 3-Ketoacyl Coenzyme A Thiolase, Circulation Research, 86:580-588.
Kotreka, 2011, Gastroretentive Floating Drug-Delivery Systems: A Critical Review, Critical Reviews in Therapeutic Drug Carrier Systems, 28(1):47-99.
Leriche, 2012, Cleavable linkers in chemical biology, Bioorg. Med. Chem. 20:571-582.
Levy, 2014, Vasodilators in Acute Heart Failure: Review of the Latest Studies, Curr Emerg Hosp Med Rep, 2 (2):126-134.
Lopaschuk, 2010, Myocardial Fatty Acid Metabolism in Health and Disease, Phys. Rev. 90:207-258.
Morin, 1998, Evidence for the existence of [3H]-trimetazidine binding sites involved in the regulation of the mitochondrial permeability transition pore, Brit. J. Pharmacol. 123:1385-1394.
Non-Final Office Action issued in U.S. Appl. No. 16/722,691, dated Aug. 19, 2020, 12 pages.
Pubchem, CID 2223657, Jul. 15, 2005, pp. 1-14.
Reddy, 2006, Lipid Metabolism and Liver Inflammation. II. Fatty liver disease and fatty acid oxidation, Am J Physiol Gastrointest Liver Physiol, 290: G852-G858.
Sabbah, 2005, Metabolic Therapy for Heart Disease: Impact of Trimetazidine, Heart Failure Reviews, 10,281-288.
Sannino, 2009, Biodegradable Cellulose-based Hydrogels: Design and Applications, Materials, 2:353-373.
Schipke, 1994, Cardiac efficiency, Basic Res. Cardiol. 89:207-40.
Spiekerkoetter, 2010, Mitochondrial fatty acid oxidation disorders: clinical presentation of long-chain fatty acid oxidation defects before and after newborn screening, J Inherit Metab Dis, 33:527-532.
The Merck Manual List of Diseases https://merckmanuals.com/professional (accessed Jan. 17, 2020), 4 pages.
Trammell, 2016, Nicotinamide riboside is uniquely and orally bioavailable in mice and humans, Nat. Commun. 7:12948, 14 pages.
Visser, 2008, Measuring cardiac efficiency: is it clinically useful? Heart Metab. 39:3-4.
Yuasa, 1988, Pharmacological Studies on the Actions of Trimetazidine and Its Derivatives, The Journal of Kansai Medical University, vol. 40, Issue 1, pp. 89-116.
Extended European Search Report issued in European Application No. 19872680.4, dated Jun. 20, 2022, 7 pages.
Extended European Search Report issued in European Application No. 22169109.0, dated Aug. 30, 2022, 7 pages.
Gallaher, 1993, Viscosity and Fermentability as Attributes of Dietary Fiber Responsible of rhte Hypocholesterolemic Effect in Hamsters, J Nutr., 123, pp. 244-252.
Related Publications (1)
Number Date Country
20210403429 A1 Dec 2021 US
Provisional Applications (1)
Number Date Country
63046123 Jun 2020 US