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DOI: 10.1055/s-0044-1792125
An Improved Synthesis Process of Ricolinostat: The First Orally Selective HDAC6 Inhibitor
Abstract
Ricolinostat (1) is the first orally available histone deacetylase 6 inhibitor in phase II clinical trials. The results from phase II clinical studies showed that the combination of Ricolinostat with bortezomib and dexamethasone is safe and active for the treatment of multiple myeloma. However, the reported synthesis routes of Ricolinostat were plagued by several limitations, including severe reaction conditions, elevated cost factors, and the employment of environmentally unfriendly reagents. This study aimed to improve the synthesis process of Ricolinostat, in which ethyl 2-chloropyrimidine-5-carboxylate (2) was used as the starting material, the target product was obtained through the reaction of nucleophilic aromatic substitution, the Ullmann coupling, hydrolyzation amide condensation, and aminolysis. The nucleophilic substitution (2 to 3) was performed in the presence of 1.2 equiv. aniline, 2.0 equiv. K2CO3 under 100°C, with a yield of 96%; the Ullmann reaction was performed in the presence of 0.5 equiv. CuI and 2.0 equiv. cesium carbonate; the post-processes of 3 and the desired product (1) that previously required column chromatography were replaced with recrystallization using the solvent of EtOH/H2O and DMF/H2O, respectively. Through the improved process, Ricolinostat was obtained with an isolated yield of 65.8% and a purity of 99.73%, which was much higher than the reported study. This route was both cost-effective and eco-friendly, making it suitable for industrial applications.
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Introduction
Histone deacetylases (HDACs) and histone acetyltransferases regulate gene expression by regulating the levels of histone acetylation in the nucleus.[1] HDACs can be classified into four classes (class I, II, III, and class IV) according to their location and functions.[2] HDACs play an important role in cancer and have been validated as targets for the development of anticancer drugs.[3] [4] [5] [6] However, in the clinic, most HDAC inhibitors are pan-HDAC inhibitors, with poor activity in solid tumors and significant toxic side effects.[7]
HDAC6 is the most unique member of the class II family of HDACs, mainly expressed in the cytoplasm and perinucleus, and highly expressed in the brain, heart, liver, kidney, and other organs.[8] [9] [10] HDAC6 is involved in a variety of intracellular physiological processes. It not only has strong HDAC activity but also mediates non-histone deacetylation.[11] Its main substrates include α-tubulin, Bax, heat shock protein 90, HIF1α, GRK2, p300, cortical actin, etc.[12] [13] It also interacts with VCP, nuclear factor-κB, Foxp3, tau, protein phosphatase 1, Ku70, PCKα, etc., and is involved in regulating cell morphology, autophagy, migration, and oxidative stress protection. Evidence suggests that overexpression of HDAC6 is closely related to a variety of disorders, including cancer, autoimmune diseases, neurodegenerative diseases, viral infections, and dilated cardiomyopathy.[14] [15] However, mice that knocked out HDAC6 survived well and developed normally, suggesting that selective inhibition of HDAC6 may not cause serious toxic effects.[16]
Ricolinostat is the first and most advanced selective HDAC6 inhibitor and is currently in a phase II clinical trial. The results from the Phase Ib clinical studies showed that Ricolinostat is a safe and well-tolerated HDAC6 inhibitor with antitumor activities in a wide range of cancers including glioblastoma, multiple myeloma, and melanoma.[17] The combination of Ricolinostat with bortezomib and dexamethasone is safe and active at the recommended phase II dose of 160 mg per day, suggesting that Ricolinostat is a promising approach for the treatment of multiple myeloma.[18]
Ricolinostat can be synthesized according to reported studies since 2018. Moore and Min[19] synthesized Ricolinostat (1) using ethyl 2-chloropyrimidine-5-carboxylate 2 as a starting material. Cuprous iodide (CuI)-catalyzed Ullmann reaction of the derivated ethyl 2-(phenylamino)pyrimidine-5-carboxylate (3) with iodobenzene afforded 2-(diphenylamino)pyrimidine intermediate (4). Hydrolysis of 4 in the presence of sodium hydroxide afforded the acid intermediate 5, which was condensed with methyl 7-aminoheptanoate (7) to afford the amide (6). Aminolysis of 6 with hydroxylamine provided the target compound Ricolinostat (1) ([Scheme 1A]).[19] However, column chromatography was repeatedly used in the separations, thereby limiting the widespread application of this route. Li et al synthesized Ricolinostat using 2,5-dichloropyrimidine (9) and diphenylamine (10) as starting materials ([Scheme 1B]).[20] The key steps include two steps of the Buchwald–Hartwig cross-coupling reaction to give the target product. However, the overall yield was only 47.3%. In addition, the use of poisonous reagents (e.g., Zn(CN)2) in the cyanation reaction is environmentally unfriendly, and expensive transition metal catalysts (e.g., Pd2(dba)3) again limit the large-scale industrial synthesis of Ricolinostat (1).
This study aimed to explore a synthesis method suitable for the industrial production of Ricolinostat (1). In this work, the synthesis route of Ricolinostat (1) in [Scheme 1A] was optimized. We focused on solving problems as follows: (1) improving the reaction conditions of nucleophilic substitution (2 to 3); (2) improving the reaction conditions of the Ullmann reaction (3 to 4); (3) using recrystallization instead of all column chromatography for purification.
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Results and Discussion
Synthesis Route of Ricolinostat (1)
As shown in [Scheme 2], the commercially available 2 was reacted with aniline to afford intermediate 3, which then reacted with iodobenzene through the Ullmann reaction to afford intermediate 4 without any purification. Hydrolysis of 4 in the solution of lithium hydroxide afforded the acid intermediate 5, which was then condensed with methyl-7-aminoheptanoate 7 to achieve the amide 6. Aminolysis of 6 with hydroxylamine provided the target compound Ricolinostat 1. We optimized the nucleophilic substitution (2 to 3), the Ullmann reaction (3 to 4) as well as the post-processes (3 and 1) that require column chromatography and used recrystallization instead ([Scheme 3]). Overall, this optimized synthesis route was operated easily and was able to deliver the product with a yield of 65.8% and a purity of 99.73%, which was much higher than the reported study (6%).[19]
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Optimization of the Nucleophilic Substitution (2 to 3)
Ethyl 2-(phenylamino)pyrimidine-5-carboxylate (3) can be obtained from the reaction of 2 with aniline.[21] [22] In this work, the equiv. of aniline was screened. We started an investigation with 1.0 equiv. of aniline, following the reported research ([Table 1], entry 1).[23] [24] When the equiv. of aniline was increased, the isolated yield of compound 3 was enhanced, with the maximum effect being seen in 1.2 equiv. When the equiv. exceeds 1.2 equiv., the yield did not increase significantly (data are not available here). Thus, 1.20 equiv. of aniline was chosen in the reaction.
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||
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Entry |
Aniline (equiv.) |
Yield (%)[b] |
1 |
1.00 |
72.4 |
2 |
1.05 |
82.5 |
3 |
1.10 |
90.3 |
4 |
1.15 |
95.5 |
5 |
1.20 |
98.8 |
a Reaction conditions: 2 (10 g scale,1.0 equiv.), K2CO3 (1.5 equiv.), DMF (5 V).
b Isolated yields.
Temperature is closely related to energy consumption and production costs in the pharmaceutical industry. We attempt to explore an appropriate reaction temperature suitable for scale-up. The initial refluxed condition was 135 to 125°C ([Table 2], entry 1) according to a reported study.[19] Reducing the temperature to 125 to 105°C had essentially no impact ([Table 2], entries 2 − 3). Reducing the temperature to 105 to 95°C resulted in a longer reaction time ([Table 2], entry 4). Reducing the temperature to 95 to 85°C resulted in incomplete conversion ([Table 2], entry 5). Therefore, the optimal temperature was found to be 105 to 95°C.
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|||
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Entry |
Temperature (°C) |
Time (h) |
Conversion (%)[b] |
1 |
135–125 |
4 |
100 |
2 |
125–115 |
4 |
100 |
3 |
115–105 |
8 |
100 |
4 |
105–95 |
8 |
100 |
5 |
95–85 |
16 |
53.9 |
a Reaction conditions: 2 (10 g scale,1.0 equiv.), aniline (1.2 equiv.), DMF (5 V).
b Measured by HPLC.
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Optimization of the Ullmann Reaction Catalyzed by Copper(I) Iodide (3 to 4)
N-Aryl amine moieties are important structural features that are ubiquitously found in numerous natural products, pharmaceuticals, agrochemicals, and material molecules.[25] A typical approach for preparing N-aryl amines is the copper-catalyzed Ullmann coupling reaction of aryl halides with amines.[26] Traditionally, the reaction requires a high reaction temperature and a stoichiometric amount of copper reagent, greatly limiting the reaction scope.[27] In this work, the Ullmann reaction of 3 to produce 4 was optimized.
Catalysis types were screed due to the low yield in the reported study. In our preliminary study, Pd2(dba)3, PdCl2(PPh3)2, Pd(PPh3)4, Cu2O, and CuI were screened for the Ullmann reaction, and we found that the copper(I) iodide from the reported study showed the best catalytic efficiency, but a small amount of starting material 3 remained ([Table S1], [Supporting Information] [available in the online version]). Fortunately, we found that increasing the amount of copper(I) iodide could improve the conversion. When the amount of copper(I) iodide increased to 0.5 equiv., the substrate could be completely converted in the reaction.
The catalysis activity can be influenced by the types of the bases.[28] [29] In the present study, an investigation of alkalis was performed in the range of organic bases and inorganic bases ([Table S2], [Supporting Information] [available in the online version]) and the results showed that cesium carbonate was the most effective. The reported literature used tetraethoxysilane (TEOS) as a solvent, which was unstable in the presence of water and had irritant properties. Therefore, we considered changing the solvent and chose N, N-dimethylformamide (DMF) as an alternative. Given the above, we selected copper(I) iodide (1.5 equiv.) as the catalysis, cesium carbonate as the base, and DMF as the solvent for the reaction in a 105 g scale, producing the target product with an isolated yield of 80.5% and a purity of 98.86%.
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Optimization of Post-processes That Require Column Chromatography
In the context of industrial production, the simplicity of post-processing becomes the most critical variable and requires careful consideration. However, the reported routes required at least one step of column chromatography, which is not suitable for industrial production. Therefore, we optimized post-processes. In this work, we succeeded in eliminating two steps of column chromatography and used recrystallization instead ([Scheme 3]).
Different recrystallization systems of crude 3 were investigated ([Table 3]). Under the EtOH/H2O (5 V/4 V) recrystallization system, the purity of 3 was 96.56%, but the isolated yield was only 31.1%. However, when EtOH or H2O was used as a single recrystallization solvent, the isolated yields of 3 were not satisfactory (21.8 and 48.8%, respectively) ([Table 3], entries 2–3). Then, different ratios of EtOH/H2O were screened. Our data showed that when EtOH/H2O (10 V/7V) was used as the solvent, the isolated yield and purity of 3 were 32.1 and 98.09%, respectively ([Table 3], entry 4). The reduction of water ratio in the mixing solvent affected the yield and purity of the product, with the EtOH/H2O (10 V/4 V) recrystallization system giving the best result ([Table 3], entry 5). Under this recrystallization system, 3 was obtained with an isolated yield of 95.8% and a purity of 99.36% on a 150 g scale.
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Entry |
Recrystallization solvent and volume |
Yield (%)[b] |
Purity (%)[c] |
1 |
EtOH/H2O (5V/4V) |
31.1 |
96.56 |
2 |
EtOH (20V) |
21.8 |
99.22 |
3 |
H2O (15V) |
48.8 |
99.45 |
4 |
EtOH/H2O (10V/7V) |
32.1 |
98.09 |
5 |
EtOH/H2O (10V/6V) |
41.0 |
98.44 |
6 |
EtOH/H2O (10V/5V) |
47.2 |
98.95 |
7 |
EtOH/H2O (10V/4V) |
95.8 |
99.36 |
8 |
EtOH/H2O (10V/3V) |
60.0 |
99.08 |
a 3.0 g scale of crude 3 was used for recrystallization.
b Isolated yields.
c Measured by HPLC.
This work reported the purification of Ricolinostat (1) by recrystallization for the first time. The data showed that under the DMF/dichloromethane (DCM) recrystallization system, the isolated yield of 1 was poor, with the best result of only 35% ([Table 4], entries 1–5). However, under the H2O/DMF (10:1, v:v) recrystallization system, 1 was obtained with an isolated yield of 85.0% and a purity of 99.73% on a 50.0 g scale ([Table 4], entries 6–7).
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Entry |
Solvent |
Volumes |
Yield (%)[b] |
Purity (%)[c] |
1 |
DCM/DMF (9:1) |
5 V |
– |
– |
2 |
DCM/DMF (9:1) |
10 V |
– |
– |
3 |
DCM/DMF (4:1) |
5 V |
– |
– |
4 |
DCM/DMF (4:1) |
10 V |
– |
– |
5 |
DCM/DMF (1:1) |
5 V |
35.5 |
98.7 |
6 |
H2O/DMF (10:1) |
5 V |
– |
– |
7 |
H2O/DMF (10:1) |
10 V |
85.0 |
99.73 |
a 3.0 g scale of crude 1 was used for recrystallization.
b Isolated yields.
c Measured by HPLC.
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Conclusion
In this work, we optimized the synthesis route of Ricolinostat (1). First, by investigating the equiv. of aniline and the temperature of the nucleophilic substitution reaction, a process for efficient construction of compound 3 was established. Second, by screening the types of catalysts and alkalis of the Ullmann coupling, the synthesis process of compound 4 was optimized. Finally, the recrystallization methods for the purification of compound 3 and Ricolinostat (1) were successfully established, which gave 3 a purity of 99.36% and Ricolinostat a purity of 99.73%. The improved synthesis route is able to deliver a product with an isolated yield of 65.8% over five steps and has been found to be both cost-effective and eco-friendly, making it suitable for industrial applications.
Experimental Section
General Method
All reagents were commercially available, and were purchased from Shanghai BiDe PharmaTech Co., Sinopharm Co., Shanghai Haohong Bio-medical Technology Co., etc., and used without further purification unless indicated otherwise. High-performance liquid chromatography (HPLC) analysis was conducted on a Dionex UltiMate 3000 HPLC (Dionex, United States) using an Agilent Eclipse plus C18 column (4.6 mm × 250 mm, 5 µm, Agilent, United States). Mobile A was aqueous sodium octane sulfonate (15 mmol/mL, pH 3.30 ± 0.2)-acetonitrile (90:10, v/v); and mobile B was acetonitrile. The gradient program was as follows: 0–25 minutes, 15% B; 25–30 minutes, 60% B; 30–31 minutes, 15% B; 31–40 minutes, 15% B. The flow rate was 1.0 mL/min, the column temperature was 30°C, and UV detection at 215 nm. Nuclear magnetic resonance (NMR) spectra were recorded on a Bruker 400 spectrometer (Bruker, Germany). Chemical shifts (δ) were given in parts per million (ppm) and referenced to the residual protonated solvent peak (DMSO-d 6: 2.50 ppm for 1H NMR and 39.53 ppm for 13C NMR or chloroform-d: 7.26 ppm for 1H NMR and 77.1 ppm for 13C NMR). Multiplicities are abbreviated as singlet (s), doublet (d), triplet (t), quartet (q), and multiplet (m). Coupling constants (J) are reported in Hertz (Hz).
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Ethyl 2-(Phenylamino) Pyrimidine-5-carboxylate (3)
Ethyl 2-chloropyrimidine-5-carboxylate 2 (138.0 g, 740 mmol) was added to a 5.0 L four-necked flask. Then DMF (1000 mL) was added and mechanically stirred. K2CO3 (204.4 g, 1480 mmol) and aniline (82.6 g, 888 mmol) were sequentially charged into a four-necked flask under N2. The reaction mixture was stirred at 100°C for 8 hours. After completion conversion of compound 2 as determined by HPLC, the reaction mixture was gradually cooled to 25°C, ice water (2.0 L) was added, and stirred for 30 minutes. The precipitated solid was collected by filtration. The cake was washed with water and dried at 60°C to afford compound 3 (95.9% isolated yield, 99.36% HPLC purity) as a white solid. 1H NMR (600 MHz, DMSO-d 6) δ 10.34 (s, 1H), 8.90 (s, 2H), 7.83–7.68 (m, 2H), 7.41–7.27 (m, 2H), 7.05 (tt, J = 7.3, 1.2 Hz, 1H), 4.30 (q, J = 7.1 Hz, 2H), 1.31 (t, J = 7.1 Hz, 3H). 13C NMR (DMSO-d 6) δ 165.42, 161.74, 159.91, 140.22, 130.36, 123.36, 118.98, 114.39, 60.96, 15.71.
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Ethyl 2-(diphenylamino) Pyrimidine-5-carboxylate (4)
Ethyl 2-(phenylamino) pyrimidine-5-carboxylate (3) (1,500 g, 617 mmol) was added to a 5.0 L four-necked flask, then, DMF (2.0 L) was added and mechanically stirred. Iodobenzene (188.0 g, 926 mmol), cuprous iodide (58.8 g, 308 mmol), and cesium carbonate (402.1 g, 1234 mmol) were charged sequentially under N2. The reaction mixture was stirred at 130°C for 5 hours. After complete conversion of compound 3 as determined by HPLC, the reaction solution was gradually cooled to 25°C, and ethyl acetate (EA; 3.5 L) was added. Thereafter, the mixture was filtered. The mother liquid was extracted with EA after the addition of water (2.0 L). The organic layers were combined, washed with water, and concentrated to produce crude 4, which was used for the next step without further purification. 1H NMR (400 MHz, chloroform-d) δ 8.90 (s, 2H), 7.39 (dd, J = 8.4, 7.2 Hz, 4H), 7.34–7.20 (m, 6H), 4.34 (q, J = 7.1 Hz, 2H), 1.35 (t, J = 7.1 Hz, 3H).
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2-(Diphenylamino) Pyrimidine-5-carboxylic Acid (5)
Ethyl 2-(diphenylamino) pyrimidine-5-carboxylate (4) (a crude product, theoretical yield: 196.9 g, 617 mmol) was added to a 5.0 L four-necked flask. A mixture of water and THF (1:1, 2.6 L) was added and mechanically stirred at 350 rpm. LiOH (77.7 g, 1,851 mmol) was added. The reaction mixture was stirred at ambient temperature for 8 hours until complete conversion of compound 4 as determined by HPLC. The THF was removed under vacuum. The aqueous layer was extracted with DCM and adjusted pH to 5.5. The precipitated solid was filtered and washed with water to obtain compound 5 (80.5% isolated yield, 98.86% HPLC purity) as a white solid. 1H NMR (600 MHz) δ 13.06 (s, 1H), 8.77 (s, 2H), 7.42–7.38 (m, 4H), 7.38–7.32 (m, 4H), 7.27 (td, J = 7.3, 1.3 Hz, 2H).
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Methyl 7-[[[2-(diphenylamino)-5-pyrimidinyl]carbonyl]amino]heptanoate (6)
DIPEA (504.0 g, 3897 mmol) and HBTU (364.0 g, 1134 mmol) were sequentially added to a solution of compound 5 (300.0 g, 1,031 mmol) and methyl 7-aminoheptanoate (7) (293.0 g, 1,495 mmol) in THF (1.5 L). The reaction mixture was stirred at room temperature for 8 hours, removed THF under vacuum, and then extracted with EA/water. The organic layers were combined, washed with water, and concentrated to produce crude 6 as a yellow oily liquid, which was used for the next step without further purification. 1H NMR (600 MHz, DMSO-d 6) δ 8.73 (s, 2H), 8.39 (t, J = 5.6 Hz, 1H), 7.44–7.36 (m, 4H), 7.35–7.28 (m, 4H), 7.28–7.22 (m, 2H), 3.58 (s, 3H), 3.23 (q, J = 6.6 Hz, 2H), 2.29 (t, J = 7.4 Hz, 2H), 1.51 (dq, J = 18.7, 7.1 Hz, 4H), 1.30 (dt, J = 7.9, 3.3 Hz, 4H).
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Ricolinostat (1)
Hydroxylamine hydrochloride (25.0 g, 360 mmol) and CH3OH were added in one portion to a 500 mL flask. A CH3OH solution containing KOH (125.0 mL; 22.3 g, 400 mmol) was added dropwise at 0°C, stirred at 0°C for 30 minutes, and filtered. Mother liquid was collected. Compound 5 (44.54 g, 103 mmol) was added to the mother liquor. CH3OH solution containing KOH was added dropwise at 0°C. Stirring was continued until HPLC determined the complete conversion of compound 5. Removing CH3OH under vacuum afforded a yellow oily liquid, which was recrystallized by DMF/H2O (DMF: H2O = 1:1, 10 V) at 70°C. The precipitated solid was filtered to obtain compound 1 (85.2% isolated yield, 99.36% purity) as a white solid. 1H NMR (400 MHz, DMSO-d 6) δ 10.33 (d, J = 1.7 Hz, 1H), 8.72 (s, 2H), 8.66 (d, J = 1.5 Hz, 1H), 8.40 (t, J = 5.6 Hz, 1H), 7.47–7.35 (m, 4H), 7.35–7.18 (m, 6H), 3.22 (q, J = 6.6 Hz, 2H), 1.93 (t, J = 7.4 Hz, 2H), 1.48 (p, J = 7.0 Hz, 4H), 1.26 (p, J = 6.3, 5.2 Hz, 4H). 13C NMR (DMSO-d 6) δ 169.05, 162.91, 157.70, 144.63, 129.68, 127.77, 126.52, 120.99, 32.67, 29.47, 28.77, 28.62, 25.52. ESI-MS (m/z): calcd. for C24H28N5O3 + [M + H]+ 434.2114; found 434.2.
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Supporting Information
Screening results of catalysts and alkalis for the Ullmann reaction ([Tables S1] and [S2] [available in the online version]) as well as 1H NMR, 13C NMR, MS, and HPLC spectra of compounds 3 and 1 ([Fig. S1]–[S8] [available in the online version]) can be found in the “Supporting Information” section of this article's webpage.
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Conflict of Interest
None declared.
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Address for correspondence
Publication History
Received: 14 March 2024
Accepted: 10 October 2024
Article published online:
28 November 2024
© 2024. The Author(s). This is an open access article published by Thieme under the terms of the Creative Commons Attribution License, permitting unrestricted use, distribution, and reproduction so long as the original work is properly cited. (https://creativecommons.org/licenses/by/4.0/)
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References
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- 2 Blixt NC, Faulkner BK, Astleford K. et al. Class II and IV HDACs function as inhibitors of osteoclast differentiation. PLoS One 2017; 12 (09) e0185441
- 3 Gu X, Peng X, Zhang H. et al. Discovery of indole-containing benzamide derivatives as HDAC1 inhibitors with in vitro and in vivo antitumor activities. Pharmaceutical Fronts 2022; 4: e61-e70
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- 5 König B, Watson PR, Reßing N. et al. Difluoromethyl-1,3,4-oxadiazoles are selective, mechanism-based, and essentially irreversible inhibitors of histone deacetylase 6. J Med Chem 2023; 66 (19) 13821-13837
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