Disclosed are nitrosourea and other compounds, pharmaceutical composition, and methods of treating cancers that are MGMT deficient regardless of their MMR status and particularly compounds, pharmaceutical compositions, and methods of treating cancers that are both MGMT and MMR deficient.

Disclosed are nitrosourea and other compounds, pharmaceutical composition, and methods of treating cancers that are MGMT deficient regardless of their MMR status and particularly compounds, pharmaceutical compositions, and methods of treating cancers that are both MGMT and MMR deficient.

The present disclosure provides processes and apparatuses for the scaled-up manufacture of lomustine via continuous flow manufacture. Such continuous flow processes may optionally include the crystallization of lomustine and the apparatuses may optionally include crystallization apparatuses/reactors in either batch or continuous flow design. In one aspect of the disclosure, a process for making lomustine is provided comprising treating solutions of 2-chloroethylisocyanate with a solution of cyclohexylamine with continuous-flow pumps in a gram-flow reactor to form a combined solution, adding deionized water with a continuous flow-pump to the combined solution to form a liquid-organic phase solution, extracting the organic phase from the solution and treating with a solution of t-butyl nitrite with a continuous flow pump in a gram flow reactor to form lomustine.

The present disclosure provides processes and apparatuses for the scaled-up manufacture of lomustine via continuous flow manufacture. Such continuous flow processes may optionally include the crystallization of lomustine and the apparatuses may optionally include crystallization apparatuses/reactors in either batch or continuous flow design. In one aspect of the disclosure, a process for making lomustine is provided comprising treating solutions of 2-chloroethylisocyanate with a solution of cyclohexylamine with continuous-flow pumps in a gram-flow reactor to form a combined solution, adding deionized water with a continuous flow-pump to the combined solution to form a liquid-organic phase solution, extracting the organic phase from the solution and treating with a solution of t-butyl nitrite with a continuous flow pump in a gram flow reactor to form lomustine.

Carmustine may be safely and efficiently produced by reacting 2-chloroethylamine hydrochloride and 1,1′-carbonyldiimidazole to afford 1,3-bis(2-chloroethyl)-1-urea, followed by nitrosation to give the final product.

Carmustine may be safely and efficiently produced by reacting 2-chloroethylamine hydrochloride and 1,1′-carbonyldiimidazole to afford 1,3-bis(2-chloroethyl)-1-urea, followed by nitrosation to give the final product.

Disclosed herein is a continuous manufacturing process for lomustine that has a short residence time and 63 percent yield. Major advantages of this process are that the total production cost for lomustine is lower, the product is higher quality, and the manufacturing operation is safer for production personnel.

Disclosed herein is a continuous manufacturing process for lomustine that has a short residence time and 63 percent yield. Major advantages of this process are that the total production cost for lomustine is lower, the product is higher quality, and the manufacturing operation is safer for production personnel.

Disclosed herein is a continuous manufacturing process for lomustine that has a short residence time and 63 percent yield. Major advantages of this process are that the total production cost for lomustine is lower, the product is higher quality, and the manufacturing operation is safer for production personnel.

Disclosed herein is a continuous manufacturing process for lomustine that has a short residence time and 63 percent yield. Major advantages of this process are that the total production cost for lomustine is lower, the product is higher quality, and the manufacturing operation is safer for production personnel.