The use of ultrasound or acoustics applied at a level below that which causes cavitation to control the energy balance between particles and the liquid phase in a metastable liquid.

A reactor and a relative process are for precipitation of a solid substance from a solution, in particular a reactive precipitation or crystallization. The reactor is a reactive precipitation/crystallization reactor, including an outer tubular element and a coaxial inner tubular element along a longitudinal axis of the reactor, to form an annular channel between an outer wall of the inner tubular element and an inner wall of the outer tubular element. The outer tubular element includes, at a first end, an inlet opening for a first reactive fluid and, at a second end, an outlet opening for a reaction mixture. The inner tubular element includes an inlet opening for a second reactive fluid and, optionally, an outlet opening for the second reactive fluid. The inner tubular element includes, along the outer surface, dispensing openings for dispensing the second reactive fluid fed into the inner tubular element.

A heat storage apparatus according to the present disclosure includes a heat storage material and a member. The heat storage material forms a clathrate hydrate by cooling. The member has a surface with a plurality of holes. In the case that the lattice constant of the clathrate hydrate is denoted by L and the outside diameter of a cage included in the clathrate hydrate is denoted by D, the plurality of holes are spaced at intervals of 1L to 10L, and each of the plurality of holes has a hole diameter of 1D to 20D.

Novel crystalline ponatinib hydrochloride forms designated Form alpha and Form beta are disclosed. Form alpha is characterized by data selected from an XRPD pattern with peaks at about 6.5, 9.0, 12.25, 14.4, 16.70, 19.6, 22.2, 24.5, 28.20.2 degrees 2-theta; an XRPD pattern substantially as depicted in FIG. 1; and/or a combination thereof. Form beta is characterized by data selected from an XRPD pattern with peaks at about 10.7, 15.2, 15.8, 16.4 23.1, 25.0, 27.80.2 degrees 2-theta; an XRPD pattern substantially as depicted in FIG. 3; and/or combinations thereof. Processes for making Form alpha and Form beta are disclosed.

The invention relates to a process of creating particles of controlled size by creating them in the interstitial regions in a batch, semi-continuous, or continuous liquid phase. The method comprises making solid particles comprising: adding a precursor material to a liquid carrier to form a liquid continuous phase, wherein the concentration of the precursor material is from about 5% to about 99% by weight of the continuous liquid phase; adding an inert phase into the liquid continuous phase of step a, resulting in an inert phase and continuous liquid phase mixture having a volume fraction of the inert phase of from about 30% to about 98% and inert phase domain size of about 0.2 to about 200 m; transforming the precursor material physically or chemically, resulting in the formation of solid particles.

A method for purifying methacrylic acid, including mixing raw material methacrylic acid and methanol; precipitating a crystal of methacrylic acid from the mixed solution; and separating the crystal and mother liquor, wherein the raw material methacrylic acid and methanol are mixed so that a concentration of methanol in the mixed liquid is 3.0 to 3.75% by mass, and the crystal of methacrylic acid is precipitated from the mixed solution in a cooling crystallization vessel.

A modular sub-unit for the production of crystals in a suspension crystallization system includes: a first crystallization segment, at least one further crystallization segment, a first mixing segment, optional further mixing segments, an inlet cap, an outlet cap. The inlet cap and outlet cap are in fluid communication with any crystallization segments and any mixing segments present within the sub-unit. The sub-unit further includes a central rotating axis for providing mechanical energy to the crystallization segments and preferably the mixing segments. The crystallization segments present in the sub-unit are separated from each other by a mixing segment. Also described are a suspension crystallization system which includes the sub-unit and a suspension crystallization process making use of the sub-unit.

A method of producing particles by bringing plural dissimilar materials A and B into contact with each other includes feeding a liquid into a reactor from a first end portion of the reactor such that the liquid flows along the inner peripheral surface of the reactor and generating a vortex flow toward a second end portion in the reactor by the feed of the liquid; disposing a flow-assisting blade capable of rotating around the central axis line in the reactor and rotating the flow-assisting blade; and injecting materials to be contacted A and B into the reactor, discharging a contacted liquid from the second end portion of the reactor, and generating the particles in the contacted liquid.

The present invention relates to an apparatus (1) for separation of a target product from a liquid phase P comprising the target product, comprising at least one primary space (3) for a heat transfer medium W, at least one first feed unit (5a) and one first removal unit (5b) for the heat transfer medium W, at least one secondary space (7) for the liquid phase P, at least one second feed unit (9) for the liquid phase P, at least one crystallization surface (13) which divides the primary space (3) and the secondary space (7), at least one second removal unit (15) for the target product and at least one application unit (11) for a liquid phase P.sub.0 essentially directly to the crystallization surface (13) or the surfaces of lines that conduct the heat transfer medium W. The present invention further relates to a process for removing a target product from a liquid phase P comprising the target product.

A heat storage apparatus according to the present disclosure includes a heat storage material and a member. The heat storage material forms a clathrate hydrate by cooling. The member has a surface with a plurality of holes. In the case that the lattice constant of the clathrate hydrate is denoted by L and the outside diameter of a cage included in the clathrate hydrate is denoted by D, the plurality of holes are spaced at intervals of 1L to 10L, and each of the plurality of holes has a hole diameter of 1D to 20D.