A solid composition, methods for preparing and using the composition, and a rehydrated crystal are disclosed. An exemplary solid composition contains at least about 2 wt % of methyl glycine-N,N-diacetic acid trisodium salt of crystal type III, based on the total weight of crystalline methyl glycine-N,N-diacetic acid trisodium salt compounds, wherein the crystal type III is the form of a crystal, comprising a crystalline modification characterized by the reflections enlisted below when analyzed with X-ray diffraction analysis using Cu K radiation: TABLE-US-00001 Type III 2 d () 5.8 15.2 7.5 11.8 8.1 10.9 9.5 9.3 11.7 7.6 13.9 6.4 15.1 5.9 16.5 5.4 17.3 5.1 18.5 4.8 19.1 4.65 20.1 4.4.

A solid composition, methods for preparing and using the composition, and a rehydrated crystal are disclosed. An exemplary solid composition contains at least about 2 wt % of methyl glycine-N,N-diacetic acid trisodium salt of crystal type III, based on the total weight of crystalline methyl glycine-N,N-diacetic acid trisodium salt compounds, wherein the crystal type III is the form of a crystal, comprising a crystalline modification characterized by the reflections enlisted below when analyzed with X-ray diffraction analysis using Cu K radiation: TABLE-US-00001 Type III 2 d () 5.8 15.2 7.5 11.8 8.1 10.9 9.5 9.3 11.7 7.6 13.9 6.4 15.1 5.9 16.5 5.4 17.3 5.1 18.5 4.8 19.1 4.65 20.1 4.4.

A solid composition, methods for preparing and using the composition, and a rehydrated crystal are disclosed. An exemplary solid composition contains at least about 2 wt % of methyl glycine-N,N-diacetic acid trisodium salt of crystal type III, based on the total weight of crystalline methyl glycine-N,N-diacetic acid trisodium salt compounds, wherein the crystal type III is the form of a crystal, comprising a crystalline modification characterized by the reflections enlisted below when analyzed with X-ray diffraction analysis using Cu K radiation: TABLE-US-00001 Type III 2 d () 5.8 15.2 7.5 11.8 8.1 10.9 9.5 9.3 11.7 7.6 13.9 6.4 15.1 5.9 16.5 5.4 17.3 5.1 18.5 4.8 19.1 4.65 20.1 4.4.

The invention generally relates to systems with anti-fouling control and methods for controlling fouling within a channel of a plug flow crystallizer. In certain aspects, the invention provides a system that includes a plug flow crystallizer having a channel, one or more heating/cooling elements, each operably associated with a different segment of the channel, and a controller. The controller is operably coupled to the one or more heating/cooling elements and configured to implement a temperature profile within the channel of the plug flow crystallizer that grows crystals in a plug of fluid that flows through a first segment of the channel and dissolves encrust in a second segment of the channel while having minimal impact on crystal growth in the plug of fluid in the second segment of the channel. In certain embodiments, these segments may be cyclically alternated, in that the segment in which crystal grows in one cycle becomes the segment in which crystal dissolves in the next cycle and vice versa, to realize a fully continuous crystallization process.

The invention generally relates to systems with anti-fouling control and methods for controlling fouling within a channel of a plug flow crystallizer. In certain aspects, the invention provides a system that includes a plug flow crystallizer having a channel, one or more heating/cooling elements, each operably associated with a different segment of the channel, and a controller. The controller is operably coupled to the one or more heating/cooling elements and configured to implement a temperature profile within the channel of the plug flow crystallizer that grows crystals in a plug of fluid that flows through a first segment of the channel and dissolves encrust in a second segment of the channel while having minimal impact on crystal growth in the plug of fluid in the second segment of the channel. In certain embodiments, these segments may be cyclically alternated, in that the segment in which crystal grows in one cycle becomes the segment in which crystal dissolves in the next cycle and vice versa, to realize a fully continuous crystallization process.

Disclosed herein are forms of L-ornithine phenyl acetate and methods of making the same. A crystalline form may, in some embodiments, be Forms I, II, III and V, or mixtures thereof. The crystalline forms may be formulated for treating subjects with liver disorders, such as hepatic encephalopathy. Accordingly, some embodiments include formulations and methods of administering L-ornithine phenyl acetate.

Disclosed herein are forms of L-ornithine phenyl acetate and methods of making the same. A crystalline form may, in some embodiments, be Forms I, II, III and V, or mixtures thereof. The crystalline forms may be formulated for treating subjects with liver disorders, such as hepatic encephalopathy. Accordingly, some embodiments include formulations and methods of administering L-ornithine phenyl acetate.

Disclosed herein are forms of L-ornithine phenyl acetate and methods of making the same. A crystalline form may, in some embodiments, be Forms I, II, III and V, or mixtures thereof. The crystalline forms may be formulated for treating subjects with liver disorders, such as hepatic encephalopathy. Accordingly, some embodiments include formulations and methods of administering L-ornithine phenyl acetate.

There is disclosed a process for the separation of long chain amino acid and long chain dibasic acid, comprising: (1) adding an ammonium salt to the mixture of alkali salts of long chain amino acid and long chain dibasic acid; (2) heating to remove ammonia; and (3) separating long chain amino acid by solid-liquid separation; and (4) acidifying the salt of long chain dibasic acid with an acid to separate long chain dibasic acid.

There is disclosed a process for the separation of long chain amino acid and long chain dibasic acid, comprising: (1) adding an ammonium salt to the mixture of alkali salts of long chain amino acid and long chain dibasic acid; (2) heating to remove ammonia; and (3) separating long chain amino acid by solid-liquid separation; and (4) acidifying the salt of long chain dibasic acid with an acid to separate long chain dibasic acid.