B01J2219/00759

Salt byproduct separation during formation of polyarylene sulfide

Methods of forming a polyarylene sulfide and systems as may be utilized in carrying out the methods are described. Included in the formation method is a filtration process for treatment of a mixture, the mixture including a polyarylene sulfide, a salt byproduct of the polyarylene sulfide formation reaction, and a solvent. The filtration process includes maintaining the downstream side of the filter medium at an increased pressure. The downstream pressure can such that the boiling temperature of the mixture at the downstream pressure can be higher than the temperature at which the polyarylene sulfide is insoluble in the solvent.

Liquid phase oxidation of aromatic feedstocks with manganate recycling to produce carboxylic acids

Systems and methods for liquid-phase oxidation of an aromatic feedstock containing at least one oxidizable aromatic compound may incorporate an oxidation reactor, a separation apparatus in fluidic communication with the oxidation reactor, a solids treatment unit, and a product recovery unit in fluidic communication with the separation apparatus. The oxidation reactor may conduct liquid-phase oxidation of the oxidizable aromatic compound in the aromatic feedstock in the presence of a manganate salt to form a slurry containing liquid product and solid manganese dioxide. The separation apparatus may accept the slurry from the oxidation reactor and separate the liquid component from the solid component. The solids treatment unit accepts the solid component from the separation apparatus, treats the solid component with a basic liquid to oxidize the manganese dioxide in the solid component and form a regenerated manganate salt, which may be recycled back to the oxidation reactor.

THREE RESIN REACTORS IN SERIES PEPTIDE SYNTHESIZER
20240399331 · 2024-12-05 ·

A Solid Phase Peptide Synthesis (SPPS) device and method of using the same for manufacturing peptides is taught herein. The system comprises at least two reactors, each reactor including a quantity of SPPS resin. The reactors are positioned in series. A de-protecting agent is added to the first reactor and then transferred to the second and third reactors, in series, thereby operating to de-protect the protected N-group. Wash solvent is added to the first reactor and then transferred to the second and this operation repeated several times. Likewise, an amino acid activated ester solution is added, in series, to the first, second and third reactors, thereby operating to couple the amino acid to the de-protected N-group. Wash solvent is added to the first reactor and then transferred to the second and this operation repeated several times prior to the next cycle. The use of the reactors in series reduces the overall solvent required. Online LCMS is also used to monitor progress and identity of reactions happening within the solid phase resin particles.

Nucleic acid synthesis and purification device, use thereof, and nucleic acid synthesis and purification method
12247198 · 2025-03-11 · ·

A nucleic acid synthesis device and a nucleic acid purification device, uses thereof, and a nucleic acid synthesis method and a nucleic acid purification method. The nucleic acid synthesis device includes a solid support, and the solid support includes a controlled pore glass (CPG), the CPG is an unmodified and bare CPG, a surface of the CPG has a hydroxyl group, and the hydroxyl group is attachable, though a covalent bond, to a phosphoramidite-protected nucleotide monomer or multimer for synthesis of nucleic acid. The nucleic acid synthesis device of the present disclosure can be used for not only synthesis of an oligonucleotide primer, but also for purification of enzymatic digestion and PCR product by using the oligonucleotide primer immobilized on the CPG, and has advantages of simple structure, small volume, light weight, high efficiency, low costs, and diversified functions.

ENZYMATIC DNA SYNTHESIZER DEVICE

A microfluidic system for performing nucleic acid synthesis includes a microfluidic plate having a reaction chamber coupled to a microfluidic plate input and a microfluidic plate output. A temperature control plate is thermally coupled to the microfluidic plate. A reagent injection plate is coupled to receive enzymatic synthesis reagents. A microvalve plate is coupled between the reagent injection plate and the microfluidic plate input. A controller is coupled the temperature control plate, and the microvalve plate to control the microfluidic system to controllably synthesize nucleic acid sequences.

Salt Byproduct Separation During Formation of Polyarylene Sulfide

Methods of forming a polyarylene sulfide and systems as may be utilized in carrying out the methods are described. Included in the formation method is a filtration process for treatment of a mixture, the mixture including a polyarylene sulfide, a salt byproduct of the polyarylene sulfide formation reaction, and a solvent. The filtration process includes maintaining the downstream side of the filter medium at an increased pressure. The downstream pressure can such that the boiling temperature of the mixture at the downstream pressure can be higher than the temperature at which the polyarylene sulfide is insoluble in the solvent.

Methods of Producing Size-Selected Nucleic Acid Libraries and Compositions and Kits for Practicing Same
20250136971 · 2025-05-01 ·

Provided are methods of producing size-selected nucleic acid libraries. The methods include contacting a nucleic acid sample and a nucleic acid binding reagent including an affinity tag, under conditions in which nucleic acids of less than a desired length are substantially bound to the nucleic acid binding reagent and nucleic acids of the desired length are substantially not bound to the nucleic acid binding reagent. The conditions include the duration of the contacting, the concentration of the nucleic acid binding reagent, or both. The methods further include separating, using the affinity tag, the nucleic acids of less than the desired length bound to the nucleic acid binding reagent from the nucleic acids of the desired length not bound to the nucleic acid binding reagent, to produce a size-selected nucleic acid library. Compositions and kits that find use, e.g., in practicing the methods of the present disclosure, are also provided.

FULL-AUTOMATIC RADIOPHARMACEUTICAL PRODUCTION APPARATUS
20250222424 · 2025-07-10 ·

Provided is a full-automatic radiopharmaceutical production apparatus including a synthesis device. The synthesis device includes a synthesis cassette and a main synthesis unit. The synthesis cassette includes a synthesis cassette body. The synthesis cassette body includes a first common pipe extending in a left-right direction. The first common pipe is located between three-way valves that are adjacent in the left-right direction. The main synthesis unit includes a main synthesis unit frame. The first common pipe is detachably fixed at a front housing of the main synthesis unit frame by a first fixing assembly.

Microfluidic apparatus and methods of use thereof

Apparatuses and methods are described herein for processing polynucleotides in a sealed path environment. The apparatuses include optical sensors to monitor operations and to track material usage for good manufacturing practice.

Three resin reactors in series peptide synthesizer

A Solid Phase Peptide Synthesis (SPPS) device and method of using the same for manufacturing peptides is taught herein. The system comprises at least two reactors, each reactor including a quantity of SPPS resin. The reactors are positioned in series. A de-protecting agent is added to the first reactor and then transferred to the second and third reactors, in series, thereby operating to de-protect the protected N-group. Wash solvent is added to the first reactor and then transferred to the second and this operation repeated several times. Likewise, an amino acid activated ester solution is added, in series, to the first, second and third reactors, thereby operating to couple the amino acid to the de-protected N-group. Wash solvent is added to the first reactor and then transferred to the second and this operation repeated several times prior to the next cycle. The use of the reactors in series reduces the overall solvent required. Online LCMS is also used to monitor progress and identity of reactions happening within the solid phase resin particles.