B01J19/06

REACTION DEVICE, MICROSPHERE PREPARATION DEVICE AND EXTRACTION METHOD AND LIPOSOME DRUG LOADING METHOD
20230149879 · 2023-05-18 · ·

Disclosed is a reaction device, comprising: a reactor body (100) and a supply device (200), wherein the reactor body (100) has a first end (106) and a second end (107) and is used for accommodating a reaction liquid, with a first injection port (101) being provided between the first end (106) and the second end (107), and a discharge port (109) being provided at the second end (107); and the supply device (200) is in communication with the first injection port (101) to inject a continuous phase, wherein the continuous phase directionally flows in the reactor body (100) to form or maintain a parameter gradient in the reactor body (100). By means of injecting the continuous phase into the first injection port (101) on the reactor body (100), the solution presents a certain parameter gradient on two sides of the first injection port (101) in the reactor body (100).

REACTION DEVICE, MICROSPHERE PREPARATION DEVICE AND EXTRACTION METHOD AND LIPOSOME DRUG LOADING METHOD
20230149879 · 2023-05-18 · ·

Disclosed is a reaction device, comprising: a reactor body (100) and a supply device (200), wherein the reactor body (100) has a first end (106) and a second end (107) and is used for accommodating a reaction liquid, with a first injection port (101) being provided between the first end (106) and the second end (107), and a discharge port (109) being provided at the second end (107); and the supply device (200) is in communication with the first injection port (101) to inject a continuous phase, wherein the continuous phase directionally flows in the reactor body (100) to form or maintain a parameter gradient in the reactor body (100). By means of injecting the continuous phase into the first injection port (101) on the reactor body (100), the solution presents a certain parameter gradient on two sides of the first injection port (101) in the reactor body (100).

Process for producing an aqueous polyacrylamide concentrate

Process for producing aqueous polyacrylamide concentrates by polymerizing an aqueous solution comprising at least acrylamide thereby obtaining an aqueous polyacrylamide gel, comminuting said aqueous polyacrylamide gel and mixing it with an aqueous liquid, wherein the manufacturing steps are allocated to two different locations A and B and the process comprises the step of transporting an aqueous polyacrylamide concentrate hold in a suitable transport unit from a location A to a location B. Modular, relocatable plant for manufacturing aqueous polyacrylamide, wherein the units of the plant are located at two different locations A and B.

Process for producing an aqueous polyacrylamide concentrate

Process for producing aqueous polyacrylamide concentrates by polymerizing an aqueous solution comprising at least acrylamide thereby obtaining an aqueous polyacrylamide gel, comminuting said aqueous polyacrylamide gel and mixing it with an aqueous liquid, wherein the manufacturing steps are allocated to two different locations A and B and the process comprises the step of transporting an aqueous polyacrylamide concentrate hold in a suitable transport unit from a location A to a location B. Modular, relocatable plant for manufacturing aqueous polyacrylamide, wherein the units of the plant are located at two different locations A and B.

SYNTHESIS OF NANOPARTICLES

A method for synthesising metal oxide nanoparticles. The method comprises mixing, to provide a reaction mixture, a precursor solution comprising metal ions with an initiator solution to initiate a nanoparticle precipitation process, and then quenching the precipitation process by adding a quenching agent to the reaction mixture so as to yield a dispersion comprising metal oxide nanoparticles. The resulting metal oxide nanoparticles may have an average diameter of less than 7 nm, for example 5 nm or less.

SYNTHESIS OF NANOPARTICLES

A method for synthesising metal oxide nanoparticles. The method comprises mixing, to provide a reaction mixture, a precursor solution comprising metal ions with an initiator solution to initiate a nanoparticle precipitation process, and then quenching the precipitation process by adding a quenching agent to the reaction mixture so as to yield a dispersion comprising metal oxide nanoparticles. The resulting metal oxide nanoparticles may have an average diameter of less than 7 nm, for example 5 nm or less.

SYSTEM AND PROCESS FOR CONTINUOUS AND CONTROLLED PRODUCTION OF METAL-ORGANIC FRAMEWORKS AND METAL-ORGANIC FRAMEWORK COMPOSITES

A MOF production system and method of making are detailed for continuous and controlled synthesis of MOFs and MOF composites. The system can provide optimized yields of MOFs and MOF composites greater than or equal to 95%.

SYSTEM AND PROCESS FOR CONTINUOUS AND CONTROLLED PRODUCTION OF METAL-ORGANIC FRAMEWORKS AND METAL-ORGANIC FRAMEWORK COMPOSITES

A MOF production system and method of making are detailed for continuous and controlled synthesis of MOFs and MOF composites. The system can provide optimized yields of MOFs and MOF composites greater than or equal to 95%.

METHODS AND DEVICES FOR THE PREPARATION OF NANOMATERIALS
20170361299 · 2017-12-21 ·

Disclosed herein are methods for preparing nanomaterials, such as nanoparticles. The methods can involve jet-mixing two or more precursor solutions to form the nanomaterials. By rapidly mixing the precursor solutions, nanomaterials of improved quality and uniformity can be prepared in high yield (e.g., in yields of at least 85%). The methods are also scalable, and allow for the continuous production of nanomaterials. Also provided are jet-mixing reactors that can be used to prepare nanomaterials using the methods described herein.

Methods for Increasing Polymer Production Rates with Halogenated Hydrocarbon Compounds
20170355793 · 2017-12-14 ·

Methods for controlling the productivity of an olefin polymer in a polymerization reactor system using a halogenated hydrocarbon compound are disclosed. The productivity of the polymer can be increased via the addition of the halogenated hydrocarbon compound.