The disclosure describes methods for the purification of protein-enriched extracts to provide concentrates and isolates and methods for incorporation of such materials into products. The purification methods are adapted for removal of, e.g., chlorophyll and may thus provide lightening the color of the protein-enriched extracts. The methods generally include treatment with peracetic acid or hydrogen peroxide and filtrations. A protein composition in the form of a concentrate or isolate is provided, the protein composition including RuBisCO, F2 fraction proteins, or combination thereof extracted from a plant material.

The present disclosure relates to a cleaning device and a chemiluminescence detector. A cleaning device is provided with a cup inlet station and a cup outlet station, wherein the cleaning device comprises a pedestal, a plurality of magnetic adsorption components, a turntable arranged on the pedestal, and a primary cleaning mechanism arranged on the pedestal, wherein each of the plurality of magnetic adsorption components comprises a plurality of magnets; magnetic adsorption heights of a plurality of magnets of the first magnetic adsorption component are equal and are recorded as A; magnetic adsorption heights of a plurality of magnets of the middle magnetic adsorption component are equal and are recorded as B, and B>A.

The present invention relates to a method for removing water from a compound solution and performing conjugate acid conversion. The method uses a nanometer film to perform reverse osmosis for the compound solution to remove water, and provides a conjugate acid to replace the acidic substances in the compound solution in order to obtain compound conjugate acid salts. The method of the present invention can effectively reduce the water content of the compound solution and replace the conjugate acid of the compound to form the desired compound conjugate acid salt.

The present invention relates to a method for removing water from a compound solution and performing conjugate acid conversion. The method uses a nanometer film to perform reverse osmosis for the compound solution to remove water, and provides a conjugate acid to replace the acidic substances in the compound solution in order to obtain compound conjugate acid salts. The method of the present invention can effectively reduce the water content of the compound solution and replace the conjugate acid of the compound to form the desired compound conjugate acid salt.

A biological sample purification apparatus is described for purifying a protein from a cell, as well as methods of use of the purification apparatus, and systems comprising the same. The described apparatus comprises a housing comprising a top opening, a bottom opening, and a membrane positioned between said top opening and said bottom opening; and a purification media comprising diatomaceous earth and a resin, wherein the purification media is positioned between the membrane and the top opening; and wherein the purification media is optionally mixed and is substantially dry.

The disclosure relates to systems and methods for improving the manufacturing of silk solutions and powders containing silk fibroin obtained from silkworm cocoons. The solutions and powders can be used to improve the post-harvest preservation of perishables and to improve the performance of packaging, including biodegradable packaging.

The present invention is directed to pulse protein products, very low in, or substantially free of, pea/vegetable flavour notes characteristic of conventional commercial pulse protein products and useful for the fortification of food and beverage products and prepared without the use of salt in the process. The pulse protein products of the present invention are obtained by extracting pulse protein source with water to form an aqueous pulse protein solution, at least partially separating the aqueous pulse protein solution from residual pulse protein source, adjusting the pH of the aqueous pulse protein solution to a pH of about 1.5 to about 3.4 to solubilize the bulk of the protein and form an acidified pulse protein solution then separating the acidified pulse protein solution from the acid insoluble solid material. The acidified pulse protein solution may be dried following optional concentration and diafiltration to form a pulse protein product, which may be an isolate. The acid insoluble solid material may be washed with acidified water and then dried to form another pulse protein product. These products may be dried at the acidic pH at which they were prepared or may be adjusted in pH before drying. Also described is the preparation of an acid soluble protein product, which may be an isolate, and which provides acidic solutions of improved clarity and is derived from the acidified pulse protein solution.

The present invention is directed to pulse protein products, very low in, or substantially free of, pea/vegetable flavour notes characteristic of conventional commercial pulse protein products and useful for the fortification of food and beverage products and prepared without the use of salt in the process. The pulse protein products of the present invention are obtained by extracting pulse protein source with water to form an aqueous pulse protein solution, at least partially separating the aqueous pulse protein solution from residual pulse protein source, adjusting the pH of the aqueous pulse protein solution to a pH of about 1.5 to about 3.4 to solubilize the bulk of the protein and form an acidified pulse protein solution then separating the acidified pulse protein solution from the acid insoluble solid material. The acidified pulse protein solution may be dried following optional concentration and diafiltration to form a pulse protein product, which may be an isolate. The acid insoluble solid material may be washed with acidified water and then dried to form another pulse protein product. These products may be dried at the acidic pH at which they were prepared or may be adjusted in pH before drying. Also described is the preparation of an acid soluble protein product, which may be an isolate, and which provides acidic solutions of improved clarity and is derived from the acidified pulse protein solution.

A process for the primary clarification of feeds, including chemically treated flocculated feeds, containing the target biomolecules of interest such as mAbs, mammalian cell cultures, or bacterial cell cultures, using a primary clarification depth filtration device without the use of a primary clarification centrifugation step or a primary clarification tangential flow microfiltration step. The primary clarification depth filtration device contains a porous depth filter having graded porous layers of varying pore ratings. The primary clarification depth filtration device filters fluid feeds, including chemically treated flocculated feeds containing flocculated cellular debris and colloidal particulates having a particle size distribution of approximately about 0.5 μm to 200 μm, at a flow rate of about 10 litres/m.sup.2/hr to about 100 litres/m.sup.2/hr. Kits and methods of using and making the same are also provided.

A process for the primary clarification of feeds, including chemically treated flocculated feeds, containing the target biomolecules of interest such as mAbs, mammalian cell cultures, or bacterial cell cultures, using a primary clarification depth filtration device without the use of a primary clarification centrifugation step or a primary clarification tangential flow microfiltration step. The primary clarification depth filtration device contains a porous depth filter having graded porous layers of varying pore ratings. The primary clarification depth filtration device filters fluid feeds, including chemically treated flocculated feeds containing flocculated cellular debris and colloidal particulates having a particle size distribution of approximately about 0.5 μm to 200 μm, at a flow rate of about 10 litres/m.sup.2/hr to about 100 litres/m.sup.2/hr. Kits and methods of using and making the same are also provided.