Described herein is a modification unit (37) for the continuous, pathogen reduced processing of a guidance molecule e.g. a conjugate of a peptide or a protein or a nucleic acid and a linker comprising the following components: at least one reservoir containing the guidance molecule in buffer solution (1) and/or at least one inlet for a product stream containing the guidance molecule in buffer solution, at least one reservoir containing the linker in solution (2), at least one mixing device (3), at least two valves (7, 8), one for dosage of the guidance molecule and one for dosage of the linker molecule at least one outlet for the product stream comprising the guidance molecule-linker complexes and/or a reservoir for taking up the guidance molecule-linker complexes (5)
further comprising at least one residence time device ensuring a defined residence time, i.e. ensuring that after mixing the guidance molecules and the linker molecules always spend a similar amount of time in a continuous process.

Disclosed herein are cell processing systems, devices, and methods thereof. A system for cell processing may comprise a plurality of instruments each independently configured to perform one or more cell processing operations upon a cartridge, and a robot capable of moving the cartridge between each of the plurality of instruments.

A modular device for treatment and/or analysis of substances comprises a supply device which supplies at least one functional fluid to at least one process device, wherein the supply device has multiple receiving means for receiving in each case one process device. The receiving means each have multiple supply ports, including an inflow supply port and an outflow supply port for transmission of a functional fluid. The process device has a functional region for the treatment and/or analysis of substances, a fluid line which encloses the functional region, and multiple coupling means for coupling to the supply ports of a receiving means. For each receiving means, a first valve device is provided in the region of the inflow supply port and a second valve device is provided in the region of the outflow supply port.

An autoxidation process for producing hydrogen peroxide may be performed using a plant that includes at least two skid mounted modules selected from: a skid mounted module comprising at least one hydrogenator to hydrogenate an anthraquinone in a working solution; a skid mounted module comprising at least one oxidizer to oxidize the hydrogenated anthraquinone with oxygen to form hydrogen peroxide; optionally a skid mounted module configured to compress air to feed oxygen into the at least one oxidizer of the oxidizer skid, and when said air compressor skid is present, a further skid mounted module configured to recover solvent; a skid mounted module configured to extract the hydrogen peroxide from the working solution; and a skid mounted module comprising at least one means to deliver a hydrogen peroxide solution to a point of use and/or optionally to a storage tank.

An apparatus contains at least one pressure-rated apparatus shell and at least one modular framework system containing ceramic fiber composite materials and arranged within the apparatus shell. A modular lining apparatus includes the modular framework system and refractory bricks. The apparatus can be used for high-temperature reactors, especially electrically heated high-temperature reactors.

A box style steam methane reformer (15) has plural sections (37), with each section having walls (27-29-31, 33) forming an interior cavity (35) and open ends (43) that communicate with the interior cavity. Each section has a feedstock supply pipe (71) and a fuel supply pipe (63) located along the top wall, as well as a syngas collection pipe (79) and a flue gas collection duct (75) located outside of the bottom wall. The pipes and ducts have ends that are aligned with each other to allow the sections to be assembled together. Burners (67) are in the interior cavity and are connected to the fuel supply pipe. Reactor tubes (59) extend through the interior cavity. Refractory members (81) are located in the interior cavity and across a slot. The spacing between the refractory members varies to control the flow of flue gas.

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) or other materials are processed to produce useful intermediates and products, such as energy, fuels, foods or materials. For example, systems and methods are described that can be used to treat feedstock materials, such as cellulosic and/or lignocellulosic materials, in a vault in which the walls and optionally the ceiling include discrete units. Such vaults are re-configurable.

Disclosed herein are cell processing systems, devices, and methods thereof. A system for cell processing may comprise a plurality of instruments each independently configured to perform one or more cell processing operations upon a cartridge, and a robot capable of moving the cartridge between each of the plurality of instruments.

This disclosure is drawn to systems, devices, apparatuses, and/or methods, related to fuel cell cartridges. Specifically, the disclosed systems, devices, apparatuses, and/or methods relate to compact fuel cell cartridges for producing hydrogen gas for use by fuel cells. Some example fuel cell cartridges may include a reactor module for storing a reactant, a water module for storing water, and an interface coupling the reactor module and the water module. The interface may permit the water to flow from the water module to the reactor module such that the water mixes with the reactant in the reactor module to form a gas (e.g., hydrogen gas) that may exit through a gas outlet.

The invention describes and claims a processing plant and a method for processing viscous oil and oil products. The processing is effectuated with a plant, which comprises a plurality of reaction modules, a plurality of rectifying chambers and pipelines. Each reaction module and each rectifying chamber comprises a tank, a pump, a hydrocavitation generator. Each reaction module comprises a plurality of intermediate reaction stages. Each rectifying chamber comprises a plurality of intermediate rectifying stages. The reaction module and the rectifying chamber are interconnected. Intermediate reaction stages are connected by pipelines, with the last one connected to a rectifying chamber.