Abstract:
A structured packing element for a column for at least one of mass transfer and heat exchange between a heavy fluid phase and a light fluid phase. The structured packing element comprises at least two layers of a grid comprising openings that are surrounded and separated from each other by separating elements. At least two of the layers are arranged in a longitudinal direction parallel and in touching contact with each other such that an open space extending from one end to an opposite end of the layers is provided between the layers such that at least one of the heavy fluid phase and the light fluid phase may flow therethrough. An average width of at least 50% of the separating elements between adjacent openings is at least 15 times a layer material thickness and is between 70% and 125% of an average hydraulic diameter of the adjacent openings.
Abstract:
The contacting device for countercurrent contacting of fluid streams and having a first pair of intersecting grids of spaced-apart and parallel deflector blades and a second pair of intersecting grids of spaced-apart and parallel deflector blades. The deflector blades in each one of the grids are interleaved with the deflector blades in the paired intersecting grid and may have uncut side portions that join them together along a transverse strip where the deflector blades cross each other or adjacent opposed ends of the deflector blades and cut side portions that extend from the uncut side portions to the ends of the deflector blades. At least some of the deflector blades have directional tabs and associated openings to allow portions of the fluid streams to pass through the deflector blades to facilitate mixing of the fluid streams.
Abstract:
A cell structure is provided that is (i) capable of handling, on inner and outer surfaces, heat transfer requirements of heat exchangers and/or be a substrate for coatings for catalytic reactors, (ii) able to be easily combined and interconnected into a variety of shapes, and (iii) may be created in an additive manufacturing process. The provided cell structure may be replicated and interconnected with other cell structures to create lattice structures in a variety of shapes. Accordingly, the cell structure may be used to build a heat exchanger or catalytic reactor that has reduced weight compared to traditional architectures.
Abstract:
Provided herein are methods and systems for converting natural gas, and specifically methane, into higher-value oxycarbon products, such as methanol, methyl formate, and formic acid. The natural gas is introduced into an aqueous solution with hydroxyl radicals and reacted in ambient conditions to form the desired products in the presence of a metal catalyst. The methods described herein overcome the “over-activation” dilemma of prior art methods that lead to the formation of undesirable carbon oxide compounds. Methods and apparatus for forming hydrogen peroxide via electrolysis and for forming hydroxyl radicals from the hydrogen peroxide via reaction with ferrous ions are also provided.
Abstract:
A reactor is described for the production of C2 to C8 olefins from gaseous oxygenate and H2O and one or more material flows containing C2 C4, C5, C6, C7, C8 olefin and paraffin at 400° to 470° C., wherein several reaction stages which the material flow can pass through from the top to the bottom, each consisting of a support base with a catalyst layer situated on it, are arranged in a closed, upright container. In order to be able in each case to lower the temperature of the reaction mixture leaving the reaction stages before it enters into the next reaction stage, it is provided that each support base consists of cells which are placed closely next to each other with no gaps and which are securely attached to each other and filled with catalyst, and in the space formed by two neighboring reaction stages, respectively, an assembly of nozzle tubes is installed for spraying a liquid phase containing H2O and DME and/or MEOH, using a water-saturated gas phase containing mainly DME and/or MEOH, in the direction of the following reaction stage downstream.
Abstract:
The invention relates to a corrugated packing grid with consecutively arranged wave crests and wave troughs for a structured packing, which is assembled from several packing grids, for gas-liquid contacting apparatuses, and to a packing assembled from said packing grids. The aim of the invention is to provide a packing grid and a packing which have a large mass transfer area and a low pressure drop at the same time and which offer a high mechanical strength. According to the invention, this is achieved in that elements lie in the region of the wave troughs of the packing grid, said elements extending into the wave troughs.
Abstract:
A bundle assembly for vertical, gravity flow driven polymerization reactors for combinations of high viscosity, high throughput, and thin polymer films is provided. The bundle assembly includes static internal components that provide large areas of free liquid surfaces in contact with the atmosphere of the reactor while still attaining sufficient liquid holdup times for polymerization to take place. The bundle assembly includes one or more stationary film generators. The bundle assembly further includes one or more stationary arrays of film support structures. Each of the film support structures has a first side and a second side. Both sides of the film support structure are coated with flowing polymer. The vertical arrangement of components in the bundle assembly cause the polymeric melt to cascade down the vertical length of a reaction vessel interior that incorporates the bundle assembly. The present invention also provides a polymerization reactor that incorporates the assembly of the invention and a method of increasing the degree of polymerization of a polymer melt by using the assembly of the invention.
Abstract:
A self-heat exchange type heat exchanger which can provide a greater heat transfer area in a limited capacity, can be easily prepared and can lead to drastic enhancement of heat exchange efficiency. A heat exchanger having a partition type heat transfer material (BF) for parting a high temperature fluid (1) and a low temperature fluid (2) from each other, characterized in that the heat transfer material (BF) is bellows-shaped and is arranged such that both the fluids (1, 2) flow counter to each other mainly through the gap portion in the bellows section of the heat transfer material (BF) along the ridge line or valley line thereof and the heat transfer material (BF) has a fluid forwarding space portion (F) at one or both ends thereof crossing the ridge line of the bellows section for forwarding one of the fluids to the gap portion in the bellows section on the opposite side thereof, whereby the fluid which has been forwarded to the opposite side via the fluid forwarding space portion (F) acts as the other fluid to be heat-exchanged to perform heat exchange.
Abstract:
A device for maximum vapor or gas throughput is provided for material and/or energy exchange, in which large vertical flow spaces are present. Vapors or gases flow without impact losses and thus with extremely low pressure loss per meter in counter flow to liquid on zigzag wires or threads arranged vertically next to one another, produced with conventional web or braiding machines, along wide-meshed fabric or grid webs and are brought for exchange with the liquid. Simultaneously, by optimizing the wire or thread diameter and its count and the arrangement of fabric or grid webs, considering the large vertical flow spaces and a uniform wetting of the large number of zigzag wires or threads arranged vertically next to one another against the wave peaks, a minimal specific volume of the device is achieved by wide-meshed fabrics or grids for the vapor or gas flow through a step-wise division of the trickling liquid.
Abstract:
The invention relates to a wash column for material and/or energy exchange between media, especially between a liquid trickling down and a gas or a lighter liquid rising in a counter-current. The invention especially relates to a novel structural packing that comprises liquid guide elements (19) in the form of wires or threads that form substantially rhomboid masses with vertical axes in imaginary surfaces (21) and that surround, for example in a polygonal grid, substantially free, vertical flow channels (22) for the counter-flowing gas. The nodes (18) of the liquid guide elements (19) are located at the respective points of intersection of a horizontal cross-section grid. The distance between the guide elements or the size of the meshes is chosen such that the liquid does not form film curtains and flows off only in defined flows, linearly along the guide elements (19). At the ends of the packing, the guide elements (19) for the introduction of liquid and for the draining-off of liquid are bundled step-wise to common strands for introducing or draining off liquid.