Abstract:
A catalyst arrangement disposed within a vertical reaction tube includes a structured catalyst within an upper part of the reaction tube, a particulate catalyst beneath the structured catalyst in a lower part of the reaction tube, and a catalyst support device located between the structured catalyst and the particulate catalyst, wherein the catalyst support device includes a cylindrical body having a first end adapted for connection to the structured catalyst, and a second end, and the cylindrical body has a diameter 70-90% of the internal diameter of the tube and a length/diameter in the range 0.5-2.5.
Abstract:
The present invention provides a packing element comprising at least one sheet having a plurality of deformations, the sheet being operable to form a folded or helical configuration wherein adjacent portions of the at least one sheet are spaced to allow for flow of at least one of fluid, air and gas therebetween.
Abstract:
The present invention relates to a process for production of acrylic acid, comprising at least the following steps: a. dehydration of glycerine to an acrolein-comprising dehydration product; b. gas phase oxidation of the dehydration product to obtain an acrylic acid-comprising monomer gas; c. bringing into contact of the monomer gas with a quench agent to obtain an acrylic acid-comprising quench phase; d. work-up of the quench phase to obtain an acrylic acid-comprising monomer phase; whereby, during the dehydration a liquid phase a1 and a gas phase a2 is present, whereby in the liquid phase a1 a plurality of gas bubbles is generated, as well as a process for production of polymers by polymerization of acrylic acid, preferably for production of water-absorbing polymers, the water-absorbing polymers obtainable by this process, a composite, a process for production of a composite, the composite obtainable by this process, and further chemical products.
Abstract:
The invention relates to a packing structure (1) for a fluid exchange column, the packing structure defining an exchange surface for at least one down-flowing liquid phase that is to be put into intimate contact with at least one up-flowing gas phase, the structure including a volume formed by a plurality of rows of bundles of tubes (10), each bundle having four tubes (10a-10d) respectively oriented along four directions (D10a-D10d) forming an angle relative to the axis of the structure, the plurality of tubes forming a plurality of passages opening out to the outside surface of the structure (1).
Abstract:
A mixing element, which is produced at low cost, has high mixture agitation effectiveness, and is easily made large, and a static fluid mixer using the mixing element are provided. Further, a gas-liquid treatment apparatus with high treatment ability is provided. A mixing element 1 includes: a cylindrical passage tube 2 trough which fluid flows; a plurality of spiral rightward rotation type first blades 3 formed of a perforated object, which are provided in the passage tube 2; a first inner cylindrical tube 5 shaped like a cylinder and disposed inside the blades 3; a plurality of spiral rightward rotation type blades 6 provided in the inner cylindrical tube 5; and an opening 9 formed in the axial center portion of the blades 6. A static fluid mixer is formed by using at least one mixing, element 1 mentioned above.
Abstract:
The invention relates to a packing structure (1) for a fluid exchange column, said structure defining an exchange surface for at least one down-flowing liquid phase that is to be put into intimate contact with at least one up-flowing gas phase, the structure being characterized in that it comprises a volume formed by a plurality of rows of bundles of tubes (10), each bundle comprising four tubes 10a-10d) respectively oriented along four directions (D10a-D10d) forming an angle relative to the axis of the structure, the plurality of tubes forming a plurality of passages opening out to the outside surface of the structure (1).
Abstract translation:本发明涉及一种用于流体交换塔的填料结构(1),所述结构限定了与至少一个向上流动的气相紧密接触的至少一个向下流动的液相的交换面, 结构的特征在于它包括由多排管束(10)形成的体积,每个束包括分别沿四个方向(D 10 a D 10 d)定向的四个管10a-10d),其形成一个角度相对 相对于该结构的轴线,多个管形成多个通向该结构(1)的外表面的通道。
Abstract:
There is provided a catalyst module having a waste liquid inlet passage for the inflow of a waste liquid, whose partition wall is formed of fibrous activated carbon, in which: the fibrous activated carbon is impregnated with or contains a catalyst; and a waste liquid in the waste liquid inlet passage passes through the partition wall and is discharged out of the waste liquid inlet passage. Further, there is provided a catalyst module, in which a plurality of waste liquid inlet passages is arranged in the form of a bundle. In the catalyst module are also provided partition walls formed of a fibrous activated carbon layer prepared by laminating a plurality of the fibrous activated carbon in the form of sheets.
Abstract:
A method and assembly for utilizing open-cell cellular solid material in a component separation unit to separate one or more process streams into component process streams having desired compositions. A method and assembly for using said open-cell cellular solid material to separate process streams into desired component process streams in a component separation unit, wherein the open-cell cellular solid material can include oxides, carbides, nitrides, borides, ceramics, metals, polymers, and chemical vapor deposition materials.
Abstract:
A fixed particle bed in a vessel wherein the bed is a structured bed in a plurality of flow channels with the cross-section of the bed in each channel being from 1 to 20 particles, more preferably 1 to 10 particles.
Abstract:
The present invention is to provide a gas-liquid processing apparatus having a high contact efficiency of a gas and a liquid and a high reaction efficiency at a low production cost. A static type fluid mixer includes a passage pipe for the passage of a fluid and a spiral blade body arranged in the passage pipe with the longitudinal direction substantially perpendicularly but being absent in the center portion of the passage pipe. A liquid and a gas are supplied into the static type fluid mixer and a fluid is returned from the bottom portion of the static type fluid mixer to the upper portion via the pipe for the fluid circulation. The fluid is maintained in the static type fluid mixer at a pressured state higher than the atmospheric pressure.