RU177155U1 - BLOCK FOR IMPLEMENTING CATALYTIC HETEROGENEOUS REACTIONS - Google Patents

Abstract

The utility model relates to the field of chemistry, namely, to devices and systems for carrying out heterogeneous catalytic reactions and can be used for the production of various chemical products and reagents, as well as for the purification and neutralization of gaseous and liquid emissions. A catalytic unit for carrying out heterogeneous reactions in a moving reaction stream is described. It consists of alternately alternating spiral layers of a flexible microfiber catalytic material in the form of pressed flat sheets and layers of a volumetric structural element permeable to the reaction stream, which together form a cylinder, the base of which is perpendicular to the direction of the layers, the catalytic the block contains alternately alternating layers with the catalytic material layers GOVERNMENTAL bulk-forming elements 1-20 mm in height and additional planar structure-forming elements thickness 0.1-3 mm. The block is characterized by increased mechanical stability and strength. 1 ill.

Description

The utility model relates to the field of chemistry, namely, to devices and systems for carrying out heterogeneous catalytic reactions and can be used for the production of various chemical products and reagents, as well as for the purification and neutralization of gaseous and liquid emissions.

A number of catalytic systems are known based on flexible structured microfiber carriers, in particular, fiberglass, the use of which in a number of catalytic reactions is extremely promising. (Pat. RF №2069584, B01J 23/38, B01J 23/70, 1996.11.27, Pat. RF №2289565, С07С 7/167, 2006.12.20, Pat. RF №2252208, С07С 19/01, С07С 19 / 045, 2005.05.20, Pat. Of the Russian Federation No. 2250890, С07С 17/10, С07С 19/01, 2005.04.27, Pat. Of the Russian Federation No. 2250891, С07С 21/06, С07С 17/25, 2005.04.27, Pat. 2252915, СВВ 17/78, B01J 23/56, 2005.05.27).

At the same time, there is the task of finding the optimal method for the location of such a catalyst in the reaction volume, which ensures the maximum efficiency of the reaction (achieving high conversions of the starting reagents and conversion selectivities) in a moving gas, liquid, or gas-liquid reaction stream with the minimum dimensions of the contact device (reactor) and minimum hydraulic resistance to the reaction flow.

A device for conducting heterogeneous catalytic reactions, containing a rectangular housing, inside which there is a combustion chamber with a burner and a pipe for supplying ventilation emissions, a afterburner with a catalytic element, the catalytic element is made of several layers of fiberglass fabric activated by metals and / or their oxides, which are stretched through the rods, fixed in a housing in two rows in a checkerboard pattern (Pat. RF №2171430, F23G 7/06, .27.07.2001). This arrangement of the catalyst allows for relative compactness of the device while maintaining a low hydraulic resistance of the catalyst layer to the flow of the reaction mixture.

The disadvantage of this device is the complexity of the installation and replacement of the catalyst, as well as the difficulty of sealing the edges of the layer, which can lead to the slip of unreacted reaction mixture past the catalyst layer along the walls of the catalytic reactor, reducing its efficiency. In addition, the dimensions and metal consumption of the device are quite large.

Also known is a catalytic system with a radial layer of fiberglass material, containing at least one layer of flexible fibrous catalyst and a support and distribution symmetrical device, the axial line of which either coincides with the direction of flow of the reaction mixture or deviates from it by an angle of not more than 30 °, where the catalyst installed on the partially or completely permeable to the flow of the reaction mixture of the side surface of the device (US Pat. RF No. 2200622, B01J 8/04, 2003.03.20). The system is characterized by low hydraulic resistance and high reaction efficiency.

The disadvantages of this system are, in some cases, the low efficiency of reactions due to the insufficiently uniform distribution of the reaction flow over the cross section of the layer, and also because of the possibility of diffusion breakthrough of the reagents associated with a small thickness of the catalyst layer (implementation of the ideal mixing mode). In addition, such a system is not compact enough.

Known catalytic system (catalytic unit) for the implementation of heterogeneous reactions in a moving reaction stream, consisting of a flexible microfiber catalytic material in the form of flat cloths or woven, or woven or pressed, and a structure-forming element in which the catalytic material is formed in the form of a spiral, and structure-forming the element is located between the turns of the spiral, providing a distance between them from 0.5 to 10 mm (Pat. RF No. 66975, B01J8 / 00, 2007.10.10). The use of the described block provides high efficiency of the catalytic reactions, low hydraulic resistance of the system to the flow of the reaction mixture while ensuring uniform distribution of the reaction mixture flow over the system cross section and preventing diffusion breakthroughs of the reagents through the catalyst bed.

The disadvantages of such a block include its lack of mechanical stability. In particular, when using a corrugated metal mesh as a structure-forming element, the layers of a flexible catalyst can take the form of structuring corrugations, as a result, the block will fold with loss of height of part or all channels, which will violate its geometric uniformity, change its external dimensions and negatively affect its hydraulic resistance.

The utility model solves the problem of simplifying the design of the catalytic unit for the implementation of heterogeneous reactions.

The technical problem is the high mechanical stability of the unit while retaining all its initial advantages, namely, the possibility of compact and technologically simple formation of catalytic systems in large catalytic reactors while maintaining high efficiency of the catalytic reactions, low hydraulic resistance of the catalytic system to the flow of the reaction mixture.

The problem is solved by the fact that a catalytic unit for performing heterogeneous reactions in a moving reaction stream is proposed, consisting of alternatingly alternating spiral layers of flexible microfibrous catalytic material in the form of extruded flat sheets and layers of a volumetric structural element permeable to the reaction stream, which together form a cylinder, a base which is perpendicular to the direction of the arrangement of the layers, which contains alternately alternating with the layers of the catalytic mat rial beds of basic volumetric building blocks 1-20 mm in height and additional planar structure-forming elements thickness 0.1-3 mm.

The system is illustrated in Fig., Which shows a General view of the catalytic block of a cylindrical shape, where: 1 - the catalyst web, 2 - the main volumetric structure-forming element, 3 - additional flat structure-forming element.

The catalytic unit consists of layers of flexible microfiber catalytic material 1, in the form of flat pressed webs, between which are located the layers of the main structure-forming element 2, which provides the necessary distance between the layers of the catalytic web for the passage of the reaction mixture while maintaining the uniformity of this distance over the cross section of the catalytic unit, as well as additional flat structure-forming elements 3, providing mechanical strength and stability of the block.

The optimal height of the main structure-forming element lies in the range of 1-20 mm. At a height of less than 1 mm, the hydraulic resistance of the catalytic unit can significantly increase; with an increase in height above 20 mm, the mass transfer of reagents to the catalyst surface may deteriorate, which will negatively affect the efficiency of the reaction. As the main structure-forming element, the use of flexible corrugated tape is possible. It is more preferable to use a permeable corrugated tape (mesh), which will allow the redistribution of the reaction stream between the corrugation channels and thereby increase the mass transfer efficiency and improve the uniformity of the distribution of the reaction stream over the cross section of the catalyst block. It is also possible to use nets of volumetric weaving, which are able to provide the necessary distances between the layers of the catalytic sheet under external mechanical stresses on the catalytic block.

The optimal thickness of the additional flat structure-forming elements is 0.1-3 mm. With a thickness of less than 0.1 mm, the strength of these elements may be insufficient, with a thickness of more than 3 mm, the material consumption for their creation may turn out to be excessively high, in addition, in this case, these elements will occupy too much of the block volume, thereby reducing its efficiency. For the manufacture of additional flat structure-forming elements, flat metal ribbons and nets can be used.

The application of the described blocks allows the formation of catalyst layers of arbitrary shape and size with high mechanical stability and resistance to mechanical and temperature shocks. In such layers, high efficiency of catalytic reactions, low hydraulic resistance to the flow of the reaction mixture will be stably ensured, while ensuring uniform distribution of the flow of the reaction mixture over the cross section of the layers and preventing diffusion breakthroughs of the reactants. The application of the described blocks allows for a catalytic reaction in a compact reactor with very small dimensions and metal consumption. In addition, the mechanical stability of the blocks allows you to arrange them in any geometric orientation (vertically, horizontally, etc.), which greatly expands the possibilities of their practical application.

Example

The catalytic unit for carrying out heterogeneous catalytic reactions consists of alternately alternating spiral layers of a flexible catalytic material based on a fiberglass support in the form of flat pressed webs and structural elements, forming a cylinder in the aggregate, the base of which is perpendicular to the direction of the layers and has a diameter of 200 mm. In this case, two alternating types of structuring elements are used: layers of a three-dimensional chain-link metal mesh with a corrugation height of 10 mm and flat metal mesh with a thickness of 1 mm.

The combination of corrugated grids and adjacent catalyst sheets form regularly arranged channels for the passage of the reaction stream along the surface of the catalytic sheets. Moreover, such channels have the same height (~ 5 mm), which determines the geometric uniformity of the block, the high mass transfer efficiency of the reagents from the flow to the surface of the catalysts, and low hydraulic resistance. Flat metal grids between the catalyst sheets provide mechanical stability and strength of the block, its long-term stability under mechanical and thermal loads.

In a similar block that does not contain flat metal grids, under external loads during operation, “collapse” of corrugated grids can occur, leading to a change in the external dimensions of the block and its internal structure. In such blocks and catalyst layers formed from such blocks, zones of increased density may appear, where the catalyst becomes inaccessible to the reagents, as well as zones of the breakthrough of the reaction stream, which significantly reduces its efficiency.

Claims (1)

A unit for carrying out catalytic heterogeneous reactions in a moving reaction stream, consisting of alternately alternating spiral layers of a flexible microfiber catalytic material or in the form of pressed flat sheets and layers of a volumetric structural element permeable to the reaction stream, forming a cylinder in the whole, the base of which is perpendicular to the direction of the layers, different the fact that the catalytic block contains alternately alternating with layers of the catalytic Container material layers main bulk-forming elements 1-20 mm in height and additional planar structure-forming elements thickness 0.1-3 mm.

Images