REACTION CHAMBER FOR A CHEMICAL REACTOR, AND CHEMICAL REACTOR CONSTRUCTED THEREFROM

Abstract

A reaction chamber for a chemical reactor comprises a casing (100) of the reaction chamber, a floor (200) of the reaction chamber having an opening (300) located in the floor, an agitator shaft (400) located in the chamber and having at least one agitator element (500), connected thereto, wherein the agitator shaft (400), seen in the longitudinal direction, has a beginning (600) and an end (700). In the opening (300) of the floor (200) a removable sleeve (800) is provided, which projects out of the reaction chamber. The sleeve (800) is arranged in alignment with the axis of rotation of the agitator shaft (400). The internal diameter of the sleeve (800) is greater than the diameter of the agitator shaft (400) and the agitator shaft (400), at the beginning (600) thereof and/or at the end (700) thereof, is adapted to absorb reversibly a torque provided by means of a further shaft and/or to transmit a torque to a further shaft. Using such a reaction chamber, it is possible to build up modular chemical reactors having decreased backmixing.

Claims

1. A process for carrying out a chemical reaction, comprising carrying out the reaction in a chemical reactor the reactor comprising a multiplicty of reaction chambers, wherein the reaction chambers comprise: a casing of the reaction chamber, a floor of the reaction chamber having an opening located in the floor, an agitator shaft located in the chamber and having at least one agitator element, connected thereto, wherein the agitator shaft, seen in the longitudinal direction, has a beginning and an end, wherein in the opening of the floor a removable sleeve is provided, which projects out of the reaction chamber, the sleeve is arranged in alignment with the axis of rotation of the agitator shaft, the internal diameter of the sleeve is greater than the diameter of the agitator shaft and in that the agitator shaft, at the beginning thereof and/or at the end thereof, is adapted to absorb reversibly a torque provided by means of a further shaft and/or to transmit a torque to a further shaft, wherein at least one first reaction chamber and one second reaction chamber are arranged following one another and the agitator shaft for the first reaction chamber is connected to the agitator shaft of the second reaction chamber to transmit a torque.

2. The process as claimed in claim 1, wherein the reaction is carried out at least intermittently with a constant amount of substances introduced into the reactor and discharged from the reactor.

3. The process as claimed in claim 1, wherein in the stirred reactor, there are arranged following one another, a first reaction chamber and a second reaction chamber and the agitator shaft of the first reaction chamber is connected to the agitator shaft of the second reaction chamber to transmit a torque and furthermore at least one operating state is monitored in the first and/or second reaction chamber, at a predetermined deviation of the operating state from a predetermined value of this operating state the feeds opening out into this reaction chamber are closed and the substances originally transported through these feeds are introduced into another reaction chamber.

4. The process as claimed in claim 3, wherein the monitored operating state is the pressure drop from one reaction chamber to the adjacent reaction chamber.

5. The process as claimed in claim 1, wherein the reaction is a multiphase reaction.

Description

[0045] The present invention will be described in more detail with reference to the figures hereinafter, without being limited thereto. In the drawings:

[0046] FIG. 1 shows a reaction chamber according to the invention in a view from the top and in cross section

[0047] FIG. 2 shows a multiplicity of reaction chambers according to the invention stacked one above the other in cross section

[0048] FIG. 3 shows a chemical reactor according to the invention

[0049] FIG. 1 shows a reaction chamber according to the invention in a combined view having a plan view (upper part of the figure) and a side cross sectional view (lower part of the figure). The reaction chamber has a casing 100, a floor 200 inclined in this case at 33, and also an opening 300 in the floor 200. The casing 100 and the floor 200 are constructed jointly as heating and cooling casing. For this purpose, a double-shell construction having a second casing 110 and a second floor 210 is used, which contains a cavity 120. Through this cavity 120, a heating or cooling medium for heat exchange can be conducted by means of inlets and outlets that are not shown here. The chamber floor is also heated or cooled thereby and not only the casing as in many conventional structures of kettle reactors.

[0050] The reaction chamber in addition has an agitator shaft 400 for driving agitator elements 500. The beginning 600 of the agitator shaft 400 is shown at the top in FIG. 1, and the end 700 at the bottom. Beginning 600 and end 700 of the agitator shaft 400 are designed as female and male, respectively, connectors or plug-in connections, in such a manner that when a plurality of reaction chambers are stacked one above the other the agitator shafts of two successive reaction chambers engage in one another in a form-fitting manner in the direction of rotation. Then they form a combined agitator shaft with which the agitator elements of the individual chambers can be driven.

[0051] Within the reaction chamber, the agitator shaft 400 is received by a bearing 1000, which itself is supported via corresponding supports 1100 in the reaction chamber. In addition, within the reaction chamber, baffles 1200 are present which, in interaction with agitator elements 500, ensure a relatively high mixing of the reactor contents.

[0052] In the opening 300 of the floor 200 of the reaction chamber, in addition there is a removable sleeve 800 which (as shown at the bottom here) projects out of the reaction chamber. The sleeve 800 is arranged in alignment with the axis of rotation of the agitator shaft 600. In FIG. 1, sleeve and axis of rotation are centered in the reaction chamber.

[0053] The internal diameter of the sleeve 800 is greater than the diameter of the agitator shaft 400 at the height of the sleeve 800. In addition, the agitator shaft 400 projects through the sleeve 800 out of the reaction chamber. As a result, a gap 900 is formed between agitator shaft 400 and sleeve 800, through which gap, in the case of a plurality of reaction chambers stacked one above the other, a mass transfer can take place between one chamber and the adjacent chamber.

[0054] To increase the versatility and modularity of the use of the reaction chambers according to the invention, not only is the sleeve 800 detachable, but also the agitator shaft 400, the bearing 500, the support 1100 and the baffle 1200, and therefore are usable for other structures adapted to a specific application case.

[0055] FIG. 2 shows a cross-sectional view of three reaction chambers according to the invention stacked one above the other, as can occur in a chemical reactor according to the invention. The individual chambers are as shown and explained in FIG. 1. As may be seen, the reaction chambers are designed in such a manner that the bottom seal of one chamber forms the upper seal of the chamber lying therebeneath. As a result, a chemical reactor may be made up in a modular manner. Obviously, a sealing composition can also further be provided between the individual reaction chambers.

[0056] The agitator shafts 400 engaging in one another in a form-fitting manner in the direction of rotation form, as related to transmission of a torque, a combined agitator shaft. In this case, it can be noted that shear forces also occur in the gap 900, which is formed between agitator shaft 400 and sleeve 800 and through which a mass transfer can take place between adjacent reaction chambers. Therefore, there is no dead zone in which the contents of the reaction chamber are not thoroughly agitated.

[0057] The width of the gap 900 and therefore the mass transfer between the individual reaction chambers may be established by means of the diameter of the agitator shaft and/or the internal diameter of the sleeves 800. For practical reasons, it is preferred only to exchange the sleeves 800 if another gap width between the chambers is desired. Owing to the fact that the sleeves 800 are removable, this is effected in a simple manner.

[0058] FIG. 3 shows schematically a chemical reactor according to the invention with a total of seven reaction chambers according to the invention. The reaction chambers are stacked one above the other in a similar manner to the arrangement shown in FIG. 2 and are sealed at top and bottom with a cover plate 2000 and base plate 2010. The arrangement is mechanically stabilized by means of tie rods 2100 and nuts 2110.

[0059] A torque for driving the agitator shafts is transmitted by means of coupling 2200 to the agitator shafts in the interior of the chemical reactor. In the cover plate 2000, in addition accesses 2300 and 2310 are arranged, through which substances or measuring sensors can be introduced into the topmost reaction chamber. Such an access 2320 is also located at the outlet 2400 which is integrated into the base plate 2010.

[0060] Via the feed lines 2500 and the outlets 2510, the heating/cooling casings of the individual reaction chambers can be provided with a heating or cooling medium. An individual heating or cooling is possible.

[0061] The individual reaction chambers are accessible via accesses 2600 and 2610 for material introduction, material discharge and measuring sensors. Via a suitably chosen piping installation, in addition, a bridging of a reaction chamber can be achieved, if a fault occurs during running operation.