SYSTEM OF INTERNALLY BACKMIXING THE REACTIVE MASS IN A ROTATING CYLINDER REACTOR

Abstract

The present invention relates to a system for backmix the reagent mass in rotating cylindrical reactors. In this context, the present invention provides a system for internal backmix of the reagent mass in a rotating cylindrical reactor (2), comprising a first set of drag fins (27) adapted for dragging the reagent mass in a first direction, and a second set of drag fins (28) adapted for dragging the reagent mass in a second direction opposite to the first direction, wherein the first (27) and the second (28) set of drag fins are positioned internally along the length of the cylindrical rotating reactor (2). The system described above allows the mixing of a portion of the reagent mass at a more advanced stage of the reactor with another portion at an earlier stage of processing, homogenizing the reagent mass temperatures and increasing the reactor's productivity.

Claims

1. Internal backmix system of the reagent mass comprised in a rotating cylindrical reactor (2), characterized by comprising: a first set of drag fins (27) arranged for dragging the reagent mass in a first direction; and a second set of drag fins (28) arranged for dragging the reagent mass in a second direction opposite to the first direction, wherein the first (27) and the second (28) set of drag fins are positioned internally along the length of the rotating cylindrical reactor (2); and wherein the drag fins of the first (27) and second (28) sets of drag fins are attached to the inner side of the rotating cylindrical reactor (2) by welding forming a drag string along a continuous helical path.

2. System, according to claim 1, characterized in that the first set of drag fins (27) is arranged for dragging the reagent mass from the feed inlet of the rotating cylindrical reactor (2) to the outlet.

3. System, according to claim 1, characterized in that the second set of drag fins (28) is arranged for dragging the reagent mass from the outlet of the rotating cylindrical reactor (2) to the feed inlet.

4. System, according to claim 1, characterized in that the first set of drag fins (27) is adjacent to the second set of drag fins (28), both being parallel to the longitudinal axis of the rotating cylindrical reactor (2).

5. (canceled)

6. System, according to claim 1, characterized in that the total area of the fins of the first set of drag fins (27) in contact with the reagent mass is greater than the total area of the second set of drag fins (28).

7. System, according to claim 6, characterized in that it comprises a greater number of fins in the first set of drag fins (27) compared to the second set of drag fins (28).

8. System, according to claim 6, characterized in that the fins of the first set of drag fins (27) have a greater length and/or width than those of the second set of drag fins (28).

Description

BRIEF DESCRIPTION OF THE IMAGES

[0013] The detailed description presented below makes reference to the attached figures and their respective reference numbers.

[0014] FIG. 1 illustrates a cross-sectional side view of the cylindrical reactor comprising the backmix system according to the preferred embodiment of the present invention.

[0015] FIG. 2 illustrates a plan view of the internal side of the rotating cylindrical reactor.

DETAILED DESCRIPTION OF THE INVENTION

[0016] Preliminarily, it is emphasized that the description that follows will start from preferred embodiments of the invention. As will be evident to anyone skilled in the subject, however, the invention is not limited to these particular embodiments.

[0017] The present invention solves the technical problem described above by providing a system for internal backmix of the reagent mass in a rotating cylindrical reactor 2. For the purposes of this description, a rotating cylindrical reactor 2 is defined as a cylindrical rotating body with openings at its ends.

[0018] The system of the present invention, according to a preferred embodiment illustrated in FIGS. 1 and 2, comprises a first set of drag fins 27 adapted for dragging the reagent mass in a first direction, and a second set of drag fins 28 adapted for dragging the reagent mass in a second direction opposite to the first direction, wherein the first 27 and the second 28 set of drag fins are internally positioned along the length of the rotating cylindrical reactor 2.

[0019] As shown in the cross-sectional side view of FIG. 1, the drag fins of the first 27 and second 28 sets of drag fin are preferably sheet metal whose height typically corresponds to approximately one-tenth of the diameter of the rotating cylindrical reactor 2.

[0020] Preferably, the drag fins of the first 27 and second 28 sets of drag fins are attached to the inner side of the rotating cylindrical reactor 2 by welding. However, the fins may be attached to the inner side of the rotating cylindrical reactor 2 by means of any attachment methods known in the state of the art.

[0021] FIG. 2 represents a plan view of the internal surface of the side of the rotating cylindrical reactor 2. In the cylindrical form, point A coincides with point A and point B coincides with B. In this example, which in fact consists of a manufacturing plan, the internal side plate of the rotating cylindrical reactor 2 was divided into 36 sections along its length and 8 sections along its width. It is worth pointing out that this sectioning is only exemplary and illustrative, so that other configurations can be performed by a technician versed in the art.

[0022] In the present example, the length and diameter of the rotating cylindrical reactor 2 are respectively L and D; the number of imaginary lines along the length and width of the planar side are respectively n and m; and the fins are mounted plates inclined with respect to the longitudinal lines a, b, c, d, e, f, g, h. The inclination of the propeller fins describes an angle with respect to these longitudinal lines such that

[00001]$\mathrm{tg}=\frac{y}{x},$

where x and y are the dimensions of each of the sectors, as illustrated in FIG. 2. Considering that

[00002]$x=\frac{L}{n}\mathrm{and}y=\frac{.Math.D}{m},$

the inclination of the fins can be written as:

[00003]$\mathrm{tg}=\frac{\frac{.Math.D}{m}}{\frac{L}{n}}=\frac{.Math.D.Math.n}{L.Math.m}.$

[0023] The plan view in FIG. 2 also shows the different sets of drag fins 27, 28 arranged along the longitudinal lines a, b, c, d, e, f, g, h, the said sets of drag fins 27, 28 being adjacent to each other and parallel to the longitudinal axis of the cylindrical rotary reactor 2. The first set of drag fins 27 is adapted for dragging the reagent mass from the feed inlet to the outlet (from left to right). The second set of drag fins 28, in turn, is adapted for dragging the reagent mass from the outlet to the feed inlet (from right to left). Obviously, since the ultimate goal is that all of the reagent mass entering the feed inlet comes out treated at the outlet, the total area of the fins of the first set of fins 27 in contact with the reagent mass is greater than the total area of the second set of fins 28. This can be realized, by way of example, in the form of a larger number of fins in the first set of drag fins 27 compared to the second set of drag fins 28. Alternatively, there is the possibility that the number of fins of the two sets is the same, but the fins of the first set of drag fins 27 have a greater length and/or width than those of the second set of drag fins 28.

[0024] In the realization where there are a greater number of fins in the first set first set of drag fins 27, the number of fins carrying the reagent mass forward (from the feed inlet to the outlet) is always greater than the number of fins carrying the reagent mass backward. For example, for every eight (8) fins in rotary cylindrical reactor 2, six (6) may belong to the first set of drag fins 27 and two (2) to the second set of drag fins 28. In this case, effectively, there are 6 (six) fins doing the work of carrying the material forward while the other 2 (two) perform the service of backmix the reagent mass, causing a portion of the reagent mass in a more advanced stage of reaction (hotter) to mix with a portion of the reagent mass in a previous stage of reaction (colder).

[0025] The distribution of fins in the

[00004]$\frac{L}{x}$

vertical bands is repeated along the entire inner length of the rotating cylindrical reactor 2, generating a forward drag string of reagent mass, with regular sectors of fins bringing the hottest mass to the rear. This arrangement consists of a way to promote the thermal exchange of the reagent mass, conferring an increase in productivity to the rotating cylindrical reactor 2.

[0026] Therefore, as exposed above, the present invention provides a system of internal backmix of the reagent mass in a rotating cylindrical reactor that allows the mixing of a portion of the reagent mass in a more advanced stage of the reactor with another in a previous stage of processing, homogenizing the temperatures of the reagent mass and increasing the productivity of the reactor. Thus, the present system dispenses with the need for an external system for moving the said mass, considerably simplifying the reactor's design.

[0027] Numerous variations affecting the scope of protection of the present request are permissible. Thus, it is reinforced that the present invention is not limited to the particular configurations/concretizations described above.